Engineering Science Series 
 
 ENGINES AND BOILERS 
 
ENGINEERING SCIENCE SERIES 
 
 EDITED BY 
 DUGALD C. JACKSON, C.E. 
 
 PROFESSOR OF ELECTRICAL ENGINEERING 
 
 MASSACHUSETTS INSTITUTE OF TECHNOLOGY 
 
 FELLOW AND PAST PRESIDENT A.I.E.E. 
 
 EARLE R. HEDRICK, Ph.D. 
 
 PROFESSOR OF MATHEMATICS, UNIVERSITY OF MISSOURI 
 MEMBER A.S.M.E. 
 
ENGINES AND BOILERS 
 
 BY 
 
 THOMAS T. EYRE 
 
 DEAN, COLLEGE OF ENGINEERING 
 
 STATE UNIVERSITY OF NEW MEXICO, 
 
 FORMERLY ASSISTANT PROFESSOR OF 
 
 MECHANICAL ENGINEERING, PURDUE UNIVERSITY 
 
 J?eto gorfe 
 
 THE MACMILLAN COMPANY 
 1922 
 
 All rights reserved 
 
PRINTED IN THE UNITED STATES OF AMERICA 
 
 COPYRIGHT, 1922, 
 BY THE MACMILLAN COMPANY 
 
 Set up and electrotyped. Published August, 1922. 
 
 . - FORESTRY 
 
 Press of J. J. Little & Ives Co. 
 New York 
 
/ J ^ 
 , 1 
 
 Yo ^es^vv 
 
 PREFACE 
 
 This text book on Engines and Boilers is intended for use in 
 engineering schools which offer an elementary course in Heat 
 Engines. No attempt has been made to cover the more advanced 
 work in Thermodynamics, or to give an exhaustive treatment of 
 the subject of Heat Power. 
 
 This work is the result of the author's experience during the 
 several years that he taught classes in Engines and Boilers and in 
 allied subjects at Purdue University. Much of the material was 
 given to the students first in lectures, and later in the form of 
 mimeographed notes. It is now presented in book form with the 
 hope that it may be of value in other engineering schools. 
 
 At the end of the book a list of representative problems is given. 
 It has been the author's experience that the student obtains a 
 better understanding of the subject if he is required to work 
 problems related to the matter in the text. 
 
 The author wishes to thank Professor C. H. Lawrence for valu- 
 able suggestions made in regard to the form of presentation of some 
 of the work. 
 
 THOMAS T. EYRE. 
 
 University of New Mexico. 
 
 M512399 
 
CONTENTS 
 
 CHAPTER I 
 
 PAGE 
 
 PRESSURE, TEMPERATURE AND HEAT UNITS ... 1 
 
 CHAPTER II 
 
 FUEL . ... 4 
 
 Anthracite Coal Bituminous Coal Lignite and Peat 
 Natural Gas Oil Coal Fields of the U. S. Coal Storage - 
 Determination of the Heating Value of Fuel Combustion 
 Composition of Flue Gas Flue Gas Analysis Heat Lost in Flue 
 Gas Value of CO 2 for Best Efficiency CO 2 Recorders. 
 
 CHAPTER III 
 
 STEAM ..... .... 16 
 
 Use of Steam Tables Throttling Calorimeter. 
 
 CHAPTER IV 
 
 BOILERS ........... 23 
 
 Requirements Rated Horsepower Heating Surface Rules 
 for Finding the Heating Surface Superheating Surface Size 
 of Boiler Tubes The B. & W. Boiler The Sterling Boiler The 
 Wickes Boiler The Return Tubular Boiler The Internally- 
 fired Return Tubular Boiler The Scotch Marine Boiler The 
 Vertical Fire Tube Boiler The Locomotive Boiler Superheaters 
 
 Horsepower of boilers Factor of Evaporation Efficiency of 
 Boilers A. S. M. E. Boiler Test Code. 
 
 CHAPTER V 
 
 BOILER ACCESSORIES AND AUXILIARIES ...... 45 
 
 Grates The Plain Grate The Rocking Grate Mechanical 
 Stokers The Chain Grate The Roney Stoker The Under- 
 feed Furnace Smoke Prevention Settings Draft Dam- 
 pers Safety Devices The Pressure Gage The Safety-valve 
 
 Safety-valve Capacity Napier's Formula Safety-valve For- 
 mula The Water Glass or Gage Glass High-water and Low- 
 water Alarm The Fusible Plug Boiler Feedwater Treatment 
 
 Scale Prevention and Removal Oil Separators Boiler Feed 
 Pumps The Injector Boiler Feed by Returning Trap The 
 Steam Line The Steam Trap Expansion Joints Steam 
 
 vii 
 
Vlll CONTENTS 
 
 PAGE 
 
 Separators Steam-pipe Covering Feedwater Heaters Econ- 
 omizers Condensers The Surface Condenser The Jet Con- 
 denser Cooling of Circulating Water. 
 
 CHAPTER VI 
 
 THE STEAM ENGINE 76 
 
 History The Plain Slide-valve Engine Parts of the Steam 
 Engine Piston Displacement Clearance Steam Back of 
 Piston During Stroke The Indicator and its Purposes Events 
 of Stroke Location of Events on Diagram Equation of Expan- 
 sion and Compression Curves Hypothetical Indicator Diagram 
 Determination of Clearance from Card Determination of the 
 Mean Effective Pressure Indicated Horsepower Brake Horse- 
 power Mechanical Efficiency Thermal Efficiency Cylinder 
 Condensation Steam accounted for by the Indicator Diagram 
 Valve Setting from the Indicator Diagram. 
 
 CHAPTER VII 
 
 COMMON TYPES OF STEAM ENGINES 100 
 
 Slide-valve Engine The Corliss Engine The Four-valve 
 Engine The Compound Engine The Tandem-compound 
 The Cross-compound Cylinder Ratio The Combined Indi- 
 cator Diagram The Diagram Factor Ratio of Expansion 
 The Unaflow Engine. 
 
 CHAPTER VIII 
 
 VALVES 112 
 
 The D Slide-valve Relative Motion of Crank and Piston 
 Valve Diagrams The Valve Ellipse The Bilgram Diagram 
 The Zeuner Diagram Types of Slide-valves Valve with Pres- 
 sure Plate The Piston Valve Double-ported Valves The ' 
 Gridiron Valve The Riding Cut-off Valve Effect of Rocker Arm 
 on the Location of Eccentric Oscillating Valves Poppet Valves 
 Reversing The Stephenson Link The Walschaert Valve 
 Gear The Joy Valve Gear Setting the Slide-valve. 
 
 CHAPTER IX 
 
 GOVERNORS ........... 137 
 
 General Classification of Governors The Gravity-balanced 
 Spindle Governor The Spring-balanced Governor Governing 
 by Changing Position of Eccentric Governing by Changing Angle 
 of Advance Governing by Changing Both Angle of Advance and 
 Valve Travel Centrifugal and Inertia Governors. 
 
 CHAPTER X 
 
 STEAM TURBINES 150 
 
 General History Fundamental Principles Available En- 
 ergy in Steam Velocity Due to Expansion Impulse and Reac- 
 
CONTENTS lx 
 
 PAGE 
 
 tion Bucket Shapes Single-stage Turbine Staging Multi- 
 stage Impulse, Velocity-staging Multi-stage Impulse, Pressure- 
 staging Multi-stage Impulse, Combination Pressure-staging and 
 Velocity-staging Multi-stage Reaction Change of Area of 
 Steam Passage Leakage Loss due to Running Partial Capacity 
 Summary of Losses in the Steam Turbine Common Commer- 
 cial Types DeLaval Single-stage Multi-pressure-stage Im- 
 pulse Turbine Curtis Turbine Parsons Turbine Westing- 
 house Turbine Other Types Low-pressure Turbine Mixed- 
 pressure Turbine Use of Superheated Steam The Marine 
 Turbine. 
 
 CHAPTER XI 
 
 GAS ENGINES .......... 193 
 
 General Historical Cycles of Operation The Four-stroke 
 Cycle The Two-stroke Cycle Classification from Fuel Used 
 Efficiency Fuels The Gasoline Carburetor The Gas Pro- 
 ducer Cooling of Cylinders Ignition Valves Governing 
 Determination of Horsepower Multi-cylinder Engines. 
 
 PROBLEMS 213 
 
ENGINES AND BOILERS 
 
 CHAPTER I 
 PRESSURE, TEMPERATURE AND HEAT UNITS 
 
 1. Pressure Units. In steam engineering, pressure is meas- 
 ured in the following units: 
 
 (1) In pounds per square inch. 
 
 (2) In inches of mercury. 
 
 (3) In inches of water. 
 
 In this country boiler pressures are ordinarily measured in 
 pounds per square inch above atmospheric pressure. Condenser 
 pressures are commonly measured from atmospheric pressure in 
 inches of mercury, i.e. the difference between the pressure in 
 the condenser and atmospheric pressure is read on a mercury 
 column. Draft pressures are usually measured in inches of water. 
 Pressure gages and vacuum gages are so constructed that they 
 read zero at atmospheric pressure. The atmosphere exerts a vari- 
 able pressure, which is about 14.5 pounds per square inch at ordi- 
 nary altitudes and under ordinary conditions. At sea-level, the 
 standard is taken as 14.7 pounds per square inch, which is equiv- 
 alent to 29.92 inches of mercury. 
 
 As the atmospheric pressure is slightly variable, it is necessary 
 in accurate work that pressures be reduced to an absolute basis. 
 Since the zero reading of a boiler pressure gage means atmospheric 
 pressure, the absolute pressure will be the sum of the gage pressure 
 and atmospheric pressure. 
 
 A partial vacuum usually exists in a condenser, since the abso- 
 lute condenser pressure is usually less than atmospheric pressure. 
 Since the vacuum gage as well as the boiler pressure gage reads 
 zero at atmospheric pressure, the absolute pressure in the con- 
 denser is the difference between the atmospheric pressure and the 
 vacuum-gage pressure. 
 
 Figure 1 shows diagrammatically the relation between these 
 pressures. In this figure, a is the boiler-gage pressure, b the 
 
 1 
 
2 ENGINES AND BOILERS 
 
 atmospheric pressure, and c the absolute boiler pressure. Like- 
 wise, d represents the vacuum-gage pressure, which is measured 
 downward from the atmospheric pressure; and e, the difference 
 between 6 and d, is the absolute condenser pressure. 
 
 I 
 
 
 1 
 
 
 a 1 
 
 
 : r 
 
 
 t i 
 
 
 6 
 
 d 
 
 \ 
 
 l_L_ Condenser pressure 
 
 V f 
 
 Z^/ pressure 
 
 FIG. 1 
 
 Barometers used in engineering work in this country are usu- 
 ally graduated in inches. The mercury barometer is used be- 
 cause mercury is the most convenient fluid for this use. A cubic 
 inch of mercury weighs very nearly 0.49 of a pound. Hence the 
 pressure in pounds per square inch is the barometric reading in 
 inches multiplied by 0.49 Vacuum gages also are commonly 
 graduated to read in inches of mercury. Therefore the absolute 
 condenser pressure in pounds per square inch is 0.49 times the 
 difference between the barometer and the vacuum-gage readings. 
 
 EXAMPLE 1. Find the absolute boiler pressure when the pressure gage 
 reads 110 pounds and the barometer reads 29.4 inches. 
 
 SOLUTION. When the barometer reads 29.4 inches, the atmospheric pres- 
 sure is 29.4 X0.49 = 14.4 pounds per square inch. The absolute boiler pressure 
 is then 14.4 + 110 = 124.4 pounds per square inch. 
 
 EXAMPLE 2. Find the absolute pressure in a condenser when the barometer 
 reads 29.8 inches and the vacuum gage reads 27.3 inches. 
 
 SOLUTION. The absolute condenser pressure is the difference between the 
 barometric and the vacuum-gage pressures, which in inches of mercury is 
 29.8-27.3 = 2.5. This reduced to pounds per square inch is 2.5. X49 = 1.22. 
 
 2. Temperature Units. Ordinary temperatures are measured 
 by means of the mercury thermometer. For higher tempera- 
 tures, such as those that occur in furnaces, special thermometric 
 devices called pyrometers are used. 
 
 Three thermometer scales are in use, the Fahrenheit, the Cen- 
 tigrade, and the Reaumur. In the Fahrenheit scale, the differ- 
 ence between the temperatures of melting ice and boiling water 
 at sea level is divided into 180 divisions or degrees; the freezing 
 point is 32 and the boiling point 212. This makes the zero 
 
PRESSURE, TEMPERATURE, AND HEAT UNITS 
 
 Fahrenheit Centigrade Reaumur 
 
 point come 32 below the freezing point of water. In the Centi- 
 grade scale, the freezing point is and the boiling point is 100. 
 In the Reaumur scale, the freezing point is and the boiling 
 point is 80. Figure 2 shows graphically the relation between these 
 scales. It is readily seen 
 how the reading on one 
 scale may be reduced to 
 that of either of the 
 others. It is serviceable 
 
 --!. - 
 
 | 67/.S- 
 
 1 
 
 80' i Boili/tf temperature 
 
 femperofare 
 
 \\ '' 
 
 -J \ A Absolute zero 
 
 FIG. 2 
 
 to remember that a 
 difference of temperature 
 equal to 5 on the Cen- 
 tigrade scale is equal to 
 9 on the Fahrenheit 
 scale. 
 
 Experiment shows 
 that a perfect gas under 
 constant pressure at 32 Fahrenheit expands 1/491.5 part of its 
 own volume for each degree (F.) that its temperature is in- 
 creased. Because of this we call the point 491. 5 below the freez- 
 ing point, or 459.5 on the Fahrenheit scale, the absolute zero. 
 This corresponds to a Centigrade temperature of 273. 
 
 3. Heat Units. In engineering work in this country, it is 
 customary to use English units. Our common heat unit is the 
 British thermal unit (B.t.u.), which is practically defined as the 
 amount of heat necessary to raise the temperature of one 
 pound of pure water from 62 to 63 Fahrenheit. In the metric 
 system the engineers' heat unit is the large calorie, which is the 
 amount of heat necessary to raise the temperature of a kilogram 
 of water from 15 to 16 Centigrade. As one kilogram =2.2046 
 pounds, and as 1 Centigrade =1.8 degrees Fahrenheit, 
 
 one calorie =3. 968 B.t.u., or one B.t.u. =0.252 calorie. 
 
 4. Mechanical Equivalent of Heat. Heat experiments have 
 been made to determine the relation between heat-energy and 
 mechanical work. The latest and most refined experiments show 
 that one B.t.u. as above defined is substantially equivalent to 778 
 foot-pounds of work. This relation is called the mechanical equiva- 
 lent of heat. 1 
 
 *For definition of the "mean B. t. u." and corresponding Mechanical Equivalent of Heat 
 see A. S. M. E. POWER TEST CODE, Edition of 1915, p. 28. 
 
CHAPTER II 
 FUEL 
 
 5. Introduction. The source of the world's supply of energy 
 is the sun. In the use of water power we are drawing, in point 
 of time, almost directly from the sun. On the other hand, in 
 the use of such fuels as coal, gas, and oil, we make use of a store 
 of energy that has been accumulating for ages. 
 
 While the world's supply of coal, oil, and gas is limited, we have 
 used but a very small part of the known deposits. The past 
 century has seen a marvelous change in our manner of living and 
 in our ways of thinking. Our vast commercial system with its 
 perplexing problems has arisen during the past few generations. 
 One of the chief causes of this great change is our ability to util- 
 ize the vast stores of energy to be found in nature. The steam- 
 engine has been the chief means by which the energy stored in 
 our coal deposits has been tapped and forced to do the work of 
 man. What will become of this modern civilization of ours when 
 the fuel supply upon which it is based is exhausted, is an inter- 
 esting problem of the future. Already conservationists are call- 
 ing to us to stop the great waste of our natural resources. 
 
 Of all our fuels, coal is the most important. Coal is the re- 
 mains of vegetable matter deposited in remote geological ages. 
 It is well known that wood rots but little when kept under water. 
 If the water be fresh, -the wood is not eaten by the teredo worm 
 or other forms of aquatic life, and will be kept in a fair state of 
 preservation for thousands of years. If tree trunks and other 
 vegetable matter fall into a fresh-water swamp and are sub- 
 merged before they rot, and if this continues for many centuries, 
 there will be a great accumulation of it. Oar coal deposits are 
 the result of such an accumulation of vegetable matter. Under 
 tropical conditions accompanied by a large supply of carbon 
 dioxide in the atmosphere the growth was very rapid and a deep 
 bed would collect in a comparatively short time. 
 
 Geologists tell us that in the past, parts of the surface of the 
 earth have gradually risen while others have fallen. At a remote 
 time, the tops of our highest mountains may have been the bot- 
 tom of the sea. Suppose a former swamp with its accumulated 
 vegetable matter is now sunk, and that great quantities of silt or 
 
 4 
 
FUEL 5 
 
 other material are deposited upon it. The weight of the material 
 above will compress the vegetable matter into a compact and 
 dense mass. It is also possible that it will be subject to a high 
 temperature, which will change its chemical composition. Vary- 
 ing conditions of pressure and heat are thought to be responsible 
 largely for the differences between the various kinds of coal. 
 
 The principal constituents of coal are carbon, hydrogen, oxygen, 
 nitrogen, sulphur, and refractory earths called ash. The wood- 
 fiber of the original vegetable matter was composed chiefly of 
 hydrocarbons. While under the influence of great pressure, it 
 has at some period of its history been subjected to considerable 
 heat and therefore undergone a process of destructive distiilization. 
 This has driven off much of the volatile matter of the original 
 vegetable material and left a considerable portion of uncombined 
 carbon, which is called fixed carbon. The remainder of the car- 
 bon exists in combination with hydrogen. These carbon and 
 hydrogen compounds are called hydrocarbons. They are easily 
 volatilized, and so comprise a part of the volatile matter of the 
 coal. 
 
 Oxygen and hydrogen are always present in coal in the form 
 of water. This water is volatilized, of course, when the coal is 
 burned. Since heat is required to evaporate and to superheat it, 
 water is a detriment if present in too large a quantity. A small 
 amount of water, however, seems to aid in the combustion of 
 some coals. 
 
 All coal then contains fixed carbon, volatile matter (hydrocar- 
 bons and water), and ash; and it may contain other substances 
 (e.g., sulphur). The combustible is the fixed carbon, the hydro- 
 carbons, and part of the sulphur that may be present. Excessive 
 sulphur is undesirable because it is harmful to the metal of the 
 boiler and the stack if moisture is present, since it may form 
 sulphurous or sulphuric acid; it combines with the ash to form 
 a fusible slag or clinker, which is commonly objectionable; and 
 it makes the fuel more liable to spontaneous combustion when 
 stored in deep piles. 
 
 Coals that have been subjected to the greatest pressure and 
 heat are composed mostly of fixed carbon, and contain only a 
 small amount of volatile hydrocarbons. Such coals are called 
 anthracite. Coals containing larger quantities of volatile hydro- 
 carbons are called bituminous. Since there is no definite divid- 
 
6 ENGINES AND BOILERS 
 
 ing line between these two classes, but the two seemingly overlap, 
 the terms semi-anthracite and semi-bituminous are commonly used 
 to designate coals to which are ascribed certain properties of 
 each class. 
 
 6. Anthracite Coal. Anthracite coal contains but a small 
 amount of combustible volatile matter. While it is considered 
 better for some uses, its heating value is less than that of good 
 grades of bituminous coal. It burns slowly, with but a small 
 flame and practically no smoke. Due to its slow burning quali- 
 ties, a relatively large grate area is needed on which to burn it. 
 The supply of this coal that is easily obtained has been diminish- 
 ing in this country, and its demand for domestic use has greatly 
 increased during the past few years. This has led to a rapid in- 
 crease in price and a great diminution of its use for power purposes. 
 
 Anthracite is considered much superior to bituminous coal for 
 the production of producer gas. This is due to the fact that it is 
 so free from the hydrocarbons that produce tars. The formation 
 of tar has been the great objection to the use of bituminous coals 
 in the producer plant. 
 
 Average anthracite coal contains about 85% fixed carbon, 4% 
 volatile matter, 9% ash, and 2% water. The heat value averages 
 about 13000 B.t.u. per pound. 
 
 7. Bituminous Coal. Most of the coal used for power pur- 
 poses is bituminous. This coal contains a larger percentage of 
 volatile combustible matter. It burns at a lower temperature 
 than does anthracite, and with a much longer flame. The length 
 of the flame varies with the composition, some kinds being called 
 long-flaming and others short-flaming. The ordinary furnace is 
 not usually so constructed as to give the volatile hydrocarbons 
 a chance to be completely burned. This results in the formation 
 of smoke. Engineers have spent much time and study on the 
 prevention of smoke. Upon yielding up their volatile matter 
 some coals fuse and form a solid mass or cake of the nature of 
 coke. These are called caking coals. This action hinders the draft. 
 If rapid combustion is desired, the mass must be broken up. 
 
 The composition of bituminous coal varies greatly, but the 
 average of the better grades may be taken as 65% fixed carbon, 
 28% volatile combustible, 5% ash, and 2% moisture, with a heat 
 value of 14000 B.t.u. per pound. 
 
FUEL 7 
 
 8. Lignite and Peat. Lignite or brown coal is high in vola- 
 tile combustible and also contains much moisture. The evapora- 
 tion of this moisture after mining causes the lignite to crumble or 
 slack. It is usually inferior to anthracite and bituminous coals, 
 but it is used where it is easily obtained and where better coal is 
 expensive. Abroad, lignite is often formed into briquettes. 
 
 Peat is the partly decayed remains of vegetation that accumu- 
 lates in bogs. While it is an inferior fuel, it is used to a consid- 
 erable extent abroad. It is sometimes pressed into briquettes. 
 
 9. Natural Gas. Natural gas is used to some extent for power 
 purposes in sections of the country within reach of the gas fields. 
 It contains about 90% marsh gas (CH 4 ) and has a heat value of 
 nearly 1000 B.t.u. per cubic foot. 
 
 10. Oil. Crude petroleum and fuel oil are used to a consid- 
 erable extent in parts of this country. The petroleum produced 
 in the eastern and middle states is of a paraffin base, while that 
 from Texas and California is of an asphalt base. Gasoline and 
 other light oils are distilled from petroleum, and the residue is 
 sold as fuel oil. Petroleum is composed principally of hydrogen 
 and carbon in the form of hydrocarbons and has a heat value of 
 about 20000 B.t.u. per pound. 
 
 11. Coal Fields of the United States. Our principal deposits 
 of anthracite coal are in eastern Pennsylvania. The deposits are 
 not of large extent and the best are rapidly becoming exhausted. 
 It is claimed that there is anthracite in Alaska. Only a small 
 proportion of the anthracite mined is being used for power pur- 
 poses, the rest going for domestic heating and like purposes. 
 
 The best of our bituminous and semi-bituminous coal is taken 
 from the field that includes western Pennsylvania, eastern Ohio, 
 a large part of West Virginia, and eastern Kentucky. Southwest- 
 ern Indiana and most of the state of Illinois are underlaid with coal 
 of a fair quality. There is also a field running north from Okla- 
 homa through eastern Kansas and western Missouri into Iowa. 
 The coal from the latter is generally of poor quality, and is used 
 only locally. Immense coal fields exist in southern Utah and 
 Colorado, and in New Mexico and Arizona. No complete survey 
 of these fields has been made as yet, and they have not been de- 
 veloped up to the present. There is also a coal and lignite field 
 in eastern Montana and western North Dakota. 
 
8 ENGINES AND BOILERS 
 
 The peat beds of the country are principally in Minnesota, 
 Wisconsin, Michigan, New York, and the New England states. 
 
 Oil is produced in the territory occupied by the eastern coal 
 fields, in Kansas, Oklahoma, Texas, California, and, to a smaller 
 extent, elsewhere. 
 
 12. Coal Storage. In the operation of most steam-power 
 plants, it is essential that a constant supply of coal be available. 
 Owing to unsettled labor conditions at the mines and to uncer- 
 tain transportation facilities, it is necessary that there be some 
 storage capacity. With anthracite coal this is a simple problem, 
 but it is not so with certain grades of bituminous coal. Upon 
 exposure of bituminous coal to the air, there is a considerable 
 oxidation of the hydrocarbons with attendant heat production. 
 If the coal pile is large, this heat may start a fire which is costly 
 and hard to extinguish. The origin of such a fire is called spon- 
 taneous combustion. Even if fire does not start, there is a loss of 
 heat-value up to as high as 10% in some grades of coal. If the 
 moisture content is large, the weathering is accompanied by a 
 crumbling or slacking. Storage piles are often ventilated in order 
 to keep them cool. In some large plants, the storage is so ar- 
 ranged that it may be submerged in water. This obviates the 
 fire risk, and reduces the other losses to a minimum. 
 
 13. Determination of Heating Values of Fuel. In plants 
 where large amounts of fuel are used, it is quite common to buy 
 coal on the basis of its heating value. In accurate tests of power 
 plants it is also necessary to know the heating value of the coal 
 used. Care must be exercised in order to get a fair sample of the 
 fuel. The heating value may be determined in two ways, by 
 combustion in a calorimeter, or by chemical analysis. 
 
 In the calorimeter method a sample of the fuel is placed in a 
 steel bomb along with compressed oxygen. The bomb is placed 
 in a calorimeter containing water, and the fuel is ignited by means 
 of an electrically heated wire. Upon the firing of the fuel, heat 
 is given to the water. It is possible to determine from the rise 
 of the temperature of the water the amount of heat generated. 
 The value thus determined is known as the higher calorific value. 
 It must be remembered that it is seldom possible actually to get 
 this amount of heat by burning in a furnace. This is due to the 
 fact that the hydrogen in the fuel combines with the oxygen of 
 
FUEL 9 
 
 the air to form water, which ordinarily passes from the furnace 
 in the form of steam, carrying with it the heat of vaporization 
 of the steam. The lower heat-value does not contain this heat 
 of vaporization. The higher value is the accepted standard. 
 
 There are two methods of chemical analysis, the ultimate, and 
 the proximate. The ultimate analysis may be made on the basis 
 either of moist or dry fuel. The latter is commonly accepted. 
 If the analysis is made on the basis of moist fuel, it may be con- 
 verted to the dry basis by dividing the percentage of the various 
 constituents by one minus the percentage of the moisture. The 
 ultimate analysis gives the percentage by weight of carbon, hydro- 
 gen, oxygen, nitrogen, sulphur, and ash. Knowing the composi- 
 tion of the fuel, the heat-value may be determined by a formula. 
 An accepted formula is a modification of that of DULONG : 
 
 B.t.u. per pound of dry fuel = 14600 C+62000 (H-O/8)-f 4000S, 
 
 in which C, H, O, and S represent the proportionate parts by 
 weight of carbon, hydrogen, oxygen, and sulphur. The heat- 
 value of pure sulphur is 4000 B.t.u. per pound, but the sulphur 
 in coal is mostly in a form that is noncombustible. The results 
 of the ultimate analysis agree closely with those obtained from 
 the calorimeter. The proximate analysis gives the proportion of 
 fixed carbon, volatile combustible, moisture, and ash. Since the 
 heating value of the volatile combustible is not determined, the 
 results are not as reliable as those of the previous method. It is 
 very often used, however, because it is easily made and affords a 
 rough comparison of various fuels. 
 
 In making the proximate analysis, a weighed sample of coal 
 is placed in a crucible of known weight and is kept at a tem- 
 perature a few degrees above the boiling point of water for an 
 hour. From the loss of weight, the moisture in the coal is cal- 
 culated. The sample is next heated in a hot flame a few minutes 
 with the lid on the crucible. This drives off the volatile matter, 
 and the difference in the new and previous weight is the amount 
 driven off. Now the sample is heated for two hours with the lid 
 off, all fixed carbon is burned out, and the weight is determined 
 by difference as before. The weight left is that of the ash. After 
 having found the percent by weight of the moisture, volatile 
 matter, fixed carbon, and ash, the approximate calorific value 
 may be found by means of the chart, shown in Fig. 3, which 
 
10 
 
 ENGINES AND BOILERS 
 
 has been constructed from the values determined in a large num- 
 ber of accurate analyses. On this chart the heat-value in B.t.u. 
 per pound of combustible is plotted against the percent of fixed 
 carbon in the total combustible. It is assumed that the volatile 
 matter and the fixed carbon constitute the combustible, the ash 
 and the moisture being noncombustible. The method of getting 
 the heating value may be shown by examples. 
 
 EXAMPLE 1. Determine the calorific value in B.t.u. per pound of dry 
 coal having the following ultimate analysis: carbon = 75.46%, hydrogen = 
 3.34%, oxygen = 2.70%, nitrogen = .53%, sulphur = 2.54%, and ash = 15.43%. 
 
 SOLUTION. The B.t.u. per pound = 14600 X .7546 +62000 (.0334 - .0270/8) 
 +400t< .0254 = 12880 B.t.u. The oxygen calorimeter gave a value of 13000 
 B.t.u. per pound for this same sample. 
 
 Chart for determining Heat Value of Combustible with Different Percentages 
 of Fixed Carbon from Proximate Analysis 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 ^ 
 
 ^ 
 
 
 
 
 
 
 
 
 
 
 ^ 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 ^ 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 "X 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 S 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 x 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 s 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 \ 
 
 
 
 
 
 
 
 
 
 
 
 3+O0 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 s 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 \ 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 s 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 \! 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 S 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 \ 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 | 
 
 / 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 / 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 ^ 
 
 
 
 
 
 
 
 ^ / </ a/t 
 
 
 
 
 
 
 
 
 
 
 
 / 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 /3/QQ 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 \ 
 
 
 
 
 
 \^ '*><*" 
 
 
 
 
 
 
 
 
 
 / 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 s 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 / 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 / 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 \ 
 
 
 
 ^ 14000 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 s 
 
 
 
 
 
 
 
 
 J 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 ^ 
 
 ^ t+fVQ 
 
 
 
 
 
 
 f 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 \ 
 
 
 
 
 
 
 / 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 V * r 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 1 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 1 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 * 
 
 
 
 1 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 I 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 tot 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 ^ -14,00 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 1 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 14400 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 JO SS 6S 70 7S &0 
 
 Percent of ftxcd C arbor? m Tbta/ 
 FIG. 3 
 
 EXAMPLE 2. Determine the calorific value of coal which has the follow- 
 ing proximate analysis: moisture =4. 7%, volatile matter = 24.6%, fixed 
 carbon =62.5%, and ash = 8.2%. 
 
 SOLUTION. The combustible being composed of the volatile matter and 
 fixed carbon comprises 24.6+62.5 = 87.1% of the weight of the coal. Of 
 this combustible the fixed carbon is 62.5/87.1 = 71.7%. From the chart 
 it is seen that for 71.7% the B.t.u. per pound of combustible is 15550 B.t.u. 
 As the combustible comprises only 87.1% of the total weight the heating 
 value will be .871X15550 = 13550 B.t.u. per pound of wet coal, or if reduced 
 to the dry basis, 13550/(1.00-. 047) = 14200 B.t.u. per pound. 
 
FUEL 11 
 
 14. Combustion. By combustion is meant the rapid chem- 
 ical combination of oxygen with the carbon, hydrogen, and sul- 
 phur in fuel. Combustion is complete when the maximum amount 
 of oxygen is used in the combination. One atom of carbon will 
 combine with one atom of oxygen to form carbon monoxide (CO). 
 This is not complete combustion, however, for one atom of car- 
 bon will combine with two atoms of oxygen, forming carbon di- 
 oxide (CO2), if sufficient oxygen is present. 
 
 Since the atomic weight of oxygen is 16, and that of carbon is 
 12, it takes 32 pounds of oxygen to 12 pounds of carbon to form 
 carbon dioxide, i.e., one pound of carbon requires for its complete 
 oxidation 2.667 pounds of oxygen. Air, by volume, is composed 
 of about 21% oxygen and 79% nitrogen, and by weight, of 23.15% 
 oxygen and 76.85% nitrogen. So one pound of oxygen is con- 
 tained in 4.32 pounds of air. It therefore takes 2.667X4.32= 
 11.55 pounds of air for every pound of carbon burned. At ordi- 
 nary room temperatures one pound of air occupies about 13.4 
 cubic feet, so that it requires theoretically 13.4X11.55= 155 cubic 
 feet of air for the complete combustion of one pound of carbon. 
 
 The hydrogen in the hydrocarbons of the coal is also com- 
 bustible. A part of the sulphur present may be combustible, 
 but it is usually present in such small amounts that it will be 
 omitted in our present computation. As explained previously, 
 not all of the hydrogen content of the coal is combustible, since 
 part of it is already combined with oxygen in the form of water. 
 Therefore the available hydrogen may be expressed as (H O/8). 
 Since hydrogen combines with oxygen to form water, in the ratio 
 by weight of 1 to 8, it will require 8 pounds of oxygen to burn 
 each pound of hydrogen. Since one pound of oxygen is contained 
 in 4.32 pounds of air, it will take 8X4.32=34.6 pounds of air to 
 burn a pound of hydrogen. Hence the total weight of air re- 
 quired to burn a pound of coal to CO 2 and H 2 O is theoretically 
 
 11.55 C+34.6 (H-O/8), 
 
 where C, H and O have the same meaning as in 13. 
 
 Since the nitrogen of the air is inert, it is of no value to the 
 combustion. Since it passes up the stack at a higher tempera- 
 ture than that at which it entered the furnace, it carries away 
 heat. Any less air than the theoretically correct amount would 
 result in the formation of a mixture of carbon monoxide and 
 
12 ENGINES AND BOILERS 
 
 carbon dioxide. The heat liberated by the formation of the carbon 
 monoxide is only 4450 B.t.u. per pound of carbon, while it is 
 nearly 14600 B.t.u. for the formation of carbon dioxide. Hence the 
 production of carbon monoxide in a furnace means a large loss 
 of heat. The presence of carbon monoxide in flue gas nearly 
 always indicates a large amount of unburned hydrocarbons and 
 hence an even greater loss of heat. If it were possible to so dis- 
 tribute the air that it all came in close contact with the fuel, and 
 also to give it time enough to combine thoroughly with the fuel, 
 the theoretical amount of air would be sufficient. Under actual 
 furnace conditions, however, it is found that 50% or more excess 
 of air is needed to give complete combustion of coal. A somewhat 
 smaller excess is needed when oil is used as a fuel, because there 
 is better distribution of the air. The greater the amount of air 
 passing through the furnace, the greater the amount of heat it 
 will carry along to the stack. Hence an unnecessary excess of 
 air is not desirable, and leads to lessened efficiency. The neces- 
 sary excess depends upon the conditions of draft and fire as well 
 as upon the kind of fuel and the type of furnace. It can only 
 be determined by actual test. 
 
 15. Composition of Flue Gas. As just explained, an excess 
 of air is needed in order to get complete combustion of the fuel. 
 If it were possible to get complete combustion without this excess, 
 our flue gas would be composed chiefly of nitrogen, carbon dioxide, 
 and water vapor. Due to the excess of air, there will be free 
 oxygen present in the flue gas. If there is an insufficient excess 
 of air there will also be carbon monoxide and probably some 
 hydrocarbons present. We have seen that the presence of carbon 
 monoxide indicates incomplete combustion and therefore low fur- 
 nace efficiency. On the other hand, a large excess of air, while 
 it may give complete combustion, gives poor furnace efficiency 
 because the air will carry a large amount of heat up the stack. 
 It is a matter of great importance that just the right excess of 
 air be admitted to the furnace. Since it is difficult to measure 
 directly the amount of air entering the furnace, an easier method 
 is used. This method consists in analyzing the flue gas to deter- 
 mine the amount of each of its constituents. From this analysis 
 we can easily compute the amount of air entering the furnace. 
 Knowing the composition of flue gas, we can regulate the amount 
 
FUEL 13 
 
 of air entering the furnace so as to give the proper excess to insure 
 the best economy of operation. 
 
 16. Flue Gas Analysis. There are various types of apparatus 
 on the market for making the analysis of flue gas, most of which 
 are modifications of the apparatus designed by ORSAT. A com- 
 plete description of the Orsat apparatus will not be given here, 
 but the principle of its operation is as follows. 
 
 A sample of gas is taken from the rear of the furnace or between 
 the furnace and the stack. After being cooled to the room tem- 
 perature, it is carefully measured by volume at atmospheric 
 pressure. All measurements are taken at room temperature and 
 at atmospheric pressure. This known volume of our sample is 
 first passed a few times through a solution of caustic potash, which 
 absorbs the carbon dioxide. The volume is measured again, and 
 the difference between the new volume and the original volume 
 is the volume of the carbon dioxide absorbed. The same sample 
 is next passed several times through a solution of potassium pyro- 
 gallate, which absorbs the oxygen. The amount of oxygen is 
 determined by the loss in volume, as before. Next the sample 
 is passed several times through a solution of acid cuprous chloride 
 and the carbon monoxide removed, and its amount determined 
 as before. The amount of carbon monoxide is usually quite small. 
 The remainder of the sample is usually assumed to be nitrogen^ 
 
 17. Heat Lost in Flue Gas. The weight of flue gas per pound 
 of fuel burned (assumed carbon and ash) may be computed from 
 the formula, 
 
 where 
 
 W = weight of flue gas per pound of fuel burned. 
 C = decimal part by weight of total carbon in fuel. 
 N = percentage by volume of nitrogen in flue gas. 
 CC>2 = percentage by volume of carbon dioxide in flue gas. 
 CO = percentage by volume of carbon monoxide in flue gas. 
 
 A = decimal part by weight of ash in fuel as fired. 
 
 Unless the ultimate analysis of the fuel is known, the weight 
 
 of carbon in the volatile matter will have to be estimated and 
 
 added to the weight of fixed carbon to give C in the preceding 
 
 formula. Marks has published a chart showing the approximate 
 
14 
 
 ENGINES AND BOILERS 
 
 relation between the volatile carbon in the combustible and the 
 total volatile matter in it. With the aid of this chart (Fig. 4), 
 the value for C in the preceding formula can be approximated 
 from the proximate analysis. The specific heat of the flue gas 
 is usually taken as .24; and the heat lost per pound of fuel 
 burned is equal to the product of the specific heat of flue gas, the 
 weight of gas per pound of fuel, and the difference in temperature 
 between the leaving flue gas and the entering air. 
 
 Chart for determining the Carbon in the Volatile Matter 
 
 Marks 
 
 ts 
 
 20 
 
 10 20 30 -9-0 SO t 
 
 Percent of Yo/otifa Afatt-rr jr? ffye Combust/hie 
 
 FIG. 4 
 
 EXAMPLE. How much heat is carried up the stack by the dry flue gases, 
 when the furnace is burning coal of the following proximate analysis? Mois- 
 ture = 3%, fixed carbon = 65%, volatile matter = 26%, and ash=6%. The 
 analysis of flue gases gives: CO 2 = 10%, O = 8%, and CO = .5%. The stack 
 temperature is 500 F. and the temperature of the air entering the furnace 
 is 80 F. 
 
 SOLUTION. From the chart of Figure 4, we find that the percent ofjvoh 
 tile carbon in the combustible is about 13.5, which corresponds 
 fuel. The total carbon is then 12.1+65 = 77.1%, and the weighiToT flue 
 gases per pound of coal is 
 
 3.032 X. 771 
 
 --6) = 19 - 1 Pounds. 
 
 The heat carried up the stack by the dry flue gases is then .24X19.1 (500 
 80) = 1925 B.t.u. for each pound of coal fired. In this problem, the heat- 
 value of a pound of coal found from the proximate analysis is 13860 B.t.u. 
 Hence the loss is 1925/13860 = 13.9% of the heat available. 
 
FUEL 15 
 
 Both the fuel and the air contain moisture. This moisture also carries 
 heat up the stack, since it is a superheated vapor upon leaving the furnace. 
 
 18. Value of CO 2 for Best Efficiency. As has been stated, 
 the efficiency of the furnace will vary with the excess of air ad- 
 mitted. Since the percentage of CO 2 also varies with the excess 
 of air, we see that an indication of the efficiency .is given by the 
 CO 2 reading. Just what percentage of CO 2 corresponds to the 
 highest operating efficiency depends upon such factors as kind 
 and state of fuel, stack temperature, etc. After the proper 
 amount of C0 2 for best efficiency has been determined under 
 these conditions, the CO 2 reading will indicate whether or not 
 high efficiency is being obtained. Since the determination of the 
 CO 2 is a comparatively simple operation, it is an excellent way to 
 keep check on operating conditions. Some plants go so far as to 
 pay their firemen on the basis of the CO 2 record. In general, 
 high CO 2 means high efficiency, unless there is some abnormal 
 condition such as too much CO. The CO should be kept as near 
 zero as possible. 
 
 At the same temperature and pressure, CO 2 occupies the same 
 volume as the oxygen from which it was formed. The volume of 
 the oxygen in the air is 21%. Hence, if the products of combus- 
 tion are cooled down to the temperature of the entering air, the 
 CO 2 reading would be 21% for perfect combustion with no excess 
 of air, assuming the fuel to be carbon and ash. In practice, the 
 CO 2 runs 17% or lower. Even 15% is usually considered an in- 
 dication of very good efficiency. 
 
 19. CO 2 Recorders. Automatic devices are on the market 
 that will analyze and record the amount of CO 2 on a chart. An 
 analysis is made every few minutes, so that a complete record is 
 kept of the operating efficiency. 
 
CHAPTER III 
 
 STEAM 
 
 20. Introduction. Definitions. A perfect gas may be at any 
 temperature under any pressure. For instance, air may be placed 
 under a certain pressure and have its temperature raised or low- 
 ered by the addition or subtraction of heat. On the other hand, 
 a saturated vapor, such as steam, can exist only at a certain 
 definite temperature for each particular pressure. Under ordinary 
 atmospheric pressure, saturated steam can exist only at a temper- 
 ature of about 212 F. Under an absolute pressure of 100 pounds 
 per square inch, saturated steam will be at a temperature of 
 327.86 F. 
 
 Let us consider a case in which a pound of water at 32 F. is 
 placed under a pressure of, say, 100 pounds per square inch. 
 The containing vessel is supposed to be so constructed that the 
 pressure remains constant, no matter what change of volume 
 takes place. Now suppose that the water is heated. There will 
 be little change in volume, but there will be a rise of temperature 
 of approximately one degree F. for each B.t.u. given to the water. 
 This will continue until we have added 298.5 B.t.u. The tem- 
 perature will then be 327.86 F. A further addition of heat up 
 to a limit will not cause any change of temperature, but will effect 
 a change in the physical condition of the water, turning it to 
 steam. We shall need to apply 887.6 B.t.u. to effect this change 
 completely. We have now added a total of 298.5+887.6 = 1186.1 
 B.t.u., and have converted the pound of water, originally at 32 F., 
 into dry saturated steam at a temperature of 327.86 F., and 
 under an absolute pressure of 100 pounds per square inch. 
 
 Now that the water is all evaporated, if more heat be added 
 to this steam, the temperature will rise at the rate of nearly two 
 degrees per B.t.u. added. We now have superheated steam. 
 
 As stated previously, the volume of the water will change but 
 little until the boiling point is reached. The space occupied by 
 the saturated steam will be 4.432 cubic feet. This is many times 
 greater than the space formerly occupied by the water. Part 
 of the 887.6 B.t.u. that was used to evaporate the water was 
 evidently used to cause this change in volume under the pressure 
 
 16 
 
STEAM 
 
 17 
 
 of 100 pounds per square inch. The remainder was used to make 
 the physical change in the water, to increase the kinetic energy 
 of its atoms. For pressures other than 100 pounds we would 
 have values different from those given above. 
 
 Figure 5 represents graphically the relation between the tem- 
 perature and the heat added to a pound of ice, starting at zero 
 degrees F. (with the assumption that the pressure is constant). 
 Upon the first addition of heat, the temperature of the ice will 
 rise until the melting point is reached. Further addition of heat 
 
 1 
 
 I 
 
 O* 32 
 
 Temperature 
 
 FIG. 5 
 
 causes the ice to melt. This occurs without a change of tempera- 
 ture. The part of the line representing the melting of the ice 
 is therefore vertical. When the ice is all melted, addition of more 
 heat causes the temperature of the water to rise. This will con- 
 tinue until the boiling point is reached. That part of the line 
 representing evaporation will be vertical since there is no change 
 of temperature during that period. When evaporation is com- 
 plete, the addition cf heat again causes a rise in temperature. 
 
 The amount of heat necessary to raise the temperature of the 
 water, the amount of heat required to change it to steam, and 
 also the volumes of steam formed under different pressures, have 
 been determined by numerous experiments and are published 
 
18 ENGINES AND BOILERS 
 
 under the name of steam tables. We shall use in our work the 
 tables prepared by C. H. Peabody. 1 These are arranged in two 
 ways. In Table I, the various absolute pressures at which water 
 boils are given for each degree F. from 32 to 428. In Table II, 
 the various temperatures at which water boils are given for each 
 pound per square inch from 1 to 336. The values are arranged 
 in two tables not because they are different, but simply as a con- 
 venience in their use. 
 
 In Table I, the first column, headed t, gives the temperature 
 at which water boils. The second column, headed p, gives the 
 absolute pressure under which it must be in order that it boil 
 at the temperature given in the first column. 
 
 The third column, headed q, gives the heat of the liquid, which 
 is the number of B.t.u. necessary to change the temperature of one 
 pound of water from 32 F. to the temperature given in the first column. 
 This does not mean that there is no heat in the water at 32. 
 'The heat in the water below the freezing point is of no moment 
 to the steam engineer; hence it is chosen as the arbitrary starting 
 point. 
 
 Column four, headed r, gives the heat of vaporization, which is 
 the B.t.u. necessary to evaporate completely a pound of water at the 
 temperature and pressure given in the first and second columns. 
 This is sometimes called the latent heat of evaporation. The 
 sum of the heat of the liquid and the heat of vaporization is 
 called the total heat. 
 
 The fifth column, headed p, is that part of the heat of vaporiza- 
 tion that is used in energizing the atoms of the water to turn it to 
 a vapor; it is called the heat equivalent of internal work. 
 
 The sixth column, headed Apu, is the rest of the heat of vaporization, 
 or that port that is needed to do the work of increasing the volume, 
 under the pressure of column two; it is called the heat equivalent 
 of external work. 
 
 Columns seven and eight will not be discussed here. Column 
 nine, headed s, gives in cubic feet the specific volume, which is 
 the volume of one pound of dry saturated steam under the pressure 
 of column two. 
 
 Column ten gives the reciprocals of the values found in column 
 nine. It is the weight of one cubic foot of dry saturated steam under 
 the pressure of column two. 
 
 i C. H. PEABODY, Steam Tables. 
 
STEAM 
 
 19 
 
 Steam generated in most boilers not equipped with a super- 
 heater is likely to carry with it, when leaving through the outlet 
 pipe, a small amount of water in a finely divided state or mist. 
 Steam containing this moisture is said to be wet steam. The 
 
 Chart Showing Specific Heat of Superheated Steam Values from 
 Knoblauch and Jakob 
 
 700 
 
 zoo 
 
 SO /OO /JO ZOO 250 
 
 Pressure In pounds per square /nch ffhso/ute 
 FIG. 6. 
 
 quality of wet steam is expressed in percent. If in a hundred 
 parts by weight of a mixture of steam and water, five parts by 
 weight are moisture, the quality of the mixture is said to be 95% 
 and the priming 5%. 
 
 As long as steam is in contact with water it will remain satu- 
 rated, and its temperature cannot be raised under constant pres- 
 
20 ENGINES AND BOILERS 
 
 sure. If it is conducted away from the water and led to a super- 
 heater, its temperature will be raised by the addition of heat. 
 It is then superheated steam. The amount of heat necessary to 
 superheat depends upon the pressure and upon the degree of 
 superheat. The chart of Fig. 6 gives the specific heat of super- 
 heated steam for the ranges of pressure and temperature com- 
 monly found in practice. The specific heat of steam varies with 
 both temperature and pressure. The chart gives the average 
 values of specific heat as the steam is raised from the temperature 
 of saturation to the temperature of superheat. 
 
 EXAMPLE 1. How much heat is required to change a pound of water at 
 70 F. into dry saturated steam at a pressure of 120 pounds per square inch 
 absolute? 
 
 SOLUTION. On page 48 of Peabody's Steam Tables, we find that the heat 
 of the liquid, q, for 120 pounds pressure is 312.3 B.t.u. This amount of heat 
 would bring the temperature of the water from 32 F. to the boiling point. 
 As the temperature of the water to start with is 70 (p. 36), it already con- 
 tains 38.1 B.t.u. It is then necessary to add to it 312.3-38.1=274.2 B.t.u. 
 in order to bring it to the boiling point. To evaporate the water requires 
 the heat of vaporization, r, at 120 pounds (p. 48), which is 876.9. Hence 
 the total heat required to bring the water up to boiling and to evaporate it 
 is 274.2+876.9 = 1151.1 B.t.u. 
 
 EXAMPLE 2. If, in Example 1, the quality of the steam formed had been 
 97%, how much heat would it have required? 
 
 SOLUTION. The water must all be brought to the boiling point, which 
 takes the same amount of heat as in Example 1, 274.2 B.t.u. As the quality 
 is 97%, only .97X876.9 = 850.6 B.t.u. are needed to evaporate the water. 
 Hence the total amount of heat required is 274.2+850.6 = 1124.8 B.t.u. 
 
 EXAMPLE 3. Find the amount of heat necessary to generate the pound 
 of steam in Example 1, if it is superheated to a temperature of 475 F. 
 
 SOLUTION. To generate a pound of dry saturated steam under the con- 
 ditions of Example 1, requires 1151.1 B.t.u. The temperature correspond- 
 ing to 120 pounds pressure is 341.3 F. The superheat is then 475 -341.3 = 
 133.7. From the chart of Fig. 6, the specific heat of superheated steam is 
 .537. It will take .537X133.7 = 71.8 B.t.u. to superheat the steam. Hence 
 the total heat required is 1151.1+71.8 = 1222.9 B.t.u. 
 
 EXAMPLE 4. Find the volume of the pound of steam in Example 2. 
 
 SOLUTION. A pound of dry saturated steam at 120 pounds pressure occu- 
 pies 3.723 cubic feet. The quality being 97%, the volume occupied by the 
 steam is .97X3.723 = 3.611 cubic feet. A pound of water occupies .016 
 cubic feet, and, as 3% of the pound of wet steam is water, the volume of the 
 water is .03 X .016 = .0005 cubic feet. Hence the total volume is 3.61 1 + .0005 = 
 3.611 cubic feet. 
 
STEAM 
 
 21 
 
 21. The Steam Calorimeter. In making tests of boilers or 
 engines it is necessary to know the quality of steam leaving the 
 one or entering the other. A steam calorimeter is used in mak- 
 ing this determination. Several types of calorimeters are in use. 
 If the quality of steam is high (between 94% and 100%), the 
 throttling type is usually used. When properly constructed this 
 calorimeter is sufficiently accurate for ordinary purposes. 
 
 Figure 7 shows a throttling calorimeter attached to a steam- 
 pipe A. If the steam is saturated, and the pressure is known 
 from a pressure gage H, its temperature may be determined from 
 the steam tables. If the steam in A is superheated, it is also 
 necessary to take its temperature by means of a thermometer, 
 and the heat contents may be calculated from the steam tables. 
 If it is wet, the quality must be known to find its heat contents. 
 The tube B in Fig. 7 is a sampling tube through which a sample 
 of steam is taken from the pipe A. This sample is throttled down 
 
22 ENGINES AND BOILERS 
 
 in pressure at C from the pressure in A, say pi, to the pressure 
 in the calorimeter G, say p%. If the calorimeter is well covered, 
 but little heat is lost by radiation and the heat contents in one 
 pound of steam in A is the same as in the chamber G. The pres- 
 sure and temperature in G are measured by the gage F and the 
 thermometer E, and the heat contents are computed by means 
 of the steam tables. 
 
 Since the heat content is the same per pound in A as in G, 
 the quality in the former may be computed as follows. The total 
 heat in A equals q\-\-xri where x is the quality and qi and r\ are 
 the heat of liquid and the heat of vaporization in A, respectively. 
 If the calorimeter is working properly, the steam will be super- 
 heated in G, and its heat contents will be equal to 
 
 where q% and r% are the heat of the liquid and the heat of vaporiza- 
 tion in G, respectively, 3 is the temperature of steam in G as 
 measured by the thermometer E, and k is the temperature of 
 saturated steam at the pressure p%. The term .48 (3 2) is the 
 heat of superheat in G, since .48 is the specific heat of super- 
 heated steam at low pressure and temperature. Then we have 
 
 from which x may be found. 
 
 EXAMPLE. Find the quality of steam leaving a boiler when the pressure 
 
 is 165 pounds gage. The gage pressure in the throttling calorimeter is 3 
 
 founds, the temperature is 265 F., and the barometer reading is 29.6 inches. 
 
 SOLUTION. From the steam tables, q\ =345, n =851, <? 2 = 189, r 2 = 964, and 
 
 * 2 = 221. Then 
 
 345+z851 = 189+964+.48(265-221), 
 
 from which x = .975 or 97.5%. 
 
CHAPTER IV 
 BOILERS 
 
 22. Introduction. The stored energy in fuels is utilized by 
 means of the steam engine as follows. The fuel is burned in a 
 furnace, resulting in a mixture of heated gases. These hot gases 
 pass over and along the surface of a boiler. A transfer of heat 
 takes place through those boiler surfaces that are exposed to 
 contact with the hot gases or to radiation from the incandescent 
 fuel bed on the one side and water or steam on the other side. 
 This boiler surface is called heating surface. This heat is con- 
 ducted through the shell of the boiler and is spent in heating and 
 evaporating the water contained in the boiler. The steam thus 
 formed is conducted from the boiler to the engine or turbine, 
 where it does work due to its pressure and to its tendency to 
 expand. 
 
 Practically all boilers have a considerable storage of heated 
 water and steam. This water and steam is under a high pres- 
 sure and would increase in volume hundreds of times if the pres- 
 sure were removed. A sudden release of this pressure causes 
 an explosion. Many lives have been lost and a great amount of 
 property destroyed by boiler explosions. Hence the consideration 
 of first importance in a boiler is its safety. Other considerations 
 are its first cost, its life, and the ease with which it may be cleaned 
 and repaired. In portable boilers and marine boilers, weight and 
 the space occupied are of great importance. 
 
 Since the purpose of the heating surface is to conduct heat 
 from the furnace to the water, it follows that the conduction 
 should be rapid and effective. To be efficient, the boiler must 
 extract a large proportion of the heat generated in the furnace. 
 The surface must be of such size and so arranged that time is 
 allowed to render this transfer as complete as possible. 
 
 Due to the erosion of some of the parts, or due to overheating 
 consequent on the formation of scale, a boiler originally fit for a 
 certain class of service may become so weakened that it is unsafe 
 for high pressures. Many states provide for an inspection of 
 boilers and equipment in order to prevent explosions. The vari- 
 ous boiler insurance companies also make periodic inspection of 
 insured boilers. As a result of this inspection, the inspector sets 
 
 23 
 
24 ENGINES AND BOILERS 
 
 a limit to the pressure that the boiler may carry. The fireman 
 must be constantly on the alert to detect any signs of a develop- 
 ing weakness. 
 
 Much of the water used in boilers will deposit scale on the heat- 
 ing surface of the boiler. This scale greatly hinders the conduc- 
 tion of heat to the water and may even become thick enough 
 to allow the metal on which it settles to become overheated to 
 such an extent that it gives way and causes an explosion. If the 
 scale becomes too thick, it must be removed. The removal and 
 prevention of scale will be considered later. 
 
 The fire side of the heating surface in many boilers will collect 
 soot and fine ash. To maintain efficient steaming these surfaces 
 must be kept clean. The soot should be swept or blown from the 
 surface as fast as it collects. 
 
 In the construction of a steam-boiler, the following require- 
 ments are to be considered. 
 
 (1) Proper materials of uniform strength and reliability must 
 be employed, and the size of all parts must be so designed that 
 a sufficient factor of safety exists. The workmanship must be 
 good. 
 
 (2) There must be steam space and water capacity such that a 
 sudden change of load will not cause an undue drop in steam 
 pressure. 
 
 (3) There must be a sufficient water surface to allow for com- 
 plete separation of the steam from the water. Too small a sur- 
 face will result in foaming. 
 
 (4) A thorough circulation of the water must be provided, so 
 that a uniform temperature is maintained throughout the boiler. 
 Water is a very poor conductor of heat, and it is therefore essen- 
 tial that there be a continuous flow over the heating surface. 
 
 (5) Stresses due to temperature change must be eliminated. 
 
 (6) In so far as possible, all joints or seams must be protected 
 from the direct action of the flame. 
 
 (7) Access must be possible to all parts for cleaning and repair. 
 
 (8) A means for the discharge of mud or sludge that is left by 
 the evaporation of the water must be provided. 
 
 The modern steam boiler is the result of an evolution starting 
 with a vessel much resembling a closed kettle. The pressure in the 
 early boilers was nearly atmospheric ; hence the shape was not 
 influenced by the consideration of the strength of the boiler. 
 
BOILERS 25 
 
 With the use of steam under pressure, boilers assumed a cylin- 
 drical or spherical shape, since these shapes are not distorted so 
 much by internal pressure. The simplest boiler is cylindrical, 
 with hemispherical ends. 
 
 For a given steam pressure, the thickness of metal required 
 varies directly as the diameter. Hence heavy plate must be used 
 for boilers of considerable size. Moreover, the ratio between the 
 heating surface and the volume decreases as the diameter in- 
 creases. Thus it is seen that the single cylinder is suitable for 
 small boilers only. 
 
 From this early and simple type of boiler the development 
 has proceeded along two distinct lines. First, in place of a single 
 large cylinder, several smaller ones were sometimes used, thereby 
 decreasing the weight of metal and increasing the rate of steam- 
 ing. Carrying this idea still further results in a large number of 
 very small cylinders or tubes filled with water and surrounded by 
 fire. This is the modern water-tube boiler. 
 
 The other way of increasing the heating surface of a cylindrical 
 boiler is to run smoke flues through it. The earliest types con- 
 tain one or two large flues. The modern type contains a large 
 number of small tubes through which the fire or the products of 
 combustion pass. This type is known as the fire-tube boiler. 
 
 23. Rated Horsepower. The rating of a boiler is usually 
 based on its heating surface. There is no standard for this rat- 
 ing. It is becoming general practice, however, to rate a water- 
 tube boiler on a basis of 10 square feet of heating surface per boiler 
 horsepower, and to rate a fire-tube boiler at 11 or 12 square feet 
 per boiler horsepower. Under average conditions of firing, care, 
 and draft, a boiler should develop good economy at its rated 
 horsepower. However, many boilers are able to carry great over- 
 load and still give excellent efficiency. Poor efficiency is due in 
 general more to overloading the furnace than to increasing the 
 evaporation from the boiler. 
 
 24. Heating Surface. It has been customary to consider as 
 heating surfaces those surfaces which have water on one side and 
 the products of combustion on the other side. No distinction 
 is made in the thickness of metal in different parts of the boiler, 
 or in the difference in temperature of the gases on their path along 
 the heating surface. However, great accuracy is seldom required 
 
26 ENGINES AND BOILERS 
 
 in computing the heating surface of a boiler. In calculating 
 heating surface, the inside of fire tubes and the outside of water 
 tubes is used. 
 
 25. Rules for Finding the Heating Surface. 
 
 1. Horizontal Return-tubular boilers. Kent l gives the fol- 
 lowing rule: 
 
 Take the dimensions in inches. Multiply two-thirds of the 
 circumference of the shell by its length; multiply the sum of 
 the circumferences of all the tubes by their common length; 
 to the sum of these products add two-thirds the area of both 
 tube sheets; from this sum subtract twice the area of all the 
 tubes; divide the remainder by 144 to obtain the area in square 
 feet. 
 
 2. Vertical Tubular boilers. Kent 2 gives the following rule: 
 Multiply the circumference of the fire-box (in inches) by its 
 
 height above the grate; multiply the combined circumference 
 of all the tubes by their length, and to these two products add 
 the area of the lower tube sheet; from this sum subtract the 
 area of all the tubes, and divide by 144 : the quotient is the 
 number of square feet of heating surface. 
 
 3. General rule. The U. S. Bureau of Mines 3 gives the fol- 
 lowing rule: 
 
 A short approximate method for any boiler is to figure the 
 square feet of heating surface in the tubes and divide it by 0.85 
 for a return tubular boiler or by 0.95 for a water tube boiler. 
 In case the return tubular boiler has an arch over the top for 
 gas passage, giving the so-called third return, it is necessary 
 to add from 100 to 200 square feet to the result to obtain the 
 total heating surface. 
 
 In this last rule the heating surface in fire-tube boilers is figured 
 from the outside diameter of tubes. 
 
 26. Superheating Surface. In modern practice, steam is often 
 led off from the main steam space and taken through other heat- 
 ing coils. Since there is no water in contact with this steam, it 
 
 1 KENT, Mechanical Engineers' Handbook, 1916 Edition, p. 888. 
 
 a Ibid. 
 
 8 BUREAU OF MINES, U. S. DEPARTMENT OF THE INTERIOR, Bulletin No. 40, p. 9. 
 
BOILERS 
 
 27 
 
 will be superheated. That surface which has this superheated 
 steam on one side and fire or hot gases on the other is called the 
 superheating surface. 
 
 27. Size of Boiler Tubes. The outside diameter is the nom- 
 inal diameter in boiler tubes. The following table given by the 
 
 5 team -pipe 
 Cffnnecfion 
 
 FIG. 8 
 
 National Tube Works gives the nominal or outside diameter, the 
 inside diameter, and the thickness, of standard lap-welded boiler 
 tubes. 
 
 SIZE IN INCHES OF STANDARD LAP-WELDED TUBES 
 
 External Diameter 
 
 1.0 
 .810 
 .095 
 3.25 
 3.010 
 .120 
 
 1.25 
 
 1.060 
 .095 
 3.5 
 3.260 
 .120 
 
 1.5 
 1.310 
 .095 
 3.75 
 3.510 
 .120 
 
 1.75 
 1.560 
 .095 
 4.0 
 3.732 
 .134 
 
 2.0 
 1.810 
 .095 
 4.5 
 4.232 
 .134 
 
 2.25 
 2.060 
 .095 
 5.0 
 4.704 
 .148 
 
 2.5 
 
 2.282 
 .109 
 6.0 
 5.670 
 .165 
 
 2.75 
 2.532 
 .109 
 7.0 
 6.670 
 .165 
 
 3.0 
 2.782 
 .109 
 8.0 
 7.675 
 .165 
 
 Internal Diameter 
 Standard Thickness 
 External Diameter 
 Internal Diameter 
 Standard Thickness 
 
28 ENGINES AND BOILERS 
 
 28. Water-tube Boiler. Babcock and Wilcox Type. One of 
 the most common forms of water-tube boilers is the Babcock and 
 Wilcox type, shown in Fig. 8. Here the tubes are fastened into 
 headers, which in turn are connected by other tubes to a forged 
 steel cross-box that is riveted to the steam drum above, as shown 
 in Fig. 9. Headers are made of cast-iron for low-pressure work, 
 and of wrought steel for high-pressure work. They are of two 
 types, vertical and inclined. In the latter the tubes enter the 
 header at right angles. The tubes between the front and rear 
 headers are inclined so that a circulation of water is insured. 
 Opposite the end of each tube in the header is placed a hand- 
 hole to permit cleaning and access to the tube. These holes are 
 closed by means of a cap. This arrangement also allows ease in 
 cleaning the scale from the tubes, as the caps are easily removed 
 and a cleaner run through the tube. Clean-out doors are placed 
 in the setting opposite the headers to give easy access for cleaning. 
 The grates are so located, and fire-brick partitions or baffles 
 are so placed, that the hot gases usually pass across the tubes 
 ^ three times on their way to the stack. The mud 
 | | drum is connected to the lower end of the back 
 
 header. This collects the sediment that is formed 
 during the evaporation of the water. This sediment 
 is blown off from time to time through the blow-off 
 pipe shown at the lower right hand of Fig. 8. 
 
 The feedwater is brought in at the front of the 
 steam drum, and is so delivered that its velocity 
 will aid in circulation of the water in the boiler. 
 The circulation is back through the steam drum, 
 down the tubes to the back header, where it is distributed to the 
 inclined tubes, up these to the front header, and thence to the 
 front of the steam drum. The steam is taken off through a dry- 
 pipe located at the top of the steam drum. If a superheater is 
 attached, as shown in Fig. 8, the steam is led from the dry-pipe at 
 the top of the steam drum into and through the superheater, and 
 then up to the steam pipe shown at the top of the steam drum. 
 Provision is made for flooding the superheater during the period 
 of getting up steam. This keeps the surface cool enough to 
 prevent its burning out. The boiler is carried by slings from 
 horizontal girders placed above it. The whole boiler is surrounded 
 by a smoke-tight brick setting. 
 
BOILERS 
 
 29 
 
 A similar form, but using boiler plate headers instead of cast 
 or forged sectional headers, is called the Heine type. 
 
 29. Water-tube Boiler. Stirling Type. A common form of 
 water-tube boiler is- shown in Fig. 10. Here banks of tubes lead 
 
 feed water inlet. 
 
 Sfatmotrffef 
 
 FIG. 10 
 
 from the lower drum, or mud drum, to the three drums above. 
 The water is taken in at the rear upper drum and the steam is 
 drawn off at the top of the middle drum. Arched tubes connect 
 the steam space of the upper drums. Access to the inside of the 
 drums, for the purpose of expanding the tubes, for cleaning, and 
 
30 
 
 ENGINES AND BOILERS 
 
 for inspection, is had by means of a manhole located at the end 
 of each drum. The sediment collects and is blown off at the 
 bottom of the mud drum through the blow off pipe and valve 
 shown at the lower left hand corner of Fig. 10. The baffling is 
 
 J/easnov/kf 
 
 connect/em 
 
 \3mo/ie out/rt 
 
 FIG. 11 
 
 so arranged that the products of combustion are forced to travel 
 practically the entire length of all the banks of tubes, up the first 
 bank, down the second and up the third. Clean-out doors for 
 the removal of soot are located at various points shown in Fig. 10. 
 
 30. Water-tube Boiler. Vertical Type. A Wickes vertical 
 water-tube boiler is shown in Fig. 11. In this type of boiler the 
 tubes are straight and are placed vertically. They are connected 
 to a mud drum below and to a steam drum above. The products 
 
BOILERS 31 
 
 of combustion pass up along the front half of the tubes and down 
 the back half, leaving at the rear. 
 
 31. Fire-tube Boiler. Externally Fired, Return-tubular Type. 
 - In this country, where moderate pressures are wanted, the 
 common type of fire-tube boiler is the externally fired return- 
 tubular boiler. Figure 12 shows the construction of a boiler of 
 this type. It consists of a cylindrical shell, made of steel or 
 wrought-iron plates rolled into a cylindrical shape and riveted 
 together. The ends or heads are formed from flat circular plates 
 flanged around the outer edge and riveted to the cylindrical 
 shell. A large number of fire-tubes extend from one end-sheet 
 to the other. They occupy the lower two-thirds of the shell, 
 the top third being steam space. The flat plates or tube-sheets 
 tend to bulge outward with the internal pressure. To prevent 
 this, the part of the sheets above and below the level of the tubes 
 must be stayed. These stays are of two kinds, "through stays," 
 and "diagonal stays." The former are steel rods that run the 
 entire length of the shell, pierce the tube-sheets and hold the 
 sheets in by means of nuts. The latter run from each tube-sheet 
 diagonally back to the shell. In certain types of large boilers, 
 some of the tubes are made heavier and are threaded on the ends. 
 These tubes are secured to the end-sheets by means of nuts on 
 the outside. Such tubes are called stay-tubes. In general, the 
 tubes act as stays, and that part of the ends occupied by the tubes 
 needs little if any extra staying. The tubes are expanded into 
 the sheet and their ends are beaded over. 
 
 The feed-pipe enters the front end of the boiler just below the 
 water line, and the steam leaves by the dry-pipe, which leads 
 out of the top of the shell. The mud is blown off through an 
 outlet at the bottom near the rear. If the feedwater is taken 
 from a pond or stream and contains much vegetable matter, 
 there should be a surface blow-off to skim the scum that forms 
 on top of the water. A manhole is located at the top near the 
 rear and a hand-hole in front beneath the tubes. The grate is 
 put beneath the front end of the shell. The products of com- 
 bustion pass over the bridge wall, back along the bottom of the 
 shell, enter the tubes from the rear, pass through them and out 
 of the uptake at the front of the boiler or through a flue over 
 the top of the boiler to an uptake at the rear. 
 
32 
 
 ENGINES AND BOILERS 
 
 1f 
 
 r-J 
 
 
 IT 
 
 
 1 i! 
 
 
 
 
 i u t , 
 
 h 
 n 
 1 1 
 
 
 , 
 
 r 
 
 K 
 
 L 
 r 
 
 L. 
 
 r--jp 
 
 ri' ^ if 
 
 .-,- J J LH 
 
 : 
 
 1 i 
 i 
 i 
 
 -1- 
 
 :d 
 
 r 
 P-. 
 
 u 
 
 r 
 
 
 
 "Hi r 
 
 . r a'J tfc 
 
 ~ J 
 
 o 
 
 J f 
 i. 
 
 1 
 H 
 
 
 c ; 
 
 
 
BOILERS 
 
 The shell is supported by brackets which are riveted to the 
 shell and rest on the brickwork of the setting. The rear bearing 
 is fitted with rollers to allow the boiler to expand without crack- 
 ing the setting. 
 
 32. Fire-tube Boiler. Internally Fired, Return-tubular Type. 
 Instead of having the fire outside the shell, as in the preced- 
 ing boiler, the fire is sometimes placed inside one or more large 
 
 Jftrahe out/ft 
 
 ooooooooc 
 oooooooo 
 ooooooooooc 
 ooooooooo 
 ooooooooooc 
 oooooo 
 
 FIG. 13a 
 
 fire-flues running the whole length of boiler. Figure 13 shows a 
 Springfield boiler of this type. These large fire-flues are of course 
 subjected to external pressure, and therefore have a tendency to 
 collapse. In order to prevent this, they must be stiffened or 
 stayed in some way. This is ordinarily done by rolling them in 
 corrugations. If the flue is braced in such a manner that the 
 metal at any one point is very thick, there is danger of its being 
 overheated, since the gases are hottest in this combustion flue. 
 
 The fire is at the front of the flue. The gases pass back through 
 the flue to the rear of the boiler, into the combustion chamber. 
 The heating surface is mostly composed of the comparatively 
 thin flue and tubes. The thick outer shell is not subjected to 
 
34 
 
 ENGINES AND BOILERS 
 
 the high temperatures of the combustion chamber, as in the 
 externally fired boiler. 
 
 33. Fire-tube Boiler. Scotch Marine Type. While water- 
 tube boilers are used to some extent in marine service, the stand- 
 ard boiler is the Scotch marine type. This is very similar to the 
 internally fired boiler described in 32, which is also sometimes 
 called a Scotch marine boiler. It commonly has three combus- 
 
 Snsafji o/oen t* 
 
 & 
 
 ^ On/pifJ^TT^^^' ' 
 
 ta^X^VXK^VXVXV^V^ I Vi^S^> 
 
 FIG. 13b 
 
 tion flues, each of which has its own set of tubes. In marine 
 practice the combustion chamber at the rear of the flue and the 
 tubes is internal, there being a water-leg between the combustion 
 chamber and the rear head. There is a combustion chamber for 
 each flue and its set of tubes. Since the surfaces of the combus- 
 tion chamber are flat, they must be stayed. 
 
 These boilers are large in diameter; the outer shell must there- 
 fore be very thick. The longitudinal seams are usually triple 
 riveted, with two-strap butt joints. The Scotch marine boiler is 
 used to some extent on land, but as the space occupied is usually 
 an element of less importance here, the type is not common. 
 
BOILERS 
 
 35 
 
 34. Fire-tube Boiler. Vertical Type. A boiler often used 
 for small or portable plants is the vertical fire-tube type (Fig. 14). 
 These boilers are internally fired, the fire being enclosed in the 
 lower part of the shell, and surrounded by an annular water-ring 
 or water-leg. The lower tube- 
 sheet is placed but a small 
 
 distance above the grate. 
 Therefore the space for com- 
 bustion is very limited. The 
 tubes are vertical and are ex- 
 panded into the lower and the 
 upper tube-sheets. 
 
 ,/ connecfioas 
 
 35. Fire-tube Boiler. Loco- 
 motive Type. The type of 
 boiler used on locomotives, 
 and also often used on portable 
 plants, is shown in Fig. 15. 
 In this boiler, the fire-box is 
 at the rear end of the shell, 
 and its top and sides are water- 
 heating surfaces. 
 
 Since the sheets that form 
 the water-legs at the sides and 
 rear of the fire-box are flat, it 
 is necessary to stay them to 
 
 prevent distortion. A screw-stay is used for this purpose; it con- 
 sists of a threaded bolt screwed through the parallel plates. The 
 threads on the center part of these stay-bolts are removed so 
 that cracks will not start in the bolt at the root of the thread. 
 On what are called safety stays a small hole is drilled in from 
 the end so that a cracked bolt will leak steam and give warning. 
 
 The flat or arched sheet at the top of the fire-box is called the 
 crown-sheet. The crown-sheet is stayed in various ways, some- 
 times by radial stay-bolts which run between it and the outer 
 shell, or by sling stays, which are girders slung from the outer 
 shell. Fire-tubes extend from the tube-sheet at the front of the 
 fire-box to the tube-sheet at the front end of the boiler. 
 
 The tubes in locomotive boilers are smaller than in the types 
 previously described, and are placed as close together as good 
 
 FIG. 14 
 
36 
 
 ENGINES AND BOILERS 
 
BOILERS 37 
 
 circulation of the water will permit. By making the tubes small 
 and numerous, a large heating surface is obtained. Where a 
 superheater is used, as shown in Fig. 15, some of the tubes are 
 made larger and contain the superheating surface. This super- 
 heating surface is formed by tubes that extend into the fire-tubes 
 from the front end of the boiler and run to within a short dis- 
 tance of the fire-box. 
 
 The outer shell extends beyond the front tube-plate to form 
 a smoke-box. In this smoke-box vertical nozzles are located, 
 through which the exhaust steam from the engines escapes. This 
 induces a strong draft that allows a very rapid rate of combus- 
 tion. The rate of combustion often exceeds 100 pounds of coal 
 per square foot of grate surface per hour. 
 
 Since the steaming of this type of boiler is very rapid, the 
 steam is taken from a steam-dome located on the top of the 
 shell. This allows the steam to be taken at a distance from the 
 water surface, thereby insuring fairly dry steam. The throttle 
 valve for the engine is located in the dome. 
 
 In smaller locomotive boilers, the fire-box is set between the 
 rear drivers. In the larger sizes, this arrangement will not allow 
 a large enough grate area, and so the fire-box is extended later- 
 ally over low trailer wheels. Manholes and hand-holes are em- 
 ployed to give access for cleaning, as in other types of fire-tube 
 boilers. 
 
 36. Superheaters. During the past few years superheated 
 steam has come into quite general use, especially if it is to be 
 used in steam turbines. The amount of superheat used is gener- 
 ally not large, usually between 100 and 200 Fahrenheit. The 
 advantages gained by the use of superheated over saturated 
 steam will be considered later. 
 
 There are two types of superheater. One type is independ- 
 ently fired. The other is formed by the addition of some super- 
 heating surface to the main boiler. The latter is the more com- 
 mon form. In this type the steam is taken from the steam space 
 and led through superheating coils. Often provision is made for 
 the flooding of these coils during the period in which steam is 
 being raised, in order to prevent the coils from burning out. The 
 boiler shown in Fig. 8 has a common form of superheater at- 
 tached. 
 
38 ENGINES AND BOILERS 
 
 37. Horsepower of Boilers. As explained previously, boilers 
 are generally rated by the manufacturer on the amount of their 
 heating surface. The rate at which a boiler is working, how- 
 ever, must be determined from a consideration of the amount of 
 steam that is being generated. 
 
 The amount of heat necessary to evaporate a given quantity 
 of water varies with the temperature of the feedwater, with the 
 pressure at which the steam is formed, and with the quality of 
 the steam produced. Hence it is desirable that there be a stand- 
 ard of temperature and pressure at which we can find the equiv- 
 alent amount of water evaporated, using the same amount of 
 heat as is used under the actual conditions of temperature and 
 pressure. The conditions of temperature and pressure set by 
 the A. S. M. E. 1 as a standard are 212 F. and 14.7 pounds per 
 square inch absolute. The equivalent evaporation is then the 
 amount of water that would be evaporated from and at 212 F. 
 if the same amount of heat were used in its evaporation as is 
 used in the evaporation under the actual working conditions. 
 From the steam tables, the B.t.u. required to evaporate one 
 pound of water from and at 212 F. is seen to be 969.9 B.t.u. 
 This is the unit of evaporation. 
 
 At the time when it first became necessary to rate boilers, a 
 good engine used about 30 pounds of steam per horsepower per 
 hour at a pressure of 70 pounds gage. The judges at the Cen- 
 tennial Exposition in 1876 awarded prizes using the following 
 unit as a standard. A one-horsepower boiler is one that will evapo- 
 rate 30 pounds of water per hour from feedwater at 100 F. into 
 steam at 70 pounds pressure by gage. 
 
 The A. S. M. E. has since adopted an equivalent standard and 
 defines a boiler horsepower to be the evaporation of 34.5 pounds 
 of water per hour at 212 F. into steam at 212 F. and at a pressure 
 of 14.7 pounds absolute pressure. As the heat of vaporization 
 at 212 F. or 14.7 pounds absolute is 969.7 B.t.u., it therefore 
 takes 969.7X34.5 B.t.u. per hour for one boiler horsepower. 
 
 To determine the horsepower at which a boiler is working, we 
 must therefore first find how many B.t.u. are used to generate 
 one pound of steam under the given conditions of steam pressure 
 and temperature of feedwater. The number of pounds of water 
 evaporated per hour multiplied by the number of B.t.u. to gen- 
 
 iA. S. M. E. POWER TEST CODE, Edition of 1915, Table 4, 21. 
 
BOILERS 39 
 
 erate one pound of steam under the conditions will give the num- 
 ber of B.t.u. used by the boiler per hour. This product divided 
 by 969.7X34.5 will give us the horsepower of the boiler. 
 
 EXAMPLE. It is required to find the horsepower of a boiler working under 
 the following conditions: 
 
 Steam pressure = 115 pounds gage. 
 Temperature of feedwater = 65 F. 
 Quality of steam = 98% (i.e., 2% priming). 
 Water fed to boiler per hour = 3640 pounds. 
 SOLUTION. From the steam tables it is seen that 
 The heat of the liquid at 115 Ib. gage (129.7 Ib. abs.) = 318.4 B.t.u. 
 The heat of vaporization at 115 pounds gage =872.3 
 
 The heat of the liquid at 65 F. =33.1 B.t.u. The heat required to evapo- 
 rate one pound of water under the above conditions is 318. 4 + . 98X872. 3 
 33.1 = 1140 B.t.u., and the B.t.u. used per hour is 1140X3640 = 4150000. 
 Hence the horsepower of the boiler is 4150000/(34.5X969.7) = 124 h.p. 
 
 38. Factor of Evaporation. Since it takes 969.7 B.t.u. to 
 evaporate a pound of water from and at 212 F., and since it 
 takes more (1140 B.t.u. in the previous example) to evaporate 
 a pound of water under the actual conditions that exist in the 
 boiler, a certain ratio exists between these amounts. The factor 
 of evaporation is the ratio of the amount of heat required to evap- 
 orate a pound of water under actual conditions to the amount re- 
 quired to evaporate a pound from and at 212 F. In the previous 
 example, the factor of evaporation was 1140/969.7 = 1.176. If 
 the factor of evaporation is known, the equivalent evaporation is 
 found by multiplying the actual evaporation by this factor. 1 
 
 By this method, the heat used to raise the temperature of the 
 moisture in the steam from the temperature of the feed water to 
 that of the steam is not considered in computing the factor of 
 evaporation. In most cases the difference in results due to this 
 omission is very small. 
 
 39. Efficiency of Boilers. Usually speaking, the efficiency of 
 anything is the ratio of what is got out to what is put in ; output 
 and input being measured in like units. For boilers, the term 
 efficiency means the ratio of the number of B.t.u. in the steam 
 generated to the number of B.t.u. available in the coal fired. Boiler 
 efficiency is usually expressed in percent. 
 
 1 In the A. S. M. E. POWER TEST CODE the "Mean B.t.u." and steam tables by MARKS 
 and DAVIS are used, thereby giving 970.4 B.t.u. instead of 969.7 B.t.u. as used above for heat 
 required to evaporate a pound of water from and at 212 F. See POWER TEST CODE, Edition 
 of 1915, pp. 28 and 47. 
 
40 ENGINES AND BOILERS 
 
 The fact that the combined efficiency of a boiler, furnace, and 
 grate is not 100% is due to several losses. These losses are due 
 to the following causes. 
 
 (1) A part of the fuel may drop through the grate and be lost 
 in the ash. 
 
 (2) Heat is lost up the stack. There are several sources of this 
 loss, and to them is due the greatest loss in efficiency. First, 
 unburned particles of solid fuel are often carried from the fur- 
 nace. The amount depends upon the draft and the kind of fuel. 
 In locomotives, with their high draft and with a fine fuel, this 
 loss may be considerable. Second, there is loss due to the un- 
 burned or partially burned hydrocarbons. Black smoke is caused 
 by the incomplete burning of some of the hydrocarbons. Third, 
 heat is carried away by the excess air and the inert nitrogen 
 which have been heated, and by the hot products of combustion. 
 Fourth, heat is required to evaporate and to superheat the 
 moisture in the fuel and in the air. Fifth, there may be loss 
 due to the burning of the carbon to carbon monoxide instead of 
 to carbon dioxide. 
 
 (3) Heat is lost by radiation from the furnace and from the 
 boiler. 
 
 It is very difficult to separate all these losses and the attempt 
 is seldom made. It must be remembered that what is often 
 called boiler efficiency is really the combined efficiency of grate, 
 furnace, and boiler. 
 
 Under the most favorable conditions, using coal as a fuel, 
 efficiencies of over 80% have been attained. Under ordinary 
 conditions of operation, efficiencies vary from 80% to less than 
 50%. The efficiency may sometimes exceed 80% when underfeed 
 stokers, described later, are used. When oil is used as a fuel, 
 higher efficiencies may be attained, due in part to the better mix- 
 ing of the air and the fuel. 
 
 EXAMPLE. It is required to find the combined efficiency of a boiler, fur- 
 nace, and grate, working under the following conditions: 
 
 Steam pressure = 127 pounds gage. 
 
 Superheat = 190 F. 
 
 Temperature of feedwater = 180 F. 
 
 Water fed to boiler per hour = 8750 pounds. 
 
 Coal fired per hour = 1 160 pounds. 
 
 B.t.u. per pound of coal as fired = 11540 B.t.u. 
 
BOILERS 41 
 
 SOLUTION. The B.t.u. required to generate one pound of steam under 
 the above conditions is seen to be 
 
 325.4+866.8 - 148+.55 X 190 = 1148.7 B.t.u. 
 
 The total B.t.u. used in the generation of steam per hour then is 8750 X 1148.7 = 
 10051000 B.t.u. The total B.t.u. in coal fired per hour is 1160X11540 = 
 13386000 B.t.u. Hence the efficiency is 10051000/13386000 = .752 or 75.2%. 
 
 40. A. S. M. E. Boiler Test Code. 1 In reporting the results 
 of a steam-boiler test it is well to put them in the form prescribed 
 by the A. S. M. E. This form is as follows. 
 
 DATA AND RESULTS OF EVAPORATIVE TEST 
 CODE OF 1915 
 
 (1) Test of boiler located. 
 
 To determine 
 
 Test conducted by 
 
 DIMENSIONS 
 
 (2) Number and kind of boilers 
 
 (3) Kind of furnace 
 
 (4) Grate surface (width length ) sq. ft. 
 
 (a) Approximate width of air openings in grate in. 
 
 (6) Percentage of area of air openings to grate surface per cent 
 
 (5) Water heating surface sq. ft. 
 
 (6) Superheating surface sq. f t. 
 
 (7) Total heating surface sq. f t. 
 
 (a) Ratio of water heating surface to grate surface 
 
 (6) Ratio of total heating surface to grate surface 
 
 (c) Ratio of minimum draft area to grate surface 
 
 (d) Volume of combustion space between grate and heating surface 
 
 cu. ft. 
 
 (e) Distance from center of grate to nearest heating surface ft. 
 
 DATE, DURATION, ETC. 
 
 (8) Date 
 
 (9) Duration hr. 
 
 (10) Kind and size of coal 
 
 AVERAGE PRESSURES, TEMPERATURES, ETC. 
 
 (11) Steam pressure by gage Ib. per sq. in. 
 
 (a) Barometric pressure in. of mercury 
 
 (12) Temperature of steam, if superheated deg. 
 
 (a) Normal temperature of saturated steam deg. 
 
 (13) Temperature of feedwater entering boiler deg. 
 
 (a) Temperature of feedwater entering economizer deg. 
 
 (6) Increase of temperature of water due to economizer deg. 
 
 i A. S. M. E. POWER TEST CODE, Edition of 1915, p. 51. 
 
42 ENGINES AND BOILERS 
 
 (14) Temperature of escaping gases leaving boiler deg. 
 
 (a) Temperature of gases leaving economizer deg. 
 
 (6) Decrease of temperature of gases due to economizer deg. 
 
 (c) Temperature of furnace deg. 
 
 (15) Force of draft between damper and boiler in. of water 
 
 (a) Draft in main flue near boiler in. of water 
 
 (6) Draft in flue between economizer and chimney in. of water 
 
 (c) Draft in furnace in. of water 
 
 (d) Draft or blast in ash-pit in. of water 
 
 (16) State of weather 
 
 (a) Temperature of external air deg. 
 
 (6) Temperature of air entering ash-pit deg. 
 
 (c) Relative humidity of air entering ash-pit per cent 
 
 QUALITY OF STEAM 
 
 (17) Percentage of moisture in steam or number of degrees of superheating 
 
 per cent or deg. 
 
 (18) Factor of correction for quality of steam 
 
 TOTAL QUANTITIES 
 
 (19) Total weight of coal as fired Ib. 
 
 C 20) Percentage of moisture in coal as fired per cent 
 
 (21) Total weight of dry coal (Item 19X 
 
 (22) Ash, clinkers, and refuse (dry) 
 
 (a) Withdrawn from furnace and ash-pit Ib. 
 
 (6) Withdrawn from tubes, flues and combustion chamber Ib. 
 
 (c) Blown away with gases Ib. 
 
 (d} Total Ib. 
 
 (e) Weight of clinkers contained in total ash Ib. 
 
 (23) Total combustible burned (Item 21 Item 22d) Ib. 
 
 (24) Percentage of ash and refuse based on dry coal per cent 
 
 (25) Total weight of water fed to boiler Ib. 
 
 (26) Total water evaporated, corrected for quality of steam (Item 25 X Item 
 
 18) Ib. 
 
 (27) Factor of evaporation based on temperature of water entering boiler. . . . 
 
 (28) Total equivalent evaporation from and at 212 degrees (Item 26Xltem 
 
 27) Ib. 
 
 HOURLY QUANTITIES AND RATES 
 
 (29) Dry coal per hour Ib. 
 
 (30) Dry coal per square foot of grate surface per hour Ib. 
 
 (31) Water evaporated per hour, corrected for quality of steam Ib. 
 
 (32) Equivalent evaporation per hour from and at 212 Ib. 
 
 (33) Equivalent evaporation per hour from and at 212 and per square foot 
 
 of water heating surface Ib. 
 
 CAPACITY 
 
 (34) Evaporation per hour from and at 212 (Same as Item 32) Ib. 
 
 (a) Boiler horsepower developed (Item 34-5-34^) bl.-h.p. 
 
BOILERS 43 
 
 (35) Rated capacity per hour, from and at 212 ........................ lb. 
 
 (a) Rated boiler horsepower .............................. bl.-h.p. 
 
 (36) Percentage of rated capacity developed ...................... per cent 
 
 ECONOMY 
 
 (37) Water fed per pound of coal as fired (Item 25-r-Item 19) ........... lb. 
 
 (38) Water evaporated per pound of dry coal (Item 26 -^ Item 21) ........ lb. 
 
 (39) Equivalent evaporation from and at 212 per pound of coal as fired 
 
 (Item 28 4- Item 19) .......................................... lb. 
 
 (40) Equivalent evaporation from and at 212 per pound of dry coal (Item 
 
 28^- Item 21) ............................................... lb. 
 
 (41) Equivalent evaporation from and at 212 per pound of combustible 
 
 (Item 28 -f- Item 23) .......................................... lb. 
 
 EFFICIENCY 
 
 (42) Calorific value of 1 pound of dry coal by calorimeter ............ B.t.u. 
 
 (a) Calorific value of 1 pound of dry coal by analysis ......... B.t.u. 
 
 (43) Calorific value of 1 pound of combustible by calorimeter ......... B.t.u. 
 
 (a) Calorific value of 1 pound of combustible by analysis ...... B.t.u. 
 
 (44) Efficiency of boiler, furnace and grate 
 
 / Item40X970.4\ 
 
 ( 100X -TtoZlar-) ................ percent 
 
 (45) Efficiency based on combustible 
 
 / in Item4lX970.4\ 
 
 ( 100X - Item 43 J ............... P6F C6nt 
 
 COST OF EVAPORATION 
 
 (46) Cost of coal per ton of ...... pounds delivered in boiler room ......... 
 
 ................ dollars 
 
 (47) Cost of coal required for evaporating 1000 pounds of water under ob- 
 
 served conditions ......................................... dollars 
 
 (48) Cost of coal required for evaporating 1000 pounds of water from and 
 
 at 212 .................................................... dollars 
 
 SMOKE DATA 
 
 (49) Percentage of smoke as observed ............................ per cent 
 
 (a) Weight of soot per hour obtained from smoke meter ..... per cent 
 
 FIRING DATA 
 
 (50) Kind of firing, whether spreading, alternate or coking ................ 
 
 (a) Average thickness of fire .................................. in. 
 
 (6) Average intervals between firings for each furnace during time 
 when fires are in normal condition ...................... min. 
 
 (c) Average interval between times of leveling or breaking up ....... 
 
 . . min. 
 
44 
 
 ENGINES AND BOILERS 
 
 (51) Analysis of dry gases by volume 
 
 (a) Carbon dioxide (CCh) per cent 
 
 (b) Oxygen (O) per cent 
 
 (c) Carbon monoxide (CO) per cent 
 
 (d) Hydrogen and hydrocarbons per cent 
 
 (e) Nitrogen, by difference (N) per cent 
 
 (52) Proximate analysis of coal 
 
 As fired Dry coal Combustible 
 
 (a) Moisture 
 
 (6) Volatile matter 
 
 (c) Fixed carbon. ... 
 
 (d) Ash 
 
 100 per cent 100 per cent 100 per cent 
 
 (e) Sulphur, separately determined referred to dry coal per cent 
 
 (53) Ultimate analysis of dry coal 
 
 (a) Carbon (C) per cent 
 
 (b) Hydrogen (H) per cent 
 
 (c) Oxygen (O) per cent 
 
 (d) Nitrogen (N) per cent 
 
 (e) Sulphur (S) per cent 
 
 (/) Ash per cent 
 
 100 per cent 
 
 (54) Analysis of ash and refuse, etc. 
 
 (a) Volatile matter per cent 
 
 (6) Carbon per cent 
 
 (c) Earthy matter per cent 
 
 100 per cent 
 (d} Sulphur, separately determined per cent 
 
 (d) Fusing temperature of ash deg. 
 
 (55) Heat balance based on dry coal . 
 
 Dry Coal 
 
 B.t.u. 
 
 Percent 
 
 (a) Heat absorbed by the boiler (Item 40X970.4) . . . 
 (6) Loss due to evaporation of moisture in coal 
 
 (c) Loss due to heat carried away by steam formed 
 
 by the burning of hydrogen 
 
 (d) Loss due to heat carried away in the dry flue gases 
 
 (e) Loss due to carbon monoxide 
 
 OLoss due to combustible in ash and refuse 
 i Loss due to heating moisture in air 
 
 (h) Loss due to unconsumed hydrogen and hydrocar- 
 bons, to radiation and unaccounted for . . 
 
 (i) Total calorific value of 1 pound of dry coal 
 (Item 42) 
 
 100 
 
CHAPTER V 
 BOILER ACCESSORIES AND AUXILIARIES 
 
 41. Grates. Grates are used to support the fuel in a furnace. 
 Most grates are made of cast iron, which is cheap and less liable 
 than other convenient materials to be distorted or twisted under 
 the high temperatures to which it is subjected. The grate must 
 be strong enough to support the load placed upon it, and it must 
 be of such a form that sections can easily be replaced when broken 
 or burned out. It must have sufficient opening for the admis- 
 sion of air to the fuel. The openings or air spaces depend upon 
 the kind of fuel used. The combined area of the openings will 
 usually be from 30 to 50 percent of the total area. 
 
 The area of the grate depends upon the amount of coal to be 
 burned and the rate of combustion. Under natural or chimney 
 draft, from 10 to 25 pounds of coal can be burned per square 
 foot of grate surface per hour. Under forced draft, from 40 to 
 130 pounds of coal may be burned per hour. If hand firing is 
 employed, the grate must not be longer than the distance the 
 fireman can throw the coal accurately (six or seven feet) . Depend- 
 ing upon the fuel, draft, and economy of the boiler, the equivalent 
 evaporation per pound of coal will vary from 5 to 12. 
 
 Various forms of grates are used. For hand firing, plain grates 
 and shaking or dumping grates are used. The plain grate is 
 harder to keep clean than a dumping grate. Moreover, it is 
 necessary to keep the fire-doors open while the cleaning is in 
 process. The grates used in mechanical stokers are of various 
 types; some are stationary, others traveling and rocking. Occa- 
 sionally grates are water-cooled, to prevent their burning out. 
 Since this water is led to the boiler after becoming heated in the 
 grate, the boiler capacity is increased, but in most cases the extra 
 care and cost are prohibitive. 
 
 42. The Plain Grate. The grate bars shown in Figs. 16 and 
 16a are of the stationary type. These grates are cast in small 
 sections so that a section may be easily and quickly replaced 
 when it is burned out. The size of the openings in the bars is 
 governed by the size and kind of coal that is to be burned. If 
 
 45 
 
46 
 
 ENGINES AND BOILERS 
 
 anthracite coal is used, the openings are small. If the coal is 
 bituminous, and if it cakes, the openings should be made large. 
 
 43. The Rocking Grate. A form of rocking grate is shown in 
 Fig. 17. The bars are supported on pivots, and are dumped or 
 rocked by means of a lever from the front of the furnace. Only the 
 largest clinker need be removed from the top, since the rocking 
 action of the bars breaks up most of the clinker that is formed. 
 In case a strong draft is used, as in the locomotive, this type of 
 grate is usually used in order to keep a clean fire, such as is required 
 with a high rate of combustion. 
 
 44. Mechanical Stokers. The first cost of a mechanical 
 stoker is greater than the equipment for hand firing, but it 
 
 Herat/on \ g 
 
 cfioi? at 4-3 ' 
 
 FIG. 16 
 
 FIG. 16a 
 
 tr rr 
 
 requires less labor and attendance in its operation. A cheaper 
 grade of fuel can be used, a higher efficiency attained, and less 
 smoke is formed than is usual with hand firing. In a fair-sized 
 or large plant, it is usually better economy to use some form of 
 mechanical stoker. There are many forms of stokers in use. 
 
 45. The Chain Grate Stoker. Where a low-grade fuel is 
 used, as is often the case in the middle west and in the central 
 states, the chain grate (Fig. 18) is extensively used. The grate is 
 composed of a large number of short links, forming an endless 
 chain. This chain runs over front and rear sprockets. Power is 
 used to drive one of these sprockets, causing the whole chain 
 to revolve slowly at a speech which is regulated by a suitable 
 mechanism. The whole grate is mounted on wheels so that it can 
 be run out in the open for repairing and cleaning. 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 47 
 
 The coal is fed to the front of the grate from a hopper which 
 extends across the entire width of the grate. At the rear of the 
 hopper there is a plate lined with firebrick that may be raised 
 or lowered, thus regulating the depth of fuel-bed. The volatile 
 matter in the fuel is distilled off as the coal first enters the fur- 
 nace. These volatile products pass back over the part of the 
 fire where the fixed carbon is burning, and are given a chance to 
 burn there. By the time the fuel-bed has reached the rear of 
 the furnace the combustion should be complete. The ash and 
 clinker are dropped off to the ash-pit at the rear. 
 
 STirry. ca- t "' o. : 'eg' .-ara>o o ^-^^L 
 
 '6'/l'6 ^0 A d^ "tffiuLllAJiH h a <iA' ' A'M rc'-'MV^AS^^ 
 
 FIG. 18 
 
 The front part of the grate is overhung by a firebrick arch. 
 This allows sufficient time and temperature for complete com- 
 bustion before the gases strike the heating surface of the boiler. 
 
 Incomplete combustion is apt to occur with a chain grate if 
 the fire is forced very hard. Excess air is likely to leak in if the 
 fuel-bed becomes too thin. This causes a drop in the tempera- 
 ture of the combustion chamber and therefore poor combustion. 
 
 Under a light load, the fuel is often burned before it reaches 
 the rear of the grate. Air is likely to leak through the ash, 
 causing poor economy. As a remedy for this condition, a con- 
 trivance similar to a damper is sometimes placed under the rear 
 portion of the grate. This makes it possible to shut off the air 
 supply from this part of the grate. 
 
48 
 
 ENGINES AND BOILERS 
 
 46. The Roney Stoker. The inclined grate stoker is one in 
 which the coal is fed from a hopper at the top, the coal burning 
 
 on its way down across the sloping grate. In the forms custom- 
 arily used, the grates are operated mechanically. There are two 
 classes of these grates, side-feed and front-feed. 
 
BOILER ACCESSORIES AND AUXILIARIES 49 
 
 Figure 19 shows the Roney type of front-feed stoker. The 
 coal is fed into the hopper, usually by gravity from bins above. 
 A reciprocating pusher forces the coal from the hopper onto a 
 dead plate beneath the front of the arch, where the distillation 
 starts. From this plate, it is made to move downward by the 
 motion of the grates. By the time the fuel reaches the ash plate 
 at the bottom of the incline the combustion is complete. The 
 ash is dumped into the pit below from time to time by means of 
 a hand-lever that is operated from the front of the furnace. The 
 grates are rocked by means of an eccentric placed on a rotating 
 shaft running horizontally along the front of the whole battery 
 of boilers. The amount the grates are rocked, and the amount 
 of coal fed, are under the control of the fireman. 
 
 Since the distilled products are driven off at the front of the 
 firebrick arch, they have time, and are at such a temperature, 
 due to the fire below, that complete combustion takes place. In 
 some cases, steam and air are admitted under the front of the 
 arch to aid in the combustion. The length of arch varies with 
 the grade of fuel to be used, and with the kind of boiler under 
 which the stoker is installed. In some cases it covers the entire 
 grate, forming a Dutch oven which sits out in front of the rest 
 of the boiler setting. 
 
 47. The Underfed Furnace. In the types of stokers previ- 
 ously described, the volatile matter is distilled and burnt over 
 the bed of burning fixed carbon. As the feeding of fuel is uniform 
 the amount of gas given off at any one time is not so great as in 
 hand firing. Hence combustion has a chance at all times to be 
 more nearly complete. Another and radically different method 
 is to feed the green coal from beneath, blowing the volatilized 
 matter along with sufficient air up through the hot fuel-bed above, 
 where complete combustion takes place. 
 
 Figure 20 shows such a stoker. The coal is fed into a hopper 
 and is forced back under the fuel-bed into retorts, by means of a 
 ram or plunger. Air under pressure is forced in through tuyeres 
 at the distillation zone, and by the time the gases pass through 
 the hot fire of fixed carbon and reach the top of the fire, they 
 are completely burned. This type requires a forced draft. The 
 refuse is forced back and down onto the dump plates at the rear 
 of the wind-box, and is dropped from there into the ash-pit below 
 through an adjustable opening. 
 
50 
 
 ENGINES AND BOILERS 
 
BOILER ACCESSORIES AND AUXILIARIES 51 
 
 Since the temperature of the fire is very high, most of the ash 
 is fused. In order to prevent clogging it is sometimes necessary 
 to have a water-cooled bridge wall. 
 
 Due to the forced draft, a plant thus equipped is not subject 
 to the variations due to changing weather conditions. The rate 
 of combustion is regulated by the amount of coal fed and the 
 amount of air blown in, which are controlled together. The under- 
 feed type of stoker therefore is more flexible and will give higher 
 efficiency under conditions of forced load than those previously 
 described. 
 
 48. Smoke Prevention. Soft coal is generally considered to 
 be smoky. Nevertheless, it is possible to burn practically all 
 grades of bituminous coal with very little smoke. Only during 
 the past few years has there been any very determined effort to 
 rid ourselves of the smoke nuisance. Several of our larger cities 
 have ordinances which are enforced more or less rigidly against 
 the excessive emission of black smoke by power plants. 
 
 The soot, which is the solid and black part of the smoke, dis- 
 figures buildings and may even injure health by keeping out the 
 sunlight and by clogging up the respiratory organs. It is fre- 
 quently stated that a great amount of fuel goes to waste in the 
 soot of the smoke. While the soot may be a nuisance, yet it 
 represents in itself but little heat loss. Soot indicates, however, 
 incomplete combustion, which often means that there is a large 
 amount of unburned hydrocarbon and probably some CO that 
 should be burned to C02- Smoke prevention, in many cases, 
 results in an increased economy of the power plant. Thus we 
 often find instances of plants that have installed modern equip- 
 ment which prevents the formation of smoke, not so much with 
 the idea of eliminating the smoke as to obtain better efficiency 
 by means of proper combustion. 
 
 Let us consider in a general way the causes of smoke produc- 
 tion. Bituminous coal, upon being heated to moderate tempera- 
 tures (600 to 1000 F.), will have certain hydrocarbons driven 
 from it in a volatile state. This volatile matter will burn when 
 mixed with a sufficient amount of air and raised to a sufficiently 
 high temperature (1800 to 2000 F.), forming carbon dioxide 
 and water. If for any reason there is an insufficient supply of 
 oxygen, or if the hydrocarbons are not raised to a sufficiently high 
 temperature, incomplete combustion will follow, and black smoke 
 
52 ENGINES AND BOILERS 
 
 may result. The fixed carbon left in the coal after the volatile 
 hydrocarbons have been driven off, with the addition of sufficient 
 air, will burn to carbon dioxide. If there is a lack of air, carbon 
 monoxide, or a mixture of carbon monoxide and carbon dioxide, 
 will result. 
 
 In conclusion, to burn bituminous coal smokelessly, a furnace 
 must have a sufficient supply of air to insure the complete com- 
 bustion of the volatile matter, and it must have a temperature 
 high enough to permit of this combustion. In the ordinary fur- 
 nace the time taken for the gases to pass from the grate to the 
 comparatively cool heating surface of the boiler, where they are 
 rapidly cooled, is quite small, perhaps less than a second. At 
 least, not enough time is allowed for the volatile matter to unite 
 properly with the oxygen of the air, and black smoke is the result. 
 If the path of the hot gases can be made longer, thus giving them 
 time to burn, a large reduction can be made in the amount of smoke. 
 It is sometimes possible to rearrange the baffling in the path of 
 the gases in such a way that this is accomplished easily. Another 
 way to lengthen the time of burning is to move the grates out 
 from under the boiler and place a long firebrick arch over the fire. 
 
 In ordinary hand firing, a large quantity of cold coal is thrown 
 on top of the fire, with the result that the fire is greatly cooled, 
 both to heat up the coal and also to cause distillation of the 
 volatile matter. This reduces the temperature to a point at 
 which the complete combustion of the volatile matter will not 
 take place, and smoke results. At the time the volatile matter 
 is given off an excess of air is needed to burn it. If this air is 
 let in over the top of the fire it will still further cool the fire, 
 which only adds to the trouble. 
 
 The use of the various over-feed stokers, such as the chain 
 grate, and those with the front or side feed, is a decided improve- 
 ment over hand firing because the fresh coal is added continu- 
 ously, and the air supply can be properly adjusted and main- 
 tained. In these types of stokers, the fresh coal, upon coming 
 to the furnace, passes through the distillation period in such a 
 position that the volatile products must pass over the fire of fixed 
 carbon and be burnt there. 
 
 In the underfeed type of stoker, the fresh coal is forced in from 
 the under side of the fire, and the distilled products along with 
 sufficient air to burn them, are forced to pass through the hot 
 
BOILER ACCESSORIES AND AUXILIARIES 53 
 
 bed of burning carbon above, with the result that a sufficiently 
 high temperature is maintained to allow for their complete com- 
 bustion. 
 
 The purpose of the down-draft furnace is much the same as 
 that of the underfeed stoker. In this type, the zones of distill- 
 ation and of burning the fixed carbon are separated. The first 
 takes place on the upper grate and the second on the lower; the 
 distilled product passes over the hot fuel bed on the lower grate 
 and complete combustion occurs. 
 
 Many devices to prevent smoke are on the market. Most of 
 them consist of some form of steam jet that carries in and mixes 
 a sufficient amount of air with the volatilized hydrocarbons to 
 effect complete combustion. The steam itself has no power to 
 prevent smoke. It is used simply to carry the air and to mix 
 it with the volatile products. If the steam jet is left on too long 
 after the period of distillation, a loss greater than the gain 
 effected by the jets may result. Some makers use a dash-pot or 
 other arrangement that automatically shuts the steam off soon 
 after each firing. 
 
 49. Settings. The brickwork that surrounds a boiler is called 
 a setting. The outer side of this setting is built of common red 
 brick. The inner surfaces that are exposed to the high tempera- 
 ture of the flame are lined with firebrick. With the very high 
 temperatures that exist in modern furnaces, it is difficult to get 
 a grade of firebrick that will give satisfactory service. It is better 
 practice not to leave an air space between the outer wall and the 
 lining, since heat is transmitted through the air space, under the 
 high temperatures that exist in a furnace, faster than it would 
 be through the same thickness of brick. 
 
 In most furnaces, a firebrick arch is placed over the fire. This 
 arch forms a chamber in which the temperature is kept very high. 
 The length of this arch varies with the kind of fuel to be used 
 and with the type of boiler. Firebrick baffles are placed between 
 the tubes of water tube boilers in such a manner that the gases 
 are forced to pass the heating surface several times on their way 
 to the stack. The burnt gases pass from the setting to the stack 
 through a duct called the breeching. 
 
 Since there is a difference in pressure between the outside and 
 inside of the setting, it is important that there be no cracks for 
 the air to leak in or for the gases to leak out. Under natural 
 
54 ENGINES AND BOILERS 
 
 draft, there is a leakage of air inward, which cools the boiler 
 and injures the draft. With a forced draft, the gases may leak 
 out into the boiler room. 
 
 50. Draft. Natural draft is obtained by means of a stack or 
 chimney. The gases as they leave the boiler are at a tempera- 
 ture of from 400 to 600 F. At this temperature they are much 
 lighter than the outside air. Since the column of gas in the stack 
 is lighter, it is forced up from the bottom by the heavier air 
 outside. The stack should be large enough so that but little 
 draft will be lost by the friction between the gas and the stack. 
 It should be insulated so that little heat is lost through the walls 
 of the stack. 
 
 There are three kinds of stacks in use, steel, brick, and con- 
 crete. The steel stack is cheaper and lighter, but it is expensive 
 in its upkeep, since it must be painted often to prevent the 
 corroding of the plates. In the better grades of steel stacks, a 
 firebrick lining is used at least a part of the way up to prevent 
 conduction of heat to the outside. Brick stacks are sometimes 
 built of hard common brick, but of late years more often of 
 special radial brick. They are sometimes lined with firebrick, 
 as in the steel stack. Reinforced concrete stacks have come into 
 use during the past few years. When properly put up, they give 
 good service. 
 
 Brick and concrete stacks must be heavy enough to resist the 
 overturning effort of the wind. Steel stacks are either anchored 
 and designed to withstand the bending action due to the wind, 
 or else they are supported by guys. 
 
 Where forced draft is used, the stack need be only high enough 
 to discharge its smoke above the surrounding buildings. Forced 
 draft is obtained by means of fans or blowers which force the 
 air into the ash-pit or wind-box and thence through the fire. 
 In locomotives, the forced draft is obtained by means of nozzles 
 through which the exhaust steam from the engines is discharged 
 into the chimney. A draft caused by this method is sometimes 
 called induced draft. 
 
 The amount of draft is measured in inches of water. Under 
 natural draft it will increase in going from the ash-pit to the stack 
 and at the base of the stack it will be from 0.5 to 1.5 inches. 
 Under forced draft the pressure in the ash-pit is greatest, and will 
 vary from 1 to 5 inches. 
 
BOILER ACCESSORIES AND AUXILIARIES 55 
 
 51. Dampers. A damper should be interposed between each 
 furnace and the stack. The efficient operation of the furnace 
 necessitates careful attention to the damper. Automatic damper 
 regulators are in use, but for the best results they should be sup- 
 plemented by intelligent manual control. 
 
 52. Safety Devices. There are in general three causes of 
 explosions of properly designed boilers: a weakened part, high 
 pressure, and low water. The first is due to the corroding or 
 wearing away of some part of the structure, or to a local over- 
 heating due to an accumulation of sediment or scale. It may 
 be due to an undetected flaw in the materials entering into the 
 makeup of the boiler, or it may be due to carelessness or poor 
 workmanship during construction. 
 
 The second cause, high pressure, is due to a pressure much in 
 excess of that for which the boiler was designed. This may be 
 due to a faulty safety valve, or to the ignorance of a fireman. 
 
 The third cause, low water, allows some of the parts to get 
 overheated and therefore much weakened. It may exist unknown 
 to the fireman on account of foaming, which is liable to cause an 
 untrue indication of the water level in the gage glass, or on ac- 
 count of some stoppage in the connection to the glass. 
 
 To safeguard against accidents due to a weak part, it is neces- 
 sary to have a thorough inspection both of materials entering into 
 construction of the boiler and of the workmanship during con- 
 struction. There also should be frequent inspection after the 
 boiler is put into service. The common test for strength is hydro- 
 static. Before being put into service a boiler should have water 
 pumped into it, and a pressure should be reached much in excess 
 of the working pressure. 
 
 53. The Pressure Gage. The pressure that exists in a boiler 
 is measured by a steam gage. In this country, the dial of the 
 steam gage is graduated to read in pounds per square inch. The 
 gage almost universally used is known as the Bourdon gage. 
 Figure 21 shows its internal construction. The pressure is ad- 
 mitted to a curved flattened tube which is closed at its free end. 
 This internal pressure tends to make the curved tube straighten 
 out. The free end is connected to the needle by means of levers, 
 a rack, and a pinion. Any movement of the free end causes the 
 hand or needle to turn, and the pressure causing the movement 
 is indicated on the properly graduated dial. The flattened tube 
 
56 
 
 ENGINES AND BOILERS 
 
 is made of brass or steel. Since a change in the temperature of 
 the tube would cause an error in the reading of the gage, it should 
 be connected to the boiler or steam-pipe by means of a siphon 
 so that steam may never enter the gage. On locomotives, where 
 the gage is subject to continual and severe jarring, two stiff er 
 tubes are used in place of the one shown in the figure. The better 
 grades of gages have a light hairspring to take up the backlash 
 in the levers and gears. 
 
 A gage similar to the one shown in Fig. 21 is often used to 
 indicate vacuum. For a vacuum, the tube is bent still more and 
 
 the levers are so arranged that 
 the motion of the needle is re- 
 versed from that of the one shown 
 in Fig. 21. The dials of vacuum 
 gages are commonly graduated to 
 read in inches of mercury. Where 
 pressures are had that may fluctu- 
 ate from a vacuum to a positive 
 pressure, gages are used that will 
 indicate either the vacuum or the 
 pressure above the atmosphere. 
 Gages should be tested from time 
 to time to see that they give the 
 correct pressure reading. 
 54. The Safety Valve. The purpose of a safety valve on a 
 boiler is to prevent an undue or dangerous pressure. It is im- 
 possible in an ordinary furnace to regulate the combustion quickly 
 enough to correspond to sudden changes of the amount of steam 
 used. For instance, a boiler may be furnishing its maximum 
 amount of steam, when for some reason the engine is shut down 
 without warning, and therefore before the fire can be deadened. 
 As a result, the rapid formation of steam will continue long 
 enough to cause an excessive boiler pressure if the safety valve 
 does not give relief. Hence the safety valve should have such a 
 capacity that it is capable of discharging all the steam that the 
 boiler can generate without allowing the pressure to become 
 dangerous. Furthermore the safety valve must be absolutely 
 reliable in its action, and it should be so constructed and placed 
 on the boiler that it cannot be put out of action through careless- 
 ness or ignorance. No stop valve should be placed between it 
 
 FIG. 21 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 57 
 
 and the boiler. Many explosions have been caused by the failure 
 of the safety valve to operate. As far as the writer knows, how- 
 ever, none have occurred that were due entirely to excessive 
 pressure when the valve was in action. Several types of safety 
 valve have been used in the past, but with the pressure ordi- 
 narily carried in this country, the use of the pop type has become 
 almost universal, and will be the only one described here. 
 
 Figure 22 shows in section a pop safety valve. Most safety valves 
 are made with a 45 seat. The valve is held on the seat by a 
 helical spring. When the steam pressure becomes sufficient to 
 overcome the force of the spring, the valve is raised enough to al- 
 low some steam to escape. This steam passes into a huddling 
 chamber. The area upon which the steam now acts is slightly 
 greater than before the valve opened, with the result that the spring 
 is compressed suddenly to a greater extent than if the steam acted 
 only upon the original area. Escape of steam will continue until 
 the pressure has dropped to a few pounds less than that at which 
 it opened. When the valve stops blowing, it seats firmly. Since 
 the pressure is less than that at which it opened, it will remain 
 shut until the steam pressure 
 again reaches the popping point. 
 The valve should be constructed 
 and set so that the difference be- 
 tween the popping pressure and 
 the closing pressure or Slowdown 
 is not too large, in order to pre- 
 vent shock to the boiler and an 
 excessive loss of steam during 
 ordinary operation. 
 
 A lever is provided at the top 
 of the casing for locking the 
 valve open. The compression in 
 the spring may be adjusted by 
 screwing the top cap up or down. 
 In most valves the spring is en- 
 cased so as to protect it from 
 the escaping steam, and to pre- 
 vent back pressure in the dis- 
 charge pipe from acting on the 
 top of the valve. (See Fig. 22.) FIG. 22 
 
58 ENGINES AND BOILERS 
 
 55. Safety-valve Capacity. The amount of steam that a 
 safety valve discharges depends upon the steam pressure and upon 
 the effective opening. The latter varies with the lift of the valve. 
 Not all valves of the same diameter have the same lift; hence 
 they differ in capacity. There has been considerable agitation 
 recently to have all pop valves put upon a uniform rating. Tests 
 have been made to determine the discharge and the lift under 
 various conditions of pressure. These tests show that the com- 
 monly used empirical formula given by Napier is substantially 
 correct when applied to the safety valve. 
 
 56. Napier's Formula. Napier's formula for steam issuing 
 from an orifice into the atmosphere is 
 
 W- A ' P 
 
 "W 
 
 in which W is the weight in pounds of steam issuing per second, 
 A is the area of the orifice in square inches, and P is the abso- 
 lute pressure in pounds per square inch in front of the orifice. 
 
 Applying this formula to the safety valve with a 45 seat, it 
 is seen that the area oi opening, A, equals approximately the 
 product of irD and the lift times the sine of 45, where D is the 
 diameter of the valve in inches. If the lift is known, the dis- 
 charge may be calculated. Some valve makers use the assump- 
 tion that the lift is 1/30 of the diameter, and rate their valves 
 accordingly. Under this assumption it is seen that 
 
 7rD 2 X.707xP 
 
 W = 
 
 70X30 
 
 and the weight of steam discharged per hour is 3600 W = 3.81 PD 2 . 
 As previously explained, the safety valve must be large enough 
 to discharge the maximum amount of steam the boiler is capable 
 of generating. We can compute this maximum amount from the 
 heating surface of the boiler, allowing an evaporation of from six 
 to ten pounds of water per square foot of heating surface per 
 hour, or we may compute it from the grate area, assuming a 
 boiler efficiency and a rate of combustion consistent with the 
 draft and with the kind of fuel used. The former method is con- 
 sidered better. After conducting numerous tests P. G. DARLING 1 
 
 i TRANS. A. S. M. E., vol. 31 (1909), p. 109. 
 
BOILER ACCESSORIES AND AUXILIARIES 59 
 
 advocated to the A. S. M. E. formulas for pop safety valves 
 derived according to the following method: 
 
 TT 
 
 for stationary boilers, D= 0.068 ^j 
 
 -L/Z 
 
 TT 
 
 for locomotive boilers, D= 0.055 f^> 
 
 Lir 
 
 in which D is the diameter of the valve in inches, H is the heat- 
 ing surface of the boiler in square feet, L is the lift of the valve 
 in inches, and P is the absolute boiler pressure in pounds per 
 square inch. It is noticed that smaller valves are required for 
 locomotives, because the maximum draft can be secured only 
 when the steam is being drawn from the boiler by the engine. 
 
 57. Other Safety-valve Formulas. Various cities and states 
 have their own rules governing the sizes of safety valves, a few 
 of which are given below. 
 
 CITY OF CHICAGO. One square inch of pop-valve area (7rD 2 /4) 
 for every three square feet of boiler grate area. 
 
 CITY OF PHILADELPHIA. For pop valves, A = 22.5XCr/(p 8.62), 
 in which A is the area of the valve in square inches (not the effec- 
 tive opening for the escape of steam), G, the grate area in square 
 feet, and p the gage boiler pressure. 
 
 U. S. SUPERVISING INSPECTORS. A = .2Q74:XWH/P, in which A 
 is the area of the valve as in the previous formula, WH is the 
 number of pounds of water evaporated by the boiler per hour, 
 and P is the absolute boiler pressure. 
 
 Safety valves are not made in sizes over 5 or 6 inches in diameter. 
 In large boilers it is therefore necessary to use more than one. 
 
 EXAMPLE. What should be the size of pop safety valve on a boiler with 
 1500 square feet heating surface if the pressure carried is 130 pounds gage? 
 
 SOLUTION. Assuming a maximum rate of evaporation of 8 pounds of 
 water per square foot of heating surface per hour, we get 8X1500 = 12000 
 pounds of steam to be discharged per hour through the valve. The weight 
 discharged per second is 12000/3600 = 3.33 pounds. From Napier's formula, 
 W = AP/70, we see that 3.33 =AX(130+15)/70, whence A, the area of 
 opening, in square inches, is 1.61 Assuming a lift of valve equal to 1/30 of 
 the diameter, the area of the opening will be approximately .7077rD 2 /30. 
 Then .7077rZ) 2 /30 = 1.61, or D = 4.67 inches. Hence a 5-inch valve should be 
 used. 
 
 58. The Water Glass or Gage Glass. In order that the 
 amount of water in the boiler may be known, a water glass is 
 attached. The lower end of the water glass is attached to the 
 
60 
 
 ENGINES AND BOILERS 
 
 water space, and the upper to the steam space. Since there is 
 danger of the glass becoming stopped in these connections, and 
 the water level thereby being falsely indicated, or of the glass 
 
 being broken, three gage-cocks 
 or try-cocks are placed on the 
 boiler or water column. The 
 top cock is placed above, and 
 the bottom one below, the 
 normal water level. By open- 
 ing these cocks in succession, 
 one may determine whether 
 or not the gage glass is giving 
 the correct level. 
 
 59. High and Low Water 
 Alarm. High- water and low- 
 water alarms are sometimes 
 used to attract the attention 
 of the fireman when the water 
 falls below or rises above the 
 safe level. The alarm is 
 operated by means of a float 
 in the water column. When 
 this float rises too high or falls 
 too low it will open a valve, 
 and allow the escaping steam to blow a whistle. (See Fig. 23.) 
 
 60. Fusible Plug. Another safety device used to detect low 
 water is the fusible plug. This plug (Fig. 24) has a tin core 
 that will melt when the water 
 level falls below it. These 
 plugs are placed in the crown 
 sheet of an internally fired 
 boiler in the rear head a little 
 above the top tubes in the 
 return-tubular boiler and in the bottom of the steam drum of a 
 water-tube boiler. They should be kept free from scale on the 
 inside and from soot on the outside. None of the above safety 
 devices are absolutely certain in their action. Under conditions 
 of very rapid steaming or with feedwater that foams, the water 
 level in the boiler may be below that in the water column. 
 
 FIG. 23 
 
 //7S/t/f or arfsjure 
 iat/Se ry/*e 
 
 Outft'efe ft/pes 
 0ttts/e/e or // 
 
 FIG. 24 
 
BOILER ACCESSORIES AND AUXILIARIES 61 
 
 61. Boiler Feedwater Treatment. The impurities in water 
 that are responsible for most of the scale formation are the car- 
 bonates and sulphates of calcium and magnesium. If muddy 
 water is used, the mud may be deposited on the heating surface 
 and aid in scale formation. 
 
 The carbonates of lime and magnesium are soluble in water 
 containing carbon dioxide. These carbonates cause what is known 
 as temporary hardness. . Upon heating to 212 F. the carbon 
 dioxide is driven off, and the carbonates are precipitated. If 
 these are the only impurities in the feedwater, an open feedwater 
 heater will remove most of the scale-forming material. Where a 
 heater is not used the carbonates may be precipitated by the 
 addition of a solution of slacked lime. The lime combines with 
 the carbon dioxide to form the insoluble monocarbonate of lime. 
 
 The sulphates of lime and magnesium are not precipitated at a 
 temperature of 212, but are precipitated at a temperature such 
 as exists in the boiler. They cause what is known as permanent 
 hardness. The addition of carbonate or hydrate of soda (or a 
 mixture of the two) will cause precipitation. The carbonate of 
 soda decomposes the sulphates and forms insoluble carbonates of 
 lime and magnesium, which precipitate, leaving neutral soda and 
 sodium sulphate in solution. If carbon dioxide is present, the 
 soluble bicarbonate of lime is formed, which may be precipitated 
 by heating or by the addition of lime as explained previously. In 
 most purification processes both the lime and soda are used. 
 
 If organic matter, from sewage or from some other source, is 
 present in the water, it may be removed by filtration. Before 
 passing the filter a coagulant, such as alum, is often used. Organic 
 matter in feedwater is often the cause of foaming. 
 
 62. Scale Prevention and Removal. Many substances have 
 been used to prevent the formation of scale. Some of these 
 probably do as much damage to the boiler as would the scale. 
 Aside from the treatment to remove the scale-forming material, 
 the best substance seems to be graphite. When it is injected 
 into the boiler, it is said to help in the prevention of scale formation. 
 
 Where no precaution is taken to prevent the scale from form- 
 ing, it is necessary to clean it from the tubes periodically. This 
 is usually done by means of a cutter or hammer that is driven 
 by a small air, steam, or water turbine. 
 
62 
 
 ENGINES AND BOILERS 
 
 Figure 25 shows one make of cleaner that is applied to a fire 
 tube. Figure 26 shows the form that is applied to a water tube. 
 
 FIG. 25 
 
 Jca/a 
 
 tfrr/zeafaf 
 jecf/o/J 
 
 t/rfer fi/bc 
 
 FIG. 26 
 
 63. Oil Separators. In plants where all or part of the steam 
 is condensed and used again as boiler feed, the oil that was used 
 to lubricate the engine will find its way to the boiler. This does 
 not apply to steam turbines, as oil is not usually used internally 
 with them. This oil forms a very hard scale that it is almost im- 
 
 possible to remove. To pre- 
 vent this, oil separators are 
 used to remove the oil, either 
 from the exhaust steam or 
 from the water after it is con- 
 densed. The removal before 
 condensation is preferable, 
 since the oil does not have to 
 be contended with in the con- 
 denser or feedwater heater. 
 Figure 27 shows an Austin oil 
 separator. Since the separator 
 is quite large, the steam passes 
 through it with a small veloc- 
 ity and deposits the oil on the 
 surface of the corrugated ver- 
 tical baffle plate shown in plan 
 and section in the figure. 
 With high vacua, a spray of 
 water keeps the surface moist, 
 which aids in the separation 
 FIG. 27 of the oil. 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 63 
 
 64. Boiler Feed-pumps. The feedwater is usually forced into 
 a boiler by means of a pump. Figure 28 shows a common type 
 of boiler feed-pump. This pump is direct acting, the steam piston 
 and water piston or plunger being fastened to the same piston rod. 
 Since the steam and the water in a boiler are both under the 
 same pressure and since pipes and fittings offer a resistance to 
 the flow of both water and steam, it is seen that it is necessary to 
 
 FIG. 28 
 
 make the steam piston of the feed-pump considerably larger in 
 diameter than the water plunger. 
 
 Steam is admitted by the steam valve alternately to the two 
 ends of the steam cylinder. At the same time that the valve 
 is admitting steam to one end of the cylinder it is allowing it to 
 exhaust from the other, thus giving the piston a reciprocating 
 motion. The water piston sucks up water from the suction pipe 
 in one end of the water cylinder while forcing it into the delivery 
 pipe on the other. 
 
 The suction pipe leads either to the hot well or to the cold well 
 from which the feedwater is taken. The lower end of the suction 
 pipe should be provided with a strainer to prevent any large 
 pieces of solid matter from getting into and clogging the valves. 
 A foot valve should be provided also to keep the suction pipe 
 
64 ENGINES AND BOILERS 
 
 full of water when the pump is not running, thus eliminating the 
 priming of the pump every time it is started. 
 
 There are two sets of valves at each end of the water cylinder. 
 On the suction stroke, the suction valves are lifted and the water 
 is sucked in back of the piston. During the forcing stroke, these 
 valves are closed and the water is forced out through the upper 
 set and into the delivery pipe. A light spring is employed to 
 help seat the valve. Most valves are faced with a composition 
 disc which may be replaced when it becomes worn. 
 
 The flow from a reciprocating pump is not steady; to insure 
 a more uniform rate of flow of the water an air chamber is placed 
 on the delivery line close to the pump. This is kept partly filled 
 with air, which acts as a cushion. A check valve is placed in the 
 feedline between the pump and the boiler. This prevents the 
 water from the boiler escaping back through leaky valves when 
 the pump is not in full operation. There should also be a stop 
 valve in the feedline. 
 
 There are two types of reciprocating steam pump, one in which 
 there is only a single steam cylinder and a single water cylinder, 
 and the other in which there are two steam cylinders and two 
 water cylinders placed side by side. The latter type is called a 
 duplex pump. In this type the valve for one steam cylinder is 
 operated by the movement of the piston of the other steam 
 cylinder. 
 
 These boiler feed-pumps take steam the full length of the stroke, 
 not allowing it to expand in the cylinder, and they are not eco- 
 nomical in the use of steam. (See Chapter VI on the steam en- 
 gine.) However, only a small proportion of the steam generated 
 by the boiler is needed to run the pump. To secure better 
 economy, feed-pumps are occasionally driven by power taken 
 from the main engine. The supply of water from these pumps 
 is not easily regulated. They are made to pump more water 
 than is normally required, the excess being passed back to the 
 suction through a relief valve. In large electric power plants, 
 triplex pumps, driven by electric motors are often used for boiler 
 feeding. Of late years centrifugal and turbine pumps have been 
 employed for boiler feeding. 
 
 An automatic regulator is sometimes installed with the pump 
 so that the pump will furnish just the proper amount of water 
 to keep the boiler water-level constant. 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 65 
 
 65. The Injector. On portable boilers and in small plants, 
 the water is often forced into the boiler by means of an injector 
 or inspirator. This is usual also on locomotives. The principle 
 upon which the injector works is illustrated by Fig. 29. Steam 
 from the boiler enters the injector through a steam nozzle, a, in 
 which it expands and some of its heat energy is transformed into 
 kinetic energy. The steam leaves the nozzle with a high velocity 
 and enters a small combining tube, b. The water inlet leads to a 
 chamber which is located between the nozzle and the combining 
 tube. As the steam flows from the nozzle to the combining tube 
 it tends to form a par- 
 tial vacuum in the 
 water chamber and 
 thus sucks up and car- 
 ries the water along 
 with it. The steam 
 mixes with the water in 
 the combining tube and 
 is condensed. This mix- 
 
 ture of condensed steam 
 and water has a high 
 velocity and therefore 
 a considerable amount 
 of kinetic energy; its 
 pressure, however, is " 
 atmospheric or less. 
 This mixture passes 
 from the combining 
 tube to the delivery FIG. 29 
 
 tube, c, which has an 
 
 increasing diameter. The mixture therefore loses a large amount 
 of its velocity and kinetic energy. What it loses in kinetic energy 
 it gains in pressure energy, so that by the time it leaves the in- 
 jector it has gained enough pressure to force open the check 
 valve leading to the boiler. An overflow is located at the end 
 of the combining tube, so that when steam is first turned on, 
 it escapes through the overflow. The overflow is fitted with a 
 valve which automatically closes when the pressure inside the 
 combining tube falls below the pressure of the atmosphere, thus pre- 
 venting air from coming into the injector and impeding its action. 
 
66 ENGINES AND BOILERS 
 
 Unless specially constructed, an injector cannot lift water a 
 very great height. Moreover, since the injector must condense 
 the steam in order to work at all, it is necessary that the water 
 be cold. Considered as a pump, the efficiency of the injector is 
 very low, because the greater part of the energy of the steam 
 goes to heat the water. If it is used to feed a boiler, the heat 
 spent in raising the temperature of the feedwater is not lost, as 
 it goes back into the boiler. Hence it is efficient for this purpose. 
 The injector is light, occupies but little space, and is cheaper 
 than a pump, but it is not so dependable. 
 
 66. Boiler Feeding by Return Trap. The condensation from 
 various parts of the plant is sometimes returned to the boiler 
 by what is known as a return trap. This trap is located above 
 the level of the boiler and the water runs into the boiler under 
 the influence of gravity and the pressure of live steam. These 
 traps are quite economical in the use of steam and they may be 
 used to supply all the feedwater. They are not nearly so reliable 
 as the pump or injector, however, and are therefore but little 
 used to furnish the entire feedwater supply. 
 
 67. The Steam Line. Steam pipe is made of wrought iron or 
 of steel. The nominal diameter corresponds approximately with 
 the inside diameter. Sizes of standard pipe vary, by the y%" 
 from y 8 " to y 2 ", by the M" from %* to IJ^", by the %' from 
 IY 2 " to 5", and by the 1" from 5" to 15". 
 
 It has been customary to allow an average velocity of steam 
 in the line of from 4000 to 6000 feet per minute. In modern 
 turbine plants, however, where the flow is uniform, and especially 
 where superheated steam is used, velocities much in excess of 
 these values are used. If a velocity of wet steam much greater 
 than that just mentioned is used, the drop in pressure due to skin 
 friction will be excessive. On the other hand, if a velocity much 
 less is allowed, too large and expensive a pipe will be required. 
 
 If the volume and velocity of steam to be carried by the pipe 
 line are known, the diameter is easily determined. The volume 
 carried per unit of time equals the product of the area of the 
 cross-section of the pipe and the velocity. If the size and speed 
 of the engine to be supplied are known, we may compute the vol- 
 ume of steam needed. At maximum it may be assumed that the 
 engine takes steam during the full length of the stroke. When 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 67 
 
 more than one boiler is used it is customary to discharge the 
 steam into a common pipe called a header. In such a case 
 each boiler should be provided with a non-return stop-valve be- 
 tween the boiler and the header. This non-return stop-valve 
 acts as a check valve in case the direction of steam flow should 
 be reversed, which would happen in case a tube blew out or some 
 other similar accident occurred. 
 
 The piping must be provided with a sufficient number of 
 hangers to prevent breaking due to its own weight. The line 
 should slope downward in the direction the steam is to flow in 
 order that the condensation may be carried along with the steam. 
 If this precaution is not followed condensed steam will collect 
 in the pipe and may be carried in slugs by the steam in amounts 
 large enough to injure and cause leakage or even breakage of 
 the fittings. Provision should be made at the low points of the 
 line to remove condensation. A pipe should be run down from 
 the low point and the 
 
 Va/re seaf 
 fa/re 
 
 water collecting in this 
 may be blown out from 
 time to time by open- 
 ing a valve by hand. 
 A trap may be installed 
 that will remove it 
 automatically. 
 
 68. The Steam Trap. 
 
 - Several types of 
 traps are in use. In the 
 more common kinds, 
 the valve is operated 
 
 by means of either a 
 
 * T 
 float, the unequal ex- 
 
 pansion of two differ- 
 ent metals with chang- 
 ing temperature, press- 
 ure of collected water 
 on a flexible diaphragm, 
 or the weight of a bucket as it fills with water. The latter kind 
 is illustrated in Fig. 30. In this type the buoyancy of the 
 bucket keeps the valve closed until enough water flows over the 
 
 FIG. 30 
 
68 
 
 ENGINES AND BOILERS 
 
 edge and collects in the bucket to sink it. The sinking of the 
 bucket opens the valve and the water collected in the bucket is 
 forced out through the valve by the steam pressure inside the trap. 
 The bucket now being lightened, it again rises, closing the valve. 
 
 In many traps, the valve is operated by a float. The water 
 collects in a float chamber and raises the buoyant float until the 
 valve is opened. The water then escapes until the float is lowered 
 enough to allow the valve to seat. An air valve is located at the 
 top of the trap to allow the air to escape if enough should be caught 
 there to interfere with the operation of the trap. 
 
 Another form of trap is one in which the valve is operated by 
 the unequal expansion of two metals. When the trap is cold the 
 valve is open and the water is allowed to escape. As soon as 
 the steam flows through, however, the parts are heated and ex- 
 
 FIG. 31 
 
 FIG. 32 
 
 pand unequally, closing the valve. Water then collects again, 
 and as the parts cool, the valve will again open and the opera- 
 tion will be repeated. When large amounts of water are to be 
 handled, dumping traps may be used. The discharged water from 
 the trap is led to the drain or is piped back to the hot well. 
 
 69. Expansion Joints. Since the pipe is laid cold, it will ex- 
 pand when steam is turned into it and its temperature becomes 
 that of the steam. The expansion amounts to 2.5 inches per 
 hundred feet of pipe with ordinary steam temperatures, and may 
 be greater when the steam is of very high pressure and is super- 
 heated. The piping must be so arranged that this expansion may 
 take place without injury to the pipe. If the pipe is not laid 
 straight but contains elbows, it may bend enough so that no dan- 
 gerous stresses will be induced. If there is a considerable run of 
 straight pipe, however, expansion joints must be provided. 
 
 There are several types of expansion joints in use. A very com- 
 mon kind for use with low-pressure steam is the slip- joint. In 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 69 
 
 this, provision is made for the slippage of one part of the joint 
 on the other. The joint is kept steam tight by means of a stuf- 
 fing box. Figure 31 shows this type. Goosenecks and expan- 
 sion loops (Fig. 32) are used when the steam pressure is high. 
 
 70. Steam Separators. Unless superheat is used, steam leav- 
 ing the boiler will always contain some moisture. If the steam- 
 pipe is very long, some condensation also takes place. Due to 
 these causes, the steam is liable to reach the engine quite wet. 
 It is desirable both for safety and for economy to have the steam 
 as dry as possible when it enters the engine. To remove the 
 moisture from the steam, a separator is placed in the line just 
 before it reaches the engine. The steam is 
 
 given a sudden change in direction upon enter- 
 ing the separator. The moisture resists this 
 change to a greater extent than does the steam. 
 In the type shown in Fig. 33 the steam is first 
 deflected downward and then upward, and as 
 the moisture cannot change its direction of 
 motion as rapidly as the steam, it is caught 
 and collected in the bottom of the separator. 
 
 In some makes the steam is given a whirl- 
 ing motion and the water, being denser than 
 the steam, is forced to the outside of the 
 separator, where it is collected. Another type, 
 which is similar to the oil separator of Fig. 27, 
 is that in which a corrugated baffle plate is 
 interposed in the path of the steam. The steam passes around 
 the baffle while the moisture is caught by it and runs down the 
 corrugations to the bottom of the separator, where it is collected. 
 
 A separator should remove most of the moisture, but it should 
 not offer too great a resistance to the passage of the steam, since 
 this would cause a drop in pressure. The moisture, after being 
 collected, is trapped off and discharged to the drain or returned 
 to the hot well. Often the separator is made large and acts as a 
 steam receiver. This reduces the pulsation in the steam line 
 when the steam is used by a reciprocating engine. 
 
 71. Steam-pipe Covering. To prevent radiation of heat from 
 the steam-pipe and the consequent condensation, a covering is 
 applied to the pipe. The covering is made from materials that 
 
 FIG. 33 
 
70 
 
 ENGINES AND BOILERS 
 
 are poor conductors of heat. A finely-divided, dead air space is 
 one of the best non-conductors of heat. In most coverings the 
 object is to get as much finely-divided dead air space as possible. 
 
 7 r <c y- 
 
 FIG. 34 
 
 The most common kinds of covering are made from asbestos 
 or a mixture of asbestos and carbonate of magnesia. The mag- 
 nesia used in pipe covering contains a great number of very small 
 air cells, and therefore makes an excellent insulator. When the 
 magnesia is used it is usually moulded into hollow cylinders to- 
 gether with enough asbestos fiber to give it strength. Another 
 form of covering much used is made of several thicknesses of 
 corrugated asbestos paper formed into hollow cylinders by wind- 
 ing on a mandrel. 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 71 
 
 72. Feedwater Heaters. In most plants, all or some of the 
 steam is exhausted at atmospheric pressure. If this steam is 
 exhausted to the air all of its heat is wasted. Some of this heat 
 may be used to heat the boiler feedwater by running the exhaust 
 steam through a feedwater heater and extracting its heat of 
 vaporization. There are two types of 
 
 heater, the open and the closed. 
 
 I^the open feed^watexjieater the 
 steam comes m direct contact with 
 the feedwater, which is made to flow 
 over shallow pans, thus exposing a 
 large area to the steam. The tem- 
 perature of the water is thereby 
 brought near to the boiling point. If 
 the water is hard, a large part of the 
 scale-forming materials will be de- 
 posited on the pans, which may be 
 easily removed and cleaned. Figure 
 34 shows a common form of open 
 heater. A skimmer is provided to 
 remove the oil that comes in with the 
 exhaust steam, and there is also a filter 
 to purify the feedwater. The pur- 
 pose of the open heater is thus seen to 
 be twofold: to utilize the heat that 
 would otherwise be wasted and to 
 purify the water. In the closed type 
 
 (Fig. 35), the steam and the feedwater do not come into direct 
 contact. The steam is led through tubes around which the feed- 
 water is forced to flow. If the water is very hard, the tubes are 
 liable to collect scale, which hinders the operation of the heater. 
 
 73. Economizers. In the ordinary steam plant, the flue gases 
 pass up the stack at a temperature of about 500 F. This tem- 
 perature usually will be higher than that of the steam and water 
 in the boiler, since the latter get their heat from the gases. More- 
 over, the higher the steam pressure and its temperature, the 
 hotter will be the flue gas. The tendency during the past few 
 years has been to use higher pressures, which means a greater loss 
 of heat up the stack than with low pressures. 
 
 FIG. 35 
 
72 ENGINES AND BOILERS 
 
 In order to utilize a part of this heat that otherwise would be 
 wasted, economizers are sometimes installed between the boiler 
 and the stack. The economizer is simply an added heating surface 
 in the form of water tubes about which the products of combus- 
 tion pass on their way to the stack. At best the feedwater will 
 be at a temperature of only 212 as it enters the boiler, if it has 
 been heated with exhaust steam at atmospheric pressure. Con- 
 siderable heat can be added before it reaches the boiling point 
 when under high pressure. This heat is added in the econo- 
 mizer. The boiler feedwater is first pumped to the economizer, 
 where it is heated to near the boiling point corresponding to 
 boiler pressure, and it then passes on to the boiler. 
 
 In a common type of economizer, the heating surface is com- 
 posed of vertical tubes through which the water flows and around 
 which the hot gases pass. These tubes are kept clean from soot 
 by scrapers that are continually moved up and down the 
 tubes, by means of a small engine or electric motor. As the 
 economizer depends for its action upon the extraction of heat 
 from the burnt gases, it follows that the gases will be much cooled, 
 and if natural draft be employed, they may be cooled enough to re- 
 duce the draft to such an extent that the efficiency of the whole 
 plant may be lowered. If forced draft is used this objection does 
 not hold to so great an extent. In any case, the economizer offers 
 some resistance to the gases, with a consequent lowering of the 
 draft. Whether or not an economizer will effect enough of a 
 saving to pay for itself must be determined in each individual 
 case. Economizers are often sold under a guarantee to add a 
 certain percentage to the efficiency of the whole plant. 
 
 74. Condensers. After steam has passed through an engine or 
 turbine, it is often led to a condenser, in which a pressure con- 
 siderably below that of the atmosphere is maintained. The pro- 
 cess has several advantages which will be studied in more detail 
 later. In general, the decreased back-pressure adds to the effi- 
 ciency and to the capacity of the engine or turbine to an extent 
 more than sufficient to pay for the additional cost of the condenser, 
 provided plenty of cool water is available for cooling the con- 
 denser so as to condense the steam. Moreover, with a surface 
 condenser, the condensed steam is led back to the boiler and is 
 thus kept free from scale-forming materials. This last factor is of 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 73 
 
 great importance where the available feedwater is poor. Boilers 
 can be operated far beyond their rated capacity if they are kept 
 free from scale. Hence the saving in boilers and in their upkeep 
 may also go a long way toward paying for the condenser. 
 
 There are two types of condensers, one in which the cooling or 
 circulating water is kept separate from the steam, as in the closed 
 feedwater heater, and one in which the water (called injection 
 water) is mixed with the steam, as in the open feedwater heater. 
 The former is called a surface condenser, and the latter a jet 
 condenser. 
 
 75. The Surface Condenser. Figure 36 shows the construc- 
 tion of a surface condenser. The exhaust steam enters at the 
 
 5urface Condenser? 
 
 FIG. 36 
 
 top of the shell, passes around the tubes, and, after being 
 condensed, is pumped out from the bottom of the shell. The 
 tubes are usually made of thin brass or of special metal, and extend 
 between two tube sheets. At the outer side of these tube 
 sheets and within the tubes is the water space. The circulating 
 water is pumped in at the opening shown in Fig. 36, flows through 
 the lower half of the tubes to the other end of the condenser, 
 and then flows back through the top tubes and out. This arrange- 
 ment is called a two-pass condenser. In some smaller types, the 
 water enters at one end and flows out at the other; these are 
 called one-pass condensers. 
 
 Occasionally three passes are made, but this type is not gen- 
 eral. In the design of a condenser, care must be taken that the 
 steam, upon entering, is directed over the entire surface of the 
 tubes and that no air pockets may be formed. The condensed 
 steam should leave that part of the condenser where the circu- 
 lating water is coldest. Packed joints are used between the 
 tubes and the sheet. 
 
74 
 
 ENGINES AND BOILERS 
 
 Since water will absorb and dissolve air when they come into 
 contact, some air will be taken into the boilers with the 
 feedwater and will pass over with the steam to the engine. Air 
 also may leak into the steam through the stuffing boxes of the 
 engine or turbine when run condensing. This air would soon 
 clog the condenser and prevent condensation of the steam if it 
 were not removed. The air is pumped out either with the con- 
 densed steam by means of a wet-air pump or else separately by 
 means of a dry-air pump. 
 
 The circulating water is pumped through the condenser by the 
 circulating pump. To maintain a high vacuum, the circulating 
 water must be at a low temperature when it leaves the condenser. 
 This means that each pound of circulating water can absorb only 
 a few B.t.u. Each pound of the steam that condenses gives up 
 to the water something like a thousand B.t.u. It therefore is 
 evident that a large volume of circulating water must be used. 
 As the pressure to be pumped against is small, a centrifugal pump 
 is commonly employed for forcing the circulating water through 
 the condenser. Air pumps are made both of the reciprocating 
 type and of the rotary type. The former are more common. The 
 design of the air pump is a rather difficult problem, since the air is 
 very rare at a high vacuum, so that if the pump 
 has much clearance it will fail to maintain this 
 vacuum. 
 
 76. The Jet Condenser. As stated before, 
 the steam and water mix in the jet condenser. 
 This mixture of condensed steam, injection 
 water, and the air contained in the steam and 
 water, may be pumped out by a wet-air pump. 
 However, the water is often allowed to run 
 out of the condenser by gravity through a ver- 
 tical pipe thirty feet or more in length that has 
 its lower end submerged. The air is pumped out 
 by a dry-air pump. This arrangement is com- 
 monly called a siphon or barometric condenser. 
 Figure 37 shows in section this latter type of jet condenser. 
 The injection water enters at A and runs over the edges of trays, 
 thus exposing a large surface to the steam which enters at B. 
 The air pump sucks the air out at the top through the pipe C. 
 
 FIG. 37 
 
BOILER ACCESSORIES AND AUXILIARIES 
 
 75 
 
 In this type, the flow of the steam, until it is condensed, is with 
 the air and opposite to that of the water. Such a condenser 
 therefore is called a counter-current condenser. 
 
 Another type of jet condenser in which the air pump is dis- 
 pensed with is shown in Fig. 38. The air is carried along with the 
 condensed steam and the injection water. This is due to the high 
 velocity of the water as it passes out of the con- 
 stricted opening A. This is called the injector 
 or ejector type. It usually is furnished with a 
 barometric tube, as in the preceding type. 
 
 The jet condenser is more compact and less 
 expensive than the surface condenser. If it is 
 well made and equipped with a good air pump, 
 it will give a very high vacuum, but it mixes 
 fresh water with the condensed steam, and this 
 may cause scale if the mixture is used for the 
 boiler feed. 
 
 77. Cooling of Circulating Water. Since a 
 large amount of cold water is costly in some lo- 
 cations, it is sometimes necessary to cool the circulating water so 
 that it may be used over and over. This may be done by run- 
 ning it into a pond where the natural evaporation from the sur- 
 face will cool it. If the space for a large pond is not available, 
 the evaporation may be increased by the use of spray nozzles 
 which break the water up into a fine spray, thereby exposing a 
 large surface for evaporation. Another method for the rapid 
 cooling of the circulating or injection water is the use of cooling 
 towers. The water is allowed to trickle down over a lattice or 
 other surface, thus exposing a large surface for evaporation. Air 
 is either passed up through the tower by natural draft, or blown 
 through by means of fans. Where large bodies of cold water, 
 such as rivers or lakes, are available, the circulating water is 
 drawn from them and is thrown away after being used. If the 
 water is taken from lakes or rivers, it is often necessary to pass 
 it through a screen to remove such material as weeds, drift, and 
 fish. These screens require cleaning periodically and are some- 
 times made in the form of an endless chain, so that while some 
 sections are being cleansed others may be in use. 
 
CHAPTER VI 
 THE STEAM ENGINE 
 
 78. History. In 1698 THOMAS S A VERY produced the first 
 steam engine that proved to be commercially successful. It was 
 used for pumping water. The engine consisted of two egg-shaped 
 vessels, each of which connected with the supply of water to be 
 pumped and to a steam boiler. In its operation steam was ad- 
 mitted to one of the vessels, and when it was full, connection 
 with the boiler was cut off. Cold water was then sprayed on the 
 outer surface of the vessel, causing the steam inside to condense 
 and to form a partial vacuum. This vacuum opened a valve in 
 the pipe leading to the well and sucked water into the vessel. 
 Steam was then turned on again, and the pressure forced the 
 water out of the vessel through the delivery pipe. When the 
 water had all been forced out, the process described above was 
 repeated. The engine was operated so that while one cylinder 
 was forcing, the other was sucking water. This engine is the 
 same in principle as the modern pulsometer. 
 
 Since the steam in the Savery engine came in direct contact 
 with the water during the forcing stroke, there was much loss 
 of steam by useless condensation. DENIS PAPIN, in 1705, made 
 an improvement on the Savery engine by making the steam vessel 
 of cylindrical shape and separating the steam and water by a 
 floating piston, thereby preventing a part of the unnecessary con- 
 densation. 
 
 About 1711, there came into use a machine that was known 
 as the Newcomen engine. THOMAS NEWCOMEN, with the aid of 
 JOHN GALLEY, and with certain ideas from Papin, made his engine 
 with a vertical cylinder into which a piston was fitted from the upper 
 end. The cylinder was placed directly above the boiler and con- 
 nected with it. Steam was admitted to the cylinder by the open- 
 ing of a valve placed between the boiler and the cylinder. The 
 piston was connected to a pump through a walking beam, one 
 end of the walking beam connecting to the pump rod and the 
 other to the piston rod. The beam was so counterbalanced that 
 it took but little steam pressure to force the piston up. Steam 
 was generated at about atmospheric pressure, and as the piston 
 
 76 
 
THE STEAM ENGINE 77 
 
 moved up the steam valve was opened and steam filled the space 
 beneath it. When at the top of its stroke, water was sprayed 
 into the cylinder, condensing the steam and forming a partial 
 vacuum. This vacuum under the piston allowed the atmos- 
 pheric pressure from above to force the piston down. 
 
 While the Newcomen engine was an improvement over the 
 Savery engine, it was very wasteful of steam because the cylinder 
 was cooled by the spray of water on each downward stroke. Much 
 condensation of steam occurred in heating up the cylinder walls 
 on each upward stroke. While repairing one of these Newcomen 
 engines, JAMES WATT conceived ways in which it might be im- 
 proved. Patents covering these ideas were granted him in 1769. 
 Watt's chief aim was to keep the cylinder walls as hot as the 
 incoming steam at all times and thereby prevent the initial con- 
 densation that rendered the older engine so inefficient. This high 
 cylinder temperature was to be maintained, first, by condensing 
 the steam in a vessel away from the cylinder, and second, by a 
 steam jacket placed around the cylinder walls. Lagging was also 
 to be placed around the outside of the cylinder to keep down the 
 heat lost to the outside air. In the previous engines, the piston 
 was kept tight by a kind of water seal on top of the piston. Watt 
 used fibrous packing and tallow to keep the piston tight and 
 saved heat that previously was lost to the water above the piston. 
 In the operation of his engine Watt found it necessary to remove 
 the air from the condenser and so he equipped the condensers 
 with air pumps. 
 
 While it is seen that Watt is not the inventor of the steam 
 engine, yet it must be admitted that he did more to advance 
 its development than any other one man. Up to the time of 
 Watt, the steam engine was used almost exclusively for pumping 
 water in collieries, but he applied it to the driving of other forms 
 of machinery. After many hardships and discouragements, Watt 
 at last was able to produce his engine in large numbers. The engine 
 became increasingly popular, and we may say that the era of our 
 present industrial development started at the time of James Watt. 
 In applications for his patents Watt advocated the use of high- 
 pressure steam from which work could be obtained by using it 
 expansively, but in the actual construction of his engines he never 
 used pressures much above that of the atmosphere. 
 
 Since the time of Watt, various improvements have been made 
 
78 ENGINES AND BOILERS 
 
 in the steam engine. The mechanical construction has been bet- 
 tered, the valve mechanism improved, compounding adopted, and 
 the steam pressures greatly increased. While its thermal effi- 
 ciency may not be as high as some forms of internal-combustion 
 engines, the steam engine is very reliable. 
 
 79. The Plain Slide-valve Engine. Figure 39 shows in ver- 
 tical and horizontal sections the parts of a simple steam engine. 
 Its action is as follows : Steam comes from the boiler through the 
 steam-pipe, and after passing the throttle valve, enters the steam 
 chest. The valve, driven by an eccentric on the shaft, moves 
 backward and forward on the valve seat, uncovering alternately 
 the two steam ports. When a steam port is uncovered by the 
 valve, the steam flows through the port into the cylinder and by 
 its pressure moves the piston in the cylinder. In Fig. 39, the 
 left steam port is shown partly open and the steam is then push- 
 ing the piston to the right. At the same time that the steam is 
 forcing the piston to the right, the valve has uncovered the right 
 port, so that the steam on the right of the piston may escape to 
 the exhaust pipe. 
 
 This motion of the piston is transmitted by the piston rod to 
 the cross-head and from this through the wrist pin and the con- 
 necting rod to the crank. The reciprocating motion of the pis- 
 ton is transformed by the connecting rod and crank into rotary 
 motion of the shaft. The power generated in the cylinder usually 
 is taken from the shaft by a belt on the flywheel or by an electric 
 generator coupled to the shaft. The valve is made to move so 
 that when" steam is being admitted to one end of the cylinder it 
 is being exhausted from the other. As the incoming steam is at 
 a much higher pressure than the exhaust, there is a resultant 
 force pushing the piston in the direction of the outgoing steam. 
 
 That end of the cylinder farthest from the crank is called the 
 head-end^ and the end nearest the crank the crank-end. With 
 the piston at the extreme left of its travel, the crank will be in 
 a direct line between the cylinder and the shaft. While the force 
 on the crank pin may be large, there is no turning effort. The 
 crank is then said to be on head-end dead center. With the pis- 
 ton at the extreme right of its travel the crank is on crank- 
 end dead center. When the engine is running, if the crank rises, 
 as the piston leaves the head-end dead center (i.e., if in Fig. 39 
 
THE STEAM ENGINE 
 
 79 
 
 the crank moves in a clockwise direction), the engine is said to 
 be running over. If the crank moves in the opposite direction, 
 the engine is said to be running under. 
 
 FIG. 39 
 
 The stroke of the engine is the distance the piston travels in 
 half a revolution. It is equal to twice the length of the crank. 
 On the head-end stroke, the piston moves from head-end to 
 crank-end dead center, and the reverse motion takes place on 
 the crank-end stroke. 
 
80 ENGINES AND BOILERS 
 
 80. Parts of the Steam Engine. CYLINDER. Steam-engine 
 cylinders are made of cast iron and the bore is carefully machined. 
 With proper lubrication, the surface exposed to wear acquires a 
 high polish and the metal is worn away very slowly. The ports 
 are cored in the casting and are not finished except along the 
 edges at the valve seat. At each end of the cylinder the diameter 
 is made slightly larger. This enlarged part is called the counter- 
 bore. It should extend far enough so that the piston ring comes 
 to its edge, in order that a shoulder may not be worn in the cylin- 
 der wall. The counterbore also serves a purpose when the cylinder 
 has to be rebored, since the boring machine may be set on the 
 counterbore, which will not be worn away, and thus the alignment 
 need not be lost. On some larger engines used in marine service, 
 a thin inner shell or liner is placed in the cylinder, so that it may 
 be replaced without changing the cylinder when it becomes worn. 
 
 The cylinder head is bolted to the cylinder, and the joint is 
 made steam-tight by means of a gasket or a ground joint. In the 
 smallest engines the cylinder is cast as a part of the frame, but 
 ordinarily it is cast separately and bolted to the frame. 
 
 In large engines where high efficiency is desired the cylinder 
 may have a steam jacket. The heads may or may not be jack- 
 eted. In any case the cylinder is covered by some non-conductor 
 of heat, called lagging. With proper lagging very little heat is 
 lost by radiation. 
 
 Unless the exhaust valves are so placed that any water in the 
 cylinder can drain to them, it is necessary to tap the bottom of 
 the counterbore at each end of horizontal cylinders and place a 
 drain cock there. These cocks are opened when the engine is 
 warming up so that the condensed steam will not be caught when 
 the piston comes to the end of the stroke. As water is incom- 
 pressible, its presence in too large a quantity would cause the 
 breaking or straining of some part. Sometimes automatic relief 
 valves are placed at the ends of the cylinders to take care of any 
 water that may get into the cylinders. Each end of the cylinder 
 is tapped for the connection of an indicator. 
 
 VALVES. The subject of valves will be taken up in detail in 
 Chapter VIII. 
 
 PISTON. Pistons for stationary engines are made of cast iron. 
 The piston is turned to a slightly smaller diameter than the 
 
THE STEAM ENGINE 81 
 
 cylinder, and leakage of steam past it is prevented by the use of 
 piston rings which fit into grooves cut around the piston. In the 
 small sizes the rings are made in one piece slightly larger than 
 the diameter of the cylinder. A piece is then cut out of each 
 ring, and they are snapped into the groove in the piston. 
 Because of their elasticity, they spring out and make contact with 
 the cylinder walls. When worn they may be replaced by new 
 rings. On larger pistons the rings are built up in sections and 
 are pushed out against the cylinder wall by springs placed under 
 them. 
 
 On small engines the pistons are cast in one piece, and usually 
 are hollow, to make them as light as possible. In the larger 
 sizes, they are built up of two or more pieces. In vertical engines 
 and locomotives, the pistons sometimes are made dished to a 
 slight extent. The dishing may be to add strength, to shorten 
 the length of the engine a small amount, or to facilitate drainage. 
 
 PISTON ROD. The piston rod connects the piston to the cross- 
 head. It is made of steel, and the connection must be such that 
 it will be always tight. If a little play is allowed, a bad knock 
 develops that rapidly grows worse. In horizontal engines, a tail- 
 rod sometimes extends from the piston out through the head-end 
 cylinder head, and its outer end is carried by a slipper on a guide. 
 This arrangement allows the weight of the piston to be carried 
 by the slipper and the cross-head and lessens the wear on the 
 piston and the cylinder. 
 
 STUFFING Box. The joint between the piston rod and crank- 
 end cylinder head is made tight by a stuffing box. The packing 
 used on low-pressure engines in this box may be fibrous, but with 
 high steam pressure a metallic packing is commonly used. A good 
 packing should keep the joint steam-tight and at the same time 
 give but little friction on the rod. Wear in the cylinder, improper 
 adjustment of the cross-head, poor alignment, or a pitted or scored 
 rod, may cause excessive wear on the packing. It is then diffi- 
 cult to keep it steam-tight. 
 
 CROSS-HEAD. The cross-head with the cross-head pin or wrist 
 pin forms the connection between the piston rod and the con- 
 necting rod. The cross-head is made to move in a straight line 
 by guides on the frame of the engine. The two-guide type shown 
 in Fig. 39 is the most common, although four-guide and one- 
 
82 ENGINES AND BOILERS 
 
 guide types are used occasionally. The slipper type also is often 
 used; in this the cross-head takes the form of a slipper which 
 slides on the flat surface of one guide. In all types the wear 
 between the cross-head and guides is taken up by the adjust- 
 ment of the wedge-shaped slippers or by the use of shims. In a 
 few steam engines and most gas engines a trunk piston is used. 
 In this type the piston itself acts as cross-head and carries the 
 wrist pin. With this latter arrangement, the engine is single 
 acting, i.e. the steam acts only on the head of the cylinder and on 
 the face of the piston. 
 
 CONNECTING ROD. The connecting rod connects the wrist pin 
 to the crank pin. It is alternately in compression and tension, 
 and usually is made of steel. On high-speed engines, considerable 
 bending stress may be developed in the connecting rod on account 
 of its fling, and hence its cross-section is usually rectangular or 
 I-section. On slow-speed engines this bending stress is small, 
 and the rod is made circular in section. Brass or other metal 
 bearing-pieces called brasses are used at the bearing points on the 
 pins. These brasses are often babbited. As wear occurs ad- 
 justment must be made to take it up. If the rod is shortened 
 in taking up the wear, the end on which such adjustment is 
 made is said to have an open stub-end. If the rod is length- 
 ened by an adjustment at one end, that end is called a closed 
 stub-end. In Fig. 39, the end at the crank pin is of the marine 
 stub type, which is used on all center-crank engines. In this 
 last type the wear is taken up by removing liners, and in the 
 former types usually by means of wedges v/hich move the brasses. 
 
 CRANK. The crank pin is made of steel, and it may be a part 
 of the same forging as the crank and shaft, or it may be set into 
 crank discs which are keyed to the shaft. When the pin is placed 
 between two crank discs, as in Fig. 39, we have a center-crank 
 engine; when it overhangs one crank disc, we have a side-crank 
 engine. 
 
 COUNTERBALANCE. The crank pin and half of the connecting 
 rod usually are considered as rotating parts and must be coun- 
 terbalanced to make the engine run smoothly. Furthermore the 
 piston, piston rod, cross-head, and half of the connecting rod have 
 a reciprocating motion. It takes a large force to start and stop 
 them on each stroke. Unless they are counterbalanced the whole 
 
THE STEAM ENGINE 83 
 
 engine will vibrate on the foundation. While it is impossible to 
 counterbalance exactly both the rotating and the reciprocating 
 parts at the same time, yet it can be partially done. The proper 
 sized counterbalance or counterweight (Fig. 39), sometimes made 
 of lead but usually of iron, is put on to give smooth running. 
 
 SHAFT. Engine shafts usually are made of steel. As explained 
 above, they are either forged to make the crank and crank pin 
 integral parts of the shaft, or else the crank is keyed to the shaft. 
 In addition to the key, a shrunk fit sometimes is used, or the 
 crank disc may be pressed on by hydraulic pressure. 
 
 BEARINGS. With a side-crank engine there is one main bear- 
 ing, and with a center-crank engine, there are two. The weight 
 of the flywheel may be carried partly by an outer bearing called 
 an outboard bearing. There will be wear on the main bearing 
 in a vertical direction on account of the weight of the flywheel 
 and of the rotating parts, and there will be wear in a horizontal 
 direction on account of the thrust from the piston. Many main 
 bearings are made up of four parts, the cap, the bottom part 
 which takes the vertical wear, and two side-pieces which take 
 the horizontal wear. The latter are called quarter-boxes. These 
 parts may be adjusted separately. 
 
 FLYWHEEL. The turning moment on the crank varies at differ- 
 ent parts of the stroke. At dead center it is zero. In order to 
 keep the shaft turning at approximately the same speed at all 
 times in the revolution, a flywheel is put on the shaft. This acts 
 to store up and give out energy at the proper times, thereby keep- 
 ing the angular velocity approximately uniform. The flywheel may 
 carry the belt or there may be a separate belt wheel in addition 
 to the flywheel, in which case the latter is sometimes called a 
 balance wheel. The flywheel commonly is made of cast iron. 
 In the smaller sizes it is cast in one piece, but in the larger sizes, 
 it is cast in sections. Great care must be taken in its manufac- 
 ture, since a crack may cause a disastrous accident. 
 
 ECCENTRIC. An eccentric is placed on the shaft or governor arm 
 to drive the valve. It is encircled by the eccentric strap, which 
 is connected to the valve by means of the eccentric rod and 
 valve stem. This is really a substitute for a crank and connect- 
 ing rod and gives to the valve a motion similar to that of the 
 piston. 
 
84 ENGINES AND BOILERS 
 
 FRAME. The frame is made of cast iron in stationary engines, 
 and the better engines have the heavier frames. The greater the 
 weight of frame the more smoothly the engine will run, other 
 things being equal. On some small high-speed engines there is a 
 cast-iron sub-base placed between the frame and the foundation. 
 Frames are given different names according to their shape and 
 the cylinder arrangement. 
 
 FOUNDATION. Foundations usually are made of brick or con- 
 crete. The latter is now the more common. The frame is fas- 
 tened to the foundation by anchor bolts. The foundation should 
 be quite massive and should rest on soil that is firm enough to 
 carry the weight of the engine and foundation without settling. 
 
 81. Piston Displacement. The volume the piston displaces 
 in moving from one dead center to the other is called the piston 
 displacement. It is commonly expressed in cubic feet. The head- 
 end piston displacement is equal to the length of stroke in feet 
 times the area of the piston in square feet. The crank-end piston 
 displacement is the area of the piston minus the area of the cross- 
 section of the piston rod, times the stroke. . 
 
 The size of an engine is given in inches, the diameter of the 
 cylinder bore first and the length of the stroke second, e.g. an 
 18 // X24' / engine is one whose cylinder is 18" in internal diameter 
 and whose stroke is 24". The size of a compound engine is given 
 by the diameter of the high-pressure cylinder, the diameter of the 
 low-pressure cylinder, and the stroke, as 10"X18' / X24' / . If the 
 volume is calculated in cubic inches, remember to change tc cubic 
 feet in giving the piston displacement. 
 
 82. Clearance. When the piston is at the extreme end of its 
 travel, there will be some volume back of it, because it is neces- 
 sary to have a little space in which to take up the wear on the 
 connecting rod brasses and to allow for unequal expansion of 
 parts as the engine heats up, and because of the space in the 
 ports. This volume, the larger part of which is often the volume 
 of the ports, is called clearance. Clearance is expressed as a per- 
 centage of the piston displacement. Thus, when we say that the 
 head-end clearance of an engine is 4.5 percent, we mean the 
 volume back of the piston when the engine is on head-end dead 
 center is .045 times its head-end piston displacement. 
 
 To determine the clearance of an engine, first place the engine 
 
THE STEAM ENGINE 85 
 
 on the dead center of the end for which the clearance is to be 
 measured. Second, disconnect the valve from the eccentric 
 rod, move it so that the port for that end is closed, and block it 
 up in that position. It is necessary to disconnect the valve be- 
 cause the port is usually open a small amount when the engine 
 is on dead center. Third, pour water into the opening for 
 attaching the indicator cock until the clearance space is full of 
 water. If the valve is placed at the top of the cylinder, as is 
 the case with horizontal Corliss engines, remove the valve and 
 pour the water into the port. Having recorded the amount of 
 water poured in, and having made correction for leakage, the 
 volume of w r ater necessary to fill the clearance space is computed. 
 This volume divided by the piston displacement for that end gives 
 the clearance. A rough method of computing clearance from the 
 indicator diagram is given in 89. 
 
 83. Steam Back of Piston during Stroke. The weight of the 
 dry steam back of the piston may be computed for any percent 
 of the stroke if we know the clearance, the size of the engine, 
 and the steam pressure at that percent of the stroke. Add the 
 percent of the stroke to the percent of clearance. Multiply this 
 by the piston displacement, and divide by 100. The result is 
 the volume of steam back of the piston at the given percent of 
 stroke. By means of the indicator, the pressure may be determined 
 for the same position. The density of steam may be read from 
 the steam tables for that particular pressure. The product of 
 this density and the volume back of the piston gives the weight 
 of the steam there. 
 
 EXAMPLE. What is the weight of dry steam back of the piston at 27% 
 of the crank-end stroke of a 14"X16" engine? The engine has a 2" rod and 
 the crank-end clearance is 6.3%. The crank-end indicator card is at hand. 
 
 SOLUTION. Measure the pressure from the card at 27% of the stroke. 
 Suppose this pressure is 115 pounds gage, and the atmospheric pressure is 
 14.5 pounds per square inch. The absolute pressure is then 115 + 14.5 = 129.5 
 pounds per square inch. The density of dry saturated steam at this pres- 
 sure is, from the steam tables, .2887 The piston displacement is seen to be 
 16(7r7 2 TT)/ 1728 = 1.398 and the volume back of the piston is therefore equal 
 to (.27 + .063) XI. 398 = .466 cubic feet. The weight of dry steam is then 
 .2888 X .466 = . 1 342 pound. 
 
 84. The Indicator and Its Purposes. The steam-engine indi- 
 cator was first used by JAMES WATT, who invented it. Since his 
 time it has been perfected and is now very extensively used. 
 
86 ENGINES AND BOILERS 
 
 The indicator records on paper a line showing the relation between 
 the pressure in the cylinder and the movement of the piston. 
 The diagram or card produced is of value in setting the valves, in 
 computing the horsepower developed in the cylinder, and in mak- 
 ing analyses of the operation of the engine. A description of the 
 mechanism of the indicator will not be given here. When we 
 speak of the scale of spring of an indicator, we do not mean the 
 actual scale of the spring used in the indicator, but rather the 
 relation between the movement of the pencil on the indicator dia- 
 gram and the pressure that causes it. That is, a 60-pound indicator 
 spring is one that gives a pencil movement of one inch for each 
 60 pounds per square inch increment of pressure in the cylinder. 
 The heavy lines of Fig. 40 show a representative diagram as 
 it comes from the indicator. It is seen that the diagram is a 
 closed irregular curve with a straight line underneath. The 
 Cuf . off straight line is the atmospheric- 
 
 pressure line, which is used for 
 reference in measuring pres- 
 ._ ____ + ^ e/eeje sures. The ordinates of the 
 points on the curve show to 
 * some scale the pressures in the 
 
 jp IGt 40 cylinder, and the abscissas the 
 
 movement of the piston. Start- 
 
 ing at the upper left-hand corner of Fig. 40, we have the pressure 
 back of the piston when it is on dead center. As the piston 
 moves forward, the pressure changes as shown by the upper curved 
 line of the diagram. It is seen that the pressure drops but little 
 for the first part of the stroke, and later more rapidly, until at the 
 end of the stroke it is nearly down to that of the atmosphere. 
 On the backward stroke, the pressure remains nearly constant 
 until near the end, when it rapidly rises to the initial point. 
 
 85. Events of Stroke. There are four events of the stroke. 
 1. Admission occurs when the valve uncovers the port and allows 
 the steam to enter the cylinder. 2. Cut-off takes place when 
 the valve closes the port and prevents any more steam from 
 entering. 3. At release, the valve uncovers the port and allows 
 the steam to escape to the exhaust. 4. Compression occurs when 
 the valve again closes the port and prevents any more steam 
 from leaving the cylinder for the remainder of the stroke. 
 
THE STEAM ENGINE 87 
 
 It is seen that the steam enters the cylinder from admission to 
 cut-off, and that the steam thus let in expands and does work 
 on the piston from cut-off to release. From release to compression, 
 the used steam is being exhausted from the cylinder. The steam 
 that is caught when the exhaust port closes is compressed into the 
 clearance space during the time from compression to admission. 
 
 86. Location of Events on Diagram. After a little practice 
 the events may be quite accurately located on the ordinary in- 
 dicator diagram or card. In Fig. 40 it is seen that the upper 
 line drops down and that there is a point of inflection in this 
 curve. This is the point of cut-off. This point of inflection is 
 easily detected by drawing a continuation of the two curves as 
 shown by the dotted lines at the point of cut-off. Release occurs 
 at the next point of inflection; it may be located in a manner 
 similar to that in which we located the cut-off. At compression 
 there is no point of inflection; therefore its proper location is diffi- 
 cult. The exhaust valve ordinarily closes rather slowly, and the 
 passageway for steam being small when it is nearly shut, the pres- 
 sure may start to rise even before the valve is completely closed. 
 
 A common error is that of taking the point of compression 
 too low on the compression curve. Admission occurs where the 
 compression curve stops and the straight line starts. 
 
 To determine the percentage of stroke at the different events, 
 draw the two end-ordinates. The distance between these, / in 
 Fig. 40. represents the length of stroke to some scale. The dis- 
 tances from the left end-ordinate to the events shown by a, b, e, 
 and d, divided by the distance /, give the ratios of the stroke 
 at these events, and the percentages of stroke are those ratios 
 multiplied by 100. 
 
 87. Equation of Expansion and Compression Curves. There 
 is a definite relation between pressure and volume during expan- 
 sion and compression. The equation pv n = p\v\ n = p 2 V2 n expresses 
 this relation, where p is the absolute pressure on these curves, 
 v is the volume back of the piston (including the clearance space), 
 and n is some constant exponent for each individual curve. An 
 analysis of many cards shows that n is sometimes a little less 
 than 1 and sometimes a little larger than 1. For rough calcu- 
 lations, it may be considered equal to 1. With this assumption, 
 the equation of the expansion and compression curves is pv=C. 
 
ENGINES AND BOILERS 
 
 This is the equation of the equilateral hyperbola. Certain geo- 
 metric facts about this curve are of importance to us. In Fig. 41, 
 let us choose any two points on an equilateral hyperbola: E, 
 whose coordinates are (pi, vi), and H, whose coordinates are 
 (P2, ^2)- We shall show that the line of the diagonal CA of the 
 rectangle EC HA drawn through these points, passes through the 
 origin. In the triangles OAB and OCD, OB = Vi, BA=p 2 , 
 OD=vz, and DC =pi. Since their sides are parallel, these two 
 triangles are similar. Hence we have 
 
 yo/ume t/j Ct/jb/c 
 
 
 which satisfies the equation of the curve. 
 
 It follows that we can construct the entire curve if one point E 
 
 on it is given. We can locate other points on it in the following 
 
 manner. Through the point E 
 draw horizontal and vertical 
 lines. Choose some point C on 
 the horizontal line, and draw 
 the line OC through the origin. 
 Drop a vertical line from C, 
 and draw a horizontal line 
 
 jj x / x " ' ' ' f%r through A, the point where the 
 
 line OC cuts the vertical line 
 through E. The intersection H 
 of the vertical line through C 
 
 and the horizontal line through A is a point on the curve. Other 
 
 points may be found in the same manner. 
 
 Another geometric fact of value is that the length of FE is 
 
 equal to HG on a line drawn through the points E and H. This 
 
 may be proved readily from Fig. 41. The area under the curve 
 
 from E to H, i.e. BEHD, may be determined by integration. 
 
 The increment of this area has dimensions p and dv, and dA 
 
 is equal to pdv. Hence the total area is 
 
 A = \ dA = \ pdv, 
 but since p\v\ = p%V2 = pv, we have 
 
 and 
 
THE STEAM ENGINE 
 
 89 
 
 88. Hypothetical Indicator Diagram. Diagrams are some- 
 times constructed on the hypotheses that the expansion and com- 
 pression curves are equilateral hyperbolas, that the pressure dur- 
 ing the admission of steam from the end of the stroke to cut-off 
 is constant, and that the back pressure is constant up to the 
 point of compression. Such a diagram will be called the hypo- 
 thetical diagram. This diagram is also sometimes called the 
 theoretical, or ideal, or conventional diagram. 
 
 The construction of such a diagram, shown in Fig. 42, is car- 
 ried out as follows. First choose a suitable length / for the dia- 
 gram, and draw in the atmospheric-pressure line. Next choose 
 
 a scale of pressures, ^ ^ 
 
 and draw the volume ~~~ e ' - - 
 
 -. 
 
 axis at a distance c, the 
 atmospheric pressure, 
 below the atmospheric 
 line. Draw the pres- 
 sure axis at a distance 
 from the point F of the 
 diagram equal to the 
 ratio of clearance times 
 the length /of the dia- 
 gram. Measure up from 
 the atmospheric-pres- 
 sure line the initial steam pressure, and draw the steam-admis- 
 sion line FA. The length of FA is equal to the ratio of cut-off 
 times the length /. From the point A, construct an equilateral 
 hyperbola as in 87. The length e is equal to the ratio of release 
 times /. From B, the point of release, draw a line to the end of 
 the diagram at C. The distance h from C to the atmospheric- 
 pressure line represents the back pressure. From C to D draw the 
 back-pressure line parallel to the atmospheric line. From D, 
 the point of compression, construct an equilateral hyperbola to 
 the point E, whose distance a from the end of the diagram is the 
 admission distance. Connect E and F by a straight line. 
 
 The actual diagram may vary considerably from the diagram 
 just constructed. The speed of the engine, the throttling of 
 steam in the ports and by the valve, the condensation in the 
 cylinder, etc., affect the form of the actual diagram, which may 
 resemble the dotted diagram FGHCIJF in Fig. 42. If the en- 
 
 in tsto/c feef 
 FIG. 42 
 
90 
 
 ENGINES AND BOILERS 
 
 FIG. 43 
 
 gine exhausts into a condenser in which a vacuum is maintained, 
 the back-pressure line will fall below the atmospheric-pressure line. 
 
 89. Determination of Clearance from Card. Since it is often 
 impossible to measure the clearance of an engine when a test is 
 being made, a rather rough approximation sometimes is used. 
 Suppose the indicator diagram is as shown in Fig. 43. Two 
 points A and B are chosen on the compression curve. On these 
 
 two points a rectangle is 
 drawn, and the diagonal is 
 extended until it cuts the vol- 
 ume axis, which is drawn 
 below the atmospheric line at 
 a distance equal to the bar- 
 ometric pressure. The point 
 of intersection of this diagonal 
 and the volume axis establishes the origin, and the pressure axis 
 may be drawn. The distance c divided by the length of card 
 gives the ratio of clearance. The pressure axis may also be 
 located by drawing the other diagonal through A and B and 
 laying off DA equal to BE. If the piston rings are not tight 
 in the cylinder, or if the valve leaks steam, this method will not 
 give even approximately correct results. 
 
 90. Determination of the Mean Effective Pressure. It has 
 been mentioned that the indicator diagram shows the pressure 
 at all points of the stroke. 
 
 Since the total pressure on the 
 piston times the distance the 
 piston moves is the work done 
 by the steam, we see that the 
 indicator card is a work dia- 
 
 FIG. 44 
 
 gram. 
 
 In order to calculate the work 
 done in the cylinder we must 
 know the average effective pressure, or the mean effective pres- 
 sure (m. e. p.) on the piston. In Fig. 44 when the piston is at G 
 on the forward stroke, the steam pressure is a. When the piston 
 is at G on the backward stroke, the steam pressure is 6. During 
 the forward stroke the steam is working on the piston, but on 
 the backward stroke the piston is doing work on the steam. 
 
THE STEAM ENGINE 
 
 91 
 
 Hence the effective pressure for the two strokes at G is a b, 
 which is shown by the dotted ordinate G H. 
 
 To get the average, or mean, of these effective pressures for the 
 whole card, we may proceed as follows. Draw in the end-ordi- 
 nates of the diagram. By means of a scale or the edge of a 
 ruled piece of paper, divide the length of the card into a number 
 of divisions of equal length. The number of divisions should be 
 more than eight, and need not be more than fifteen. Through 
 these division points, draw in ordinates as shown by the full 
 lines. The diagram is thereby cut into a number of strips of 
 equal width. The average height of each strip is about equal 
 to the dotted ordinate located midway between the solid lines, 
 
 ' *3vm / Jotted orSin'*t*s' 
 
 FIG. 45 
 
 i.e. the average height of the strip CEFD is GH. While this 
 may not be true in every case, the fact that some parts of the 
 diagram are concave while other parts are convex will tend to 
 neutralize the error when the dotted ordinates are averaged. 
 Next add the lengths of the dotted ordinates. This is best done 
 by laying a strip of paper on the diagram and marking the dif- 
 ferent ordinates directly on the edge of the strip. Figure 45 
 shows the strip of paper with the dotted ordinates added graph- 
 ically. The average of the ordinates is this sum divided by their 
 number. This average height of card, multiplied by the scale 
 of spring, gives the mean effective pressure (m. e. p.). 
 
 If the m. e. p. of many cards is to be found, it may be quicker 
 to use a polar planimeter to get the area of the card. This area 
 divided by the length gives the mean height. This mean height 
 multiplied by the scale of spring gives the m. e. p. This method 
 is usually no more accurate than the former, when the former 
 is done with reasonable care. 
 
92 ENGINES AND BOILERS 
 
 91. Indicated Horsepower. The mean effective pressure 
 (m. e. p.) in pounds per square inch times the area of the piston 
 in square inches gives the total average effective force exerted 
 by the steam on the piston during the forward and backward 
 stroke, or for one complete revolution of the crank. The work 
 done by this force is equal to the force times the distance the 
 piston moves. It must be remembered that the effective force 
 on the piston was obtained by taking the difference of pressures 
 during the forward and backward strokes. With this in mind, 
 we see that the work done on the piston per revolution is equal to 
 the m. e. p. times the area of the piston, times the length of the stroke. 
 If the length of stroke is expressed in feet, the result will be in 
 foot-pounds. 
 
 If N denotes the revolutions per minute (r. p. m.), L the length 
 of stroke in feet, P the m. e. p. in pounds per square inch, and A 
 the area of piston in square inches, the foot-pounds of work done 
 per minute is equal to PL A N. The horsepower of the engine is 
 then PLAAV33000. Since this result is obtained by means of 
 the indicator, it is called the indicated horsepower (i. hp.). 
 
 If the engine is double-acting, the i. hp. for the crank-end is 
 found in a similar manner, taking the m. e. p. from the crank- 
 end card and using the area of the piston on the crank-end, which 
 will be less than that for head-end because the piston rod occu- 
 pies some of the area of the piston. For very rough work, the 
 average of the m. e. p. for the two ends is sometimes taken and 
 the area of the piston rod is neglected; then we have, approxi- 
 mately, 
 
 total indicated horsepower = QQQQQ * 
 
 EXAMPLE. The head-end m. e. p. is 42.6 and the crank-end m. e. p. is 
 45.1 pounds per square inch in a 12" X 18" engine running at 220 r. p. m. The 
 diameter of the piston rod is two inches. What is the indicated horsepower? 
 
 SOLUTION. The area of a 12" circle is 113.1 square inches and of a 2" 
 circle is 3.1 square inches. The area of the head-end of the piston is then 
 113.1 square inches and of the crank-end 113.13.1 = 110.0 square inches. 
 The stroke is 18", or 1.5'; hence we have 
 
 and 
 
 . . ,., 42.6X1.5X113.1X220 .__, 
 head-end i. hp. = - 33QQO - =48.2 hp., 
 
 45.1X1.5X110.0X220 
 crank-end i. hp.= 33000 =49.7 hp. 
 
 whence the total i. hp. is 48.2+49.7 = 97.9 hp. 
 
THE STEAM ENGINE 
 
 93 
 
 92. Brake Horsepower. It is usually not difficult to take 
 cards from an engine and to compute the i. hp. from them. This 
 does not give the horsepower that the engine is actually deliv- 
 ering, of course, but that which is developed in the cylinder. 
 In testing an engine that is in actual use, it is often impossible 
 to measure its actual output without considerable trouble and 
 expense. Under such conditions one must be content with the 
 i. hp. If the engine is not too large and conditions will permit, 
 the actual power delivered by the engine is often measured. If 
 it is direct-connected to an electric generator and the losses in the 
 generator are known, this is fairly simple. If not, some form of 
 dynamometer may be used. The most common means of meas- 
 uring the delivered horsepower is by a brake on the flywheel. 
 
 FIG. 46 
 
 If a number of tests are made, the Prony brake is generally used. 
 For an occasional test a rope brake may answer the purpose. 
 
 Figure 46 shows a common form of Prony brake. Two or more 
 bands of strap iron with wooden blocks fastened to them are 
 put around the circumference of the flywheel or the belt wheel. 
 The tension in the band is regulated by means of a hand-wheel 
 shown at the top of the figure. Two arms are fastened to the 
 band which at the right end in the figure carry a knife-edge that 
 rests on a block placed on a platform scales. The flywheel 
 rotates in the direction of the arrow, and the friction between 
 the blocks and the wheel causes a pressure on the scales. 
 
 When the engine is not running, there will be some pressure 
 on the scales due to the weight of the brake-arm. This may be 
 determined by weighing the brake before putting it on the wheel 
 and balancing it so that its center of gravity is determined. If 
 
94 ENGINES AND BOILERS 
 
 the weight of the brake is w and its center of gravity is located 
 at a distance b from the knife-edge and at a distance a from the 
 center of the wheel, we have, taking moments about the center 
 of the wheel, 
 
 wa = component of weight on scales X (a +6). 
 From this we can compute the effect of the weight of the brake 
 arm on the scales. This component of weight must be subtracted 
 from the pressure on the scales when the engine is running. If we 
 denote by P the net pressure on the scales, which is due to the 
 friction between the blocks and the wheel with the engine running, 
 we may compute the power being absorbed by the brake as fol- 
 lows. The work absorbed by the brake per revolution is equal 
 to PX2?rr, in which r is the horizontal distance from the center 
 of the wheel to the knife-edge and is known as the radius of the 
 brake-arm. If the engine is running N revolutions per minute, the 
 work absorbed per minute is 'ZnrPN, and the horsepower absorbed 
 is 27rrPAV33000. This is called the brake horsepower (b. hp.). 
 The radius of the brake wheel R does not enter into the compu- 
 tation of the b. hp. To prevent the burning of the wooden blocks, 
 the wheel is kept cool by putting water inside the rim which 
 evaporates and carries off the heat. 
 
 EXAMPLE. During the test of an engine, the r. p. m. was 220. The pres- 
 sure of the brake arm on the scales was 318 pounds (Fig. 46). The weight of 
 the entire brake is 118 pounds, and its center of gravity (c. of g.) is 6.05 
 feet from the knife-edge. The radius of the brake-arm, r, is 7.16 feet. Find 
 the brake horsepower. 
 
 SOLUTION. If the c. of g. of the brake is 6.05 feet from the knife-edge, it 
 is 7.166.05 = 1.11 feet from the center of the wheel when the c of g. is in 
 line between the knife-edge and the center of the wheel. That part of the 
 weight of the brake supported by the scales is 118X1.11/7.16 = 18.4 pounds. 
 The net pressure on the scales then equals 318 18.4 = 299.6 pounds. The 
 brake horsepower=27rrPAY33000 = 27rX7.16X299.6X220/33000 = 89.7 hp. 
 
 93. Mechanical Efficiency. The ratio of the brake horse- 
 power to the indicated horsepower is called the mechanical effi- 
 ciency. It is usually expressed in the form of a percentage. 
 The difference between the indicated horsepower and the brake 
 horsepower is the frictional horsepower. 
 
 EXAMPLE. If the i. hp. of an engine is 97.9, and the b. hp. is 89.7 hp. 
 find the mechanical efficiency and the frictional horsepower. 
 
 SOLUTION. The mechanical efficiency = 89.7/97.9 = .916 = 91.6%. The 
 frictional horsepower = 97.9 - 89.7 = 8.2 hp. Hence the frictional horsepower 
 = 8.2/97.9 = 8.4% of the indicated horsepower. 
 
THE STEAM ENGINE 95 
 
 94. Thermal Efficiency. In general the efficiency of a ma- 
 chine is the ratio of the out-put to the in-put. In the steam 
 engine heat is put in and mechanical work is taken out. The 
 thermal efficiency of the steam engine is the ratio of the work got 
 out to the work equivalent of the heat put in. The thermal effi- 
 ciency may be based on either the i. hp. or the b. hp. The latter 
 is called the overall efficiency, and is equal to the thermal efficiency 
 based on i. hp. times the mechanical efficiency. 
 
 A common but approximate way of stating the efficiency of a 
 steam engine is to give the weight of dry steam consumed per 
 hour per horsepower. This may be based on either the i. hp. 
 or the b. hp. It is not an exact way of stating the efficiency 
 because steam may contain different amounts of heat, depending 
 on pressures and superheat. Efficiency may also be expressed 
 in terms of B.t.u. per minute per horsepower. 
 
 In computing the B.t.u. given to the engine in a unit of time, 
 proceed as follows. The weight of dry steam is found by deduct- 
 ing the weight of moisture in the steam from the amount of 
 wet- steam used. The heat in this moisture is not charged to 
 the engine, since it is not possible for the engine to extract work 
 from it. From the steam tables find the total heat in a pound 
 of dry steam, or the total heat in a pound of superheated steam 
 if superheated steam is used. From this total heat per pound, 
 subtract the heat of the liquid at the pressure of the exhaust. 
 The reason for subtracting the heat of the liquid at the pressure 
 of the exhaust is that although the engine has used the steam, 
 the heat of the liquid can be saved by feeding the condensed 
 steam back to the boiler, which is often done. Whether it is 
 done or not, it is not fair to charge this heat to the engine. Mul- 
 tiply the amount of heat in a pound of dry steam that is charged 
 to the engine by the weight of dry steam used in unit time. The 
 result gives the B.t.u. upon which the efficiency is computed. 
 
 EXAMPLE. An engine during a test developed 97.9 i. hp. and 89.7 b. hp. 
 The engine used 3060 pounds of 97% quality steam per hour. The steam 
 pressure was 125 pounds gage, and the engine exhausted to the atmosphere. 
 The barometer reading was 29.3 inches. Find the thermal efficiency of the 
 engine. 
 
 SOLUTION. The weight of dry steam used per hour is 3060 X. 97 = 2970 
 pounds. 125 pounds gage pressure = 125+ 14.4 = 139. 4 pounds per square 
 inch absolute. At this pressure, the total heat in a pound of steam is 318. 2 -j- 
 872.3 = 1190.5 B.t.u. The heat of the liquid at the atmospheric pressure is 
 
96 ENGINES AND BOILERS 
 
 179.3, therefore the heat to be charged to the engine per pound of dry steam 
 used is 1190.5-179.3 = 1011.2 B.t.u. The dry steam used per hour per i. hp. 
 is 2970/97.9 = 30.35 pounds. The work delivered per hour per horsepower = 
 33000X60 foot-pounds. The foot-pounds of energy equivalent to the B.t.u. 
 supplied per hour per horsepower is 778X1011.2X30.35. Therefore, since 
 the efficiency is the out-put divided by the in-put, 
 
 This is based on the i. hp. The dry steam used per hour per b. hp. is 
 2970/89.7 = 33.1 pounds; hence the thermal efficiency based on the b. hp. is 
 
 33000X60 
 778X1011.2X33.1 
 
 In this solution the factor 33000X60/778=2545 will always 
 occur in the equation for thermal efficiency. Hence the formula 
 may be written in the form 
 
 4i i a 2545 
 
 thermal efficiency = - . p . , , , -- - - > 
 
 nX B.t.u. per pound of dry steam 
 
 where n is the number of pounds of dry steam used per hour per 
 horsepower. 
 
 The thermal efficiency of a steam engine will seldom, if ever, 
 exceed 25 per cent. This may seem to be a very low value, but 
 it is impossible for the engine to use a very large part of the 
 heat supplied due to the fact that the exhaust steam carries 
 with it its heat of vaporization. On account of condensation of 
 steam in the cylinder and other causes of heat loss, the efficiency 
 of a reciprocating engine seldom approaches the efficiency of an 
 ideally perfect engine working under the same range of pressure, 
 but a well-designed steam turbine of large size may do so. 
 
 95. Cylinder Condensation. The largest single loss in the 
 average engine is due to what is known as initial condensation. 
 Since the cylinder walls are made of iron, which is a good con- 
 ductor of heat, they naturally absorb heat from any hotter 
 body or substance placed in contact with them and they give 
 up heat to a cooler body. The steam comes into the cyl- 
 inder at a relatively high pressure and temperature. Both the 
 pressure and the temperature drop in the cylinder, and the steam 
 leaves at a relatively low pressure and temperature. Since the 
 cylinder walls are exposed first to hot, and then to cool steam, 
 their temperature will never be as great as that of the incoming 
 steam, nor as low, during operation, as that of the outgoing steam. 
 
 When the steam first enters the cylinder and strikes the cooler 
 walls, a part of its heat will be absorbed by the walls. This 
 
THE STEAM ENGINE 97 
 
 causes a partial condensation of the steam. Since the engine 
 operates by virtue of the steam pressure and volume, it is readily 
 seen that a shrinkage in volume causes a loss of work, and a lower- 
 ing of efficiency. By the time the steam leaves the cylinder, it 
 is cooler than the cylinder, and it takes back some of the heat 
 it gave to the walls, but at too late a time to avoid the loss in 
 efficiency. Depending upon the type of engine and the condi- 
 tions of operation, the condensation may continue until release 
 occurs, or re-evaporation may start during the expansion of the 
 steam between cut-off and release. By computing from the in- 
 dicator diagram the weights of steam at cut-off and at release, 
 we find a net condensation during expansion if the weight at 
 release is less than at cut-off, and a net re-evaporation if the 
 weight at release is greater than at cut-off. The computation of 
 condensation or re-evaporation during expansion is of little value 
 since most of the re-evaporation occurs after release and before 
 the steam leaves the exhaust ports. 
 
 96. Steam Accounted for by the Indicator Diagram. The 
 
 A. S. M. E. code for testing steam engines calls for the computa- 
 tion of the steam accounted for by the indicator diagram at points 
 near the cut-off and release. Mark the points of cut-off and 
 release and a point on the 
 compression curve where we 
 are sure the exhaust valve is 
 closed, as in Fig. 47. Find the 
 ratio of stroke at these points. 
 The volume back of the piston 
 at cut-off is the ratio of stroke 
 at cut-off plus the ratio of p IG 47 
 
 clearance, shown by a, times 
 
 the piston displacement. Scaling the pressure at cut-off from the 
 diagram, we may compute the weight of dry steam back of the 
 piston at cut-off by means of steam tables. 
 
 Not all of the steam back of the piston at cut-off entered on 
 that one stroke from admission to cut-off, since some of it was 
 in the cylinder during compression. The amount that was ad- 
 mitted is the weight at cut-off minus the weight caught at com- 
 pression. The weight of steam compressed may be computed 
 in a manner similar to that at cut-off. The weight of steam 
 per hour accounted for by the indicator diagram is then equal to 
 
98 
 
 ENGINES AND BOILERS 
 
 FIG. 48 
 
 FIG. 49 
 
 FIG. 50 
 
 FIG. 51 
 
 FIG. 52 
 
 FIG. 53 
 
 FIG. 54 
 
 FIG. 55 
 
 FIG. 56 
 
 FIG. 57 
 
 
THE STEAM ENGINE 99 
 
 (Wc.o.-TF C omp.)XWx60/i. hp., where W c . . and TF comp . are the 
 weights of steam back of the piston at cut-off and compression, 
 respectively. The weight is calculated separately for the head-end 
 and crank-end of the cylinder, and the two values added to give 
 the total for the engine. The weight accounted for at release is 
 computed in the same way, but the two results usually differ slightly 
 on account of the net condensation or the re-evaporation during ex- 
 pansion from cut-off to release. The weight of steam accounted for 
 by the indicator diagram will be considerably less than the actual 
 amount used by the engine, because of the initial condensation 
 of steam when it first enters the cylinder. 
 
 97. Valve-setting from the Indicator Diagram. It has been 
 mentioned previously that one of the uses of the indicator is to 
 assist in the setting of the valves While the subject of valve- 
 setting will not be discussed thoroughly here, faulty setting may 
 be recognized from the appearance of the diagram. Figure 48 
 shows the effect when the admission valve opens too soon. 
 
 Figure 49 shows the results of late admission. Due to the 
 tardiness of the valve opening, the steam is throttled, and the 
 pressure for a large part of the stroke is lowered considerably. 
 
 Figure 50 shows the effect of early compression. The steam 
 caught when the exhaust valve closes is compressed to a pressure 
 above that in the steam chest, the admission valve is lifted off 
 its seat, and some of the steam escapes into the steam chest. 
 
 Figure 51 shows almost no compression. This would cause no 
 harm in a very slow-speed engine, but with higher speeds the 
 steam caught at compression acts as a cushion and makes for 
 smooth running. 
 
 Figure 52 shows too early a release, and Fig. 53, too late a 
 release. Both cause a loss in the area of the diagram. 
 
 Figures 54 and 55 show unequal cut-off in the two ends of the 
 cylinder. The crank-end is doing a much larger proportion of 
 the work. The work done by the two ends should be about equal. 
 
 Figure 56 shows improper lubrication of the indicator piston 
 or the binding of some part. A wavelike motion of the curve is 
 sometimes noticed when the diagram is taken from a high-speed 
 engine, due to the vibration of the indicator spring, but it differs 
 materially from Fig. 56. In Fig. 57, the indicator drum is strik- 
 ing the stop on account of improper adjustment of the length of 
 the cord connecting the indicator and the reducing mechanism. 
 
CHAPTER VII 
 COMMON TYPES OF STEAM ENGINES 
 
 98. Slide-valve Engine. Where simplicity and reliability 
 are of more importance than high efficiency, the slide-valve en- 
 gine is used. The simplest type of slide-valve was shown in Fig. 
 39, and the principles of its operation were explained to some 
 extent in the previous chapter. There are many varieties of 
 slide-valves, the more common of which will be described later. 
 Most of the smaller stationary engines in use are equipped with 
 the slide-valve, and all American locomotive engines are of this 
 type. 
 
 While the plain slide-valve is very simple, it has certain defects. 
 One of these is the impossibility of obtaining the proper steam 
 distribution at all loads, i.e. of making the events of stroke occur 
 at the proper place to give the highest efficiency at light load 
 and also at heavy load. Various modifications and improvements 
 have been made on the slide-valve to remedy this defect, the 
 chief one of which is to place a second slide-valve on top of the 
 main valve, and to control cut-off by a rider. 
 
 Another defect of the plain slide-valve is the slowness with 
 which the steam ports open up and close at some loads, which 
 cause what is known as wire-drawing. This is simply a throttling 
 of the steam by the valve as it enters the cylinder. This throt- 
 tling usually causes a lowering of the efficiency of the engine. 
 
 99. The Corliss Engine. By far the most common type of 
 high-grade reciprocating stationary steam engine in this country 
 is the Corliss engine. The name comes from its inventor and 
 first producer, GEORGE CORLISS, an engineer and engine builder of 
 Providence, R. I. There are two distinguishing features of this 
 engine. The first of these is the oscillating cylindrical valve. 
 The second is the means for disengaging the valve from the mech- 
 anism that drives it, and the quick closing of the valve after its 
 disengagement. To understand the Corliss valve mechanism 
 thoroughly, it is necessary to make a rather thorough analysis of 
 its motion. We shall not do this in this chapter. The general 
 principle of operation of the gear is fairly simple, however. 
 
 Figure 58 shows a typical Corliss engine cylinder. The right 
 end is cut in section to show the construction of the valves and 
 
 100 
 
COMMON TYPES OF STEAM ENGINES 
 
 101 
 
 their locations relative to the cylinder. The left end shows an 
 ordinary form of the mechanism that moves the steam valves and 
 the exhaust valves. An eccentric on the shaft is connected to 
 the hook rod which operates the valves through an eccentric rod 
 and rocker arm. This gives the hook rod a horizontal recipro- 
 cating motion that is nearly harmonic. The hook rod is attached 
 
 - 3 fa am fff>e 
 
 FIG. 58 
 
 to a wrist plate which is pivoted to the cylinder at C. The wrist 
 plate is thereby given an oscillating motion. 
 
 Four rods are attached to the wrist plate. The two upper 
 rods are the steam rods, which transmit the motion to the two 
 steam valves, and the lower or exhaust rods drive the two exhaust 
 valves. The steam rods are attached to bell cranks or double 
 arms that are pivoted on the valve spindle but are not attached 
 to it. It is thus possible for the wrist plate and the bell crank 
 
102 ENGINES AND BOILERS 
 
 to move without affecting the valve in any way. The cylindrical 
 steam valve has a spindle which extends out of the steam chest. 
 To the outer end of this spindle there is keyed a steam arm. 
 Any motion of this arm causes the valve to move. A block is 
 attached to the back side of the steam arm, and a hook which is 
 carried by the upper arm of the bell crank catches over it. As 
 the steam rod moves to the right, the steam arm is picked up 
 and the valve is turned. After having lifted the steam arm a 
 certain distance, the hook is made to disengage -with the block 
 and the steam arm is released. 
 
 The steam arm is connected to the piston of a dash-pot by a 
 dash-rod. As the steam arm is raised, a partial vacuum is 
 formed in the dash-pot. When the steam arm is released from 
 the hook, it is suddenly pulled downward by the vacuum in the 
 dash-pot. As the steam arm is lifted, the valve opens and admits 
 steam to the cylinder. When it is pulled down, the valve is 
 closed suddenly, giving a quick cut-off. The time at which the 
 hook is made to release the steam arm is controlled by a cam 
 whose position is regulated by the governor. This cam engages 
 with the tail of the hook and causes the disengagement. At light 
 loads, the trip occurs soon and an early cut-off is given, and the 
 cut-off is retarded as the load of the engine is increased. 
 
 Figure 59 shows the trip mechanism on a larger scale. DAC 
 is the bell crank. As the point D moves backward and forward 
 in a nearly horizontal direction, the point C moves up and down 
 in a nearly vertical direction. The pin C carries the steam hook. 
 The tail of the hook engages with the knock-off cam, and its jaw 
 engages with the block attached to the steam arm at B. For 
 any one load the knock-off cam is stationary, and as C goes up, 
 the tail of the hook is pushed away from A by the cam, which 
 causes the latch to disengage with the block B. When there is 
 a heavy load on the engine, the governor rod moves to the left, 
 which raises the knock-off cam and makes the trip come later, 
 giving a long cut-off. There is also a safety cam, shown in Fig. 
 59. If the governor fails to rotate, the safety cam comes into 
 contact with the tail of the hook and prevents the picking up of 
 the steam arm and therefore causes a failure to admit steam to 
 the cylinder. 
 
 There is no disengagement between the exhaust arm and the 
 exhaust valve, so that the events of release and compression occur 
 
COMMON TYPES OF STEAM ENGINES 
 
 103 
 
 at the same ratio of the stroke for all loads. Both the steam 
 valve and the exhaust valve of Fig. 58 are double-ported, which 
 gives twice the opening for the passage of steam with the same 
 valve movement as with the single-ported type. 
 From the description just given it is seen that cut-off is inde- 
 
 To forer/ior 
 
 FIG. 59 
 
 pendent of the other events, and that the steam valve closes 
 quickly, thereby preventing wire-drawing at closing. If a care- 
 ful analysis of the motion is made, it will be seen that the steam 
 valve opens the port nearly as widely at light loads as at full 
 loads. The force necessary to operate the valve mechanism is 
 not large and the work done in moving the valves is a very small 
 part of the total output of the engine. 
 
 100. The Four-valve Engine. With a single slide-valve, 
 the changing of one event necessitates the changing of all the 
 others. To avoid this difficulty, engines are often made that 
 
104 
 
 ENGINES AND BOILERS 
 
 have four valves, a steam valve for each end of the cylinder, and 
 an exhaust valve on each end. The exhaust valves are driven 
 by a fixed eccentric, so that the release and compression are the 
 same at all loads. The steam valves are controlled by the gov- 
 ernor; hence cut-off and admission will vary for different loads. 
 
 f FIG. 60 
 
 Figures 60 and 61 show one style of four- valve engine. This par- 
 ticular engine has oscillating cylindrical valves similar to those 
 shown in Fig. 58 for the Corliss engine. Some makers, probably 
 to make use of the enviable reputation of the Corliss engine, call 
 this type a non-releasing Corliss. This engine lacks, however, 
 the distinct advantage of the trip found in the true Corliss type. 
 
 FIG. 61 
 
 101. The Compound Engine. When all the expansion of 
 steam takes place in one cylinder, we have what is known as a 
 simple engine. If the steam passes through two successive cyl- 
 inders, the engine is said to be a compound engine. If there are 
 three successive cylinders, it is called a triple-expansion engine. 
 
COMMON TYPES OF STEAM ENGINES 105 
 
 If there are four successive cylinders, it is called a quadruple- 
 expansion engine, etc. An engine may have two cylinders and 
 not be compound, i.e. it may be a twin-cylinder engine, in which 
 half the steam passes through one cylinder and half through the 
 other. Likewise a compound engine may have three cylinders, 
 all the steam passing through one high-pressure cylinder, and then 
 dividing, half passing through each of the two low-pressure 
 cylinders. 
 
 The purpose of compounding is to reduce the initial conden- 
 sation. It does not necessarily follow that there is a greater 
 ratio of expansion of steam in a compound engine than in a 
 simple engine, since that depends upon the point of cut-off. We 
 have seen that initial condensation is caused by the range in 
 temperature within the cylinder. The temperature range is less 
 in each cylinder of a compound engine than in the single cylinder 
 of a simple engine of the same capacity. Since the amount of 
 condensation does not vary directly as the total temperature 
 range, there may be considerably less total condensation if the 
 steam is passed through two successive cylinders than if all the 
 expansion occurred in one cylinder. 
 
 Several years ago the idea of compounding was very popular 
 and was carried to the extreme. Many triple-expansion engines, 
 and some quadruple-expansion engines, were built. Experience 
 proved, however, that there was a practical limit to which the 
 idea might be carried. Now stationary engines are seldom built 
 with more than two pressure-stages, except in direct -acting pumps. 
 In the marine service, the triple-expansion engine is still popular, 
 partly for the reason that it is desirable to have three cranks on 
 the same shaft to give a greater uniformity of torque on the pro- 
 peller shaft, and partly on account of the uniformity of load on 
 marine engines. Of the many types of compound engines that 
 have been built, only two are in common use in land service at 
 present. We shall proceed to consider these. 
 
 102. The Tandem-compound Engine. In the tandem-com- 
 pound engine, the pistons of the two cylinders are placed on the 
 same piston rod, as shown in Fig. 62. The cylinder to the left 
 is the high-pressure cylinder, and the one to the right is the low- 
 pressure cylinder. The steam ports of the high-pressure cylinder 
 are at a and 6; the exhaust ports of the low-pressure cylinder are 
 
106 
 
 ENGINES AND BOILERS 
 
 at c and d. The pistons, in Fig. 62, are shown moving to the 
 right. Steam is entering the high-pressure cylinder through a, 
 and leaving it through /. The exhaust steam from the crank end 
 of the high-pressure cylinder passes to the head end of the low- 
 pressure cylinder either directly or through a stationary vessel 
 called a receiver, i.e. the back pressure on the piston A is the 
 forward pressure on the piston B. On the return stroke, steam 
 
 FIG. 62 
 
 enters the port b and the exhaust from the high-pressure cylinder 
 leaves through e and enters the low-pressure cylinder at h either 
 directly or through the receiver. With the tandem arrangement 
 only one cross-head, connecting rod, crank, and frame are needed. 
 In locomotive work, the Baldwin or Vauclain compound engine 
 is sometimes seen. In this engine, the cylinders are placed side 
 by side, and both piston rods attach to the same cross-head. 
 The method of steam distribution is similar to that of the tan- 
 dem type. Figures 63 and 64 show the high-pressure and low- 
 
 FIG. 63 
 
 FIG. 64 
 
 FIG. 65 
 
 pressure indicator diagrams, as taken from a Baldwin compound 
 engine. The high-pressure card comes from the crank end of the 
 high-pressure cylinder and the low-pressure card from the head 
 end of the low-pressure cylinder. These cards were taken with 
 springs of different scales. Figure 65 shows the same diagrams when 
 drawn to the same scale of pressure. It is noticed that the back- 
 pressure line of the high-pressure card parallels the admission 
 line of the low-pressure card from the left end up to the point 
 of cut-off in the low-pressure cylinder. The reason for this is 
 
COMMON TYPES OF STEAM ENGINES 
 
 107 
 
 obvious, since the exhaust from the high-pressure cylinder passes 
 directly to the low-pressure cylinder. When the admission 
 valve of the low-pressure cylinder closes, compression must 
 necessarily start in the high-pressure cylinder. Since it is neces- 
 sary, with such a high pressure at exhaust as exists in the high- 
 pressure cylinder, to have the compression occur late, it follows 
 that cut-off must come very late in the low-pressure cylinder. 
 This is not an ideal condition, but it is necessary if no receiver 
 is placed between the two cylinders. If a receiver were placed 
 between the two cylinders so that it could act as a reservoir into 
 which to discharge, and from which to draw steam, it would not 
 be necessary to have the preceding relation between compression 
 and cut-off. 
 
 103. The Cross-compound Engine. In the cross-compound 
 engine (Fig. 66), each cylinder has its own cross-head, connect- 
 
 " 
 
 FIG. 66 
 
 ing rod, crank, and frame. The cranks are usually spaced 90 apart. 
 A by-pass is arranged so that the engine can be started even if 
 the high-pressure cylinder stops on dead center, by admitting 
 steam directly to the low-pressure cylinder. 
 
 Each cylinder has its own valve mechanism, and the exhaust 
 from the high-pressure cylinder passes into a receiver from which 
 the low-pressure cylinder takes its steam. This arrangement per- 
 mits a better steam distribution than that used in the tandem 
 
108 
 
 ENGINES AND BOILERS 
 
 type without a receiver. If the receiver is quite large, the back 
 pressure in the high-pressure cylinder during exhaust will be 
 nearly constant. Figures 67 and 68 show the indicator diagrams 
 from a cross-compound engine. It should be noticed that the 
 engine exhausts into a condenser. 
 
 104. Cylinder Ratio. The cylinder ratio of a compound engine 
 is the ratio between the piston displacements of the low-pressure and 
 the high-pressure cylinders. While it is not essential that the length 
 of stroke be the same for both high-pressure and low-pressure 
 
 cylinders of a cross- 
 compound engine, they 
 are made so. The cyl- 
 inder ratio is then the 
 ratio of the squares of 
 the diameters of the 
 low-pressure and high- 
 pressure cylinders. 
 
 105. The Combined 
 Indicator Diagram. 
 
 The combined diagram 
 is constructed by plot- 
 ting both cards to the 
 same scale of pressure 
 and volume. Usually 
 we do not change the 
 low-pressure diagram 
 but change the scale of 
 the high-pressure card 
 conform to it. Figure 
 69 shows the combina- 
 tion of diagrams of Figs. 
 67 and 68. The low- 
 pressure diagram is 
 identical with Fig. 68, while the length of the high-pressure dia- 
 gram equals the length of the low-pressure diagram divided by 
 the cylinder ratio. The high-pressure diagram is placed to the 
 right of the pressure axis its clearance distance, i.e. its distance 
 from the axis equals the ratio of the high-pressure clearance 
 times the new length of the high-pressure diagram. 
 
 Condenser Pressure. 
 
 FIG. 69 
 
COMMON TYPES OF STEAM ENGINES 109 
 
 106. Diagram Factor. The definition of the diagram factor 
 as given in the 1915 edition of the A. S. M. E. Power Test Code is 
 as follows : 
 
 The diagram factor is the proportion borne by the mean 
 effective pressure measured from the actual diagram to that 
 of a hypothetical diagram which represents the maximum power 
 obtainable from the steam accounted for by the actual diagram 
 at the point of cut-off; assuming first, that the engine has no 
 clearance; second, that there are no losses through wire- 
 drawing the steam either during admission or release; third, 
 that the expansion line is a hyperbolic curve; and, fourth, 
 that the initial pressure is that of the boiler, and the back 
 pressure that of the atmosphere for a non-condensing engine, 
 and of the condenser for a condensing engine. 
 To determine the steam accounted for by the actual diagram 
 at the point of cut-off, draw hyperbolic curves through the point 
 of compression P and the point of cut-off (Fig. 70) until they 
 
 FIG. 70 
 
 cut the boiler-pressure line at R and S. The length of RS 
 is the length of the admission line for the hypothetical diagram, 
 FA in Fig. 42, drawn to proper scale. The hypothetical diagram 
 is drawn as in Fig. 42 except that the boiler pressure is taken as the 
 initial pressure, release comes at the end of the stroke, the back 
 pressure is the atmospheric pressure (condensing pressure in a con- 
 densing engine), there is no compression, and there is no clear- 
 ance. The hypothetical diagram for the combined diagrams of 
 Fig. 69 is shown dotted. Since we assume there is no clearance, 
 the length of the hypothetical diagram is equal to that of the 
 low-pressure card. The distance RS at boiler pressure is deter- 
 mined from the high-pressure diagram, as in Fig. 70. From S 
 to T construct a hyperbolic curve, using the origin 0', and not 0. 
 Release is at the end of the stroke and the back-pressure line is 
 at the condenser pressure. 
 
*-*'*' /}b 
 i<$ CX^Trar 
 
 110 ENGINES AND BOILERS 
 
 In Fig. 69, the mean effective pressure of the combined dia- 
 grams and of the hypothetical diagram are in the same ratio as 
 the areas of the combined and hypothetical diagrams, because 
 they are of the same length. To find the diagram factor of the 
 combined cards, divide their area by the area of the hypothetical 
 diagram. 
 
 107. Ratio of Expansion. The A. S. M. E. Power Test 
 Code gives the following rule: 
 
 To find the percentage of cut-off, or what may best be termed 
 the commercial cut-off, the following rule should be observed: 
 
 Through the point of maximum pressure during admission 
 draw a line parallel to the atmospheric line. Through a point 
 on the expansion line where the cut-off is complete, draw a 
 hyperbolic curve. The intersection of these two lines is the 
 point of commercial cut-off, and the proportion of cut-off is 
 found by dividing the length measured up to this point by 
 
 e total length> 
 
 To find the ratio of expansion, divide the volume correspond- 
 
 bg to the piston displacement, including clearance, by the 
 olume of the steam at the commercial cut-off, including clear- 
 
 ance. 
 
 In a multiple-expansion engine the ratio of expansion is found 
 
 by dividing the volume of a low-pf essure cylinder, including 
 
 clearance, by the volume of the high-pressure cylinder at the 
 
 commercial cut-off, including clearance. 
 
 108. The Unaflow Engine. The unaflow, or uniflow, engine 
 is shown diagrammatically in Fig. 71. There is an admission 
 valve at each end of the cylinder. The exhaust steam escapes 
 through a port located around the circumference of the cylinder 
 midway between the two ends. The piston, which is longer than 
 in most engines, itself uncovers the exhaust port at about 90 
 per cent of the stroke. Compression must start when the piston 
 is at the same place on the return stroke. Under non-condensing 
 conditions this would give a very excessive compression pressure; 
 hence the engine normally is run condensing, under which con- 
 ditions the compression pressure is moderate. The thermal 
 efficiency is about the same as that of a compound engine. The 
 gain in efficiency over the ordinary double flow engine is due 
 to the reduction of initial condensation. The condensation 
 
COMMON TYPES OF STEAM ENGINES 
 
 111 
 
 is reduced with the unaflow principle because the ends of 
 the cylinder are kept hotter than the central portion. High- 
 pressure steam never comes in contact with the central part of 
 the cylinder and the flow of steam is from the ends toward the 
 middle. The exhaust steam passing out through the central port 
 does not cool the walls as much as it would if it flowed back to 
 
 the ends of the cylinder upon leaving. In actual engines, pro- 
 vision must be made for relieving the excessive compression pres- 
 sure, should the vacuum break. This is done by a relief valve 
 that adds to the clearance or allows the compressed steam to 
 re-enter the steam chest, or by adding an auxiliary exhaust port 
 nearer the end of the cylinder, which is opened automatically 
 when the vacuum fails. 
 
CHAPTER VIII 
 VALVES 
 
 109. Introduction. From our previous study of the steam 
 engine we have learned that the purpose of the valve is to admit 
 steam to the cylinder, and to release steam from it. The time 
 at which the events occur must be such that the engine is capable 
 of doing the work required, and that it may have as high an 
 efficiency as possible under the conditions of operation. An en- 
 gine may run with the valves improperly set or designed, but 
 more steam will be used than if the valves functioned properly. 
 
 110. The D Slide-valve. The engine of Fig. 39 has what 
 is commonly known as a D slide-valve. The valve slides back 
 and forth on its seat, alternately opening and closing the ports. 
 An eccentric on the shaft drives the valve. The eccentric rod 
 is usually quite long in comparison with the throw of the eccen- 
 tric, so that the valve may be considered to have the same motion 
 as the horizontal component of the eccentric. 
 
 In Fig. 72a, the valve is shown in mid-position; consequently 
 the eccentric will either be directly above or directly below the 
 center of the shaft. In mid-position, the valve laps over the 
 edges of the port; the amount it extends over on the steam side 
 is called the steam lap, and on the exhaust side, the exhaust lap. 
 
 At the right side of Fig. 72a is shown the relative position of 
 the eccentric and the crank. The eccentric leads the crank by 
 angle 8. This angle 8 will be the same at all times during the 
 revolution. In Fig. 726, the crank is on head-end dead center, 
 and the valve is uncovering the head-end port a small amount. 
 The amount the port is open when the crank is on dead center 
 is called the lead. It is measured in inches. The valve in Fig. 
 726 is to the right of its mid-position by an amount equal to the 
 steam lap plus the lead. In moving from the position shown 
 in Fig. 72a to that in Fig. 726, the eccentric has moved a hori- 
 zontal distance equal to the steam lap plus the lead, and has turned 
 through a certain angle which is called the angle of advance. 
 It is evident that the eccentric is ahead of the crank by an angle 
 of 90 plus the angle of advance. It is customary to speak of 
 the angle of advance and -not of the whole angle 6. 
 
 Figure 72c shows the valve at head-end admission. The valve 
 
 112 
 
VALVES 
 
 113 
 
 FIG. 72 
 
114 ENGINES AND BOILERS 
 
 is on the point of opening the head-end port for the admission 
 of steam, and is traveling to the right. In the admission posi- 
 tion it is to the right of its mid-position by a distance equal to 
 the steam lap. 
 
 Likewise the eccentric will be to the right of its mid-position 
 by a horizontal distance equal to the steam lap. The crank 
 is back of the eccentric by the angle 6 and is seen to be 
 approaching its head-end dead-center position. If there is 
 any lead, the crank will never be quite up to its dead-center 
 position at admission. 
 
 At head-end cut-off, Fig. 72d, the valve is to the right of its 
 mid-position by a distance equal to the steam lap and its direc- 
 tion of motion is to the left. The position is the same as for 
 admission, but it is going in the opposite direction. The eccen- 
 tric is now below the center line of the shaft. 
 
 Figures 72e and 72/ show the relative positions at head-end 
 release and compression. At both of these events, the valve is 
 at the left of mid-position by an amount equal to the exhaust- 
 lap distance. It is moving to the left at release and to the right 
 at compression. 
 
 In all the six diagrams of Fig. 72, the positions of the piston 
 and its direction of motion are shown. The cylinder section in 
 each diagram is in a horizontal plane and therefore is at an angle 
 of 90 from the diagram showing crank and eccentric positions 
 
 For an understanding of the slide-valve and the analyses to follow, 
 it is essential that the student have a precise conception of the rel- 
 ative positions of the valve on the seat, the eccentric and the crank 
 relative to the center positions, and the position of the piston in the 
 cylinder. 
 
 111. Relative Motion of Crank and Piston. Since the con- 
 necting rod is not very long compared with the crank arm, we 
 cannot assume that the horizontal movement of the crank is the 
 same as the piston movement. This is clearly seen from the 
 diagram in Fig. 73. As the crank moves from A to C, the cross- 
 head moves from E to D. That part of the stroke completed 
 by the cross-head is a'. It is evident that a' is considerably 
 larger than the horizontal movement of the crank in going from 
 A to C. 
 
 In our analysis of valve motions, it is not customary to draw 
 
VALVES 115 
 
 in the cross-head D to find the proportion of the stroke at dif- 
 ferent crank positions, but the following scheme is used. The 
 horizontal diameter of the crank circle AB is extended to the 
 left. With the length of connecting rod DC as a radius at the 
 desired scale, and with D as a center, strike the arc shown by 
 the dotted line CG. This gives the distance AG = a, on the diame- 
 ter of the crank circle, that is equal to ED = a', the movement of 
 
 FlG. 73 
 
 the piston or cross-head from E to D. In the valve analysis it 
 is not necessary to draw the crank circle to any particular scale 
 if we keep the proper ratio between the lengths of the crank and 
 the connecting rod. This ratio usually is expressed as R/L. 
 No matter what the scale of the crank circle may be, the ratio of 
 a to the length of stroke will be constant. 
 
 112. Valve Diagrams. Many diagrams have been used to 
 show graphically the relation of the movement of the valve to 
 the movement of the piston, or of the relative movements of 
 eccentric and crank. Only those most commonly used in this 
 country will be explained here, i.e. the valve ellipse, the Bil- 
 gram diagram, and the Zeuner diagram. 
 
 113. The Valve Ellipse. In this diagram the system of rec- 
 tangular coordinates is used. The valve displacement is plotted 
 vertically and the piston displacements are plotted horizontally. 
 On the left of Fig. 74 is shown a crank and eccentric. The eccen- 
 tric is ahead of the crank by 90 plus a. 
 
 With the crank at C, the piston is at a distance x from the cen- 
 ter of the stroke. At the same time, the valve is at a distance y 
 from its mid-position. If we plot x against y, we get a point G. 
 
116 
 
 ENGINES AND BOILERS 
 
 The coordinate axes are the horizontal and vertical diameters 
 of the crank circle. 
 
 On the right of Fig. 74 this same operation is carried out for 
 twelve crank positions with their corresponding eccentric posi- 
 tions. The crank positions are denoted by Ci, 2, C%, etc., and 
 the corresponding eccentric positions by E\, E^ E%, etc. Plotting 
 the displacements, we get the points 1, 2, 3, etc. Connecting the 
 points thus found by a smooth curve, we get what is known as 
 a valve ellipse. It is evident from Fig. 74 that this is not a true 
 
 fro re/ ' ~ - -^ 
 
 FIG. 74 
 
 ellipse. It would have been but for the distortion due to the 
 short length of the connecting rod. 
 
 The upper half of the ellipse ABD represents the valve move- 
 ment to the right of its mid-position. The lower half, DFA, 
 represents the valve movement to the left of its mid-position. 
 From A to B it gives the movement from mid-position to ex- 
 treme right; from B to D, from the extreme right to mid-posi- 
 tion; from D to F from mid-position to extreme left; and F to 
 A, from the extreme left to mid-position. 
 
 The valve ellipse of Fig. 74 is reproduced in Fig. 75. Four 
 horizontal lines are drawn through the ellipse. The head-end 
 steam lap is the distance from the top line to the horizontal axis. 
 The crank-end steam lap is the distance from the bottom line 
 to the axis. The head-end exhaust-lap line is drawn below the 
 axis and the crank-end exhaust-lap line above. When the valve 
 has moved to the right a distance equal to the head-end steam 
 lap, head-end admission takes place. Admission is shown by the 
 
VALVES 
 
 117 
 
 point H on the ellipse, and the crank position corresponding to 
 H is determined by projecting vertically from H to the axis. 
 
 As the valve moves from its extreme right position back to 
 mid-position, head-end cut-off takes place. This is shown by the 
 point / on the ellipse. The crank position corresponding to I is 
 found by projecting down from I to the axis and striking an 
 arc upward from this point to the crank circle. The radius of 
 the arc is the length of the connecting rod. In like manner, the 
 
 A 
 
 fxg/w 
 
 Ce.mof.ft.0. 
 
 FIG. 75 
 
 crank position at head-end release is found from the intersection 
 of the head-end exhaust-lap line with the ellipse at J. 
 
 The head-end compression point is at M , where the exhaust- 
 lap line cuts the ellipse. The crank-end events are determined 
 from the points K, L, N, and P. The vertical distance from the 
 top point of the ellipse to the head-end steam-lap line is the head- 
 end maximum port-opening, and the head-end lead is given by 
 the distance from the extreme left point of the ellipse to the 
 head-end steam-lap line. The crank-end maximum port-opening 
 and lead are found in a similar manner. 
 
 In actual use, the ellipse is rather burdensome because it takes 
 considerable time to construct it. It is evident also that the 
 crank position at admission is not easily determined with accuracy. 
 The ellipse is little used except in locomotive work. 
 
 114. The Bilgram Diagram. On the left of Fig. 76, the 
 crank and the eccentric are shown by C and E, respectively. 
 The displacement of the valve from mid-position is y. The dis- 
 tance y is laid off perpendicular to the crank, and a line is drawn 
 parallel to the crank 'at a distance y from it. 
 
118 ENGINES AND BOILERS 
 
 At the right of Fig. 76, this has been done for twelve crank 
 positions. It is seen that these lines all pass through two points 
 P and P', and that a line drawn from P to P' passes through the 
 center of the crank circle and makes an angle a with the hori- 
 zontal. Hence the perpendicular distance from the points P or 
 P' to the crank at any position is the distance that the valve 
 is from mid-position. The points P and P' are called the con- 
 struction points in the Bilgram diagram. 
 
 Figure 77 shows the application of the Bilgram diagram. 
 About the point P draw two circles, one whose radius is equal 
 to the head-end steam lap, and the other with a radius equal 
 
 FIG. 76 
 
 to the head-end exhaust lap. Draw the crank-end lap circles 
 with center at P'. The crank positions tangent to these lap 
 circles give the positions at the different events. Head-end ad- 
 mission occurs when the valve is at a distance from its mid- 
 position equal to the head-end steam lap, and when the valve 
 is going away from its mid-position. The head-end admission 
 position shown in Fig. 77 fulfills these conditions. At that 
 time the crank is at a distance from the point P equal to the 
 head-end steam lap, and further motion moves it farther from P. 
 The crank position at head-end cut-off is tangent to the head-end 
 steam-lap circle on the other side, i.e., the valve is then at a dis- 
 tance equal to the steam lap from mid-position and further mo- 
 tion brings the valve nearer mid-position. 
 
 The crank positions for the other events are shown in Fig. 77. 
 Reasoning similar to the preceding will show them to be correct. 
 It is customary to draw the head-end lap circles about P, and the 
 
VALVES 
 
 119 
 
 crank-end lap circles about P f , although there is no inherent 
 reason for so doing. 
 
 Half of the valve-travel minus the steam lap equals the maxi- 
 mum port opening if the valve has no over-travel, i.e. if it does 
 not move beyond the far edge of the port. Therefore the maxi- 
 mum port-opening is as shown in the figure; It is remembered 
 that the port is open a distance equal to the lead when the 
 crank is on dead center. In other words the valve is then at a 
 distance equal to the steam lap plus the lead from its mid-position. 
 Therefore the perpendicular distance of P from the horizontal 
 
 c,e. t a 
 
 FIG. 77 
 
 axis is equal to the steam lap plus the lead. The distance of 
 the steam-lap circle from the axis is then s the lead. 
 
 115. The Zeuner Diagram. On the left of Fig. 78, the valve 
 displacement y is laid off radially on the crank from the center 
 outward. This gives a point G on the crank. This has been done 
 for twelve crank positions on the right of Fig. 78 and the points 
 connected by a smooth curve. The points fall on the circum- 
 ferences of two equal circles, the diameter of each of which is 
 one-half the valve-travel. The line which forms the diameters 
 of these two circles makes an angle a with the vertical. The 
 
120 
 
 ENGINES AND BOILERS 
 
 circle whose center is at A shows the movement of the valve to 
 the right of its mid-position, and is called the right valve-circle. 
 The other circle is called the left valve circle; it shows the move- 
 ment of the valve to the left of the mid-position. When the 
 crank is drawn in any position, the displacement of the valve 
 is given by the distance from the center of the crank circle to 
 the intersection of the crank with the valve circle. 
 
 The application of this diagram is shown in Fig. 79. With 
 the crank on head-end dead center, the eccentric is at E, at an 
 angle a to the right of the vertical. The diameters of valve 
 circles, P'P', are at an angle a on the other side of the vertical. 
 
 FIG. 78 
 
 The extremity P of the diameter of the valve circle is called the 
 construction point in the Zeuner diagram. The lap circles are 
 drawn as shown. The head-end steam-lap circle intersects the 
 right valve-circle at the point T. The crank position through 
 T is then head-end admission, because with the crank in this 
 position the valve is at a distance equal to the steam lap to the 
 right of mid-position. The crank position at cut-off is drawn 
 through the point K, where the steam-lap circle intersects the 
 right valve-circle. Head-end release and compression occur when 
 the head-end exhaust-lap circle intersects the left valve-circle. 
 
 It may be proved by means of the similar triangles OWE and 
 PRO or by actual construction that a line drawn from A to B is 
 tangent to the steam-lap circle at W . This line is perpendicular 
 to the diameter of the valve circles. In like manner a line drawn 
 from I to F is tangent to the head-end exhaust-lap circle, and is 
 perpendicular to the diameter of the valve circles. The same 
 thing is true of the lines HG and JD for the crank end. It is 
 
VALVES 
 
 121 
 
 often better to draw the lines A B, IF, HG, and JD than to 
 determine the crank positions at the events by the intersections 
 of the valve circle and the lap circle. 
 
 ON is equal to the steam lap plus the lead, because the valve 
 circle cuts the crank on dead center at N. But ONP is a right 
 triangle, since it is inscribed in a semicircle. If QS is drawn 
 parallel to AW, the triangle OSQ is a right triangle, and it is 
 similar and equal to the triangle, ONP. Therefore OS is equal 
 
 Right w/re ctrck 
 
 be. c.o. 
 
 fivnfr circle 
 Eccentric c/n,/e 
 
 4t. comp 
 t.rel. 
 
 ce. co.- 
 
 c/rc/e 
 
 FIG. 79 
 
 to the steam lap plus the lead, and WS is equal to the lead. If 
 we then draw a circle about Q as a center, tangent to the line 
 AW, its radius is the lead. This is called the head-end lead 
 circle. The crank-end lead circle is drawn about X tangent to 
 HG. The head-end maximum port opening equals PW, which is 
 one-half the valve-travel minus the steam-lap. The line PK is 
 perpendicular to the crank at cut-off, because PKO is a right 
 angle since it is inscribed in a semicircle. 
 
 The application of these valve diagrams to practical problems 
 will show their value. Space will not be taken here to give the 
 solutions of the various common problems in which these dia- 
 grams are used. The Bilgram and Zeuner diagrams are both 
 
122 
 
 ENGINES AND BOILERS 
 
 
 adapted to problems of valve setting, but the Bilgram diagram is 
 the more convenient for use in designing valve gears. 
 
 116. Types of Slide-valves. The simple D slide-valve has 
 been discussed and its action explained. This type of valve is 
 much used, but it has certain defects which have been overcome 
 in other types. One of the defects of the simple D valve is the 
 large force necessary to move it when high steam pressure is used. 
 The steam pressure on the back of the valve presses it against 
 the seat. This pressure times the coefficient of friction between 
 the valve and the seat is the force that must be exerted to move 
 the valve. The work done in operating the valve is the force 
 times the distance the valve is moved. If either the force or the 
 distance is decreased, the work necessary to operate the valve will 
 be lessened. 
 
 117. Valve with Pressure Plate. The pressure on the back 
 of the valve may be removed by putting a pressure plate above 
 it, somewhat in the manner shown in Fig. 80. A steam-tight fit 
 
 between the valve and the 
 plate is made by strips set into 
 s | ots j n t h e va i v e. These are 
 pressed up against the plate 
 by springs from beneath, and 
 they act in much the same way 
 as rings on a piston. If any 
 steam leaks by the strips, it 
 may escape to the exhaust 
 through a vent in the valve. 
 This scheme enables us to remove as much of the pressure from 
 the back of the valve as we desire, but some pressure downward 
 is desirable in order to keep the valve firmly seated. Many flat 
 slide-valves have pressure plates. Aside from removing the pres- 
 sure, the plate does not affect the valve in any way. 
 
 118. The Piston Valve. Instead of a flat valve such as we 
 have considered, a piston valve is used extensively. Figure 81 
 shows a form of this type where the valve is cylindrical and slides 
 in a cylindrical chamber. It is readily seen that it is perfectly 
 balanced, since the steam causes no thrust either endwise or 
 on the seat. Piston valves are very easy to operate, but are 
 liable to leak steam when they become worn. Many of them 
 
 FIG. 80 
 
VALVES 
 
 123 
 
 have rings similar to piston rings to keep this leakage of steam 
 to a minimum. If rings are used it is necessary to bridge the 
 ports. A broken ring is liable to cause severe damage and care 
 must be exercised to keep them in good condition. 
 
 In Fig. 81, the steam is led to the inside of the valve, so that 
 the steam lap is on the other side of the port from the valves 
 previously considered. A valve so constructed is said to be an 
 
 FIG. 81 
 
 indirect valve, or to have inside admission. Most piston valves 
 have inside admission, but this is not a necessity. It is easier 
 to keep the stuffing-box tight against exhaust steam than against 
 high-pressure steam. With the inside admission arrangement, 
 also, the live steam has less surface exposed to radiation. With 
 an inside admission valve, the eccentric follows the crank by an 
 angle of 90 a. The valve diagrams studied will have the same 
 form as before, but what was right-hand is now left-hand, i.e. 
 in the Zeuner diagram, for instance, what was formerly the right 
 valve-circle is now the left, but otherwise there is no change in 
 the diagram and no difference 
 is made in the solution of a 
 problem. 
 
 119. Double-ported Valves. 
 As has just been mentioned, 
 the work required to move the 
 valve is the product of the 
 force required to move it and 
 the distance it is moved. The 
 
 distance may be cut in half by making the valve double-ported. 
 Figure 82 shows a so-called double-ported valve. It is seen that 
 for a certain valve movement twice the area for the passage of 
 steam is given in this type compared with a simple slide-valve. 
 There are many different forms of double-ported valves, but they 
 are much the same in principle as that shown in Fig. 82. 
 
 FIG. 82 
 
124 ENGINES AND BOILERS 
 
 120. The Gridiron Valve. If the idea of a double-ported 
 valve is carried a step farther, we may get a very large aggregate 
 opening for the passage of steam with but a small movement 
 of the valve. Figure 83 shows a gridiron valve. In many valves 
 of this type there are a large number of openings, whereas Fig. 83 
 shows only three. A valve of this character can have no exhaust 
 functions, and separate exhaust valves must be provided. If one 
 exhaust valve takes care of both ends of the cylinder, the engine 
 is called a two-valve engine; if there is a separate exhaust valve 
 
 FIG. 83 
 
 for each end, it is called a three-valve engine. When gridiron 
 valves are used, it is more common to have a steam valve and 
 an exhaust valve for each end of the cylinder. The engine 
 then has four valves. 
 
 If a governor is so constructed that it regulates the amount 
 of steam admitted to the cylinder by changing cut-off, it is evi- 
 dent from the valve diagrams that the events of release, com- 
 pression, and admission are changed when cut-off is changed if 
 a single valve is used. Under some conditions this is a serious 
 defect, and it makes the use of separate steam and exhaust valves 
 desirable. 
 
 121. The Riding Cut-off Valve. To utilize the expansive 
 force of the steam in an engine, it is necessary to have an early 
 cut-off. With a single valve, early cut-off will necessitate either 
 early release or early admission. With an early cut-off and with 
 release near the end of the stroke, compression is bound to occur 
 too soon for satisfactory operation under non-condensing con- 
 ditions. The student only needs to draw a valve diagram to con- 
 vince himself of this fact. To use an early cut-off, and to have 
 at the same time reasonable percents of release and compression, 
 
VALVES 
 
 125 
 
 a riding cut-off valve is often used. There are several forms of 
 riding cut-off valves, but we shall describe only one of them. 
 
 Figure 84 shows the Myers riding cut-off valve. A main valve 
 slides on the seat in the same manner as an ordinary D valve. 
 The steam lap is made small so that the proper relation exists 
 between the events of admission, release, and compression. If 
 the main valve were acting alone, cut-off would occur very late. 
 To give an early cut-off, a rider valve which controls only the 
 event of cut-off is placed on the back of the main valve. The 
 working edge of the rider valve effects cut-off when it matches 
 with the edges of the main valve at B and at D. 
 
 In Fig. 84 both valves are shown in their mid-position. This 
 would not occur normallv unless one of the valves were discon- 
 
 FIG. 84 
 
 nected from its eccentric, but the figure is drawn in this manner 
 to give a clearer idea of the laps. Each valve is driven by its 
 own eccentric. The rider valve is made in two parts and the 
 relative position of the two parts may be changed by revolving 
 the valve stem. One part of the rider valve is secured to the 
 valve stem by a right-hand thread and the other part by a left- 
 hand thread. The hand wheel to the left is arranged so that by 
 turning it the valve stem is rotated and the parts of the valve 
 are brought nearer together or moved farther apart, thereby 
 effecting a change in cut-off. With the parts farther apart, cut- 
 off occurs earlier. When the valves are both in mid-position, 
 as shown in Fig. 84, it is easily seen that the rider valve has 
 negative steam lap or steam clearance. 
 
 To determine the crank position at cut-off from the valve dia- 
 grams, it is necessary to consider the relative motion of the two 
 valves. Figure 85 is the Zeuner analysis for the rider valve. 
 The crank circle and the two eccentric circles are shown by the 
 light lines. The point PI is the extremity of the diameter of the 
 
126 
 
 ENGINES AND BOILERS 
 
 right valve-circle for the main valve, and a\ is the angle of ad- 
 vance for the main eccentric. The point P% is the extremity of 
 the diameter of the right valve-circle, and a 2 is the angle of advance 
 for the rider-valve eccentric. If a number of crank positions be 
 chosen and the displacement of the rider valve relative to the 
 main valve be laid off on the crank from the center radially 
 outward, a number of points will be established. Connecting 
 
 Relative 
 ffiqht l/e/ve Ctrt/e 
 
 C.e. f?/cfer fa/re 
 Steam top (neyafiri) 
 
 ff/JfrVafoe 
 c.e a/t-o/f. 
 
 FIG. 85 
 
 these points by a smooth curve, we find that it is composed of 
 the two circles shown by heavy lines in Fig. 85. The point PS 
 is the extremity of the diameter of the right relative valve-circle 
 and 3 is the angle which that diameter makes with the vertical. 
 
 It is seen that the diameter of the right relative valve-circle, 
 OPs, is equal in amount and parallel to the dotted line PiP2. 
 Knowing this fact, the solution of a rider-valve problem is quite 
 simple, for it is not necessary to plot the points to determine 
 the relative valve-circle. 
 
 Since the steam lap for the rider valve is negative, the intersec- 
 tion of that lap circle with the left valve-circle gives the crank 
 position at head-end cut-off. The cut-off positions of the crank 
 are shown by the heavy lines in Fig. 85. The crank positions 
 for admission, release, and compression are determined from a 
 valve diagram for the main valve in exactly the same manner as 
 previously explained for the D valve. 
 
 122. Effect of Rocker Arm on Location of Eccentric. In 
 
 the previous discussion of slide-valves, it has been supposed that 
 
VALVES 
 
 127 
 
 the eccentric rod is attached directly to the valve rod, and that 
 the movement of the valve is the same as the horizontal move- 
 ment of the eccentric. Quite often a rocker arm is interposed 
 between the eccentric and the valve rods, in which case it may 
 be necessary to modify our previous assumption. 
 
 In Fig. 86, three arrangements of rocker arms are shown. In 
 I, the eccentric rod and the valve rod are both connected to the 
 same pin at B, and our assumption is not changed. 
 
 In II, the arm B AC reverses the motion of the eccentric. In 
 this case, if a direct valve is used, the eccentric must be placed 
 on the shaft at 180 from the position it would have had without 
 the rocker arm, i.e. if a direct valve is used, the eccentric must 
 follow the crank by an angle of 90 a. 
 
 If an indirect valve is used with a reversing rocker, the eccen- 
 
 Eccentr/e /foe/ 
 
 Eccentric flotf 
 
 n 
 FIG. 86 
 
 m 
 
 trie is placed 90+ a ahead of the crank. This modification does 
 not effect the work in making the valve analysis. 
 
 In case III, the two arms of the rocker AB and AC are not 
 of the same length. The travel of the valve is the diameter of 
 the eccentric circle times AB/AC. 
 
 123. Oscillating Valves. One of the most common valves is 
 cylindrical and oscillates or rocks on a cylindrical seat. A spindle 
 fastened to the valve extends out of the steam chest and carries 
 an arm that is moved back and forth by the eccentric. The 
 Corliss valve shown in Fig. 58 and the valves of Figs. 60 and 61 
 are of this type. It would be possible to make an oscillating 
 valve control both the admission and exhaust events, but this is 
 seldom done. Where the oscillating valve is used, four valves 
 usually are employed. Because of the distortion of motion due 
 to the valve arm, it is not possible to show by the valve diagrams 
 
128 
 
 ENGINES AND BOILERS 
 
 the exact motion of the valve. However, the relation of horizontal 
 motion of the eccentric still holds, and so the valve diagrams are 
 of value in the analysis of these valves. 
 
 124. Poppet Valves. While they are not common for steam 
 engines in this country, most gasoline engines are equipped with 
 poppet valves. This is a lifting valve and there is no sliding of 
 the valve on the seat. Figure 87 shows this type of valve. These 
 valves do not have to be lubricated and would seem to be well 
 adapted to conditions where highly superheated steam is used, 
 since one of the troubles met with in the use of superheated steam 
 is the difficulty of proper lubrication of the valve. Where poppet 
 
 valves are used on steam engines, 
 they usually are operated either by a 
 cam or by an eccentric from a lay 
 shaft that is parallel to the axis of 
 the cylinder. The lay shaft usually 
 is driven by mitre gears from the 
 main shaft. 
 
 125. Reversing. The direction of 
 rotation of an engine may be changed 
 FIG. 87 by shifting the eccentric to the proper 
 
 position. Occasionally an ordinary 
 
 engine must be reversed. Unless the eccentric is keyed to the 
 shaft, this is not usually a difficult task. With a direct valve, 
 the eccentric leads the crank by an angle of 90+ a. This is true 
 irrespective of the direction of rotation. To reverse, then, move 
 the eccentric in the direction the engine has been running through 
 an angle of 180 2 a. The same rule applies with an indirect or 
 inside-admission valve. 
 
 With certain classes of engines, such as are used for locomotives, 
 in marine work, etc., reversing is a common occurrence. Some 
 handier and quicker means must then be provided than that men- 
 tioned above. The devices used for this purpose are called re- 
 versing gears. There are a very great many types of reversing 
 gears in use, but space will not permit the discussion of more 
 than the most common types. 
 
 126. The Stephenson Link. One of the most widely used 
 reversing gears is the Stephenson link gear, which is much used 
 for small locomotives. In this arrangement, there are two ec- 
 
VALVES 
 
 129 
 
 Gentries placed on the shaft at an angle of 180 2 a apart. The 
 forward eccentric controls the forward motion, and the back- 
 ward eccentric controls the reverse motion. In the diagram of 
 Fig. 88, the crank is shown on head-end dead center, and the 
 valve is indirect, so that the eccentrics will be at an angle of 90 a 
 
 FIG. 88 
 
 from the crank. In Fig. 88, FE is the forward eccentric, and 
 BE the backward eccentric. The two eccentric rods connect to 
 the eyes of a link at H and I. This link may be raised or low- 
 ered by the bell-crank BAD and the link DJ. When the link 
 is down, as shown in Fig. 89, the forward eccentric entirely con- 
 trols the motion of the valve. With the link all the way up, the 
 backward eccentric controls the valve. In Fig. 88, the link is 
 
 FIG. 89 
 
 shown in mid-position with both eccentrics controlling an equal 
 amount. With the crank on head-end dead center as in Fig. 88, 
 the valve is as far to the left as it can get, the port is open a dis- 
 tance equal to the lead, and the valve is at a distance equal to 
 the steam lap plus the lead from its mid-position. With the 
 
130 
 
 ENGINES AND BOILERS 
 
 valve opening only lead distance, the engine will not get enough 
 steam to run. At mid-gear, half the travel of the valve is equal 
 to the steam lap plus the lead. 
 
 With the link in some position between those shown in Figs. 88 
 and 89, both eccentrics will control the motion of the valve, but 
 the forward one will predominate, and the engine will run for- 
 ward. The cut-off will now be earlier than it would be if the 
 link was all the way down in full gear. It is evident that the 
 Stephenson gear may be used to change the cut-off as well as to 
 reverse. 
 
 It is possible to give the same motion to the valve 
 with the link in intermediate position, by a simple equivalent 
 eccentric. The method of determining this equivalent eccentric 
 is not difficult but it will not be discussed here. 
 
 127. The Walschaert Valve Gear. Most large locomotives 
 in this country are equipped with the Walschaert gear, or some 
 
 FIG. 90 
 
 similar reversing gear. In this type of gear, shown in Fig. 90, 
 the motion of the valve is derived partly from the cross-head, 
 and partly from a return crank or eccentric. That part of the 
 motion coming from the cross-head is constant, while that de- 
 rived from the eccentric is varied for different conditions of load 
 and direction of rotation. Since the eccentric is placed outside 
 the driver, it is commonly called a return crank. The bar CE 
 is fastened to the outer end of the crank pin C, and the eccentric 
 pin E moves in the dotted circle (Fig. 90), about as a center. 
 
VALVES 131 
 
 The angle between the crank and the eccentric is 90. The hori- 
 zontal motion of the eccentric is transmitted through the eccen- 
 tric rod EM to the lower point of a link. The link is pivoted 
 at its center G to the frame of the engine, so that the point M 
 oscillates about the point G. In this link is fitted a block which 
 can be raised or lowered in the link by the bell crank DAB. 
 As shown in the dotted position, the block is at its lowest posi- 
 tion in the link, and the engine is running forward, taking steam 
 during the largest possible part of stroke. In the full line posi- 
 tion, the block is at the center of the link, and the engine will 
 not get enough steam to drive it. With the block in mid-position 
 in the link, the eccentric will give no motion whatever to the 
 valve. Under this condition the motion of the valve comes 
 entirely from the cross-head. 
 
 The lever HIJ is called the combination lever, because it com- 
 bines the motion from the eccentric with the motion from the 
 cross-head. The ratio I H/JH is fixed by the condition that 
 
 I H __ 2(steam lap plus lead) 
 J H length of stroke 
 
 With the block in the center of the link at G, H has no horizontal 
 motion, but the horizontal motion of / is equal to 
 
 length of stroke X I H n , , , , , ,. 
 
 T-PT - = 2 (steam lap plus lead). 
 
 J ti 
 
 As the motion of the valve at mid-gear is 2 (steam lap plus lead), 
 it is seen that the valve will open only a distance equal to the 
 lead on each end, and the engine will not get enough steam to 
 run. When the block is dropped to the dotted position, the point 
 H does have a horizontal motion which comes from the eccen- 
 tric, and with the engine running in the direction shown, the 
 horizontal motion of H will add to the port opening. To reverse, 
 the block is raised above the center of the link. 
 
 By changing the position of the block in the link we may get 
 not only a reversal of direction of rotation but also a change in 
 cut-off. As in the Stephenson gear, it is possible to find an equiv- 
 alent eccentric which would give the motion actually obtained 
 from the mechanism. 
 
132 ENGINES AND BOILERS 
 
 128. The Joy Valve Gear. The Joy gear is a so-called radial 
 gear. Unlike those previously described, it has no eccentric. 
 Figure 91 shows diagrammatically the principle of its operation. 
 A point such as D on the connecting rod FC will move in the 
 path of an ellipse, which is shown dotted. A bar BED is pinned 
 to the connecting rod at D. The other end of the bar is con- 
 nected to the frame of the engine by the link AB, A being a point 
 on the engine frame. It is evident that a point E on this 
 bar will have a combination of the elliptic motion of D 
 and the nearly vertical motion of B. The path of E is shown 
 dotted. A bar EGH is connected to BED by the pin E. The 
 point G is in a block which is at liberty to slide along a curved 
 
 FIG. 91 
 
 link. At any particular cut-off this link is held stationary, and 
 the block G slides up and down in it. It is thus seen that the 
 point H gets a combination of the motions of the point E and 
 of the point G. The horizontal component of the motion of H 
 is transmitted through the link I H to the valve. By rotating 
 the link about its center J, a reversal in the direction of rotation 
 of the shaft may be obtained. As in the other gears, cut-off 
 may be varied as well as the engine reversed. 
 
 Under conditions of light load an early cut-off may be used 
 and sufficient power obtained if the steam is not throttled between 
 the boiler and the engine. It is the practice on locomotive engines 
 to vary the cut-off to suit the load under normal running condi- 
 tions. The power generated by the engine might also be regu- 
 lated by throttling the steam, but it has been found that a higher 
 efficiency is obtained at light loads by using an early cut-off 
 
VALVES 133 
 
 than by using a late cut-off and a low steam pressure, especially 
 where valve gear is used which increases compression when cut- 
 off is shortened, as in the Stephenson gear. In the reversing 
 gears commonly used, an early cut-off is accompanied by an early 
 compression. The increased efficiency at light loads is due, how- 
 ever, more to the early cut-off than to the high compression, 
 although the high compression aids by heating the clearance 
 space, piston, and cylinder head, thereby keeping initial conden- 
 sation within more reasonable limits. 
 
 129. Setting the Slide-valve. On a small engine that can 
 be turned over easily by hand, the setting of a slide-valve is a 
 simple matter. With proper valve setting an engine should run 
 smoothly, should be easy to start, and each end of the cylinder 
 should furnish about half the power. If an indicator is at hand, 
 it should be employed in the setting. If no indicator is available, 
 the valve may be set by linear measurement. In the setting of 
 a slide-valve there are but two things to do, shift the eccentric on 
 the shaft, and lengthen or shorten the valve stem or rod. 
 
 VALVE SETTING BY INDICATOR. In order to get approximately 
 the same amount of work from each end of the cylinder, cut-off 
 for the two ends should be about the same. A rough adjust- 
 ment may be made easily by placing the eccentric somewhere 
 near its proper position, and adjusting the position of the valve 
 on the rod so that the engine may be started. After the engine 
 is started, take cards and then adjust the length of the valve 
 stem until the cut-off is the same percent on both ends. Next, 
 shift the eccentric until the desired percentage of cut-off is attained. 
 Shifting the eccentric ahead makes cut-off come earlier. By the 
 use of the indicator it is easy to get the exact setting desired. 
 
 Knowing the valve-travel and the dimensions of the valve, we 
 may compute by means of the Zeuner valve diagram the exact 
 amount the valve stem must be lengthened or shortened and the 
 angle the eccentric must be shifted to give a desired setting. 
 In the upper part of Fig. 92 are shown two cards taken with a 
 valve as now set. It is desired to change the setting so that 
 cut-off will be 50 per cent for each end. The cards are shown 
 in length equal to the valve-travel, but they need not have been, 
 as the percentages of stroke could have been scaled and the 
 corresponding crank positions found. 
 
134 
 
 ENGINES AND BOILERS 
 
 From the cards, locate on the crank circle (assumed for con- 
 venience with its diameter the same as that of the valve-travel 
 circle), the crank positions at the different events. Draw lines 
 between the crank positions at admission and cut-off, and from 
 release to compression, for each end. The distance between the 
 admission-cut-off lines should be the sum of the steam laps as 
 measured on the valve itself. A radial line drawn perpendicular 
 to the line joining admission and cut-off establishes the angle of 
 advance a\. The laps may be measured from the diagram as 
 shown. Now construct a Zeuner diagram (Fig. 93) for the desired 
 
 c.e.ad/n 
 
 FIG. 92 
 
 FIG. 93 
 
 cut-off (50 per cent in the diagram) keeping the sum of the steam laps 
 the same as before. This amount, and also the sum of the steam 
 lap and the exhaust lap for each end, will be the same no matter 
 what adjustment is made. The angle of advance for the new 
 condition is 0:2. Then <* 2 a.\ is the angle that the eccentric must 
 be shifted forward. The difference X between the new and the 
 old head-end steam laps is the distance the valve must be moved 
 on the rod. Since the new head-end steam lap is larger than the 
 old, the valve rod must be lengthened if the valve is direct, and 
 shortened if the valve is indirect. The upper part of Fig. 93 shows 
 the cards that may be expected after the setting has been changed. 
 
VALVES 135 
 
 VALVE SETTING BY MEASUREMENT. If an indicator is not avail- 
 able, the valve may be set by linear measurement. The steam chest 
 cover must be removed so that the measurements may be taken. 
 It is customary to set either for equal cut-offs or for equal leads. 
 We cannot have equal leads and equal cut-offs at the same set- 
 ting because of the angularity of the connecting rod.* In either 
 case adjust the valve on the stem so that the valve travels about 
 as far beyond the head-end port as beyond the crank-end port. 
 
 SETTING FOR EQUAL CUT-OFF. By means of marks on the guides 
 and on the cross-head the stroke may be determined, and that 
 proportion from each end at which cut-off is to take place may 
 be laid off on the guides. The procedure is as follows: 
 
 (1) Place the cross-head at the position for head-end cut-off. 
 
 (2) Loosen the eccentric on the shaft and turn it on the shaft in 
 the direction the engine is to run until the valve is just on the point 
 of cutting off. Fasten the eccentric to the shaft in this position. 
 
 (3) Turn the engine to the position for cut-off at the crank-end 
 and measure the distance from the valve to its correct position 
 to give cut-off on this end. Divide the error by two and take 
 up half the error by shifting the valve on the stem and the other 
 half by turning the eccentric on the shaft. 
 
 (4) Turn the engine back to the position for head-end cut-off 
 and check the setting. If there is an error left, repeat as ex- 
 plained above. 
 
 Be sure the eccentric is fastened firmly to the shaft and the 
 valve to the stem. Replace the cover of the steam chest. 
 SETTING FOR EQUAL LEAD. 
 
 (1) Place the engine accurately on head-end dead center. 
 
 (2) Loosen the eccentric on the shaft and turn it in the direc- 
 tion the engine is to run until the port is open a distance equal to 
 the desired lead. Be sure the valve will open the port if the eccen- 
 tric is turned ahead more. Fasten the eccentric to the shaft. 
 
 (3) Turn the engine to crank-end dead center and measure the 
 error. Divide the error by two and take up half by turning the 
 eccentric on the shaft and the other half by adjusting the length 
 of the valve stem. 
 
 (4) Turn the engine back to head-end dead center and check. 
 If there is an error, correct it by repeating as previously explained. 
 
 * This expression means the deviation from parallelism with the axis of the cylinder, of a 
 connecting rod of finite practical length, except when the crank is at one of the dead centers. 
 
136 
 
 ENGINES AND BOILERS 
 
 The reason that half the error is taken up by moving the valve 
 on the stem and half by turning the eccentric on the shaft may 
 be explained as follows. Suppose the valve has been set to give the 
 correct cut-off on the crank-end, but that when turned over to 
 head-end position for cut-off there is an error as shown in Fig. 94. 
 
 The eccentric is now at E\. 
 By turning the eccentric from 
 Ei back to E 2) this error 
 would be adjusted, but nothing 
 would have been gained as will 
 be seen when the engine is 
 turned back to the position for 
 crank-end cut-off. The same 
 error now exists on crank-end as shown in Fig. 95. That is, the 
 eccentric is at E* and should be at E%. If we try to take up the 
 error by lengthening the valve stem (Fig. 96), nothing is gained 
 because the valve will be moved to the left a distance equal to the 
 error, and when it is turned back to the position for crank-end cut- 
 off, the valve will be open a distance equal to the error. If now 
 we divide the error by two, and move the edge of the valve to A, 
 
 FIG. 94 
 
 FIG. 95 
 
 FIG. 96 
 
 in Fig. 94, by turning the eccentric back from EI to D, we will 
 find that the other edge of the valve will be at B in Fig. 95, when 
 turned over to the crank-end cut-off position. If the other half 
 of the error be taken up in Fig. 94 by lengthening the valve stem 
 i.e. by moving the valve to the left on its stem, the valve will be 
 in the correct position for head-end cut-off. Moreover, moving 
 the valve to the left moves the crank-end edge (Fig. 95), from B to 
 the edge of the port, where it should be for crank-end cut-off. 
 Therefore, by taking up half the error in each way at the posi- 
 tion of head-end cut-off, we have made no net change in the 
 position of the valve for the crank-end cut-off position. 
 
CHAPTER IX 
 GOVERNORS 
 
 130. General. The function of the governor is to keep the 
 engine running at nearly the same speed at all loads. It does 
 this by controlling the amount of steam admitted to the cylinder. 
 It is impracticable for the governor to keep the speed exactly 
 constant at all loads. This may be seen when we understand 
 how a governor must work. Under conditions of changing load, 
 the governor must change the amount of steam admitted to do 
 the work. At any instant we have a certain load on the engine, 
 the governor is admitting enough steam to carry that load. If 
 an extra load is thrown on, the engine will momentarily slow 
 down. This slower speed affects the position of the parts of the 
 governor, and this in turn allows more steam to enter to do the 
 extra work required. This change cannot be affected instantane- 
 ously, although some governors respond in a very short time. 
 Governors that are quick in making the change are said to be 
 sensitive, and those that are slow, sluggish. 
 
 Under full-load conditions, the engine usually runs slower than 
 that at no load, by an amount that depends upon the construction 
 of the governor. Governors are made that give an engine speed 
 which is nearly as great at full load as at no load. These are said 
 to give doss regulation. It is possible to design and construct 
 a governor that gives the same average engine speed at all loads, 
 in which case the governor is said to be isochronous. Such a 
 governor would tend to hunt, i.e. there would be a constant 
 fluctuation in speed as the governor attempted to regulate the 
 steam supply to balance the load conditions. 
 
 Practical considerations limit the nearness to which isochronism 
 may be approached. If the no-load speed is greater than the 
 full-load speed the governor is said to be stable. If the governor 
 is isochronous or gives a full-load speed greater than no-load 
 speed, it is unstable. An unstable governor is clearly undesir- 
 able. Various schemes are used to express the relation of speeds 
 at various loads. A common way is to express the variation of 
 speed from no load to full load and from no load or full load to 
 normal load in percent of the speed at normal load. We may 
 
 137 
 
138 ENGINES AND BOILERS 
 
 then say, the percent of variation in speed from no load to full 
 load is equal to 100(ni n^/n, where HI and n% are the speed at no 
 load and the speed at full load, respectively, and n is the speed 
 at normal load. 
 
 131. Classification of Governors. Governors may be classi- 
 fied according to the following characteristics. 
 
 (a) As to the manner of regulating the steam supply: Under 
 this head we have (1) throttling governors, which regulate the 
 amount of steam admitted to the cylinder by controlling a throttle 
 valve, and (2) cut-off governors, which control the steam supplied 
 by changing the point of cut-off. 
 
 (b) As to the predominant controlling force in the mechanism: 
 We speak of centrifugal governors, inertia governors (although 
 inertia is not a force), and resistance governors. All mass has 
 inertia. If the mass of the moving parts is small and the inertia 
 effect is not used in governing, we call the governor a centrifugal 
 governor. If the inertia is large and its effect is used to aid in 
 governing, we have what we call inertia governors. Even in inertia 
 governors, the centrifugal force is a very important factor. 
 
 (c) As to the force used to balance the centrifugal force of the 
 rotating parts*: We have gravity-balanced governors and spring- 
 balanced governors. 
 
 (d) As to the arrangement of the mechanism: There are 
 spindle governors and shaft governors. 
 
 132. The Gravity-balanced Spindle Governor. The diagram 
 of Fig. 97 represents a simple gravity-balanced spindle governor. 
 This is sometimes called a conical pendulum, and is also often 
 called the Watt governor, because James Watt first used it on 
 his engines. Two flyballs, at the ends of arms, rotate about a 
 vertical spindle. The arms are pivoted to the spindle at 0. The 
 height of the balls is caused to control the steam supply. In 
 Fig. 97 this is done by raising or lowering the point A with the balls, 
 which, by a suitable mechanism, causes either the movement of 
 a throttle valve or a change in the point of cut-off. 
 
 A definite relation exists between the height hi of the cone of 
 revolution, and the speed of the spindle. To determine this rela- 
 tion consider one of the balls as a free body. At any certain 
 speed it may be considered to be in equilibrium under the action 
 of the following forces: the tension in the arm T, the weight W, 
 
GOVERNORS 
 
 139 
 
 and the centrifugal force acting radially outward (W/g)X(v z /R). 
 Taking moments of these forces about the point 0, we have 
 
 X^Xh-WXR = 0. 
 g ti 
 
 But v = 2irRn, where n is the number of revolutions per unit time. 
 Therefore we may write 
 
 1 =WR 
 
 gR 
 
 or 
 
 If we wish to express hi in inches and the speed of the governor 
 in r. p. m., our equation becomes 
 
 hi 
 
 32.2X12X3600 35200 
 - . 9 9 zj 
 
 4?r 2 n 2 n 2 
 
 approximately. 
 
 From this equation it is seen that the height hi of the cone of rev- 
 olution does not depend upon the length of the arm. Figure 97 
 
 FIG. 97 
 
 shows the r. p. m. corresponding to the height /ii for two-inch 
 increments of /i, up to 20 inches. From these values it will be 
 noticed that for a certain vertical movement of the ball there will 
 be less speed variation with the ball in the lower positions. In 
 other words, to get a reasonable speed variation it will be neces- 
 sary to run the governor very slowly. At low speeds the gov- 
 ernor will not have much power unless the balls are made exces- 
 sively heavy. This practical limitation precludes the use of this 
 governor on modern engines. 
 
140 
 
 ENGINES AND BOILERS 
 
 FIG. 98 
 
 If the governor arms are crossed, as shown in Fig. 98, it will 
 be noticed that much less variation in speed exists for the same 
 vertical movement of the balls than for the form shown in Fig. 97. 
 Moreover, this governor is nearly isochronous at 50 r. p. m. 
 
 By the proper selec- 
 tion of the pivots B 
 and C, we may get 
 quite satisfactory 
 speed regulation for a 
 certain limited range 
 of vertical movement 
 at any desired speed. 
 
 The pendulum gov- 
 ernor may be made 
 exactly isochronous by 
 making the balls swing up in the arc of a parabola, as in Fig. 99. 
 The subnormal of a parabola is constant, and it is seen in Fig. 99 
 that hi is the sub-normal of the parabola which is the path of 
 the balls as they swing upward. The balls may be made to take 
 the parabolic path by having the arms made flexible and to unwind 
 from the evolute of the parabola or by having them guided by 
 an arrangement of 
 cams. Of course it is 
 understood that, in 
 practice, the governor 
 never would be made 
 exactly isochronous, 
 but it is seen that iso- 
 chronism may be ap- 
 proached as nearly as 
 practical conditions 
 will permit. 
 
 In order to run a 
 spindle governor at 
 fairly high speed, and FlG> 99 
 
 still have a reasonably 
 
 small speed variation in the engine, it is customary to load it as 
 shown in Fig. 100. The load L tends to pull the balls down; 
 hence they must rotate faster, to get to the same height as 
 before. To find the relation between the height of the cone of 
 
GOVERNORS 
 
 141 
 
 revolution and the speed, consider the load and the ball each as 
 a free body. With the forces acting on them as shown, we can 
 express the conditions of equilibrium as follows. Expressing the 
 fact that the sum of the vertical forces is zero for the load L, 
 
 (1) 
 or 
 
 2T 2 sin j8 = L, 
 
 T -- 
 
 2sin/3 
 
 Considering the ball as a 
 free body, and taking 
 moments about as a 
 center, we have, since the 
 sum of these moments must 
 be zero, 
 
 W v 2 
 (2) -p 
 
 Q rt 
 
 -WXR- !F 2 sin 
 By (1) this may be written in the form 
 (3) ~^ Xhi ~ WR ~ f X# - | ctn 
 
 or, since v = 2irnR, 
 
 W T T 
 
 0. 
 
 (4) j WRtfh, -WR-^R-^ctu 
 
 whence, since ctn /3 = R/h 2 , 
 
 TT n l - 
 and finally, solving for n 2 , 
 
 r^+K^+A.)] , 1 + 
 
 (6) * = i- 
 
 If /Z-i = ^2 
 
 o, 
 
 = 0, 
 
 = 0, 
 
 L1 )J 
 
 7 
 
 or 
 
 fe 
 
 /Tf +ZA 
 V IT / 
 
 If hi be expressed in inches and n in r. p. m., 
 
 W + L\ 35200 
 
 
142 
 
 ENGINES AND BOILERS 
 
 The usual form of loaded governor is shown in Fig. 101. This 
 is seen to vary slightly from Fig. 100. Taking the load as a free 
 body, T 2 = L/(2 sin /3), as in (1) above. 
 
 FIG. 101 
 
 Taking the upper arm as a free body, and expressing the fact 
 that the sum of the moments about equal to 0, 
 
 (9) Xj^XH -WXR- 
 
 (10) -X^XH- 
 
 g R 
 
 in PX^R- T 2 cos ftXhi = 0. 
 Substituting the value of T 2 from (1), we have 
 
 6 2 ^b 2 
 
 But we have 
 
 (ID 
 
 hence 
 
 (12) ~X^H - 
 
 Since we have also v = 2irRn, 
 
 hi = H T and 
 o 
 
 _ w __ _ 
 
 2 b 2/i 
 
 whence 
 
 ' 
 
 
 . 
 
GOVERNORS 143 
 
 Taking as our units inches and r. p. m., this becomes 
 
 (15) n 2 = 
 
 H 
 
 In the solution of a problem for this type of governor it is best 
 to make a drawing and to scale from it the values of H, h 1} and 
 hz at the different positions of the weights. With these values 
 substituted in the formula (15), the r. p. m. of the governor is 
 readily determined. The governor of Fig. 101 is the one commonly 
 used on Corliss engines. 
 
 133. The Spring-balanced Governor. In most high-speed 
 engines, the centrifugal force of the revolving weight is balanced 
 
 FIG. 102 
 
 by the force of a spring. Figure 102 shows a weight W, revolv- 
 ing about the center of a spindle or shaft. The centrifugal force 
 C of the weight is balanced by the spring tension S. The weight 
 is at a distance R from the center of rotation. Hence we have 
 
 For a certain value of n, C varies directly as R. In Fig. 103, 
 this variation is shown graphically. At speed n and with a 
 radius R, the centrifugal force is C. If R is doubled, C is doubled. 
 For other values of n, as HI and WQ, C will have different values 
 with the same radius R. 
 
144 
 
 ENGINES AND BOILERS 
 
 In any kind of uniform spring the elongation, shortening, or 
 deflection is proportional to the force producing the deformation. 
 Figure 104 shows graphically the relation between the pull of the 
 spring and the elongation. If Figs. 103 and 104 be superimposed, 
 as in Fig. 105, we easily can see the relations that must exist if 
 
 of p0/h of 
 FIG. 103 
 
 o 
 
 FIG. 104 
 
 the spring pull equals the centrifugal force. For the three speeds 
 HI, n and n 2 , the spring pull equals the centrifugal force, as seen 
 at the points b, d, and /. That is, the spring pull will balance 
 the centrifugal force at the speed %when the elongation of the spring 
 is ei. The weight will then be revolving at a radius Ri=a+e, 
 where a is the distance the weight would be from the center 
 
 of rotation if there were zero 
 tension in the spring. At a 
 speed n, the forces will balance 
 when the elongation is e and 
 the radius is R=a-\-e. In like 
 manner, the forces balance at 
 the speed n 2 with an elongation 
 62 and radius R%. If the origin 
 A should be moved over to the 
 origin 0, i.e. the distance a be 
 made zero, it is seen that the 
 spring pull could balance the 
 centrifugal force at only one speed. This means that the gover- 
 nor would then be isochronous. If the origin A were moved to 
 the left of the origin 0, the governor would be unstable, because 
 the speed HI at no load would be less than the speed 712 at full 
 load. As stated before, an unstable or isochronous governor could 
 not be used in practice. 
 
 - Q . 
 
 FIG. 105 
 
GOVERNORS 145 
 
 What is known as scale of spring is the force necessary to pro- 
 duce an elongation of one inch in the spring. If the spring pull 
 is Si at elongation e\, and $2 at elongation e 2 , the scale of the 
 spring is equal to 
 
 Suppose that we desire to find the scale of spring necessary for 
 a governor such as that shown in Fig. 102. Let us suppose that 
 the no-load speed HI and the full-load speed n 2 , and the corre- 
 sponding radii RI and R 2 , are known. First compute Ci and C 2 
 for the two speeds. Then, since the spring pull must equal the 
 centrifugal force at all loads, the scale of spring is seen to be 
 
 because R\ R^=ei e%. 
 
 In actual governors it is very seldom that the spring pull acts 
 in the same line as the centrifugal force. Figure 106 represents 
 
 FIG. 106 
 
 a more usual case. In the solution of this problem, moments will 
 be taken about the pivot point of the governor arm B. In the 
 full-line position, the moment of the centrifugal force equals the 
 moment of the spring pull about the point B. That is, CXh = 
 SXd. In like manner, CiXi=SiXf. The scale of spring equals 
 (S Si) divided by the elongation of the spring as the weight 
 goes from R to RI. 
 
146 ENGINES AND BOILERS 
 
 134. Governing by Changing Position of Eccentric. Most 
 shaft governors regulate the steam supply by changing the per- 
 cent of cut-off. This is accomplished by changing the position 
 of the eccentric relative to the crank. In Fig. 107, a Zeuner 
 valve diagram is shown on which appear two positions of the 
 crank at cut-off. In the full-line construction, cut-off comes late 
 and the angle of advance is i, i.e. when the crank is on head- 
 end dead center, the eccentric will be at E\ (direct valve). By 
 shifting the eccentric forward to E^ the angle of advance is 
 
 FIG. 107 FIG. 108 
 
 changed to 0$. The dotted construction gives the position of 
 the crank with the new angle of advance. It is seen that the 
 cut-off comes earlier with the larger angle of advance. By turning 
 the eccentric on the shaft, the time of cut-off can be changed but 
 the value of the steam lap will be the same for all values of a, 
 because the only way to change the laps is to move the valve 
 on the stem. 
 
 Figure 108 shows the effect on cut-off of changing the valve 
 travel while keeping the angle of advance constant. The Zeuner 
 construction for a large valve-travel is shown in full line. Cut- 
 off is seen to come fairly late. With a smaller valve-travel, as 
 shown by the dotted construction, cut-off is seen to come earlier. 
 Hence it appears that late cut-off is obtained with large valve- 
 travel and earlier cut-off with small valve-travel. 
 
 A governor can regulate cut-off by changing either a or the 
 valve-travel. It may be so constructed that it will control by 
 making only the one change or it may change the valve-travel 
 and the angle of advance at the same time. 
 
GOVERNORS 
 
 147 
 
 Changing the angle of advance affects the other events as well 
 as cut-off. When a is increased all events occur sooner. Thus 
 on one-valve engines that control the steam supply by shifting 
 the eccentric, it is found that a high compression accompanies 
 early cut-off, such as is characteristic of the Stephenson valve-gear. 
 
 135. Governing by Changing a. In Fig. 109, a governor is 
 shown that controls cut-off by turning the eccentric around the 
 shaft. The two weight arms are pivoted at the points G and F. 
 
 FIG. 109 
 
 Any rotation of these arms about their pivots causes the eccentric 
 to turn on the shaft. The weight arms are connected by the 
 links AC and BD to AB, which carries the eccentric. At light 
 loads the speed of the engine is greater than at heavy loads, and 
 the weights will be farther from the center of rotation. This 
 movement of the weights away from the center of rotation causes 
 the eccentric to turn in a clockwise direction relative to the 
 crank. It is evident that this increases a arid therefore makes 
 cut-off come earlier, as it should at light loads. 
 
 136. Governing by Changing both a and the Valve-travel. - 
 
 In Fig. 110 a governor is shown that changes both a and the 
 valve-travel at the same time. The pivot point on the flywheel 
 carries the governor arm. The eccentric is shown as a pin. 
 When the governor arm moves about the pivot point in a clock- 
 wise direction, it carries the center of the eccentric with it and 
 
148 
 
 ENGINES AND BOILERS 
 
 makes a smaller and the valve-travel larger. It is known that 
 small a and large valve-travel both give late cut-off. Conversely, 
 a counter-clockwise movement of the arm about the pivot point 
 gives early cut-off because it makes a larger and the valve-travel 
 smaller. The centrifugal force acts through the center of rota- 
 tion and the center of gravity. Hence this force tends to give 
 the arm counter-clockwise movement about the pivot. At light 
 loads, and therefore higher speeds, the centrifugal force will be 
 greater than for heavy loads. This tends to give the arm counter- 
 clockwise rotation about the pivot and this makes cut-off come 
 
 FIG. 110 
 
 earlier for light loads, as it should. A great many other governors 
 besides the one shown in Fig. 110, change a and the valve-travel 
 in the same way. 
 
 137. Centrifugal and Inertia Governors. As has been previ- 
 ously stated, all governor weights have inertia. If the tendency 
 of the weight to keep moving at the same speed helps to effect 
 the change of position that causes the governing, the governor 
 will respond more quickly than it would if the inertia opposed 
 the change. In the gravity-balanced spindle governors that were 
 considered in 132, inertia acts against the rapid change of posi- 
 tion of the balls and so tends to make the governor sluggish. 
 
 In the governor of Fig. 110, the inertia of the arm assists in 
 the governing. If the load is suddenly thrown off the engine, 
 
GOVERNORS 149 
 
 it will momentarily speed up. This means that the flywheel will 
 go ahead of the governor arm or rotate in a clockwise direction 
 relative to the arm. This swings the eccentric nearer the center, 
 which makes a large and the valve-travel small. Hence cut-off 
 occurs sooner, which tends to re-establish the conditions of equi- 
 librium. In Fig. 110 the arm is made very heavy, so that it will 
 have considerable inertia. 
 
 It must not be assumed that the inertia of the arm is the only 
 factor in the governing. The centrifugal force also plays its 
 part, as has been explained previously. The governor of Fig. 
 110, while it is very simple in construction, is at the same time 
 sensitive and quick in its action. It is widely used and is known 
 as the Rites inertia governor. 
 
CHAPTER X 
 STEAM TURBINES 
 
 138. Introduction. The steam turbine of to-day is of as much 
 importance in the world of engineering as is the reciprocating 
 steam engine. Practically all large steam power plants which 
 produce electric current employ the turbine engine. The devel- 
 opment of the turbine has been remarkably rapid. However, it 
 would not be true to say that the turbine has crowded the recip- 
 rocating engine from the power-plant field. The fact is rather 
 that it has developed along new and different lines of use, and 
 now occupies a field that was never held by the reciprocating 
 engine, i.e. as the direct connected prime mover for high-speed 
 electric generating units. 
 
 The turbine and the alternating-current generator have devel- 
 oped together. Both the turbine and the alternating-current gen- 
 erator are well adapted to high-speed rotation. The cost of a slow- 
 speed electric generator is much higher than that of a high-speed 
 generator of the same capacity. Before the days of the turbine, 
 generators were nearly all of the direct-current type, which could 
 not run at very high speeds. 
 
 The electric system of power transmission is more economical 
 than the old belt system. Hence the turbine has replaced the 
 reciprocating engine in some manufacturing plants on account of 
 the development of systems of electric power transmission. On 
 land, large turbines are seldom used to drive anything but 
 electric generators. 
 
 139. History. The steam turbine is not a modern invention. 
 Hundreds of years ago people knew, as every child knows today, 
 that a pin-wheel would rotate when blown upon. There are rec- 
 ords of turbines built in the quite distant past. They were little 
 but toys, however, like pin-wheels, and of no practical importance. 
 The modern turbine dates from the years between 1880 and 1890. 
 During this period two types of turbines that have become of 
 great practical importance were developed. 
 
 DE LAVAL, the inventor of the cream separator, sought to drive 
 his separator by means of a turbine. After several experiments, 
 he perfected a type that was satisfactory for that purpose. The 
 
 150 
 
STEAM TURBINES 151 
 
 same turbine, with improvements, has been used in large numbers 
 for driving centrifugal pumps, fans, and even small generators. 
 
 During practically the same time, C. A. PARSONS developed the 
 type of turbine that now bears his name. These two pioneers 
 were soon followed by other experimenters. Various forms of tur- 
 bines were developed. Some of these are still used. Others are 
 obsolete and are of interest only from an historical standpoint. 
 
 In the development of the turbine, there were two obstacles 
 that had to be overcome. The first of these was the lack of 
 knowledge of principles. The second was the need of better 
 mechanical means of manufacture. As will be shown later, the 
 velocity of the rotor in a turbine must be very high. This causes 
 large stresses, and makes necessary a very perfect balance. The 
 clearances between the rotors and the stationary parts must be 
 small to prevent undue leakage. This calls for an excellence of 
 design and construction that did not commonly exist for heavy 
 machines in the past. As in the development of any new machine, 
 satisfactory solutions of the problems grew out of the necessities, 
 so that the modern turbine is as reliable and dependable as any 
 piece of machinery in the power plant. 
 
 140. Fundamental Principles. Before making a study of the 
 common types of turbines now in use, we shall discuss the fun- 
 damental principles of the steam turbine. It is not our purpose 
 to give an exhaustive discussion, but only to present the principles 
 in their simplest form. The sketches of blades and nozzles are 
 not exactly correct in shape for the conditions assumed. They are 
 to be considered as only diagrammatic. 
 
 Steam under pressure contains a certain amount of usable heat. 
 The available amount depends upon the initial pressure, the 
 degree of superheat, and the pressure to which the steam may 
 be dropped. There is the same amount of available heat if the 
 initial and final conditions of the steam are the same, no matter 
 whether we are considering the reciprocating steam engine or the 
 steam turbine. The turbine, or the reciprocating engine, is effi- 
 cient, or is not, according as it uses a large or a small amount 
 of this available energy. 
 
 Since the turbine and the reciprocating engine both use the 
 same medium, it is not to be expected that one will be much 
 more efficient than the other. Both reciprocating engines and 
 
152 ENGINES AND BOILERS 
 
 turbines may be made of about the same thermal efficiency. The 
 choice of type of engine depends upon other considerations than 
 efficiency. 
 
 The greatest loss in the reciprocating engine is due to the initial 
 condensation in the cylinder. Since the cylinder walls are made 
 of a heat-conducting material, they will never be as hot as the 
 incoming high-pressure steam, and they will be hotter than the 
 low-pressure steam leaving the cylinder. The relatively hot 
 steam coming to the cylinder strikes the cooler cylinder walls 
 and some condensation takes place, with a consequent shrinkage 
 in the volume. The condensed steam is mostly re-evaporated 
 before the steam leaves the cylinder, owing to an absorption of heat 
 from the then hotter cylinder walls. 
 
 The loss in the turbine is due to other causes, such as leakage, 
 friction, etc. The leakage occurs around the ends of the blades 
 or from stage to stage. The friction exists between the steam and 
 the parts of the turbine in the passage of steam through both 
 the stationary and the moving parts. There is also a windage 
 loss between the moving parts and the steam. This friction does 
 not cause a complete loss, because a part of the heat generated 
 may be used in later stages of the turbine. 
 
 141. Available Energy in Steam. In order to make clear the 
 nature of the available energy in steam, a concrete example will 
 be taken. 
 
 (1) Let us assume that the steam is dry saturated steam at a 
 pressure of 150 pounds gage (165 pounds absolute), and that it 
 is allowed to expand adiabatically to a pressure of 15 pounds 
 absolute.* The heat contents of a pound of dry saturated steam 
 at 165 pounds absolute is 1194 B.t.u. The heat contents of a 
 pound of steam at 15 pounds absolute, after expanding adiabati- 
 cally from 165 pounds, is 1019 B.t.u. The difference between 
 these values, which is the amount of heat available for doing 
 work, is 11941019 = 175 B.t.u. At 165 pounds pressure, dry 
 saturated steam occupies a volume of 2.75 cubic feet per pound. 
 At 15 pounds pressure, after the expansion just mentioned, the 
 quality is 87 per cent, and the volume is about 23 cubic feet. 
 
 In the reciprocating steam engine, this change in volume, work- 
 ing by its pressure, does work on the piston in forcing it forward. 
 
 * Adiabatic expansion is that in which no heat is added to the steam and none is extracted 
 except by the conversion of heat into work. 
 
STEAM TURBINES 153 
 
 The velocity of the piston is immaterial. In the turbine, the 
 same change in volume takes place, but the steam is allowed to 
 acquire velocity in expanding. The energy of the steam due to 
 its velocity is imparted to the rotor of the turbine. The efficiency 
 of a perfect engine working on the Rankine cycle,* between the 
 pressures of 165 and 15 pounds absolute, is 175/(1194 181) =17 
 per cent. Since neither the reciprocating engine nor the turbine 
 is perfect, neither would have an efficiency as great as 17 per 
 cent when worked between the pressure limits named. 
 
 (2) Assume that the steam is allowed to expand adiabatically 
 from 165 pounds absolute to 1 pound absolute. The heat-drop 
 is 1194 871 = 323 B.t.u. and the efficiency on the Rankine cycle 
 is 323/(1194-70) = 28.6 per cent. 
 
 142. Velocity Due to Expansion. Let us next compute the 
 velocity of the steam if all the heat-drop goes to giving the steam 
 velocity. 
 
 (1) Suppose that the drop in pressure is from 165 to 15 pounds 
 absolute. Since one B.t.u. = 778 foot-pounds, the energy is 175 X 
 778 = 136,100 foot-pounds per pound of steam. The energy of 
 motion, or kinetic energy, is mv 2 /2 = (1/32) Xv 2 /2. This must be 
 equal to the value 136,100 foot-pounds just calculated. Hence 
 
 v 2 = 64X136,100 = 8,710,400, 
 v = 2950 ft./sec. 
 
 (2) If the drop in pressure is from 165 to 1 pound, we find, in a 
 similar manner, 
 
 K.E. = 778X323 = (1/32) Xv*/2, 
 whence 
 
 v = 4010 ft./sec. 
 
 In the steam turbine, the steam must be expanded, and the 
 velocity due to this expansion must be used by imparting its 
 kinetic energy to the rotor of the turbine. If this is done by 
 allowing the steam to expand in the stationary parts of the tur- 
 bine and imparting the velocity thus produced to the moving 
 parts, the turbine is said to be of the impulse type. If it is done 
 
 * To compare steam engines, the efficiencies based on the Rankine cycle are often used. The 
 efficiency of a steam engine operating on the Rankine cycle is given by the expression 
 (Qi Qi/Q\, where Q\ is the amount of heat required to make dry steam at boiler pressure from 
 water at the temperature of the exhaust, and Qz is the amount of heat rejected from the engine 
 minus the heat of the liquid at the temperature of the exhaust. 
 
154 ENGINES AND BOILERS 
 
 by allowing the steam to expand in the moving parts, the unbal- 
 anced steam pressure reacting on the rotor, the turbine is 
 called a reaction turbine. In some turbines the steam expands 
 both in the stationary parts and in moving parts, and the turbine 
 is said to be of the impure reaction type. 
 
 143. Impulse and Reaction. In order to understand the prin- 
 ciples involved, consider the simplest cases involving the principles 
 of impulse and reaction in which the velocity is created and used. 
 It may be easier to think of the jet as a jet of water, for in that 
 case the fluid does not expand when the pressure on it is reduced. 
 
 Otherwise, the steam jet and the 
 
 """"*'* . e '^ * : i water jet follow the same laws of 
 
 impulse and reaction. 
 FlG jjj Suppose that water issues from 
 
 a nozzle, as in Fig. 111. The 
 
 nozzle is stationary, and the issuing jet has a velocity of v feet 
 per second. The unit mass m of water that will be considered is 
 that issuing from the nozzle in one second. A particle of water 
 in the jet will move v feet in one second. The kinetic energy 
 of this unit mass will be mv 2 /2. 
 
 (1) Consider the case in which the jet strikes a stationary flat 
 surface (Fig. 112). After striking the flat surface, the water flows 
 or splatters out to the sides at right angles to its former direction 
 of motion, that is it loses all its 
 
 velocity in the direction of the 
 
 jet. The force exerted by the | ^"," "' * ^ * 
 
 jet on the flat surface may be 
 
 measured by the force F neces- 
 
 sary to hold the flat surface 
 
 stationary. Since force = mass X change in velocity per second, 
 
 and since the time in which mass m emerges from the nozzle 
 
 and strikes the plate is one second, we have F = mv. The force 
 
 exists in the case of the stationary plate, but no work is done 
 
 because the plate does not move. 
 
 (2) Suppose that the flat surface moves with a velocity V (Fig. 
 112). Then the force F=mX(v-V). The quantity (v-V) is 
 the velocity of the jet relative to the flat surface. It is seen that 
 F is less than before, and will be zero if the velocity of the sur- 
 face is the same as the velocity of the jet. The work done in one 
 
 Force F 
 
 * t/t/. & 
 
STEAM TURBINES 155 
 
 second by the jet on the plate equals F times the distance the 
 plate moves, or 
 
 W=FxV=m(v-V)V. 
 
 The velocity of the plate at which the work is a maximum may 
 be found by equating to zero the first derivative of the work 
 with respect to V. This gives 
 
 Hence the maximum work occurs when V =v/2, that is, when 
 the velocity of the plate is half that of the jet. 
 
 (3) If instead of striking a flat surface, the jet strikes a station- 
 ary curved surface, such that 
 
 the jet is turned completely 
 back on itself, or through an 
 angle of 180 (Fig. 113), the 
 force F exerted on the surface 
 
 is mX2v, which is twice that "*'' ^~* f 
 
 ,, a , f PIG. 113 
 
 exerted on the nat surtace. 
 
 Since the curved surface is stationary, there is no work done. 
 
 (4) Suppose the curved surface (Fig. 113) is moving with a 
 velocity V. The velocity of the jet relative to the curved surface is 
 (vV). It follows that the absolute velocity of the jet leaving 
 the surface is (v V) V = (v 2 V ) . Consequently the change in 
 the velocity of the jet is v-\-(v 2V) = 2(v V), because the 
 direction of motion is completely reversed. As before, we have 
 
 F=mX2(v-V), 
 and the work done per second is 
 
 W=FV = 2m(v-V)V = 2m(vV-V*), 
 whence 
 
 For maximum work we must have 
 
 ^=0 
 
 dV 
 
 Hence 
 
 v=2V, or V=v/2. 
 
 That is to say, the curved surface should move at half the velocity 
 of the jet for the production of maximum work. If the latter condi- 
 
156 ENGINES AND BOILERS 
 
 tion exists, the absolute velocity of the jet as it leaves the sur- 
 face is zero. That is, all of the velocity of the jet has been used. 
 (5) In Fig. 114 we have a tank that is free to move horizontally 
 upon a track. In one side of this tank is placed an orifice or 
 nozzle. The water issues from this nozzle due to the pressure of 
 the water from above. If the tank is stationary, the water leaves 
 the tank with an absolute velocity v. The force F, due to the 
 
 unbalanced pressure of the water 
 in the tank, tends to force the 
 tank to the left, but since the tank 
 | is held stationary, the force F 
 
 ^: fe/.v-^ does no work. If the tank is 
 ' allowed to move to the left with 
 
 .....,, ,,,JJj$,,,,,,^), f ,,,,,,,,,,, r a ve l c ity V, however, the work 
 
 p iG 114 done will be FV. The absolute 
 
 velocity of water leaving the tank 
 
 is (vV). The maximum work will be done when V =v, that is 
 when the escaping water has no absolute velocity. 
 
 In the first four cases considered, the jet impinged on a sur- 
 face. Work was done by the jet striking and moving the surface. 
 A turbine in which the pressure-drop occurs in a stationary nozzle 
 or part is said to be an impulse turbine (142) because the energy 
 is given to the moving parts by the impulse of the jet. In the 
 fifth case the drop in pressure occurred in the moving nozzle. 
 When this occurs in a turbine, it is said to be a reaction turbine 
 (142). A comparison of the above simple examples shows that 
 the velocity of the moving parts of a reaction turbine must be 
 nearly twice as great as that of the impulse type, other factors 
 being equal. 
 
 144. Bucket Shapes. In the common types of steam tur- 
 bines, buckets or blades are mounted on the periphery of a wheel 
 or rotor. The shape of these blades is something like that of 
 the curved surface considered in (3), 143. Of necessity the jet 
 cannot be completely turned through an angle of 180 as in 
 (3), 143, because the steam must have a velocity in the direc- 
 tion of the axis of rotation of the rotor in order to get to the 
 bucket and to leave it. 
 
 In Fig. 115, let Vi denote the velocity of the jet relative to the 
 bucket or blade at the point where the jet first strikes it, and let a 
 
STEAM TURBINES 
 
 157 
 
 denote the angle it makes with the tangent to the rim of the rotor. 
 Let v% and 0, respectively, denote the velocity and the angle upon 
 leaving the bucket. We see that the component of the velocity 
 of the jet relative to the bucket in the direction of the tangent 
 is vi cos a and the component in the direction of the axis of the 
 rotor is v\ sin a. In like man- 
 ner, the relative velocity v^ 
 has similar components v% cos /3 
 and t>2 sin /3. These compo- 
 nents Vi sin a and v% sin /3 
 must be large enough to get 
 the jet through the row of 
 buckets on the rotor, in order 
 that the following buckets 
 shall not interfere with the 
 flow. 
 
 If the relative velocity of FIG. 115 
 
 the jet is Vi and the angle that 
 
 it makes with the tangent is a, the absolute velocity v of the 
 jet makes a different angle 6 with the tangent (Fig. 116). If V 
 denotes the tangential velocity of the bucket, v is the resultant of 
 the two velocities Vi and V, and 6 is the angle that this resultant 
 v makes with the tangent. 
 
 In like manner, the resultant of v% and V at the exit is the abso- 
 lute velocity v' at the exit, and 
 it makes an angle <f> with the 
 tangent. 
 
 If we assume that the jet 
 strikes the bucket in the direc- 
 tion of the tangent to the rim 
 of the rotor, the preceding par- 
 agraph shows that an error will 
 be introduced. In order to 
 make the calculations as simple 
 as possible, however, we shall 
 assume that the jet does strike 
 tangentially, and we shall bear in mind that some error has 
 been introduced. The results previously derived for steam veloci- 
 ties for certain heat drops will now be applied to the problem 
 of the turbine. 
 
 FIG. 116 
 
158 ENGINES AND BOILERS 
 
 145. The Single-stage Turbine. In a single-stage impulse 
 turbine, the steam is expanded in a stationary nozzle, and is 
 directed against the moving buckets or blades, which are mounted 
 on the rim of the rotor. In the single-stage reaction turbine, the 
 rotor itself carries the nozzles, and the steam expands in passing 
 through them. 
 
 If the expansion of the steam is from 165 to 15 pounds absolute 
 we have seen in (1), 142, that the steam or jet velocity is 2950 
 feet per second. For maximum work done, the bucket velocity 
 of the impulse turbine is half that of the jet velocity ( 143). 
 Hence the peripheral velocity of the rotor should be 2950/2 = 1475 
 feet per second. With a reaction turbine, the peripheral velocity 
 of the rotor should be the same as the jet velocity, or 2950 feet 
 per second. 
 
 If the rotor speed is assumed to be 3000 revolutions per minute, 
 or 50 revolutions per second, the diameter of the rotor should be 
 
 1475 
 
 -^r- =9.4 feet 
 
 50-7T 
 
 for an impulse wheel. This is obviously very much too large. 
 For a reaction wheel, the diameter should be 18.7 feet, which is 
 absurd. If a speed of 24,000 r. p. m. is assumed, the diameter 
 of the rotor for an impulse turbine should be 
 
 1475 
 
 or 14 inches. These values for the speed and the diameter of 
 the rotor are not far from those which are used in the DeLaval 
 single-stage turbine. 
 
 The preceding examples show what a very high peripheral veloc- 
 ity is necessary for a fair efficiency in a single-stage turbine. 
 With a vacuum, a much larger velocity should be used. Since 
 immense stresses are induced in the wheel by these high velocities, 
 it is readily seen that a single-stage reaction turbine is almost out 
 of the question. If such turbines were operated, their efficiency 
 would necessarily be very low. Hence they are not used. 
 
 In Fig. 117, a diagram of the single-stage impulse turbine is 
 shown. Steam enters the nozzle from the left, expanding as 
 it passes through. As the pressure drops, a high velocity is 
 imparted to the steam. The steam leaves the nozzle at low pres- 
 sure and at a high velocity. The steam now impinges upon the 
 
STEAM TURBINES 
 
 159 
 
 buckets or blades of the rotor, imparting to the rotor its velocity, 
 and therefore its kinetic energy. Upon leaving the rotor, the 
 absolute velocity of the steam is quite low. 
 
 The graphs at the lower part of the diagram show the changes 
 in the pressure and in the velocity. The steam pressure is shown 
 by the full line, and the steam velocity by the dotted line. While 
 single-stage impulse turbines are widely used, they are never 
 made in large sizes. 
 
 The diagram of Fig. 118 represents a single-stage reaction tur- 
 bine. The steam passes from the left directly to the rotor. The 
 rotor carries blades so shaped that the spaces between them act 
 as nozzles. The steam expands in these spaces or nozzles. As 
 it expands, its pressure drops, and it reacts upon the blades. This 
 
 Single-Stage Impulse 
 FIG. 117 
 
 Single - Sfagre Reac tioh 
 FIG. 118 
 
 force of the steam on the blades causes the rotor to move and to 
 absorb the energy liberated by the expansion. It will be noticed 
 from the graphs that the velocity does not change much in pass- 
 ing through the rotor, but the pressure drops during the passage. 
 In order to decrease the peripheral velocity of the rotor, and 
 at the same time to expand and use all the velocity of the steam, 
 more than one set of rotor blades or buckets are employed. This 
 is called staging. The steam passes successively through the 
 sets of blades in each stage, giving up part of the energy to each set. 
 
160 
 
 ENGINES AND BOILERS 
 
 Staging. In multi-stage impulse turbines, two methods 
 are in use. The first method is to expand the steam in one set 
 of stationary nozzles, and to take out part of the velocity in 
 each stage. This is known as velocity-staging. 
 
 The second method is to expand the steam partially in one set of 
 stationary nozzles, using up the velocity caused by this expan- 
 sion in one stage, then to expand the steam again in another set of 
 stationary nozzles, using the velocity thus generated in the 
 second stage, and so on. This scheme is called pressure-staging. 
 A combination of pressure-staging and velocity-staging is also 
 used, in which there are two or more velocity stages in each pres- 
 sure stage. 
 
 147. Multi-stage Impulse Type with Velocity-staging. The 
 diagram in Fig. 119 shows the velocity-stage impulse turbine. 
 
 - Velocit y - Stage /mpulse . 
 
 FIG. 119 
 
 The steam enters from the left and passes through the stationary 
 expanding nozzle, where the pressure drops and the velocity is 
 acquired in exactly the same manner as in the single-stage im- 
 pulse turbine of Fig. 117. The rotor in this case, however, has 
 much less velocity than the rotor shown in Fig. 117. Hence the 
 steam loses only a part of its velocity in passing through the first 
 
STEAM TURBINES 161 
 
 set of buckets. Emerging from the first set of buckets, it passes 
 through a set of stationary blades or vanes which change the 
 direction of flow of the steam, but not its velocity. These sta- 
 tionary blades are necessary, because the steam has a large up- 
 ward component of velocity after leaving the rotating buckets 
 of the first stage; and since the velocity of the rotor is downward, 
 the direction of flow must be reversed so that the steam may 
 impinge on the second set of rotating buckets. In passing through 
 the second set of moving buckets, more of the steam velocity is 
 taken up by the rotor. The direction of flow is again changed 
 by the stator, and so on, till the steam finally emerges from the 
 turbine with its velocity practically all expended. 
 
 Suppose, for example, that the downward velocity of the steam 
 as it leaves the nozzle is 4000 feet per second, and that the bucket 
 velocity downward is 500 feet per second. As it leaves the first 
 set of buckets on the rotor, the steam will have an upward velocity 
 of 4000-2X500=3000 feet per second, the effect of friction 
 being neglected. In going through the first set of stator blades, 
 the direction of flow is reversed, but is unchanged in magnitude. 
 Upon leaving the second set of rotor buckets its velocity will be 
 upward, and its magnitude will be 3000-2X500=2000 feet per 
 second, and so on for the other two stages. Each set of moving 
 buckets takes out 1000 feet per second of its velocity, and it 
 emerges with no vertical component of velocity. 
 
 It was shown in 145 that the rotor of a single-stage turbine 
 has to have an absurdly large diameter unless it has a very high 
 speed or the efficiency is very low. The objection to such high 
 speed is that the turbine must have a reducing gear in order that 
 the power may be used. With a multi-stage turbine we can 
 choose the diameter and also the speed, and make the number of 
 stages such that all the velocity can be used. 
 
 Let us assume that the speed is 3000 r. p. m., and that the 
 diameter of the rotor is 3 feet. Then the peripheral velocity 
 must be (3000/60) X37r =471 feet per second. Neglecting the 
 effect of friction, each stage will absorb a steam velocity of twice 
 the bucket velocity, or 942 feet per second. If the steam expands 
 from 165 to 15 pounds absolute, the steam velocity is 2950 feet 
 per second. Hence the number of stages necessary will be 
 2950/942 =3.1, and three stages should be used. If the turbine is 
 condensing, and the pressure drops from 165 to 1 pound absolute, 
 
162 ENGINES AND BOILERS 
 
 the steam velocity will be 4010 feet per second, the number of 
 stages 4010/942 =4.2, and four stages should be used. 
 
 In a velocity-stage turbine, the efficiency is very low after the 
 first two stages, principally because the jet is broken up by its 
 passage through the blades. As a result, more than two velocity 
 stages are seldom used. It must be remembered also that a very 
 high steam velocity produces a very great friction between the 
 steam and the surfaces of the blades, thereby causing a consid- 
 erable loss. 
 
 Impulse Type with Pressure-staging. If, 
 
 instead of expanding the steam completely in one nozzle, we ex- 
 pand it only a little in the first nozzle, then use its velocity, ex- 
 pand it some more in a second nozzle, and again use the velocity 
 generated, and so on, the process is called pressure- staging (146). 
 Figure 120 shows the method diagrammatically. In this diagram 
 there are five sets of nozzles and five pressure stages. The steam 
 enters from the left and passes through the stationary nozzle. 
 The pressure and velocity lines below show that the drop in pres- 
 sure is accompanied by an increase in velocity. The steam with 
 its acquired velocity impinges on the blades of the rotor. The 
 velocity is absorbed in the rotor. As the steam leaves this rotor 
 with low velocity, it is collected and led to a second stationary 
 nozzle in which the pressure is again dropped, and velocity is 
 acquired. The second rotor absorbs this velocity and the steam 
 passes on through the following stages, until its pressure and 
 velocity are practically all used up at its exit. 
 
 Making the same assumptions for speed and diameter of the 
 rotor as in the preceding type, let us compute the number of 
 stages necessary with the pressure-stage type. If the diameter 
 of the rotor is 3 feet and the speed is 3000 r. p. m., there is a 
 steam velocity of 942 feet per second to be absorbed per stage 
 (147). If a pound of steam loses a velocity of 942 feet per 
 second, it gives up 
 
 ~XrX942 = 13900 foot-pounds 
 
 Z oZ 
 
 of kinetic energy. This is equivalent to 13,900/778 = 17.9 B.t.u. 
 For the non-condensing condition assumed in 147, there was a 
 
^ . 
 
 STEAM TURBINES 
 
 163 
 
 heat-drop of 175 B.t.u. available in the whole turbine. The num- 
 ber of stages will then be 
 
 For the condensing conditions assumed in 147, the number of 
 stages will be 
 
 17.9" 
 
 In making a comparison of this type with that of 147, it 
 might seem at first sight that the velocity-staging were the better, 
 as the number of stages is so much smaller. While this is an 
 advantage, it is overbalanced by the fact that the pressure-stage 
 type is more efficient. This type is used very extensively in 
 
 Multi- Pressure -Stage Impulse. 
 
 FIG. 120 
 
 medium-sized turbines. It is often called the multi-cellular type 
 because each pressure stage is composed of a cell that is steam- 
 tight except for the openings through the inlet and outlet nozzles. 
 It is evident that it is necessary to keep each cell steam-tight in 
 order to prevent a leakage of steam from one stage to the next. 
 Where no difference in pressure exists, there is no tendency to 
 leak. In the velocity-stage type, the pressure was the same 
 throughout the whole turbine beyond the expanding nozzles, and 
 so there could be no leakage. 
 
164 
 
 '; 
 
 ENGINES AND BOILERS 
 
 149. Multi-stage Impulse Type with Combined Pressure- 
 staging and Velocity-staging. Very often a combination of 
 pressure-staging and velocity-staging is used, with the result that 
 some of the advantages of both types are utilized. The diagram 
 of Fig. 121 shows this arrangement. In the sketch three pressure 
 stages are shown, and each pressure stage has two velocity stages. 
 The drop in pressure occurs in the three stationary nozzles. After 
 expanding in the nozzle, the steam passes through the buckets 
 
 /*" Pressure 
 
 g & Pressure 5fe?e 3 & Pressure 5hj<?e 
 
 Multi- Pressure, Multi -Velocity Stage (Cvrf/sJ 
 FIG. 121 
 
 of the rotor wheel, where a part of the velocity is absorbed. It 
 then emerges from this rotor, and its direction of flow is reversed 
 in the stationary vanes, as in the velocity-stage impulse type. 
 It then passes through a second set of moving buckets, where 
 most of the remaining velocity is absorbed. The steam is now 
 collected and expanded some more in the next nozzle, and the 
 process of the first pressure stage is repeated. 
 
 By dropping the pressure in three successive nozzles, the velocity 
 generated is not nearly so great as it is in the velocity-stage type 
 of Fig. 119. This means that there will be less friction loss due 
 to excessively high steam velocities. Ordinarily two velocity 
 
STEAM TURBINES 165 
 
 stages are used for each pressure stage, so that the drop in 
 efficiency due to a disturbance of the jet is not so great as in the 
 pure velocity-stage type. 
 
 Applying the above problem to this combination type, let us 
 determine the number of pressure stages required. Assuming, as 
 before, that the speed is 3000 r. p. m., and that the diameter is 
 3 feet, we find that the bucket velocity is 471 feet per second 
 (147). Since there are two velocity stages for each pressure 
 stage, it is seen that 2X2X471=1884 feet per second of steam 
 velocity per pressure stage can be absorbed. The heat-drop per 
 pound of steam that corresponds to this velocity is 
 
 yXX 1884 x l/778= 71.3 B.t.u. 
 
 With a pressure-drop from 165 to 1 pound absolute, in which 
 there are available 323 B.t.u. for doing work, there will be 
 323/71.3 = 4 pressure stages. 
 
 Comparing this with other types, it is seen that the number 
 of pressure stages is the same as the number of velocity stages 
 in the velocity-stage type. But as there are two rows of rotor 
 buckets in each pressure stage, there will be twice as many rotor 
 wheels as in the former type. With pressure-staging, there were 
 18 rows of rotor buckets, or more than twice as many as in the 
 mixed type. This combination type is more efficient than the 
 velocity-stage type, and at the same time it is more compact than 
 the pure pressure-stage type. Due to these distinct advantages, 
 the combination type is extensively used. 
 
 150. Multi-stage Reaction Type. In the pure reaction tur- 
 bine, all of the expansion of the steam occurs in the moving 
 parts. At the present time, no pure reaction turbines are used. 
 The so-called reaction turbine in use expands its steam both in 
 the stationary and in the moving parts. It therefore employs a 
 mixture of the impulse principle and the reaction principle. This 
 mixed type is shown diagrammatically in Fig. 122. The steam 
 enters from the left and passes through a set of stationary blades 
 in which there occurs some drop in pressure. In passing through 
 the next set of blades, which are moving, a further drop in pres- 
 sure occurs. In this first set of rotor blades, the velocity gen- 
 erated in the stationary blades, and also that produced in the 
 rotor blades is absorbed. Hence there is a drop in pressure 
 
166 
 
 ENGINES AND BOILERS 
 
 throughout the whole length of the turbine. As the velocity is 
 used up as fast as it is produced, no very high steam velocity 
 exists at any time during its passage through the turbine. The 
 graphs show the drop in pressure and also the change in velocity 
 as the steam passes through the turbine. The exact ratio of 
 pressure-drop or velocity-change is not shown in the curves, as 
 the scales used in the curves on the small cut are only illustrative. 
 
 Multi 3tage Impure Reaction 
 FIG. 122 
 
 It has been shown previously ( 143) that the velocity of the 
 blades of a pure reaction turbine should be the same as that of 
 the steam relative to the blades, in order to obtain the highest 
 efficiency. This means that, for the conditions we assumed in 
 147, the steam velocity to be used up per stage should be 471. 
 This velocity corresponds to a kinetic energy per pound of steam 
 of 
 
 = 3470 foot-pounds. 
 
 This is equivalent to 3470/778 =4.46 B.t.u. per pound of steam, 
 which is one-fourth of the value that was obtained for the im- 
 
STEAM TURBINES 
 
 167 
 
 pulse turbine. For a heat drop of 175 B.t.u. (165 to 15 pounds 
 absolute), it will require 175/4.46=39 stages. Under the con- 
 densing conditions assumed in 147, 323/4.46 = 72 stages 
 would be necessary. For the pressure-stage impulse type, the 
 values were 10 and 18. Since the reaction turbine under discus- 
 sion employs a combination of the impulse principle and the 
 reaction principle, the values for the number of stages may be 
 taken as a mean between the values for the pure impulse type 
 and pure reaction type, that is 25 for the non-condensing condi- 
 tion, and 45 for the condensing condition. 
 
 The preceding computations show how much greater length 
 the reaction turbine must have than the impulse turbine. The 
 disadvantage of great length is offset to some extent by the fact 
 that the loss due to friction is less in the reaction type, since the 
 steam velocities are low. 
 
 151. Summary. To recapitulate, assuming that the speed is 
 3000 r. p. m., and that the diameter of the rotor is 3 feet, the 
 necessary stages for each of the various types is shown in the 
 following table. 
 
 
 Number of rows of buckets or 
 blades on the rotor 
 
 
 Heat-drop of 
 175 B.t.u. 
 
 Heat-drop of 
 323 B.t.u. 
 
 Velocity-stage impulse 
 
 3 
 10 
 4 
 
 40 
 25 
 
 4 
 
 18 
 8 
 72 
 45 
 
 Pressure-stage impulse . . 
 
 Mixed pressure- and velocity-stage impulse . 
 Pure reaction 
 Impure reaction 
 
 152. Change of Area of Steam Passage Space. It is neces- 
 sary to design a turbine so that the area of opening for the passage 
 of steam gives the proper velocity at all times. As the pressure 
 drops, the volume of steam increases. Hence there must be a 
 very much larger area for the passage of steam in the later stages 
 than in the first stages. This increase is accomplished in various 
 ways. If the diameter of all the rotor wheels is kept the same, 
 the area may be increased by having only partial peripheral 
 admission of the steam in the early stages. That is, the nozzles 
 or stationary vanes may extend only part way around the perim- 
 
168 
 
 ENGINES AND BOILERS 
 
 eter of the stator. In Fig. 123 a is the opening for the passage 
 of steam in the first stage of the turbine. In the next stage, the 
 opening extends farther around the stator, thus giving a large 
 area for the passage of steam, and so on till, in the later stages, 
 the opening extends entirely around the stator. 
 The area may be increased by having full 
 peripheral admission in all the stages, but 
 having the length of nozzles and blades or 
 buckets increase with each successive stage. 
 Figure 124 shows this scheme. Or if full 
 peripheral admission is given and the blades 
 and nozzles are kept the same length, the 
 area for the passage of steam may be in- 
 creased by increasing the diameter of each successive stage, as 
 shown in Fig. 125. ,Ih practice, combinations of these methods 
 of increasing the area for the passage of steam are used. This 
 increase in area to allow for the increase in the volume of steam 
 passing, must not be confused with the increase in area in a 
 
 FIG. 123 
 
 FIG. 124 
 
 FIG. 125 
 
 FIG. 126 
 
 velocity-stage turbine which is necessary to allow for the decrease 
 in steam velocity for the different velocity stages. 
 
 153. Leakage. The leakage of steam through an opening 
 depends upon the difference in pressure that exists on the two 
 sides of the opening, and upon the area of the opening. In most 
 steam turbines, there are necessarily differences in pressure, and 
 openings through which steam may escape. With the rotor of a 
 turbine moving at a high speed, it is not possible to have tight 
 joints at all places between the stationary and the moving parts, 
 for then the friction between these parts would create an even 
 
STEAM TURBINES 169 
 
 greater loss. In design and construction the clearances are kept 
 as small as is consistent with economy and safety, but even then 
 some leakage is sure to occur. 
 
 In Fig. 126, a difference in pressure exists between the two 
 sides of the stator at c and d; hence there will be a leakage of 
 steam at a. If there is a difference in pressure between d and e, 
 a leakage occurs at 6, and so on for the various stages. In the 
 velocity-stage impulse turbine there is no difference in pressure 
 after the steam leaves the nozzles; hence there is no tendency 
 to leak at either a or b. In the pressure-stage impulse type, there 
 is a difference in pressure between c and d, and therefore leakage 
 at a; but there is none between d and e. 
 
 In the impure reaction type there is a difference in pressure 
 between c and d, and also between d and e; hence there is leakage at 
 both a and b. The leakage at a can be kept at a minimum by 
 making the opening there as small as possible. This opening at a 
 depends upon the closeness of the fit and upon the diameter of 
 the shaft. Carbon or other form of packing is sometimes used 
 here to give a close fit. In most reaction turbines, however, the 
 shaft is very large, in fact it is even a drum, and in that case the 
 area of the opening is quite large. Packing cannot well be used 
 with large diameters. 
 
 In the reaction turbine the difference in pressure is not so 
 great between c and e as in the impulse type. In the reaction 
 turbine a leakage occurs at 6; hence the clearance there is kept as 
 small as is consistent with safety and economy. A certain amount 
 of spillage occurs at b because the rotor throws some of the steam 
 out by centrifugal force and it escapes through g, even if there 
 is no difference in pressure between d and e. 
 
 154. Loss Due to Running at Partial Capacity. Every tur- 
 bine is designed to expand the steam from a certain initial pres- 
 sure to a certain back pressure. This does not mean that the 
 turbine will run only under the pressure conditions assumed in 
 its design, but it does mean that the efficiency will be low if 
 there is any great difference from the assumed conditions. For 
 instance, if a turbine is designed to run non-condensing, and is 
 operated condensing, it means that the efficiency will be consid- 
 erably less than it would be if the turbine had been designed to 
 run condensing. The reason for this is easy to understand. 
 
170 ENGINES AND BOILERS 
 
 Every nozzle and each steam passage is designed to carry a cer- 
 tain volume of steam with a certain velocity. We have shown 
 that velocity is caused by drop in pressure, so that if the pressure- 
 drops are not as designed, the velocities are not such that the 
 efficiency will be a maximum. 
 
 When a turbine is designed for a certain load, and that load 
 is greatly increased or decreased, it is evident that the efficiency 
 will be decreased. In the design of the governor the aim is to 
 make this drop in efficiency as small as possible, while at the same 
 time maintaining uniform speed for all loads. It is also essential 
 that the governor be reliable and therefore not too complicated. 
 The simplest form of governor is a throttling governor, and many 
 of the smaller turbines are equipped with that kind. However, with 
 light loads, the throttling governor causes a large loss in efficiency 
 because the range in pressure between admission and exhaust 
 is so largely decreased. 
 
 On the larger machines some other means than throttling us- 
 ually is used. If the machine is of the impulse type, it has sta- 
 tionary nozzles, and the governor can be arranged to open the 
 proper number to take care of the load. If the machine had a 
 single stage, or if a proportional number of nozzles could be kept 
 open in the later stages of a multi-stage turbine, this would seem 
 to be an ideal arrangement. But the large machines never are 
 made single-stage and a governor to control all the nozzles in 
 all the stages would be very complicated. 
 
 In practice, as in the ordinary Curtis turbine, the governor 
 controls the nozzles of the first stage only. At light loads only 
 a few nozzles of the first stage are open, while at maximum load 
 all the first-stage nozzles are open. This arrangement assures 
 good economy in the first stage at light loads, but as all the later- 
 stage nozzles are open, there will be a loss there. 
 
 In the single-stage DeLaval turbine, a throttling governor is 
 used, but an effort is made to maintain the best economy by 
 having some of the nozzles controlled by hand-operated valves. 
 By this method, most of the nozzles can be shut off at small 
 load and opened up by hand for heavy load. The governor is 
 incapable of controlling the load entirely if manual control is 
 attempted. 
 
 In a reaction type of machine in which there are no stationary 
 nozzles, the preceding method of governor-control cannot be used. 
 
STEAM TURBINES 171 
 
 The Westinghouse Company, on their Parsons type of turbine, 
 has attempted to secure good efficiency at light loads by having 
 the governor admit the steam in puffs, which is the plan intro- 
 duced by Parsons. That is, the steam is admitted at full pres- 
 sure for a short time and then entirely cut off. The interval 
 between puffs is practically constant, but the length of time the 
 full steam pressure is on during the puff is controlled by the 
 governor. In the later stages, the effect of this kind of governor 
 approximates that of a plain throttling governor. In other makes 
 of reaction turbine a throttling governor is commonly used. 
 
 Large overloads are often carried in the various types of tur- 
 bines by turning full steam pressure into a later stage. In this 
 way the machine is able to carry a large excess of load at a re- 
 duced efficiency. If an electric generator is attached to the tur- 
 bine, care must be exercised that it is not overloaded long 
 enough to get too hot. This method is used only in emergencies, 
 and then only for short periods of time. 
 
 155. Summary of Losses in the Steam Turbine. The losses 
 that occur in a turbine have been mentioned in 140, 147, 
 153, 154, and elsewhere. We shall now make a summary of the 
 more serious causes of loss. 
 
 FRICTION LOSSES. Losses due to friction occur as follows : 
 
 (1) Between the shaft and the bearings, and in the packing 
 rings where the turbine is made steam-tight. With proper design 
 and construction this loss is quite small. 
 
 (2) Between the steam and parts of the turbine. The steam 
 friction varies directly as the steam pressure, and as the square 
 of the velocity between the steam and the parts. It also varies 
 as the amount of surface in contact with the steam. Hence the 
 amount of surface in contact with the steam should be kept as 
 small as possible and the velocity should be kept as low as possible. 
 The steam-friction loss in the first stages may be partially reclaimed 
 in the later stages since the heat generated tends to raise the tem- 
 perature of the steam. The steam friction occurs as the steam 
 flows through the nozzles and blades. 
 
 (3) There is also a friction loss between the rotor discs and the 
 steam surrounding them, at d, e, /, and g in Fig. 126. This loss 
 is called windage; it may be reduced by having the rotor discs 
 smooth and polished. 
 
172 ENGINES AND BOILERS 
 
 LEAKAGE LOSSES. Leakage occurs wherever a difference in pres- 
 sure exists on the two sides of an opening. It is thus seen that 
 there may be a leakage out of the casing or through the joints 
 between the pressure stages, or around the balance pistons of the 
 reaction turbine ( 160). 
 
 Another loss occurs under condensing conditions because air 
 leaks into the low-pressure parts of the turbine. This air tends to 
 lower the vacuum in the condenser, and may thereby cause a loss. 
 
 DISTURBANCE OF FLOW. A breaking up of the jet of steam, and 
 the consequent formation of eddies, causes a considerable loss in 
 some types of turbines. This is one of the causes of the low 
 efficiency of the velocity-stage impulse turbine ( 147). 
 
 LACK OF PROPER VELOCITY. It has been shown that the proper 
 relation must exist between the velocity of the buckets and that 
 of the jet to obtain the highest efficiency ( 143). If the velocity 
 of the blades or buckets is not correct, there will be a loss. Throt- 
 tling of steam by the governor will cause a loss. (See 154.) 
 
 EXIT VELOCITY. The turbine derives its energy by absorbing 
 the steam velocity. A high velocity of steam in the exhaust en- 
 tails a decided loss. The turbine should be designed and operated 
 to extract nearly all the steam velocity, and to leave only enough 
 in the exhaust to cause the steam to flow to the condenser. 
 
 156. Common Commercial Types. A great many makes of 
 turbines have been used in the past. Some of these were not 
 economical and have been replaced. Others have ceased to exist 
 for other reasons. At the present time there are a great many 
 different forms in use, but space will not permit us to consider 
 all of them. Some of the more common forms will be explained. 
 
 157. DeLaval Single-stage Steam Turbine. The DeLaval 
 single-stage turbine is the oldest of the types used at present. 
 It dates back to the years 1880-1890. DE LAVAL, the inventor of 
 the cream separator, sought to drive that device by means of a 
 direct-connected turbine. In his experiments he developed the 
 type that bears his name. Some minor changes have been made, 
 but its essential features remain the same. The DeLaval tur- 
 bine used in America is manufactured by an American company 
 that originally produced their machines under the DeLaval 
 patents. The same company now makes a multi-stage machine, 
 but it is not to be confused with the single-stage type. 
 
STEAM TURBINES 
 
 173 
 
 The essential features of the DeLaval turbine are as follows: 
 
 (1) The expanding nozzle in which all the pressure-drop occurs. 
 
 (2) The rotor wheel which carries a single row of buckets. 
 
 (3) A slender, flexible shaft that carries the wheel and transmits 
 the power to the gears. 
 
 (4) A set of reduction gears which lowers the speed so that it 
 is usable. 
 
 One style of the DeLaval turbine is shown in Fig. 127. The 
 
 FIG. 127 
 
 bucket wheel R is mounted on a flexible pinion shaft which is 
 supported by the bearings B, B'. This small shaft also carries 
 the small pinion P which is supported by the bearings &', 6'. 
 The pinion meshes with the two large helical gears shown in 
 the figure. The shafts that carry the large gears are supported 
 by the bearings b, b. The shafts of the electric generators or pumps 
 to be driven by the turbine are coupled to the large-gear shafts. 
 The governor also is driven 
 
 from one of these shafts. 
 
 The expanding nozzle is 
 shown in Fig. 128. The steam 
 enters from the left and the 
 
 FIG. 128 
 
 area of the opening gradually increases to a size that produces the 
 proper pressure and velocity. The amount of flare given to 
 the nozzle is governed by the drop in pressure that is desired. 
 
174 ENGINES AND BOILERS 
 
 The nozzle used if the turbine exhausts to the atmosphere is 
 called a non-condensing nozzle. If the turbine exhausts into a 
 condenser, the nozzle is called a condensing nozzle. The flare in the 
 non-condensing nozzle is less than that in the condensing nozzle. 
 
 One or more of the nozzles are open at all times; the rest are 
 opened or closed by hand, depending upon the amount of the 
 load. The governor is of the centrifugal type, and governs by 
 throttling the steam. The nozzles are placed in the casing par- 
 tition at N (Fig. 127). The steam chest is at $; the steam passes 
 from it through the nozzles, then through the row of buckets on 
 the rotor, and out into the exhaust space E. From E, the steam 
 is led to the condenser or to the atmosphere. 
 
 We saw in 145 that the bucket velocity of a single-stage tur- 
 bine must be very high in order to extract a reasonable part of 
 the kinetic energy of the steam. The high bucket-velocity causes 
 large stresses in the rotor. The rotor disc therefore is made of high 
 quality alloy steel and is very carefully designed and constructed. 
 A sufficient factor of safety exists at the rated speed, but any 
 large increase above this speed will cause failure in the wheel. 
 It is customary to make the rotor weakest at a point just inside 
 the rim where the buckets are attached, so that, if the breaking 
 speed is reached, only the rim of the rotor will tear loose. When 
 that happens, the speed will die down of itself because the buckets 
 are gone. If the shaft becomes sprung, the safety bearings around 
 the hub keep the main part of the rotor in place, so that no great 
 damage results. The steel casing around the rotor is strong 
 enough to keep any small fragments from breaking through; but if 
 the whole rotor should break in two, it is likely 
 that considerable damage would be done. 
 
 The buckets are drop-forged. They are at- 
 tached to the wheel as shown in Fig. 129. 
 Slots are machined into the perimeter of the 
 rotor and the buckets are forced into the slots 
 from the side. Should an individual bucket 
 become damaged, it may be removed and an- 
 FIG. 129 other put in its place. 
 
 At high speed, there is a tendency for the 
 rotor to vibrate because it is impossible to get the center of gravity 
 exactly in the center of rotation. There is a critical speed at which 
 the vibration is a maximum. At a speed above this critical value, 
 
 JM*!M of a-t 
 
STEAM TURBINES 175 
 
 the shaft or the bearings yield slightly, and the center of gravity 
 of the rotor comes into the axis of rotation. The rotor then runs 
 smoothly again. For smooth running, the speed must be either 
 very much less, or considerably greater, than the critical value. 
 Making the shaft small tends to reduce the critical speed. The 
 shaft of this turbine is made very small so that it may give 
 easily, and so run smoothly at its desired speed, which is normally 
 above the critical speed. While the diameter of the shaft is small, it 
 is ample to carry the power at the high velocity at which it runs. 
 
 The rotor speed in the smallest sizes is as high as 30,000 revo- 
 lutions per minute. For a 300-horsepower turbine, the speed is 
 10,000 revolutions per minute. It will be seen that it is imprac- 
 ticable to run an electric generator or a pump at such speed, 
 and to utilize the power developed, a speed reduction must be 
 used. Helical gears are used for this reduction in order to insure 
 smooth, quiet running. In some models, one large gear is used; 
 in others there are two, as shown in Fig. 127. The latter neces- 
 sitates two generators or pumps. When the gears are new, the 
 loss of power in the reduction is small. This loss increases as 
 the wear increases. Reduction gears are now used in some other 
 turbines, though they were used originally only in the DeLaval 
 turbine. 
 
 Aside from its use in the cream separator, the single-stage De- 
 Laval turbine has been used in driving electric generators, cen- 
 trifugal pumps and blowers. It is not used in sizes above 500 
 horsepower. The size is limited because the buckets would have 
 to be unreasonably long, or else the diameter of the rotor would 
 have to be too large, in order to get enough nozzles to play on 
 the buckets, 
 
 158. The Multi-pressure-stage Impulse Turbine. We have 
 seen that there is a practical limit to the size of single-stage tur- 
 bines. Because it gives the designer greater liberty of choice 
 of speeds, velocities, and bucket lengths, the multi-stage impulse 
 turbine is quite common in small and medium sizes. Moreover, 
 the efficiency of this type is comparatively high in these sizes. 
 For these reasons, it is quite common in sizes up to 5000 horse- 
 power. 
 
 Since it has a number of pressure stages or cells, this kind of 
 turbine is sometimes called the multi- cellular type. It is also 
 
176 
 
 ENGINES AND BOILERS 
 
 called the Rateau type, because RATEAU was the first to develop 
 it, but there is no essential difference between the Eateau tur- 
 bine and the numerous other multi-cellular turbines. 
 
 Figure 130 shows an Economy turbine, made by the Kerr Tur- 
 bine Company. As seen in the figure, there is a rotor shaft which 
 carries a number of rotor wheels or discs. Each wheel runs in a 
 pressure cell. The cells are separated by the heavy diaphragms 
 shown at a. The joint between the diaphragm and the shaft is 
 kept as nearly steam-tight as possible by making as close a fit 
 as is practicable under the circumstances. The buckets are fastened 
 
 FIG. 130 
 
 on the rim of the wheels in much the same manner as in the single- 
 stage DeLaval turbine. The shaft is supported by the bearings 
 B, B. Nozzles are located in the cell partitions as at N. The 
 number of nozzles increases from the first to the last stage, in 
 order to allow for the increased volume of the steam as the pressure 
 drops. 
 
 The steam enters the steam chest S, and passes through the 
 nozzle N t where it is partially expanded. Leaving the nozzle, it 
 passes through the first row of buckets 6, on the rotor, then 
 through the second set of nozzles, and so on till it arrives at the 
 exhaust E. Leakage of steam from the high-pressure end of the 
 turbine, and of air into the exhaust, is prevented by the stuffing- 
 boxes G, G. 
 
 The casing is lagged with a non-conducting material to prevent 
 the loss of heat by radiation. The bearings are equipped with 
 
STEAM TURBINES 177 
 
 ring oilers. As in other impulse turbines, there is no difference 
 between the pressure on the two sides of the rotor. Hence there 
 is no tendency to leak steam over the ends of the buckets, and it 
 is unnecessary to make the clearances between the buckets and 
 the stationary elements small. This obviates the necessity of 
 careful adjustments, and the danger of contact due to any un- 
 equal expansion of the parts. The diaphragms which compose 
 the cell walls are made rigid so that they will not spring as a 
 consequence of the differences in pressure on their opposite sides. 
 
 The turbine is supplied with a throttling governor of the cen- 
 trifugal type, driven from a worm on the main shaft. In the 
 smaller sizes it is direct-acting, that is, the position of the gov- 
 ernor weights directly controls the opening of the throttle valve. 
 In the larger sizes, it has been found desirable to have a relay 
 arrangement by which the throttle valve is thrown by steam or 
 by hydraulic pressure, which in turn is controlled by the position 
 of the governor weights. This arrangement gives better speed 
 regulation and does not require so large a governor. Consider- 
 able force is required to operate the large throttle valves. 
 
 Machines of this type made by other companies closely re- 
 semble the one just mentioned in essential features. Designers 
 often increase the length of the blades or buckets with each succes- 
 sive stage, thus helping to allow for the increase in volume. The 
 diameter of rotor wheels is sometimes made larger in the later 
 stages for the same purpose. Various devices are used to keep the 
 leakage from stage to stage at a minimum. 
 
 Carbon packing rings are sometimes used. In other makes, 
 labyrinth joints are used. No large mechanical pressure is allow- 
 able at the contact points between stages. The result is that 
 there is often a considerable loss from leakage of steam around 
 the wheels, sometimes as high as 15 to 20 per cent. 
 
 Thrust bearings are also used to prevent end-play of the shaft, 
 which might cause the buckets to rub and to become injured. 
 
 The practice of cutting holes in the rotor disc to insure an equal- 
 ization of pressure on the two sides of the rotor is common. The 
 shaft should be made large enough so that the speed at which it 
 is to run is well below the critical speed, and then excessive vibra- 
 tion will not occur. It is necessary to use good workmanship and 
 make the rotor well balanced; otherwise, severe strains would be 
 induced at the high speeds at which the turbine is run. 
 
178 ENGINES AND BOILERS 
 
 It is not our purpose to describe the details of construction of 
 all the various makes of turbines. It must be remembered that 
 each make has its own minor variations in construction, but the 
 preceding description holds in general for all makes of this type of 
 machine. 
 
 159. The Curtis Steam Turbine. The original patents for the 
 Curtis turbine were issued about 1895, and the General Electric 
 Company started production of this machine shortly afterwards. 
 For several years it was built in this country only by them. More 
 recently, however, the Curtis principle has been used largely in. 
 the high-pressure stages of some other machines. At first the 
 General Electric Company built the larger turbines with the axis 
 of the rotor vertical. The generator, which was direct-connected 
 to the rotor shaft, was placed on top of the turbine, and the con- 
 denser was placed directly beneath it. This was claimed to be an 
 ideal arrangement, and in some respects it was excellent, but all the 
 weight of the rotating parts of both the generator and the turbine 
 had to be supported by a step-bearing. With every precaution, 
 and the best of design, this step-bearing would sometimes fail, and 
 this failure often caused the buckets to strip. For very large, 
 fast-speed turbines, it was difficult to secure sufficient mechanical 
 rigidity for the bearing supports in vertical machines. The makers 
 therefore have come to prefer the horizontal type. A great many 
 of the vertical turbines are still in successful operation, however. 
 The following description is taken from General Electric Co. 
 Bulletin No. 4883. 
 
 Figure 131 shows diagrammatically the progress of the steam 
 in a Curtis turbine. Entering at A from the steam pipe, it 
 passes into the steam chest B, and then through one or more 
 open valves to the bowls C. The number of valves open de- 
 pends upon the load, and their action is controlled by the gov- 
 ernor. From the bowls C, the steam expands through diverg- 
 ing nozzles D, entering the first row of revolving buckets of 
 the first stage at E, then passing through the stationary buckets 
 F, which reverse its direction and redirect it against the second 
 revolving row G. 
 
 This constitutes the performance of the steam in one stage, 
 or pressure chamber. Having entered the first row of buckets 
 at E with relatively high velocity, it leaves the last row G 
 
STEAM TURBINES 
 
 179 
 
 with a relatively low velocity, its energy between the limits 
 of inlet and discharge pressure having been extracted in passing 
 from C to H. It has, however, a large amount of unexpended 
 energy, since the expansion from C to E has covered only a part 
 of the available pressure-range. The expansion process is, there- 
 fore, repeated in a second stage. 
 
 The steam, having left the buckets G, and having had its ve- 
 locity greatly reduced, reaches a second series of bowls H, 
 opening upon a second series of nozzles /. Through these the 
 
 FIG. 131 
 
 steam expands again from the first-stage pressure to some lower 
 pressure, again acquiring relatively high velocity in its expan- 
 sion through these nozzles, leaving them at J and impinging 
 upon and passing through the moving and stationary buckets 
 K, L and M, precisely as in the first stage. Again the velocity 
 acquired in the nozzle is expended in passing through the mov- 
 ing and stationary buckets, and the steam leaves the second row 
 M with relatively low velocity. 
 
 This process is continued in most large turbines through 
 several stages. Curtis machines as now constructed have a 
 
180 ENGINES AND BOILERS 
 
 single stage in the very small sizes, up to six or seven stages in 
 the larger ones. 
 
 Again referring to Fig. 131, it should be noticed particularly 
 that the pressure of the steam has not changed in its passage 
 from E to H, that is the pressure is practically constant at all 
 points in the stage. This fact leads to one of the principal 
 structural advantages of the Curtis type. . . . For, since the 
 pressure is uniform at all points, there is no tendency for the 
 steam to pass elsewhere than where directed by the nozzles, 
 i.e. through the buckets. Hence there is no necessity of main- 
 taining a close clearance between the ends of the revolving 
 buckets and the turbine casing. In practice free clearance is 
 provided from one to two inches. The reaction type, to se- 
 cure high economy, must be provided with a minimum clearance 
 at this point. 
 
 Also since the pressure on both sides of each wheel, i.e. at 
 E and H, Fig. 131, is the same, the wheel is in perfect equilib- 
 rium, there being no tendency for the steam to force the wheel 
 in an axial direction. As this is true of each wheel, the entire 
 rotor is in equilibrium, and there is practically no unbalanced 
 thrust. 
 
 As the steam expands from stage to stage, its volume rapidly 
 increases, and a greater area of steam passage must be pro- 
 vided. This is accomplished in two ways. First, by increas- 
 ing the height of the buckets and second, by increasing the 
 number and area of nozzles from stage to stage. Referring to 
 Fig. 131, it should be noted that the primary admission noz- 
 zles D actually extend around a small portion of the first stage 
 periphery; therefore only those buckets adjacent to the nozzles 
 at any instant are carrying active steam. This applies equally 
 to the stationary row and the second revolving row; in fact, 
 the stationary or intermediate buckets, as built, extend over a 
 small arc not much larger than the nozzle arc. In the second 
 stage, however, the nozzle arc becomes longer and wider, thus 
 permitting the flow of steam through a greater number of re- 
 volving buckets and necessitating a longer arc of stationary 
 buckets. Finally, when the low-pressure stages are reached, 
 the nozzles and stationary buckets extend all the way around 
 the circumference. 
 
 As previously mentioned, greater area for the steam flow is 
 
STEAM TURBINES 181 
 
 also provided by increasing the bucket lengths. For example, 
 
 the first-stage, or high-pressure, buckets are generally less than 
 
 an inch long, while those in the low-pressure stages may be 
 
 eight or ten inches in length. 
 
 It will be noticed that the length of the second row of moving 
 buckets in each stage, G and M, is greater than that of the first 
 row. This is made so, not to allow for any expansion of the 
 steam, but to provide for a decrease or velocity of the same vol- 
 ume of steam. 
 
 Customarily the buckets of the Curtis turbine are dovetailed 
 into the rim of the rotor wheel, somewhat as shown in Fig. 131. 
 At intervals the dovetail channel in the rim of the rotor is open 
 for the insertion of buckets. These openings are afterwards filled 
 with a spacing blank, and closed up. After the buckets are as- 
 sembled a shroud ring is riveted to their outer ends. The func- 
 tion of this ring is partly to stiffen the complete row and to reduce 
 vibration, but more especially to assist in retaining the steam 
 flow in the bucket space. Centrifugal force tends to throw the 
 steam out to the end of the bucket. 
 
 The governor is of the centrifugal type and controls the steam 
 supply by opening and closing some of the nozzles of the first 
 stage. Those nozzles that are open, are wide open, and those 
 that are closed, are tight shut. This scheme is positive and 
 reliable. It gives close speed regulation, and high efficiency at 
 light loads. In addition to the governor, the machine is equipped 
 with an emergency stop, whose function is to prevent excessive 
 speeds, should the governor fail for any reason. It consists of 
 an unequally weighted ring attached to, and revolving with, the 
 shaft. At any speed up to the normal speed, the weights are held 
 concentric with the shaft by springs, but at excessive speeds the 
 force of the springs is overcome. Then the ring revolves eccen- 
 trically, and trips the valve mechanism, causing the main throttle 
 valve to close instantly, thereby shutting off the steam supply. 
 
 Figure 132 shows a marine Curtis turbine. In marine service, 
 the speed must be very much less than is common in land prac- 
 tice, if the rotor is coupled directly to the propeller shaft. To 
 get this low speed, it is necessary to use very large diameters or 
 a great number of stages. Usually both, schemes are combined. 
 As has been stated previously, the efficiency after the second 
 stage of a velocity-staged impulse turbine is low, but in order to 
 
182 
 
STEAM TURBINES 183 
 
 reduce the speed properly, it may be desirable to use more than 
 two velocity stages, even if the efficiency is reduced. In land 
 practice this concession is not often made. In the forward tur- 
 bine shown in Fig. 132, there are four velocity stages in the first 
 pressure stage, three velocity stages in each pressure stage from 
 the second to the sixth, and two velocity stages in each pressure 
 stage from the seventh to the fourteenth. In the reverse tur- 
 bine, there are four velocity stages in each of the pressure stages. 
 
 It is customary in marine turbines to have the reverse turbine 
 mounted on the same shaft with the forward or ahead turbine. 
 It is put on the exhaust end of the shaft so that when it runs 
 idle, the rotor is in a high vacuum and therefore offers as little 
 resistance as possible to rotation. Since the friction loss varies 
 as the steam pressure, the loss is not great for low pressures. 
 
 The efficiency during reverse operation is quite poor because 
 there are only two pressure stages in the reverse turbine. The 
 reverse is in use only briefly and rather unfrequently. Hence the 
 the low efficiency of the reverse turbine is a negligible factor. 
 
 After a study of the previous types, Fig. 132 should be largely 
 self-explanatory, hence no detailed description need be given. 
 It is to be noted that the buckets of the seventh to fourteenth 
 stages are carried by a drum. As the pressure on the right end 
 of this drum is greater than that on the left end, it is seen that 
 there will be an end-thrust of the shaft. This thrust is taken 
 up by the thrust bearing T. The thrust bearing T is for the 
 turbine only, and not for the propeller. On every propeller shaft 
 there is a thrust bearing to take up the thrust of the propeller. 
 The bearings are provided with a water jacket to prevent heating. 
 In all large turbines, the bearings are cooled either by means of 
 water or oil. When oil is used, it is often cooled by a device 
 similar to the surface condenser. 
 
 160. The Parsons Steam Turbine. The Parsons turbine is 
 not only one of the oldest, but also one of the most common types. 
 It is usually made in medium and large sizes. In small sizes the 
 Parsons turbine is expensive, and is not very efficient. All of the 
 previous types have operated on the impulse principle, but this 
 one uses a mixture of impulse and reaction. It is ordinarily 
 called a reaction turbine. There are no distinct nozzles, as in 
 the impulse turbine. Instead, there are alternate fixed and mov- 
 
184 
 
STEAM TURBINES 185 
 
 ing blades, and expansion occurs in both. It is made by the 
 Westinghouse Company and by the Allis-Ch aimers Company. 
 
 Figure 133 shows one style of Parsons Turbine. Instead of 
 rotor wheels as in the previous types, the shaft carries a drum 
 on which the moving blades are mounted. Steam enters at the 
 steam inlet and passes through the governor valve to the left 
 of the first set of blades. Passing through the alternate fixed 
 and moving blades, it leaves through the exhaust outlet. 
 
 Full peripheral admission is used. The increase in passage 
 area is accomplished by increasing the length of blades from 
 stage to stage. The first-stage blades are very short, usually less 
 than an inch in length. After a large number of stages, the blades 
 are of considerable length. To avoid further increase in blade 
 length, the diameter of the drum is increased, and the first blades 
 on the larger diameter are made smaller so as to give the proper 
 passage area. Progressing to the right the length of blades again 
 increases, and again the diameter is increased. In the last stage 
 the blades are quite long. In the larger machines, the final blades 
 may be as much as a foot long. 
 
 Where the drum size is increased, there is an area exposed to 
 steam pressure from the left. This pressure causes an end-thrust 
 on the rotor to the right. To balance this end-thrust dummy 
 or balance pistons are placed on the left end of the drum, each 
 one being made of such a diameter that the steam pressure on its 
 right side produces the proper force to the left. Initial steam 
 pressure acts on the right of the smallest piston PI. An equaliz- 
 ing passage, EI, leads from the left of the second stage on the 
 drum to the right side of the middle balance piston P 2 , so that the 
 same steam pressure exists at 6 as at c. In like manner, the pres- 
 sure at e is the same as at d, on the right side of the largest balance 
 piston PS. A third equalizing pipe, E$, connects the exhaust space 
 with the left side of the piston P 3 . Of course there is some leak- 
 age of steam by the balance pistons, but this is minimized by 
 cutting annular grooves in the pistons and having rings on the 
 casing extend into these grooves to form a labyrinth packing. 
 
 Since the pressure drops in both the fixed and movable blades, 
 a leakage takes place, both between the ends of the fixed blades 
 and the drum, and over the ends of the moving blades. It is 
 therefore essential that the radial clearance be made as small as 
 is safe. Even with the smallest clearance possible, there is bound 
 
186 ENGINES AND BOILERS 
 
 to be some leakage. The proportion of radial clearance space to 
 the area of the steam passageway through the blades is propor- 
 tionally greater with the short blades than with the longer ones. 
 Hence more leakage occurs in the first stage than in the last. 
 It follows that there is better economy in a reaction turbine in 
 the low-pressure stages than in the high-pressure stages. 
 
 In some makes of Parsons turbines a shroud ring is fastened 
 over the ends of the blades. In others, the shroud is left off, but 
 the blades are lashed together by means of wires that pierce the 
 blades. This wire is comma shaped in cross section, and the tail 
 of the comma is caulked down on each side of the blades, thereby 
 keeping them in the same relative position. These shroud rings 
 or lashing wires do not add strength to resist the centrifugal force, 
 but they keep down the vibration or flutter of individual blades. 
 With long slender blades, the flutter might be more than the axial 
 clearance and the contact at high speed might cause the blades 
 to be torn loose. With only one blade loose, the whole system 
 of blading might be almost instantly torn out. With this type 
 of turbine, it is of the utmost importance that each blade be 
 properly secured and adjusted. With the previous types, the 
 stripping of blades may be localized to one stage, but in this, 
 the damage is apt to be more general. 
 
 The machine represented in Fig. 133 is equipped with an over- 
 load valve. If the load is more than the turbine is ordinarily 
 able to carry, this valve is opened, allowing high-pressure steam 
 to enter at the second step, as shown by the dotted arrows. The 
 steam consumption will be greatly increased, but a much larger 
 load may be carried. Since the governor still controls, the speed 
 may be considerably reduced. The overload valve is for emer- 
 gency operation only, and is not supposed to be used often. 
 
 The two joints between the shaft and the casing are made 
 tight by a water seal. As a turbine is ordinarily run condensing, 
 there is a tendency for air to leak in at these joints. This leak- 
 age of air into the turbine is likely to produce a greater loss of 
 efficiency than would a leakage of steam outward. The reason 
 for this is that the vacuum in the condenser is greatly impaired 
 by the air in the steam. If the seal is kept full of water, the 
 leakage inward will be of the water, which will have little or no 
 bad effect on the economy of the turbine. In some turbines low- 
 pressure steam is used in place of water with the same effect. 
 
STEAM TURBINES 187 
 
 As the weight of the rotor is very great, the bearings B, B must 
 be well constructed and kept cool. As in the previous type, the 
 bearings are usually kept cool by means of a circulation of oil. 
 With small clearances, no end-play can be allowed. To keep 
 the rotor from moving axially, a thrust bearing is used. The ad- 
 justment of the thrust bearing is made by means of the two 
 screws shown in the figure. 
 
 The number of stages in a reaction turbine is very great, which 
 necessitates a long rotor. With a long rotor, the changes in 
 length due to temperature changes is considerable. This distor- 
 tion increases with the amount of superheat. Hence little super- 
 heat can be used with some long reaction turbines. 
 
 To use more superheat, and also to limit the length of blades 
 in the later stages, the designers sometimes resort to a scheme 
 called compounding, i.e., the turbine will be cut into two separate 
 parts. The steam passes first through the high-pressure turbine, 
 and then is led to the low-pressure turbine. If the high- and 
 low-pressure turbines are both placed on the same shaft, the 
 machine is called a tandem-compound turbine. Since they are 
 on the same shaft, they must both have the same angular speed. 
 Sometimes better results can be obtained by mounting each tur- 
 bine on its own shaft and running the two at different speeds. 
 With the latter arrangement, the machine is called a cross-com- 
 pound turbine. In marine service, cross-compound turbines are 
 sometimes used, and then each turbine is connected to its own 
 propeller shaft. 
 
 In order to get rid of the balance pistons, Parsons turbines are 
 sometimes made double-flow. In the double-flow turbine, the 
 steam enters at the center of the casing and half flows to the 
 right, while the other half flows to the left. The two halves of 
 the drum are exact duplicates and any end-thrust on one half 
 is balanced by the thrust on the other. While this adds to the 
 total number of blades in the turbine, it does away with the 
 dummy pistons. Figure 134 shows the double-flow arrangement, 
 and is self-explanatory. Quite often the low-pressure turbine in 
 the compound arrangement is made for double flow. 
 
 The governor used on the Parsons turbine made by the West- 
 inghouse Company is of the blast type. As mentioned in 154, 
 the steam is admitted in blasts or puffs. The speed of the gov- 
 ernor is much less than that of the shaft, since it is reduced by 
 
188 
 
 ENGINES AND BOILERS 
 
 a worm gear from the main shaft. A diagram of this type of 
 governor is shown in Fig. 135. The rod C is given an up and 
 
 FIG. 134 
 
 down motion from an eccentric on the governor shaft. The pivots 
 D and E being fixed, the reciprocating motion is communicated 
 by means of the links and levers to the small pilot valve A. The 
 
 recess on the valve A 
 allows steam to enter 
 periodically through 
 the pipe, to pass 
 through the ports, and 
 to push up on the 
 under side of the pis- 
 ton B. The fit around 
 the rod running down 
 from B is loose, so 
 that the pressure soon 
 drops. The vertical 
 
 p IG 135 position of the point F 
 
 is controlled by the 
 
 position of the balls of the governor. This in turn controls the 
 length of time the pilot valve admits steam under the piston B. 
 
STEAM TURBINES 
 
 189 
 
 The piston B is connected to the main steam valve of the turbine. 
 When B is down, the main steam valve is wide open. When it is 
 up, the steam is shut off. The length of the time it is up for each 
 puff is seen to depend upon the position of the governor weights. 
 
 161. The Westinghouse Turbine. Aside from the Parsons 
 turbine just described, the Westinghouse Company has made for 
 several years a turbine which they call the Westinghouse. The 
 same type is made under other names, and has become quite 
 popular abroad. It consists of one impulse stage, such as exists 
 in the Curtis turbine, i.e., one pressure stage, with two velocity 
 stages, and the remainder of the turbine of the Parsons type. 
 This Curtis stage may be used with a single-flow Parsons, or a 
 double-flow Parsons, or with single-flow intermediate Parsons 
 stages combined with double-flow Parsons in the final stages. 
 
 Figure 136 illustrates the Westinghouse type in which there is 
 
 FIG. 136 
 
 a Curtis stage combined with a double-flow Parsons. The steam 
 enters the inlet at A and passes through the first stage exactly 
 as in the Curtis turbine; it then divides, half going to the right 
 and half to the left, through the reaction stages, and comes out 
 to the exhaust at the two ends of the casing. Partial peripheral 
 admission is used in the Curtis stage and the governor controls 
 the number of nozzles in use, as in the Curtis type. 
 
 There are certain advantages to be gained by the mixed Westing- 
 house type. First, the length of the rotor is shortened, because 
 
190 ENGINES AND BOILERS 
 
 the length taken up by the Curtis stage is only a small part of 
 that which would be required by the same pressure drop in the 
 reaction type. Second, the efficiency in the high-pressure part 
 of the turbine is increased. We have seen that there is much 
 leakage in the high-pressure stages of the Parsons type because 
 the blade lengths are short in these stages, and the leakage is 
 proportionately large. Third, it allows the governor to control 
 the steam supply by shutting off nozzles, which is superior to 
 either the throttling or blast governing. 
 
 Turbines are also in use that have one or two Curtis high-pres- 
 sure stages, and low-pressure stages of the Rateau type. This 
 combination is not common at present in this country, but it is 
 found in some turbines in Europe. 
 
 There are many factors that determine the choice of type of 
 a turbine. A satisfactory discussion is impossible here. Given 
 the size, the kind of service, and the various operating conditions, 
 the designer is able to say which type is the best. 
 
 162. Other Types. In addition to the types heretofore de- 
 scribed, there are various other small turbines in use. They are 
 principally of the Pelton type, i.e. they are built on the same 
 lines as a Pelton water wheel. Buckets are cut in the outer 
 rim of a rotor and the steam enters them in a direction nearly 
 tangential to the rotor. They are usually built in small sizes 
 and are used for driving fans, blowers, and pumps. In such 
 service simplicity counts for more than high efficiency. 
 
 163. Low-pressure Turbines. The reciprocating steam engine 
 utilizes economically a greater amount of the available energy 
 of the steam at high pressures than at low pressures. That is, 
 the efficiency of a reciprocating engine is relatively higher at a prac- 
 tical range of pressures above the atmosphere than below atmos- 
 phere. This does not mean that the non-condensing engine is 
 more efficient than the condensing, but that of two engines, one 
 taking steam at a high pressure and expanding to atmospheric 
 pressure, and the other taking steam at atmospheric pressure 
 and expanding down to that of a good vacuum, the former will 
 be the more efficient. There is about the same amount of energy 
 available for doing work in expanding from a medium boiler 
 pressure down to that of the atmosphere, as there is in expand- 
 ing from atmospheric pressure to that of a good vacuum. How- 
 
STEAM TURBINES 191 
 
 ever, the amount of expansion is much larger in the second case. To 
 utilize this great amount of expansion at low pressure, the cylinder 
 would have to be very large; consequently a large cylinder loss 
 would occur. With the turbine, the reverse is true, i.e. the turbine 
 suffers relatively less loss at low pressures than at high pressures. 
 It has been shown by experience that the power out-put of a 
 plant using non-condensing engines can be increased between 80 and 
 100 per cent by taking steam from the engines and sending it 
 through what are called low-pressure turbines which exhaust into 
 a notably excellent vacuum. This power increase is obtained 
 from the steam without any extra coal cost or any increase in 
 the size of the boiler plant, through changing the exhaust pres- 
 sure from that of the atmosphere to that of the vacuum by the 
 introduction of the turbine and its condenser. It sometimes 
 happens that an existing plant, equipped with reciprocating en- 
 gines, is to be enlarged, and in some instances the low-pressure 
 turbine has been used to solve this problem. In case the existing 
 engines are already condensing, it has been found that a net gain 
 in power of 25 to 40 per cent may result by using their exhaust for 
 the turbines, on account of the more perfect vacuum used with 
 turbines since they are not subject to cylinder condensation and 
 since the air leakage is less. The low-pressure turbine may take 
 steam from engines, pumps, air compressors, hoists, etc. 
 
 164. Mixed-pressure Turbines. The mixed-pressure turbine 
 is much the same as the low-pressure turbine. It uses low- 
 pressure steam, but it may also use some high-pressure steam 
 at the same time. The high-pressure steam is admitted in vary- 
 ing amounts, to make up any deficiency in the supply of the low- 
 pressure steam. This may be done by throttling the high-pressure 
 steam down to the low-pressure before using it, or the turbine 
 may be equipped with high-pressure stages to use the steam 
 without throttling. The latter is the more efficient way of using 
 the high-pressure steam. 
 
 165. Bleeder Turbines. In some plants equipped with tur- 
 bines, a supply of low-pressure steam is required for heating or 
 for some manufacturing process. Rather than take high-pressure 
 steam and throttle it down to the required pressure, the low- 
 pressure steam may be drawn from the turbine at an intermediate 
 stage. Then the machine is said to be a bleeder turbine. 
 
192 ENGINES AND BOILERS 
 
 166. The Use of Superheated Steam. Turbines are, in gen- 
 eral, well adapted to the use of superheated steam. Comparative 
 tests show a marked increase of efficiency when superheated steam 
 is used. It has been claimed that this is due partly to a lessening 
 of friction between the steam and the parts, but it is due mainly 
 to the increased available energy in the steam which enters the 
 turbine. Superheated steam also gives an increased efficiency 
 when used in the reciprocating engine, but its use there is accom- 
 panied by an added difficulty in lubrication. With the turbine, 
 lubrication is no more difficult with superheated steam than with 
 saturated steam, since the steam-wet metal moving parts are not 
 in rubbing contact with other metal parts. Superheating the 
 steam used for turbines reduces the wear on the blading, com- 
 pared with steam which is saturated or wet at the inlet. 
 
 167. The Marine Turbine. The turbine has been used in 
 marine service since the early years of its development. Many 
 factors make the turbine particularly well adapted to this service. 
 It occupies less space than a reciprocating engine, and it is lighter. 
 It gives a uniform torque on the propeller shaft and does not 
 cause as much vibration of the ship's hull as does the recipro- 
 cating engine. On the other hand, the turbine is a high-speed 
 machine, while for good efficiency the propeller must be run at 
 rather a low speed. Direct connection of the turbine to the pro- 
 peller shaft is, of course, the simplest arrangement. When this 
 is done, it is necessary to design the turbine to run as slowly as 
 possible, and to design the propeller to run as fast as possible. 
 Even then a compromise often has to be made: the propeller 
 has to run too fast, and the turbine too slow, for best efficiency. 
 Hence direct-connected turbines are limited to swift boats. One 
 way out of this difficulty is to reduce the speed by means of gears. 
 While this is sometimes done, it is not entirely satisfactory, since 
 the gears are not highly efficient when worn. 
 
 A method of drive that is being used to a considerable extent 
 is the electric drive. With this, turbines similar to those used 
 on land are used to drive electric generators, and the current 
 is used by motors direct-connected to the propeller shafts. This 
 allows both the turbine and the propeller to run at the proper 
 speed. It also permits great flexibility of arrangement, and con- 
 venience in steering and in maneuvering. 
 
CHAPTER XI 
 GAS ENGINES 
 
 168. Introduction. The small-sized internal-combustion en- 
 gine is perhaps better known to the average person than any 
 other prime mover. During the past twenty years it has exerted 
 a very marked effect upon our manner of living. It has made 
 possible the automobile, the motor truck, the gasoline tractor, 
 and the airplane. It has replaced the more expensive, small 
 hand machines and horse machines on our farms. It is indeed 
 hard to estimate the value to mankind of the gasoline engine. 
 
 In plants in which there are combustible waste gases, such as 
 those from the blast furnaces and coke ovens, large-size gas 
 engine units have come into use, and they are there more eco- 
 nomical than steam engines. In marine service, where space is 
 a prime consideration, as in the submarine, the internal-combus- 
 tion engine is generally used. 
 
 169. History. Many years ago, men of an inventive turn 
 of mind dreamed of gunpowder engines or explosive engines, and 
 many patents were taken out for these devices. Records show 
 that as early as 1680 HUYGHENS produced a working model of a 
 gunpowder engine. It was of no practical importance. Many 
 other inventors produced various forms of engines, but not till 
 1860 was an internal-combustion engine produced commercially. 
 At that time LENOIR started building gas engines. In the course 
 of a few years four or five hundred of these engines were built, 
 but the engine was not very efficient as it lacked compression for 
 the unignited gases. 
 
 The first really scientific work done on the gas engine was that 
 of the French engineer, BEAU DE ROCHAS, who laid down the fol- 
 lowing four conditions as being essential to high efficiency. 
 
 (1) The largest cylinder volume, with smallest exposed surface, 
 i.e., the proper relation of diameter to length of stroke. 
 
 (2) The greatest possible rapidity of explosion, i.e., the maxi- 
 mum piston speed. 
 
 (3) Highest possible pressure at the beginning of the expansion. 
 
 (4) The greatest possible expansion of burnt gases. 
 
 The same engineer proposed to obtain the above results by 
 means of a single cylinder and to operate his engine upon the 
 
 following cycle. 
 
 193 
 
194 ENGINES AND BOILERS 
 
 (1) Draw in a charge of mixed air and gas through an entire 
 stroke. 
 
 (2) Compress this mixture during the next stroke. 
 
 (3) Ignite the compressed combustible mixture at the beginning 
 of the third stroke, and expand the products of combustion dur- 
 ing the stroke. 
 
 (4) Discharge the burned gases on the following stroke. 
 
 The above is known as the four-stroke cycle, or the Otto cycle, 
 and is the one most commonly used. It will be considered more 
 in detail later. 
 
 A few years after Beau de Rochas secured his patent, two in- 
 ventors, OTTO and LANGEN, produced an engine that had a ver- 
 tical cylinder with a free piston. The explosion of uncompressed 
 gases drove this piston upward. On its downward stroke, a rack 
 attached to the piston engaged, through a clutch, with a spur gear 
 that drove the machinery. While this engine was more efficient 
 than any produced before, it was noisy. Although several thou- 
 sand were produced, the design was abandoned after a new design 
 using compression of the admitted gases was produced by Otto. 
 
 The new Otto engine was shown at the Paris Exhibition in 
 1878. It operated on the cycle formulated by Beau de Rochas, 
 and may be considered as the first modern gas engine. 
 
 A few years later, DUGALD CLERK brought out an engine with a 
 two-stroke cycle. Many machines of this type are in use, es- 
 pecially in motor boats and the like. 
 
 Mention should be made of the Brayton engine, which was 
 produced at about the same time as the Otto-Langen engine. 
 GEORGE B. BRAYTON was an American, and many of his engines 
 were used in this country. The principle of its operation is quite 
 different from that of the others mentioned, but it need not be 
 explained here. 
 
 The Diesel engine dates back to 1892, but it was not perfected 
 until some time later. Since then, the semi-Diesel and other oil- 
 burning engines have come into use. 
 
 These historical notes are given, not to explain the principles 
 of operation of the early engines, but to indicate the length of 
 the period in which the internal-combustion engine was evolved. 
 
 170. Cycles of Operation. Modern internal-combustion en- 
 gines operate upon either one of two cycles: the four-stroke 
 
GAS ENGINES 
 
 195 
 
 cycle or the two-stroke cycle. These terms are usually abbre- 
 viated to four-cycle and two-cycle. The four-stroke cycle is some- 
 times called the Otto cycle, and the two-stroke cycle is occa- 
 sionally known as the Clerk cycle. Each of these cycles is used 
 with gas, gasoline, Diesel, semi-Diesel, and other oil engines. 
 
 171. The Four-stroke Cycle. In the four-stroke cycle there 
 are four strokes of the piston, two forward, and two backward. 
 These occur as the shaft makes two complete revolutions. Figure 
 
 Met 
 
 fxhoust 
 
 FIG. 137 
 
 137 represents an engine cylinder with its piston P. The inlet 
 valve is at A, and the exhaust valve at B. When the piston is 
 at its crank-end dead-center position, the volume to the left of 
 it is the piston displacement plus the clearance. Both valves, A 
 and B, are closed, and the space to the left of the piston is filled 
 with a mixture of air and fuel. 
 
 During the first stroke, the piston moves from its crank-end to 
 its head-end dead center, compressing the mixture into the clear- 
 ance space. Near the head-end dead center, the compressed mix- 
 ture is ignited, whereupon it burns, and its pressure suddenly 
 increases. 
 
 On the second stroke the piston moves from the head-end dead 
 center to the crank-end dead center, while the burnt gases expand 
 and do work upon the piston. Near the end of the second stroke, 
 the exhaust valve B opens. 
 
 As the piston moves to the left on the third stroke, the burnt 
 gas is forced out to the exhaust. The burnt gas that is left in 
 the clearance space is not expelled. At the end of the third 
 stroke the exhaust valve closes. 
 
 At the beginning of the fourth stroke, the inlet valve A opens. 
 As the piston moves to the right, a fresh charge of air and fuel 
 
196 
 
 ENGINES AND BOILERS 
 
 is sucked into the cylinder. At the end of the fourth stroke the 
 inlet valve closes. This completes the cycle of operation. 
 
 Figure 138 shows the indicator card of the four-stroke cycle 
 engine. Starting from E, at a little below the atmospheric pres- 
 
 Atmospheric Line 
 
 FIG. 138 
 
 sure, the charge is compressed during the first stroke to the 
 pressure at the point A. From A to B, the charge is burned 
 and the pressure rises. From B to C expansion takes place. From 
 C to D the burnt gases are expelled. The suction stroke is rep- 
 resented by DE. The four strokes then represent compression, 
 burning and expansion, scavenging, and suction. On the card, L 
 represents the length of stroke, and F the clearance. 
 
 172. The Two-stroke Cycle. This cycle is completed in one 
 revolution. Figures 139 and 140 show a two-stroke cycle engine 
 
 FIG. 139 
 
 such as is often used on motor boats. Due to the fact that the 
 piston covers and uncovers the admission and the exhaust ports, 
 it is often called a valueless engine. 
 
GAS ENGINES 
 
 197 
 
 In Fig. 139, the piston is shown at the crank-end dead center. 
 Both the inlet and exhaust ports are open. There is a small 
 compression in the crank case and the combustible mixture of 
 air and fuel is forced up and into the cylinder through the port A. 
 There is a baffle on the top of the piston which deflects the in- 
 coming mixture to the top of the cylinder. At the same time the 
 burnt gases from the previous stroke are escaping through the 
 
 FIG. 140 
 
 exhaust port B. Naturally a little of the unburned gas will es- 
 cape before the exhaust port is closed. 
 
 As the piston moves upward on its first stroke, it covers the 
 ports A and B, and then compresses the mixture into the clear- 
 ance space. At the head-end dead center, Fig. 140, ignition takes 
 place, and the piston is forced downward on the second stroke 
 by the pressure produced. The burnt gases expand until the 
 exhaust port B is uncovered. They then escape to the exhaust. 
 As the piston moves on down, the inlet port A is uncovered, and 
 the fresh gas coming in at A sweeps out more of the burnt gas. 
 As the piston moves upward a slight vacuum is formed in the 
 crank case. When the piston gets nearly to the top of its travel, 
 a port communicating to the carburetor or fuel and air supply 
 is uncovered, and the combustible mixture is sucked into the 
 crank case. Upon the piston's downward stroke this mixture is 
 compressed enough to force it into the cylinder when the port A 
 is uncovered. 
 
 In Fig. 141 another two-stroke cycle engine is shown. In the 
 large size of these engines, separate pumps for air and gas are 
 
198 
 
 ENGINES AND BOILERS 
 
 used instead of the compression in the crank case. The engine 
 is double-acting, and the exhaust port is placed around the cylinder 
 midway between the two ends. The piston P uncovers this ex- 
 haust port near the end of each stroke. Gas and air is com- 
 pressed in the pumps shown. The piston valves of the pumps 
 deliver the gas and air alternately to the two ends of the cylinder. 
 
 FIG. 141 
 
 The air and gas are mixed just before they enter the admission 
 valve I. In Fig. 141, gas and air are compressed in the left ends 
 of the pumps, and are forced into the left end of the engine cylinder. 
 As the piston starts to the left, the left admission valve closes, 
 and the mixture is compressed into the clearance space. At dead 
 center the charge is fired, and expansion takes place as the piston 
 moves to the right. When the piston uncovers the exhaust port, 
 the burnt gases escape. In Fig. 141, the amount of gas forced 
 into the cylinder is controlled by butterfly valves whose position 
 is controlled by the governor. 
 
 The indicator card of the two-stroke cycle engine of Figs. 139 
 and 140 is shown in Fig. 142. Compression takes place from 
 E to A, burning from A to B, and expansion from B to C. From 
 C to D, and from D to E, the 'exhaust of the burnt gases takes 
 place. The admission of the charge occurs from H to D and 
 
GAS ENGINES 
 
 199 
 
 from D to G. It is seen that the exhaust port opens a little 
 sooner than the inlet port. 
 
 173. Classification from Fuel Used. Internal-combustion en- 
 gines are called by different names, according to the fuel used. 
 We have the gas, gasoline, oil, Diesel and semi-Diesel engines. 
 The fundamental principle is much the same in all of them, dif- 
 ference being largely a matter of detail in design and in the feed 
 of the fuels. 
 
 In the earlier gas engines, city or coal gas was often used. 
 Then, in the days of the natural gas booms in this country, gas 
 engines became quite common. With these kinds of gas, it was 
 
 -& Atmospheric /ne 
 
 FIG. 142 
 
 not possible to give the mixture of fuel and air a very high com- 
 pression, because the temperature during compression might 
 be so high that ignition would occur before the end of the com- 
 pression stroke. With the use of producer gas or blast-furnace 
 gas the compression can safely be carried higher; hence we find 
 it common to use a less amount of clearance with engines designed 
 to use a lean gas for fuel. With a small clearance the compres- 
 sion is higher. 
 
 The internal combustion engine with which we are most familiar 
 is the gasoline engine. Gasoline will vaporize partially at ordi- 
 nary temperatures; hence a spray of the liquid fuel is mixed 
 with the air as it goes to the cylinder. While this spray is com- 
 monly not all vaporized before reaching the cylinder, it is sufficiently 
 vaporized so that an explosive mixture results, and the charge 
 is fired. If the spray is fine enough and if sufficient time is given 
 during the stroke, the gasoline will be very nearly all buined. 
 Of course there are differences in gasolines, some kinds being more 
 volatile than others. The device that introduces the spray into the 
 
200 
 
 ENGINES AND BOILERS 
 
 air intake is called a mixing valve, or a carburetor. With the less 
 volatile liquid fuels, such as kerosene, heat is sometimes applied 
 to help in vaporizing it before it is introduced into the cylinder. 
 
 When liquid fuels heavier than gasoline are used, it is common 
 to spray them into the cylinder during the compression stroke. 
 Often the spray strikes a hot plate in the cylinder and the fuel is 
 sufficiently vaporized so that ignition can take place at the end of 
 the stroke. The compression in low-pressure oil engines is no 
 greater than in some gas engines, usually about 60 pounds per 
 square inch. 
 
 In the Diesel engine the clearance is much less and a com- 
 pression of 500 to 600 pounds per square inch is attained. Prac- 
 
 df/nospheric Line 
 FIG. 143 
 
 tically all liquid fuels will partially burn at a temperature at- 
 tained by the compression of air to 200 to 300 pounds per square 
 inch. To prevent premature ignition, the liquid fuel is sprayed 
 into the cylinder at the beginning of the forward or working 
 stroke in Diesel engines. 
 
 Air alone is compressed during the compression stroke. At a 
 pressure of 500 to 600 pounds its temperature will be in the 
 neighborhood of 1000 F. This is sufficient to ignite and com- 
 pletely burn the oil that is sprayed in. The length of time the 
 oil is injected into the cylinder usually is regulated by the gov- 
 ernor. The Diesel engine may operate on either the four-stroke 
 or on the two-stroke cycle. 
 
 The indicator diagram for the four-cycle Diesel engine is shown 
 in Fig. 143. On the first stroke, air is compressed from a pressure 
 a little below that of the atmosphere, shown at E, to 500 or 600 
 
GAS ENGINES 
 
 201 
 
 pounds per square inch, as shown at A. From A to B, the fuel 
 is injected and burned. Expansion of the burnt gas takes place 
 from B to C. The cylinder is scavenged from C to D, and a 
 fresh charge of air is drawn in from D to E. 
 
 The high pressures necessary in the Diesel engine have been 
 found troublesome from a mechanical standpoint, and there has 
 been a tendency to reduce the high compression. With a com- 
 pression around 200 to 300 pounds the term semi-Diesel is used. 
 There is but little difference in the theory of operation between 
 the Diesel and semi-Diesel. Oil is injected at the opening of 
 the expansion stroke as before. However, on account of the 
 
 FIG. 144 
 
 lower temperature of compression, aid to the vaporization of the 
 oil is given by the addition of a hot bulb located in the head 
 of the cylinder. 
 
 Figure 144 shows this type of engine. Before starting, the 
 bulb is heated by means of the burner B. After the engine has 
 started the bulb will be hot enough without the aid of the burner. 
 In Fig. 144, air is drawn into the crank case and compressed as 
 the piston moves forward. With the piston near the crank-end 
 dead center, the exhaust port is uncovered and the air is blown 
 in through the ports at the top of the cylinder. As the piston 
 returns to the left, the charge of fresh air is compressed. With 
 
202 ENGINES AND BOILERS 
 
 the piston on head-end dead center, the oil pump injects the fuel 
 into the cylinder, and the spray strikes the lip of the hot bulb. 
 The temperature of the bulb is high enough so that the fuel is 
 ignited and practically all burned. 
 
 This engine operates on the two-stroke cycle. On the larger en- 
 gines the four-stroke cycle is more common. On heavy loads, 
 there is often a tendency to knock in the semi-Diesel engine. This 
 is relieved by the injection of a small amount of water with the 
 fuel, which does not seem to lessen the efficiency of the engine. 
 
 174. Efficiency. The efficiency of an engine operating on the 
 Carnot cycle is (T\Tz)/Ti, where T\ is the absolute tempera- 
 ture during combustion, and T^ the absolute temperature of the 
 gases in the exhaust. Of course none of our engines operate on 
 the Carnot cycle, but their efficiency does depend upon the range 
 of temperature in the cylinder. Other factors being the same, it is 
 evident that the highest thermal efficiency will occur in that engine 
 which has the largest range of temperatures during the working 
 stroke. From this it is seen that those engines with the highest 
 compressions, and therefore the highest combustion temperatures, 
 will have the highest efficiency. This also explains the fact 
 that gas engines using a lean gas, such as blast-furnace gas, may 
 have a higher efficiency than those that operate on natural gas 
 or gasoline vapor. Of all the internal-combustion engines, the 
 Diesel has the highest thermal efficiency. The efficiency based 
 on the brake horsepower ranges from 30 to 35 per cent. Other 
 gas engines give somewhat lower efficiency. 
 
 175. Fuels. Gas engines may operate on almost any com- 
 bustible gas. Naturally the more expensive gases are but little 
 used. Ordinary city gas is commonly a mixture of coal gas and 
 water gas. As ordinarily produced it is too expensive for exten- 
 sive use in gas engines. Where natural gas is plentiful and cheap, 
 it is commonly used for gas engines. 
 
 At some blast-furnace plants, the gas from the furnace is used 
 for fuel in the gas engines that drive the blowers. This gas is 
 not of what we commonly call high quality, that is its heat con- 
 tent per cubic foot is much lower than that of natural gas or 
 coal gas, but it gives excellent results when used in the engines. 
 
 The by-product gas from coke ovens is being used more and 
 more as the efficiency of these plants is looked after. There are 
 
GAS ENGINES 203 
 
 also quite a number of plants, especially in the east, where pro- 
 ducer gas is used for gas engines. 
 
 Natural gas, while it varies in composition, may be said to be 
 composed mainly of marsh gas, CH 4 . In some natural gases, 
 there is a considerable free hydrogen and also an appreciable 
 amount of olefiant gas, C 2 H4. The heat value of natural gas usu- 
 ally is between 900 and 1000 B.t.u. per cubic foot. 
 
 The illuminating gas used in cities varies widely in its com- 
 position, depending upon how it is made. It usually contains 
 about 40 per cent H2, 30 per cent CH 4 , and varying amounts of 
 CO and C 2 H 4 besides CO2 and N 2 . The heating value aver- 
 ages from 500 to 600 B.t.u. per cubic foot. 
 
 Coke-oven gas contains about 50 per cent H2 and 35 per cent 
 CH 4 . Its heating value is about the same as that of illuminating 
 gas. 
 
 The principal combustible substance in blast furnace gas is CO, 
 which ordinarily runs about 25 per cent. The heating value of 
 blast-furnace gas is but little over 100 B.t.u. per cubic foot. 
 
 Producer gas, while it is variable, contains about 15 per cent 
 H 2 , and 25 per cent CO. It has a heat value of about 145 B.t.u. 
 per cubic foot. 
 
 Practically all these gases contain a little 02 and varying amounts 
 of C02 and N2. These substances in the gas add no heating value 
 to it. 
 
 The liquid fuels used in internal-combustion engines vary from 
 crude oil to more refined products, such as gasoline. Many 
 Diesel engines seem able to burn crude oil very well, but some 
 of the semi-Diesel and oil engines do better on the more volatile 
 product, such as kerosene. The great demand for gasoline has 
 led to a gradual lowering of the flash-point of this product. Car- 
 buretors that used to give good results with the gasoline sold a 
 few years ago, now have trouble in using the commercial grades. 
 The development of carburetors has had to keep step with the 
 change in the quality of the product they have to handle. 
 
 176. The Gasoline Carburetor. There are a great variety of 
 mixing valves or carburetors on the market. We cannot hope 
 to describe all of the various types in this course. Only one simple 
 form will be described, but the fundamental principle is the same 
 in all. This principle is to divide the liquid fuel into as fine a 
 
204 
 
 ENGINES AND BOILERS 
 
 spray as possible and to mix it thoroughly with air. Some of 
 the liquid is evaporated, but it is doubtful whether it is ever all 
 vaporized. 
 
 Evaporation is not necessary if the liquid particles are finely 
 enough divided and are thoroughly mixed with the air. Even 
 solid combustible matter is explosive when mixed with air, as 
 is shown by flour-mill explosions and the explosions in mines due 
 to dust of inflammable materials. 
 
 Figure 145 shows a gasoline carburetor. The main body of 
 the carburetor B is partly filled with gasoline. The height of 
 
 FIG. 145 
 
 the liquid is kept very near to a constant level by means of a 
 float F, which is attached by means of a lever to the valve H 
 which leads from the supply. Air enters through the opening 
 at the top and passes down through the passage C. Turning to 
 the left, it passes out to the pipe leading to the engine. A spray 
 of liquid is injected into the air through the needle valve D. 
 The opening in the needle valve D is adjusted by the handle E. 
 The opening of the needle valve into the air passage is a little 
 above the liquid level in B, so that no gasoline runs out unless 
 there is a current of air to suck up the liquid. There is at all 
 times an opening for the air to enter the carburetor at A, but 
 this opening may be increased when a large supply is needed by 
 the suction pulling back the valve A. The valve A is held on 
 its seat by a light spring 0. The tension in the spring may be 
 
GAS ENGINES 205 
 
 adjusted by turning the screw M. By the proper adjustment 
 of the air valve A and the needle valve Z), any richness of mix- 
 ture may be secured. The amount of mixture of air and gaso- 
 line leaving the carburetor to enter the engine is regulated by the 
 throttle K. The bowl of the carburetor may be drained by open- 
 ing the cock T. 
 
 177. The Gas Producer. A large amount of publicity has 
 been given to the subject of gas producers for the gas engine, 
 and much research work has been done on the subject. It is only 
 just, however, to say that the producer plant has been somewhat 
 of a disappointment in America. While trial tests show up re- 
 markably well, and the claims of makers are unusually good, 
 actual experience has shown that the time has not yet come when 
 they can replace the steam plant. It is not safe to predict as 
 to the future, and every power plant engineer should be some- 
 what acquainted with the subject. 
 
 When air is passed through a bed of hot carbon, combustion 
 takes place. If there is sufficient air, the combustion is complete 
 and CC>2 is formed. If not enough air is supplied, the burning 
 is only partial and CO is formed. This CO may later be burned 
 to CO2 by the addition of more air, which is done in the engine 
 cylinder in the case of the producer and engine plant. 
 
 If steam is passed through a hot carbon bed, a decomposition 
 of the steam takes place. The hydrogen is liberated as H 2 and the 
 oxygen combines with the carbon to form CO. Both of these 
 gases are valuable as fuel, and the mixture is often called water 
 gas. 
 
 When air is passed through the hot carbon bed, and CO is 
 formed, heat is generated, so that the bed gets hotter and hotter. 
 On the other hand, when steam is passed through, heat is ab- 
 sorbed and the bed gets cooler and cooler. By the proper pro- 
 portioning of air and steam passed through, it is possible to keep 
 the fuel bed at the proper temperature. This is what is done 
 in the gas producer. It is evident that most of the gases in 
 producer gas will be CO, H and N, the nitrogen coming from the 
 air and being inert. 
 
 The fuel used in the producer may be coke or coal. Better 
 results are obtained by using anthracite coal than by using bitu- 
 minous coal. This is partly due to the fact that bituminous coal 
 
206 
 
 ENGINES AND BOILERS 
 
 tends to cake and needs constant working or poking to keep holes 
 from burning through the cake, thereby letting excess air get 
 through. Moreover, bituminous coal gives off various tars when 
 it is heated. If these are not removed, they clog up the pipes 
 and the engine. The removal of the tar is not easy. It is some- 
 times done by throwing the tarry material out of the gas by 
 centrifugal force by means of a kind of fan arrangement, or by 
 passing the gas through scrubbers. Devices have been tried 
 
 FIG. 146 
 
 whereby the distilled products are passed through the hot fuel 
 bed and their composition thereby changed. This last method 
 resembles the underfeed furnace used in steam plants. 
 
 Figure 146 shows a form of gas producer. Coal is fed into the 
 hopper A. From this, it is dropped into the chamber B. Pass- 
 ing out of the bottom of B, it is scattered in a uniform layer over 
 the fuel bed by means of the spiral spreader C, which is rotated 
 by the bevel gear Q. 
 
 The fuel bed may be divided roughly into three zones. The 
 top zone is the green-coal zone, where distillation takes place. 
 The volatile products pass on out with the other gas. 
 
 As the volatile products are driven off, and the bed settles, the 
 fuel reaches the coke zone. It is here that the burning and de- 
 composition mentioned above take place. As the carbon is burnt 
 
GAS ENGINES 207 
 
 out, the ash settles to the bottom of the producer, where it is 
 raked out through the water seal R. 
 
 Air from the duct E is led to the bottom of the fuel bed through 
 D, and passes up through the coke zone and the green-coal zone. 
 Steam is admitted to the air supply through the pipe G. Holes 
 are provided in the furnace walls at F for the working of the fuel 
 bed. 
 
 The gas leaves the producer through the opening at 7, and 
 passes down the pipe shown to K. From K it passes through 
 the pipe L to the wet scrubber. The wet scrubber is filled with 
 coke, Pj which is continuously sprinkled with water from the 
 nozzle N. The gas passing up through the wet coke is cooled 
 and deposits dust, tar and other impurities. The gas leaves the 
 wet scrubber at 0, and may go either directly to the engine or 
 else to a dry scrubber. The dry scrubber is filled with wood 
 shavings or excelsior, which takes out the remaining tar. 
 
 Upon starting the producer, the gas is vented to the roof through 
 the valve J. As soon as the quality of the gas becomes good 
 enough, the valve J is closed and the engine is started. The coal 
 in B is kept cool enough to prevent it from burning, by a water- 
 jacket S. The producer is lined with firebrick. 
 
 Air either may be blown into the producer, or it may be drawn 
 through by the suction of the engine. In the former case a 
 storage tank for the gas is necessary. With the suction type the 
 storage is unnecessary, as the engine draws through only what it 
 needs. When a water seal is used at the bottom, the producer 
 is called a wet bottom producer. The poking of the fuel bed 
 may be done by hand or mechanically. 
 
 178. Cooling of Cylinders. The cylinder walls of the internal- 
 combustion engine must be kept cool enough to insure proper 
 lubrication. This cooling is commonly done by circulating water 
 through a jacket around the cylinder, as shown at W, in Figs. 
 137, 139, 140, 141 and 144. As far as the efficiency of the engine 
 is concerned, the hotter the cylinder walls the better, so that it 
 is evident that they should not be cooled any more than is neces- 
 sary to insure lubrication. In small engines, the cylinder is 
 sometimes placed in the lower part of a hopper filled with water. 
 Fresh water is added as it boils away in the hopper. 
 
 Another method that is used occasionally to cool the cylinder 
 
208 
 
 ENGINES AND BOILERS 
 
 Met 
 
 FIG. 147 
 
 is by having the outer walls of the cylinder and head covered with 
 fins. These present a large surface to the air and the heat is 
 radiated from them. To increase this transfer of heat, a cur- 
 rent of air is kept moving over the 
 surface of the fins by means of a 
 fan. This latter method is called 
 air-cooling. Figure 147 shows an 
 air-cooled cylinder. 
 
 179. Ignition. The charge of 
 combustible mixture in an internal- 
 combustion engine is fired in vari- 
 ous ways. A method formerly used 
 quite extensively but now not very 
 common is the hot-tube method. 
 This method is illustrated by the 
 sketch in Fig. 148. The tube which 
 connects with the cylinder is heated 
 by a gas jet. Arrangement is made 
 
 so that the flame can be shifted along the tube, heating it closer 
 
 or farther away from the cylinder. 
 
 To explain how the scheme works, suppose the charge has been 
 
 fired. The tube will then be filled with burnt gas. After the 
 
 fresh charge has been drawn in 
 
 and compression started, the fresh 
 
 gas is forced into the tube. When 
 
 it is compressed into the tube far 
 
 enough to strike the heated part, 
 
 ignition occurs. Naturally, this 
 
 scheme can be used only when the 
 
 load is constant. 
 
 As has been explained previ- 
 ously, ignition may be had by 
 
 using a high compression, so that 
 
 the temperature of compression 
 
 will be high enough to fire the 
 
 charge. This method is used 
 
 mostly in oil engines and is assisted in those using the lower 
 
 pressures by a hot bulb or plate. The hot bulb acts somewhat 
 
 in the same manner as the hot tube just mentioned. With gas 
 
 FIG. 148 
 
GAS ENGINES 209 
 
 or the more volatile liquid fuels this method is not satisfactory, 
 since early ignition is apt to occur. 
 
 The most common method is electric ignition. There are two 
 general types of electric ignitors, the jump-spark and the make- 
 and-break. In the former, a spark plug is used (Fig. 149), which 
 has two fixed terminals exposed to the gases of the cylinder. 
 At the proper time for ignition a current with voltage high enough 
 to jump the gap is introduced in the circuit. The 
 heat of this spark ignites the charge. The details of 
 timing and of producing the current will not be dis- 
 cussed here, except to say that the current may be 
 furnished either by dry-cell or storage batteries, or by 
 a magneto. 
 
 In the make-and-break system, two electrodes are 
 brought into contact within the cylinder and are sepa- 
 rated at the proper time for ignition. As the circuit is 
 broken a spark is formed between them. The details 
 of the many schemes used will not be discussed here. 
 This make-and-break system does not require as high 
 an e.m.f. as the jump-spark system, but it is limited to the slower 
 engine speeds. 
 
 180. Valves. The earlier types of gas engines were equipped 
 with slide-valves. These required lubrication, which is some- 
 what difficult at high temperatures. Except for a few engines 
 that use sleeve-valves, gas engines of today have the so-called 
 lifting or poppet valves , which are commonly lifted .by cams on 
 a cam shaft. In the four-stroke cycle engines the cam shaft is 
 geared to run at half the speed of the crank shaft, so that the 
 cam shaft makes one revolution per cycle. The cams are placed 
 on the cam shaft so that the valves open and close at the proper 
 time. Each valve is kept seated by means of a spring around 
 the valve stem. Figure 147 shows the cams, and how they are 
 made to lift the valves. In some of the slower speed engines, 
 the inlet valve is not opened by means of a cam, but by the 
 suction inside the cylinder. With this arrangement a strong 
 spring cannot be used to seat the valve. 
 
 181. Governing. As far as the governor itself is concerned, 
 the gas-engine governor does not differ materially from the steam- 
 engine governor. Both centrifugal and inertia governors are used. 
 
210 ENGINES AND BOILERS 
 
 Depending upon how the governor regulates the amount of work 
 done in the engine cylinder, we have three general types of gas 
 engine governors: (1) hit-and-miss governors, (2) quantity gov- 
 ernors, and (3) quality governors. 
 
 HIT-AND-MISS GOVERNOR. With this type of governor there 
 is a working stroke for every cycle under conditions of maximum 
 load. At lighter loads the governor mechanism fails to admit 
 a charge occasionally, giving what might be termed a blank cycle 
 in which no work is done by the cylinder. This drops the speed 
 of the engine and the governor acts so that fuel is again taken in 
 as before. With this scheme the engine either operates under 
 conditions of maximum efficiency, or it does not fire at all. This 
 method of governing gives better economy at light loads than the 
 other methods, but it does not give close speed regulation. When 
 the engine misses, the exhaust valve is commonly held open so 
 that there is no work done in useless compression. 
 
 QUANTITY GOVERNOR. For every engine there is a ratio of gas 
 to air, which is nearly constant, with which the engine gives the 
 best efficiency. With the quantity governor, this ratio is kept 
 (theoretically) constant. Regulation is accomplished in two ways : 
 (1) by the cut-off governor, and (2) by the throttling governor. 
 With the cut-off or throttling governor, the normal mixture is 
 allowed to enter the cylinder only during a part of the suction 
 stroke at light loads. The length of time the mixture is ad- 
 mitted is controlled by the governor. With the throttling gover- 
 nor, the normal mixture is taken in during the whole of the suc- 
 tion stroke, but the opening is throttled so that not as much 
 enters at light loads as at full load. 
 
 QUALITY GOVERNOR. This governor changes the ratio of the 
 fuel to the air at different loads. At full load, a rich mixture is 
 used, and at light load a lean mixture. Mechanically, this scheme 
 is quite simple, but it has the disadvantage of giving low effi- 
 ciency at light loads. If the mixture gets too rich or too lean, 
 it may be impossible to secure ignition. Oil engine governors 
 commonly control the amount of oil admitted per working 
 stroke. This is seen to be the same as the quality-governing 
 scheme. 
 
 It should be mentioned that the speed of an engine can be 
 regulated by changing the time of ignition. With either too 
 early or too late ignition the full power is not developed in the 
 
GAS ENGINES 211 
 
 cylinder. The speed of motor-boat engines is often controlled 
 in this way. With high speeds, the spark should occur earlier 
 than in low-speed engines. With a variable-speed engine, such 
 as exists in an automobile or truck, the time of ignition should 
 be adjusted to the speed in order to get the best results. 
 
 182. Determination of Horsepower. The indicated horse- 
 power of a gas engine is determined in the same way as for the 
 steam engine, with the exception that for four-stroke cycle en- 
 gines only half the r.p.m. is used in the computation. If a 
 hit-and-miss governor is used on the engine, the number of hits 
 per minute must be counted rather than the r.p.m. of the shaft. 
 
 183. Multi-cylinder Engines. The single cylinder, single-act- 
 ing four-stroke-cycle gas engine has one impulse stroke in two revo- 
 lutions. The double-acting steam engine has two impulse strokes 
 per revolution. Thus it is seen that the single cylinder gas en- 
 gine has a much greater variation in angular acceleration of crank 
 shaft than does the steam engine. For some kinds of service this 
 variation in angular velocity is immaterial; in other cases it is 
 a serious disadvantage. For instance, in the generation of elec- 
 tric current to be used for lighting, a single-cylinder engine is 
 impracticable, unless an exceedingly heavy flywheel is used. To 
 approximate the uniformity of torque that exists in a single- 
 cylinder steam engine, it is necessary to use four cylinders on the 
 gas engine. 
 
 In automotive service, a fairly uniform torque is desirable, and 
 therefore four or more cylinders are used. If more than four 
 cylinders are used, there will be less variation in the angular 
 torque, and the engine speed may be controlled more easily by 
 the throttle. Too large a number of cylinders may cause a de- 
 crease in the efficiency of the engine. This may be explained 
 by the fact that with a multi-cylinder engine, there is more area 
 of cylinder wall exposed to the burned gas for the same volume 
 of gas than there is in the single-cylinder engine. Principle I of 
 169, as set forth by Beau de Rochas, is a statement of this 
 same fact. While a lowered efficiency may result from the use 
 of a large number of cylinders, this loss may be more than com- 
 pensated by the added smoothness of running. Many of the 
 higher grade automobiles made at the present time are equipped 
 with six, eight, or even twelve cylinders. 
 
212 
 
 ENGINES AND BOILERS 
 
 
PROBLEMS 213 
 
 PROBLEMS 
 
 1. (a) What is the pressure in pounds per square inch that corresponds to 
 a mercury column 16 inches high? 
 
 (6) What is the atmospheric pressure when the barometer reads 27.4 inches? 
 
 2. A steam gage is used to show the pressure in a steam line and is at- 
 tached as shown in Fig. A. If the small pipe leading to the gage is full of 
 water and the gage reads 183 pounds, what is the pressure in the steam line? 
 
 3. If the pressure gage on a 
 boiler reads 150 pounds and the 
 barometer reads 29.3 inched, what 
 is the absolute pressure in the boiler 
 in pounds per square inch? 
 
 4. The vacuum gage on a con- 
 denser reads 27.2 inches and at the 
 same time the barometer reads 29.1 
 inches. 
 
 (a) What is the absolute pres- 
 sure in the condenser in pounds per 
 square inch? (6) What is the vac- 
 uum-gage reading reduced to a JT IG 
 30-inch basis? 
 
 6. A condenser with its air pump is guaranteed by the manufacturer to 
 produce a vacuum of 28.5 inches (on the basis of a 30-inch barometer). Dur- 
 ing the acceptance test the barometer read 28.73 inches. What should be 
 thevacuum-gage reading to maintain the guaranteed vacuum? 
 
 Q) A boiler-feed pump is located 14 feet below the water line of the boiler. 
 The pump draws water from a tank located 7 feet below the pump cylinder. 
 If the pressure in the boiler is 40 pounds gage, neglecting friction losses due 
 to the flow of water, etc., what is the least total head the pump must act 
 against: (a) In feet? (6) In pounds per square inch? (c) What is the 
 least height of water level in a standpipe above the boiler in order that the 
 water will flow into the boiler by gravity? 
 
 (Y) Reduce: (a) A temperature reading of 50 Centigrade to the corre- 
 sponding Fahrenheit reading. (6) A temperature of 320 Fahrenheit to 
 Centigrade. (c) 75 (great) calories to B.t.u. (d) 46 B. t. u. to calories. 
 (e] 33000 foot-pounds to B.t.u. 
 
 8. If 1,576,000 B.t.u. are given to an engine in an hour and if the engine 
 can convert 6 per cent of this heat into work, what is the horsepower of the 
 engine? (One horsepower is 33,000 foot-pounds per minute.) 
 
 9. A sample of Indiana coal gave the following proximate analysis: 
 
 Moisture =3.81%, Fixed carbon = 76. 16%, 
 
 Volatile combustible = 13.62%, Ash = 6.41%. 
 The same sample when dried gave the following ultimate analysis: 
 Carbon =84.26%, Oxygen =1.73%, Sulphur = 1.22%, 
 
 Hydrogen= 4.38%, Nitrogen = 1.75%, Ash =6.66%. 
 
 The oxygen calorimeter gave a calorific value of 14682 B.t.u. per pound of 
 dry fuel. Find the calorific value of the preceding sample per pound of dry 
 fuel, from (a) the proximate analysis, (6) the ultimate analysis. 
 
214 ENGINES AND BOILERS 
 
 A sample of West Virginia coal gave the following proximate analysis : 
 Moisture =4.85%, Fixed carbon = 68.36%, 
 
 Volatile combustible = 16.31 %, Ash = 10.84%. 
 The same sample when dried gave the following ultimate analysis: 
 Carbon =80.34%, Oxygen = 3.11%, Sulphur = .49%, 
 Hydrogen = 4.00%, Nitrogen = 1.05% Ash =11.01%. 
 The oxygen calorimeter gave for a similar dried sample a calorific value of 
 14,180 B.t.u. per pound. Find the calorific value per pound of dry coal from 
 ^ (a) the proximate analysis (b) The ultimate analysis. 
 
 (llj Find the theoretical weight of air required to burn completely a 
 pound of the dry coal of Problem 10. 
 
 12. A boiler test was run using the coal from which the sample of Problem 
 10 was taken. During the test the analysis of dry flue-gas was as follows: 
 Carbon dioxide = 8.58%, Carbon monoxide = .05%, 
 
 Oxygen =11.32%, Nitrogen = 80.05%. 
 
 Find the approximate weight of air used to burn one pound of dry coal. 
 (13? In the test of Problem 12, the temperature of air entering the furnace 
 was'64 F., and the stack temperature was 559 F. Find the percentage of 
 available heat carried up the stack by the dry flue-gas. 
 
 14. Water is fed to a boiler at a temperature of 170 F. The pressure 
 gage reads 140 pounds, and the barometer 29.6 inches. How many B.t.u. 
 are needed to generate a pound of dry steam? What is the temperature of 
 thesteam generated? The volume per pound? 
 
 Q$ Steam at a gage pressure of 135 pounds is generated from water at 
 120 F. The temperature of the steam is 490 F. The barometer reads 
 29.3 inches. Find the B.t.u. required to generate one pound of steam. 
 
 16. If the temperature of steam in a condenser is 115 F., what is the great- 
 estjaossible vacuum-gage reading, if the barometer reads 29.16 inches? 
 
 Qj) If water boiling under a pressure of 185 pounds gage is allowed to 
 escape to the atmosphere (as in a boiler explosion), what percentage of its weight 
 turns to steam? What is the ratio of its new volume to the old? Assume 
 that the barometer reading is 29.6 inches. 
 
 18. Dry steam leaves a boiler at a pressure of 180 pounds gage and reaches 
 the engine with a quality of 98 per cent, and a pressure of 177 pounds gage. 
 What percentage of its heat contents has it lost in its passage through the 
 pipe? What percentage of its volume? Assume that the barometer reading 
 is 29.43 inches. 
 
 Q9^ If one pound of steam of 95 per cent quality at atmospheric pressure is 
 mixed with 8 pounds of water at 70 F., what will be the resultant tempera- 
 ture? Assume that the barometer reading is 29.00 inches. 
 
 20. Dry steam enters a turbine at a pressure of 180 pounds gage; leaving 
 the turbine it passes into a condenser in which the vacuum is 27.6 inches (30- 
 inch basis). The quality of steam as it leaves the turbine is 87%. Neglect- 
 ing all losses, find how many foot-pounds of work may be obtained from each 
 pound of steam that passes through the turbine. 
 
 /2L) A frictionless piston weighing 7000 pounds is placed in a vertical 
 cyimcler 10 inches in diameter. Two pounds of water at 70 F. are placed 
 
PROBLEMS 215 
 
 under the piston. If 800 B.t.u. are added to the water, how far will the pis- 
 ton move? The barometer reads 29.6 inches. 
 
 22. If, in Problem 21, 2500 B.t.u. are added to the water, what will be 
 the weight of steam formed? What will be its temperature? How far will 
 thejMston move? 
 
 2iP A sample of steam is taken from a steam line in which the pressure 
 is 150 pounds gage and is led to a throttling calorimeter in which the tem- 
 perature is 230 F. and the gage pressure is 3 pounds. The barometer reads 
 29.4 inches. What is the quality of steam in the line? 
 
 24. A horizontal water-tube boiler (B. and W. type) has 10 vertical rows 
 of four-inch tubes, 9 tubes to the row. The tubes are 18 feet long, and the 
 steam drum is 24 feet long and 42 inches in diameter. Find the heating 
 surface and the rated horsepower (a) by using as heating surface the out- 
 side surface of the tubes and one-half the surface of the drum; (6) by 
 RuJle3, p. 26. 
 
 j2J5c A horizontal return tubular boiler 60 inches in diameter and 18 feet 
 long has 44 four-inch tubes. Find the heating surface and rated horsepower 
 (a) by Rule 1, p. 26, (6) by Rule 3, p. 26. 
 
 26. A Scotch marine boiler-shell is 16 feet 3 inches in diameter and 12 
 feet long. There are three furnaces, each 43 inches in diameter. The boiler 
 contains three sections of tubes, each section consisting of 110 three-inch 
 tubes 10 feet long. Find the approximate heating surface and the horse- 
 power. 
 
 27. A vertical fire-tube boiler (exposed-tube type) has a diameter of 30 
 inches and a height of 6 feet. The furnace is 25 inches in diameter and 27 
 inches high. There are 55 two-inch tubes 45 inches long. The normal water 
 level is 10 inches from the top of the tubes. Find the heating surface and 
 rated horsepower by Rule 2, p. 26. 
 
 ^5P In a test of a B. and W. boiler with a hand-fired furnace at the Sew- 
 age Pumping Station, Cleveland, Ohio, the following data were taken: 
 
 Rated horsepower of boiler 150 
 
 Grate surface 27 square feet 
 
 Duration of test 24 hours 
 
 Steam pressure 156.3 pounds gage 
 
 Temperature of feed water 58 F. 
 
 Quality of steam formed 99 per cent. 
 
 Total weight of coal fired (wet) 15078 pounds. 
 
 Moisture in coal 7.5 per cent. 
 
 Total weight of water fed to boiler 105100 pounds. 
 
 Find: 
 
 (a) Factor of evaporation. 
 
 (6) Dry coal per square foot of grate surface per hour. 
 
 (c) Equivalent evaporation per hour (from and at 212 F.). 
 
 (d) Equivalent evaporation per hour per square foot of water-heating 
 surface. 
 
 (e) Boiler horsepower developed. 
 
 (L Percentage of rated capacity developed. 
 (297 In the test of Problem 28, the dry coal had a calorific value of 12292 
 
216 ENGINES AND BOILERS 
 
 B.t.u. per pound, and the cost delivered at the boiler room was $3.50 per 
 ton of 2000 pounds. Find: 
 
 (a) Equivalent evaporation from and at 212 per pound of dry coal. 
 Combined efficiency of boiler, furnace and grate. 
 Coal cost per 1000 pounds of equivalent evaporation. 
 In a test of a B. and W. boiler the following data were taken: 
 
 Rated horsepower of boiler 508 
 
 Grate surface 90 square feet 
 
 Duration of test 16.25 hours 
 
 Steam pressure 199 pounds gage 
 
 Temperature of feedwater 48.4 F. 
 
 Superheat 136.5 F. 
 
 Total weight of coal fired (wet) 39670 pounds 
 
 Moisture in coal 4.22 per cent 
 
 Total weight of water fed to boiler 336200 pounds 
 
 Find: 
 
 (a) Factor of evaporation. 
 
 (6) Dry coal per square foot of grate surface per hour. 
 
 (c) Equivalent evaporation from and at 212 per hour. 
 
 (d) Equivalent evaporation from and at 212 per hour per square foot 
 of water-heating surface. 
 
 (e) Boiler horsepower developed. 
 Percentage of rated capacity developed. 
 
 The coal in the test of Problem 30 gave the following proximate anal- 
 ysis when dry: volatile combustible, 19 66 per cent; fixed carbon, 75.41 per 
 cent; ash, 4.93 per cent. The cost delivered to the boiler room was S3. 75 per 
 ton of 2000 pounds. Find: 
 
 (a) Equivalent evaporation per pound of dry coal. 
 (6) Combined efficiency of boiler, furnace and grate. 
 
 Coal cost per 1000 pounds of equivalent evaporation. 
 Is the boiler of Problems 28 and 29 working harder than that of 
 Problems 30 and 31, or conversely? Give the reason for your answer. 
 
 33. Find the size of a pop safety-valve with a 45 seat for a 60-horsepower 
 return-tubular boiler which is to carry a gage pressure of 75 pounds. Assume 
 that the maximum evaporation is 5 pounds of water per hour per square foot 
 of wetter-heating surface, and that the lift of the valve is 1/30 of the diameter. 
 (3p How many 2.5-inch pop safety-valves would one 4.5-inch valve re- 
 place, assuming that the lift is proportional to the diameter? 
 
 35. How many 3.5-inch pop safety-valves are required for the boiler 
 of Problem 30? Assume the rate of maximum evaporation as 6 pounds of 
 water per square foot of water-heating surface per hour, and that the lift 
 is 1/30 of the diameter. 
 
 36. What should be the size of the pop safety-valve for the boiler of 
 Problem 28 
 
 (a) Computed as in Problem 35? 
 
 (6) Computed from the P. G. Darling formula? See p. 59. 
 
 (c) Computed from the city of Chicago formula? See p. 59. 
 
 (d) Computed from the city of Philadelphia formula? See p. 59. 
 
PROBLEMS 217 
 
 (e) Computed from the U. S. Supervising Inspectors' formula? See p. 59. 
 
 (/) Computed from the A. S. M. E. Boiler Code Committee's require- 
 menjt^? See Report of Boiler Code Committee of A. S. M. E. 
 /3T,/ What should be the size of a steam pipe leading from a 250-horse- 
 power boiler if the pressure carried is 160 pounds gage? Assume a velocity 
 of florin the pipe of 5000 feet per minute. 
 
 (ZSy/A 5000-kw. steam turbine requires 16 pounds of dry steam per 
 hour per kw. at 160 pounds gage pressure. The vacuum in the exhaust 
 of the turbine is 27.5 inches of mercury (30-inch barometer). The quality 
 of steam in the exhaust is 85%. If the velocity of flow of steam to and 
 away from the turbine is to be 7500 feet per minute, what should be the 
 size _ol steam and exhaust pipes? 
 
 /39.) If a steel steam pipe is to carry steam at a pressure of 200 pounds 
 gageand may be as cold as 30 F. when the steam is cut off, how far apart 
 should expansion joints be placed if each joint gives a 3-inch movement? 
 
 40. If 9536 pounds of water at a temperature of 60 F. are mixed with 
 1160 pounds of steam at 3 pounds gage pressure, the steam being of 90 per 
 cent quality, what will be the resultant temperature of the mixture? 
 ^41. The exhaust from a 65-horsepower steam engine is led to an open 
 feedwater heater. The engine uses 30 pounds of steam per hour per horse- 
 power, and the quality of the exhaust steam is 80%. The heater is at atmos- 
 pheric pressure; water enters at 50 F. and is heated to 200 F. 
 
 fa) What horsepower of boilers will the heater supply? 
 
 (6) What should be the size of steam and water pipes leading to the 
 heater? Assume a steam velocity of 5000 feet per minute and a water veloc- 
 ity of 150 feet per minute. 
 
 42. A 4000-kw. steam turbine is equipped with a surface condenser 
 The turbine uses 16 pounds of steam per kw. per hour, which enters the 
 condenser at a quality of 85 per cent. The vacuum to be maintained is 28 
 inches (30-inch basis). The circulating water enters the condenser at a 
 temperature of 60 F., and leaves at a temperature 10 cooler than that of 
 the incoming steam. (a) How much circulating water is needed per hour? 
 
 (6) If the same amount of water is circulated as in part (a), but if it enters 
 at 90 instead of 60, and leaves at 10 cooler than the incoming steam, what 
 vacuum can be maintained? 
 
 43. An 18"X24" steam engine has a piston rod 2.75 inches in diameter. 
 Find the head-end and the crank-end piston displacements in cubic feet. 
 
 44. If it takes 10.6 pounds of water to fill the head-end clearance space 
 and 11.2 pounds to fill the crank-end clearance space of the engine in Problem 
 43, what is the percentage of clearance for each end of the engine? 
 
 45. Find the volume of steam back of the piston of the engine of Problem 
 43: when the piston is at 12.4 per cent of the head-end stroke; when it is 
 at 14.0 per cent of the crank-end stroke. 
 
 ^ 46. Find the weight of dry steam back of the piston of a 24" X 36" engine 
 when it is at 30 per cent of the head-end stroke. The head-end clearance is 
 4 per cent and the steam pressure back of the piston at the above position 
 is 105 pounds gage. If we know that at this time there is actually 1.06 pounds 
 of wet steam back of the piston, what must be its quality? 
 
218 
 
 * 
 
 ENGINES AND BOILERS 
 
 Construct a hypothetical indicator diagram, using the following data. 
 Length of diagram =4 inches (this does not include clearance). 
 Initial pressure = 150 pounds per square inch (gage). 
 Back pressure =5 pounds per square inch (gag). 
 Cut-off = 25 per cent, Release =95 per cent. 
 Compression = 15 per cent, Admission = 2 per cent. 
 Clearance = 7 per cent. 
 
 Atmospheric pressure = 15 pounds per square inch, 
 as a scale of pressure 60 pounds per inch. 
 
 (Construct a hypothetical indicator diagram for a uniflow engine 
 108), using the following data. 
 Length of diagram =4 inches. Initial pressure = 170 pounds. 
 Back pressure = 12 pounds (engine is running condensing). 
 Cut-off = 20 per cent. Release and compression each =90%. 
 
 Admission = 2 per cent. Clearance = 3 p r cent. 
 
 Also show, by a dotted line on the same diagram, the compression curve when 
 the engine runs non-condensing (back pressure = 0). 
 
 State in what ways this excessive compression may be relieved. 
 49. Compute approximately the percentage of head-end and of crank-end 
 
 clearance of the engine from which 
 the cards of Fig. B were taken. Use 
 two methods. Cards were taken 
 with an 80-pound spring. 
 
 50. Compute the engine con- 
 stant, or the horsepower constant 
 (LA/33000), for the head end and 
 for the crank end for a 10"X14" 
 engine with a 2" piston rod. Your 
 answer must be correct to within 
 
 onephalf of one per cent. 
 
 -p IG -g (51/ Find the indicated horse- 
 
 power (i. hp.) of the steam engine of 
 
 Problem 50 when the head-end mean effective pressure is 34.2, and the crank- 
 endgjke.p. is 35.4 pounds per square inch. The engine is running at 260 r.p.m. 
 (52/ A test was run on a 14" X 18" steam engine with a 2" rod. The 
 head-end m. e. p. was found to be 35.2 pounds per square inch and the crank- 
 end m.e.p. 34.6 pounds per square inch. The speed of the engine was 
 250 r.p.m. The power was absorbed by a Prony brake whose arm is 6' 5" 
 long. The effective weight of the brake arm on the scales was 45 pounds. 
 During the test the pressure on the scales was 382 pounds. Find (a) the indi- 
 cate4\h rse P wei S (&) the brake horsepower; (c) the mechanical efficiency. 
 
 H>3/ The test of Problem 52 was run for 45 minutes, during which time 
 thVengine used 2750 pounds of steam at a pressure of 120 pounds gage, and 
 at a quality of 97 per cent. Find: 
 
 (a) Dry steam used per indicated horsepower per hour. 
 (6) B.t.u. per indicated horsepower per minute, 
 
 (c) Thermal efficiency based on i. hp. 
 
 (d) Thermal efficiency based on b. hp. 
 
PROBLEMS 
 
 219 
 
 The indicator diagram in Fig. C and the following data were taken during 
 
 cut-off 
 
 re/ease 
 
 compression 
 FIG. C 
 
 a test of a Buckeye engine. 
 
 Size of engine, 7.75" X 15", \\\" 
 
 rod. 
 Radius of Prony brake arm =6.02 
 
 feet. 
 
 Room temperature = 73.5 F. 
 Temperature in throttling calo- 
 rimeter =221.5 F. 
 Steam pressure at throttle = 128.7 
 
 pounds per square inch gage. 
 Steam pressure in calorimeter = 
 
 1.125 pounds gage. 
 Barometer = 28.5 inch. 
 R.p.m.= 222.5. 
 Net brake load = 140 pounds. 
 Scale of indicator spring = 80 pounds. 
 Steam used per hour = 1161 pounds. 
 
 54. Find the m.e.p. of the cards by the mean-ordinate method. 
 65. Find the indicated horsepower, head-end, crank-end, and total. 
 Find the brake horsepower. 
 Find: 
 
 Mechanical efficiency. 
 Pounds of steam per i. hp. per hour. 
 B.t.u. per i. hp. per minute. 
 Thermal efficiency based on b. hp. 
 
 Determine from each card the percentage of stroke and the steam pres- 
 sure for each of the following events : 
 (a) Cut-off. 
 (6) Release 
 (c) Compression. 
 
 59. Determine the weight of dry steam back of the piston for each end 
 
 at the events of cut-off, release, and 
 compression. 
 
 60. Find the amount of re-evapo- 
 ration or condensation per hour dur- 
 ing expansion. 
 
 61. Find the weight of dry steam 
 per hour per indicated horsepower 
 accounted for by the cards. 
 
 56. 
 57. 
 
 (a) 
 (6) 
 (c) 
 (d) 
 58. 
 
 ZO pound s/orinq. 
 
 FIG. D 
 
 62. Combine the indicator dia- 
 grams shown in Fig. D, and deter- 
 mine the diagram factor. The cards 
 of Fig. D were taken from an 8.02" 
 X15"X24" cross-compound Corliss 
 
 steam engine, running at 85 r.p.m. The head-end clearance of the high-pres- 
 sure cylinder is 7.4 per cent and the head-end clearance of the low-pressure 
 cylinder is 6.01 per cent. 
 
220 
 
 ENGINES AND BOILERS 
 
 Determine the size of cylinders for a compound, two-cylinder, double- 
 acting steam engine (receiver type), assuming the following data: i. hp. = 120, 
 r. p.m. = 100, cylinder ratio = 1/3, piston speed = 600 feet per minute, initial 
 steam pressure = 140 pounds absolute, termin^ljgressure of hypothetical dia- 
 gram =14 pounds absolute, vacuum = 24 inches (30-inch basis), and diagram 
 f actor = .85 
 
 QJ4,/ In a certain two-cylinder compound steam engine the number of ex- 
 pansions is 10, the initial steam pressure is 120 pounds absolute and the back 
 pressure is 5 pounds absolute. The receiver pressure is 30 pounds abso- 
 lute. The cylinder ratio is 1 to 3. Neglecting clearance and piston rods, 
 compare the work done in the two cylinders and the stresses on the two 
 piston rods. 
 
 65. Given a cross-compound steam engine, show by means of a graph the 
 
 l/j/ve shown in mid-position 
 
 
 
 f- 
 
 >- 
 
 "4* >l 
 
 \ head 
 end 
 
 
 /ohfon 
 
 
 -*r 
 
 cnwft \ 
 
 end 
 
 
 FIG. E 
 
 variation in power distribution when the governor varies the cut-off equally 
 in each cylinder (choose at least three cut-offs). 
 
 66. Proceed as for Problem 65, but assume that the governor varies the 
 point of cut-off in the high pressure cylinder only. 
 
 67. Consider a 12"X18" steam engine (section of cylinder and valve 
 shown in Fig. E), with the following given data. 
 
 Connecting rods 6 feet long. 
 
 Val ve- travel = 6 inches. 
 
 Head-end lead = crank-end lead = .25 inch. 
 
 Head-end steam lap = 1.25 inches. 
 
 Head-end exhaust lap = .5 inch. 
 
 Width of port = 1.75 inches. 
 
 (a) Draw the valve on its seat, the crank position, the eccentric position, 
 and the position of the piston in the cylinder when the crank is on head-end 
 dead center. (Make your drawing y actual size.) 
 (6) Draw the same parts for head-end cut-off. 
 
 (c) Draw the same parts for head-end admission. 
 
 (d) Draw the same parts for head-end release. 
 
 (e) Draw the same parts for head-end compression. 
 
 (/) Determine the percentage of the stroke for each of the above events. 
 
PROBLEMS 
 
 221 
 
 'Consider a 14"X16 
 L aruTwith the following data. 
 
 engine, running over, with direct slide-valve 
 
 valve-travel = 4 inches, 
 
 lead = 1 A inch,' 
 
 steam lap = 1 inch, v 
 
 exhaust lap = K inch/ 
 
 / (a) Valve ellipse. Draw the crank circle K actual size, and about the 
 same center draw the eccentric circle full size. Choose 12 equidistant crank 
 positions and find the corresponding eccentric positions. 
 
 For any crank position (as C, Fig. F 2 ), the piston is at a distance x from 
 its mid-position, and at the same time the eccentric is at a distance y from its 
 
 Jfeam /ap+/ead 
 
 Crank on 
 head-end 
 dead center 
 
 FIG. F 2 
 
 FIG. F 4 
 
 mid-position. Plot y vertically and x horizontally, for all 12 positions of the 
 crank. 
 
 Connect the points thus found by a smooth curve. Label on this diagram 
 the following details: the crank position at each event of the stroke, the lead, 
 the steam lap, the exhaust lap, the maximum port-openings, and the angle 
 of advance. 
 
 (6) Bilgram diagram. Draw the crank and eccentric circles and choose 
 12 equidistant crank positions as in (a) . For each crank position (as C in Fig. 
 F 3 ), draw a dotted line parallel at a distance y from the crank. The inter- 
 section of these dotted lines is the Bilgram construction point P. About this 
 point P, draw in the steam-lap and exhaust-lap circles. 
 
 Show on this diagram the crank position at each event, the lead, the steam 
 lap, the exhaust lap, the maximum port-openings, and the angle of advance. 
 
 (c) Zeuner diagram. Draw the crank and eccentric circles as before, and 
 choose 12 equidistant crank positions. Lay off radially on the crank from the 
 center of the crank circle the eccentric displacement y (Fig. F 4 ) ; connect all 
 points thus found by a smooth curve. 
 
 Show on this diagram the crank position at each event, the lead, the steam 
 lap, the exhaust lap, the maximum port-openings, and the angle of advance. 
 
222 ENGINES AND BOILERS 
 
 69. Consider an engine with the following given data. 
 
 Direct slide-valve. Head-end steam lap = 1| ". 
 
 Engine running over. Crank-end steam lap = 1 inch. 
 
 Valve-travel = 5 inches. Head-end exhaust lap = J4 inch. 
 
 Head-end lead = 1/8 inch. R/L = 1/5. 
 
 Find the head-end and crank-end crank positions, and the percent of stroke 
 at each event by means of 
 
 (a) The valve ellipse, (6) the Bilgram diagram, fc) the Zeuner diagram. 
 
 70. Consider an engine with a direct slide-valve and with the following 
 given data: 
 
 Engine running over. Crank-end cut-off =50 per cent. 
 
 Valve-travel = 3 inches. Head-end compression = 25 per cent. 
 
 Head-end admission = 1 per cent. Crank-end compression = 25 per cent. 
 Head-end cut-off = 50 per cent. R/L = 1/6. 
 
 Find the percentage of stroke at all events, the angle of advance in degrees, 
 the steam laps, the exhaust laps, the maximum port-openings, and the leads, 
 by means of 
 
 (a) The Bilgram diagram, (6) the Zeuner diagram. 
 
 Draw the eccentric circle full size and the crank circle to such a scale that 
 it is the same size as the eccentric circle. Label all of the dimensions asked 
 for directly on the diagrams, also label the head end of the diagram and in- 
 dicate by an arrow the direction of rotation of the crank. 
 
 71. Consider an engine with an indirect slide-valve and with the follow- 
 ing given data. 
 
 Engine running over. 
 
 Valve-travel = 4 inches. 
 
 Head-end lead = | inch. 
 
 Crank-end lead = Y inch. 
 
 Head-end cut-off = 35 per cent. 
 
 Head-end compression = 15 per cent. 
 
 Sum of steam lap and exhaust lap the same for both ends. R/L = %. 
 Find the percentage of stroke at all events, the angle of advance in degrees, 
 the steam laps, the exhaust laps, and the maximum port-openings, by means of 
 (a) The Bilgram diagram, (6) the Zeuner diagram. 
 
 72. Consider an engine with a direct slide-valve and with the following 
 data. 
 
 Engine running over. 
 
 Head-end admission = 2 per cent. 
 
 Head-end cut-off = 60 per cent. 
 
 Head-end maximum port-opening = 1 .25 inches. 
 
 Crank-end maximum port-opening = 1.25 inches. 
 
 Head-end compression = 20 per cent. 
 
 Crank-end compression = 20 per cent. 
 
 Find the valve-travel, the angle of advance, and each of the laps, by means 
 of 
 
 (a) The Bilgram diagram, (6) the Zeuner diagram. 
 
 Also draw to scale the valve on the seat in its mid-position. 
 
PROBLEMS 
 
 223 
 
 73. Consider an engine with a direct slide-valve and with the following 
 data. 
 
 Engine running under. 
 
 Head-end lead = J^ inch. 
 
 Crank-end lead= f inch. 
 
 Head-end cut-off = 55 per cent. 
 
 Head-end compression = 20 per cent. 
 
 Crank-end compression = 20 per cent. 
 
 Head-end maximum port-opening = 1.25 inch. 
 
 Find the valve-travel, the angle of advance, and each of the laps by 
 (a) The Bilgram diagram, (6) the Zeuner diagram. 
 Draw the valve to scale in mid-position. 
 
 FIG. G 
 
 74. Consider an engine with a valve whose dimensions and seat are as 
 shown in Fig. G. The valve is not shown in mid -position. The valve-travel 
 is 4 inches; R/L = l/5; the engine runs over. 
 
 The cards of Fig. H are taken with the valve as now set. Find the angle 
 through which the eccentric must be shifted (state whether backward or for- 
 
 Cut-otf 
 
 Cuf-off 
 
 Crank-end card 
 
 FIG. H 
 
 ward), and the amount the valve stem must be lengthened or shortened (state 
 which), in order to give a cut-off of 25 per cent on each end. Draw the ap- 
 proximate cards for the new setting. 
 
224 
 
 ENGINES AND BOILERS 
 
 75. Consider an automatic shaft governor with the following given data 
 (The Rites inertia governor is shown in Figs. I and J.) : 
 Head-end steam lap = 1.75 inches. 
 Head-end exhaust lap = 0. 
 
 Lead at normal position of eccentric = 5/32 inch. 
 Distance of eccentric center from pivot (R) = 12". 
 Distance from center of shaft to pivot point (x) = 13f ". 
 
 FIG. I 
 
 Location of point DE = 25", /=18". 
 Location of point A: c = 30", 6 = 52". 
 
 I. 
 
 Cut-off at no load = 10 per cent. 
 Cut-off at full load = 65 per cent. 
 Direct slide-valve, engine running over. 
 
 Draw the governor analysis (full size) and find the valve-travel and 
 
 angle of advance 
 
 (a) At 10% cut-off, (6) at 65% 
 cut-off, (c) at normal cut-off. 
 
 (d} Also find percent of normal 
 cut-off. 
 
 II. Draw the head-end Zeuner 
 diagram, or the Bilgram diagram, for 
 (a) 10% cut-off, (6) normal cut- 
 off, (c) 65% cut-off. 
 
 From the events thus deter- 
 mined, draw the theoretical indicator diagrams, using 6 per cent clearance, 
 150 pounds initial steam pressure, 5 pounds back pressure, and 80 pounds per 
 inch as the scale of spring. 
 
 Find the elongation of governor spring (drawing J/ size) . 
 (a) From no load to normal, (6) from normal to full load. 
 
 FlG 
 
PROBLEMS 
 
 225 
 
 76. Consider a four-valve engine, such as is shown in Figs. 60 and 61, p. 
 104, with head-end valves as shown in Fig. KI and K 2 , and with the follow- 
 ing data. 
 
 Radius of steam valve arms = 5". 
 
 Maximum diameter of steam or cut-off eccentric circle = 4". 
 
 Diameter of exhaust eccentric circle = 4". 
 
 With the crank on head-end dead center, the pivot point of the governor 
 arm for the cut-off eccentric is on the horizontal center line 8^" beyond 
 the center of the shaft. Radius of locus of eccentric centers = 7 5/16". 
 
 Cut-off at maximum load = 65 per cent. Compression = 15 per cent. 
 
 Cut-off at normal load = 25 per cent. Release = 95 per cent 
 
 va/ve in extreme open position 
 (Fu// /oad) 
 
 'exhaust rtt/ye !/r 
 extreme c/osed joosift'on 
 
 FIG. K 
 
 At normal load the steam-valve arm is vertical when the valve is in extreme 
 closed position. The exhaust-valve arm is vertical when that valve is in ex- 
 treme open position. R/L = 1/Q. Engine runs over. 
 
 Find the angle of advance for each eccentric at normal load. 
 
 Find the location of the steam-valve arm when in mid-position, at cut- 
 off, at admission, and when it is in extreme open position at normal load. 
 
 Find the maximum port-opening at normal load, and the lead at normal 
 load. 
 
 Draw the head-end steam valve in extreme position, and in open position 
 at normal load. 
 
 Draw the head-end exhaust valve in extreme open position. 
 
226 
 
 ENGINES AND BOILERS 
 
 77. The necessary dimensions of a Corliss engine are given in Figs. L 
 and M. 
 
 Consider such an engine with the following data. 
 
 A 12"X24" Corliss engine running at 150 r.p.m. 
 
 All valves operated by one eccentric. 
 
 Engine runs over. 
 
 FIG. L 
 
 Diameter of all valves =3" (d, Fig. L). 
 
 m, Fig. L=sy 2 "; 
 
 k, Fig. L = 15". 
 
 Length of valve arms = 4' / . 
 
 Center of wrist plate is equidistant from all valves. 
 
 Radius AO and BO on wrist plate = 5". 
 
 Radius HO on wrist plate (0 =6". 
 
 Angles EC' A' and FD"B" = 90. 
 
 Release = 98 per cent. 
 
PROBLEMS 227 
 
 Compression = 4 per cent. 
 
 Crank angle at admission = 3. 
 
 Throw of eccentric = 6f." 
 
 Radii of rocker arms are equal for eccentric and hook rods. 
 
 Normal cut-off = 20% . 
 
 Width of admission port = %". 
 
 Width of exhaust port = l". 
 
 Single-ported valves. 
 In Fig. M, 
 
 Radius of arm EG =3%' 
 
 Radius of arm EH =4^". 
 
 Radius of arm El =4". 
 
 Radius of cam EJ =2". 
 
 Radius of latch EK = %1". 
 
 Center G is V/i" above horizontal center line at trip position for 
 
 normal cut-off. 
 
 Make the general layout % actual size, and that of the trip mechanism 
 full size. 
 
 Find the lengths of the steam rod AC and the exhaust rod BD, the 
 angle of advance, the steam lap, the lead, the exhaust lap, the maximum 
 
 FIG. M 
 
 cut-off with trip working, the maximum cut-off when beyond control of trip, 
 the maximum port-opening for maximum cut-off, the maximum port-open- 
 ing for normal cut-off, the maximum port-opening for 10% cut-off, the move- 
 ment of the governor rod from normal to 10% cut-off, and the movement of 
 governor rod from normal to maximum trip cut-off. 
 
228 
 
 ENGINES AND BOILERS 
 
PROBLEMS 229 
 
 78. The necessary dimensions of a Stephenson link are as follows. (Fig. N.) 
 Valve-travel at full gear = 5>". 
 Steam lap = I". 
 Exhaust lap = T y. 
 Lead at full gear=0". 
 Steam port = W. 
 Exhaust port = 2Y 2 ". 
 Bridge = 1". 
 = l/7.5 
 a = b = 45". 
 m = 3". 
 e=U". 
 
 h=U". 
 
 .7 = 1713/32". 
 k = l8". 
 #==48.8". 
 Make the drawing one-half actual size and proceed as follows. 
 
 (1) Make a template of the link as shown in Fig. N. 
 
 (2) Locate the center of the link-block with the crank at head-end dead 
 center at full gear. 
 
 (3) Find the center of travel of the link-block, neglecting for the time 
 being the angularity of the eccentric rods. 
 
 (4) Place the center of the rocker shaft above the point found. 
 
 (5) Place the crank and eccentrics in their positions at 40% head-end cut- 
 off, running forward. 
 
 (6) Find by trial the position of the link (template) for the preceding 
 position of the crank. (Remember the center of the link-block is now at a 
 distance equal to the steam-lap from its mid-position.) Locate the saddle- 
 block pin and the position of the bell crank. 
 
 (7) Assume twelve equidistant crank positions and the corresponding ec- 
 centric positions for the preceding cut-off. Then draw in the center of link 
 for each crank position, by trial by means of the template. 
 
 (8) Draw a valve ellipse from the valve displacement found above. Locate 
 all events. 
 
 (9) Check as to the assumed cut-off. 
 
 (10) Find the amount of slip between the link-block and link when running 
 at the assumed cut-off. 
 
230 
 
 ENGINES AND BOILERS 
 
PROBLEMS 231 
 
 79. The arrangement of parts and the necessary dimensions of a Wal- 
 schaert gear are shown in Fig. O. The valve is of the piston type and has 
 inside admission. This is the common type used on modern locomotives. 
 Fig. O shows the piston in its mid-position and the link-block set at mid-gear. 
 As the link is pivoted to the frame of the engine at the point L, there will 
 be no motion of the link-block when set at mid-gear. Hence all the motion 
 the valve gets at this position of the block comes from the cross-head. There- 
 fore, as the cross-head is in mid-position, the valve will also be in mid-position. 
 
 Suppose that such a gear is used on an engine with the following data. 
 
 26J/TX30" engine. 
 
 Engine runs forward (under). 
 
 Diameter of valve = 14." 
 
 Maximum valve-travel = 6>". 
 
 Steam lap = l 1/16". 
 
 Exhaust lap = 0. 
 
 Lead =3/16". 
 
 Dimensions as in Fig. O. 
 Make the drawing one-fourth actual size, and proceed as follows: 
 
 (1) Lay out the gear in the position shown in Fig. O, with the piston in 
 mid-position and the link-block set at mid-gear. Indicate each of the parts 
 by its center line only. 
 
 (2) Make a template of the link. 
 
 (3) Set the valve and the point H for head-end cut-off. Then place the 
 crank at 40% of forward stroke, assuming that the engine is running forward. 
 
 (4) Locate the eccentric E at 90 back of the crank, and the point F, and 
 draw in the center line of the link. 
 
 (5) With the cross-head K in position for 40% cut-off, the location of the 
 point / will be determined. Since H was located in (3), the point G is found 
 by connecting / and H. The distance that G is to the right of the mid- 
 position gives the distance that the link-block center is to the right of its 
 mid-position. This locates the link-block for 40% cut-off. Now locate the 
 points D, M and B. 
 
 (6) With the link-block set for 40% head- end cut-off, take twelve equidis- 
 tant crank positions and find the valve displacement for each position. Plot 
 these valve displacements against the corresponding piston displacements 
 either as in a Zeuner diagram or as in a valve-ellipse diagram, and connect 
 the points thus found by a smooth curve. 
 
 (7) Draw in the laps on the diagram just constructed, and check the cut-off 
 with the assumed value of 40%. 
 
 (8) Find the amount of slip between the link-block and the link when the posi- 
 tion is that of 40% cut-off, with the engine running forward. 
 
 80. The Russell Engine Co. makes a four- valve engine. In this engine, 
 the exhaust is taken care of by oscillating or Corliss valves, and the admis- 
 sion by a direct slide-valve. This slide-valve admits steam and carries on 
 its back a rider-valve that cuts off the steam. The main valve is driven 
 by an eccentric keyed to the shaft, while the rider-valve is driven by an 
 eccentric whose angle of advance is controlled by the governor. The gov- 
 ernor simply rotates the eccentric about the shaft, changing the angle of 
 
232 
 
 ENGINES AND BOILERS 
 
 advance, but affecting in no way the absolute travel of the valve. Hence, 
 it is necessary to consider the relative motion of the rider-valve and the main 
 valve in making an analysis of the cut-off valve. 
 
 The necessary dimensions of the valves and the seat are given in Fig. P. 
 The throw of both eccentrics is 5K inches, and the angle of advance of the 
 main eccentric is 32.5 degrees. 
 
 Proceed with the analysis in the following manner. 
 
 (1) Draw the two eccentric circles about the same center and locate the 
 extremity of the diameter of the valve circle for the main valve. 
 
 Trgyf/ grf both IM/HCS S4? 
 
 Seaf 
 
 FIG. P VALVES AND SEA^T OF RUSSELL FOUR-VALVE ENGINE 
 
 (2) Place the crank for cut-off at 25% of the head 7 end stroke, and locate 
 the main eccentric. Then determine from the dimensions in Fig. P how far 
 from the mid-position the cut-off eccentric must be to give the proper posi- 
 tion of rider-valve for cut-off. This determines the angle of advance of the 
 cut-off eccentric at this particular cut-off. 
 
 (3) Take twelve equidistant crank positions and determine the relative 
 position of the rider-valve to the main valve for each position. Plot these 
 distances as in a Zeuner diagram. It will be noticed that the diameter of 
 the relative valve-circle is equal in amount and parallel in directio'n to a 
 line connecting the extremities of the diameters of the valve circles in the 
 Zeuner diagrams for the main valve and the rider- valve. Also determine 
 the relative steam lap, which is negative. It will be found that this is equal 
 to the distance between the working edges of the rider-valve and the main 
 valve when both are in mid-position. 
 
PROBLEMS 
 
 233 
 
 (4) Now determine the diameters of the relative valve-circles in amount 
 and in direction by repeating the process of (3) for eight cut-offs (0% to 70%), 
 and draw the locus of the extremities of the diameters of the relative valve- 
 circles. It is seen that this locus is the arc of a circle whose radius is equal 
 to the eccentricity of the rider-valve eccentric and whose center is the ex- 
 tremity of the diameter of the valve circle for the main valve. 
 
 (5) Make the Zeuner analysis for cut-offs of 10%, 30% and 60%, finding 
 the relative angle of advance and the relative valve- travel by drawing a per- 
 pendicular to the crank position at the point where the crank cuts the rela- 
 tive steam lap. The point where this perpendicular intersects the locus of 
 the extremities of the diameters of the relative valve-circles determines the 
 construction point for the relative Zeuner diagram. 
 
 81. A gravity-balanced spindle governor built as shown in Fig. Q has 
 arms 20 inches long. At normal speed the arms are at an angle of 45 with 
 the horizontal. 
 
 ' (a) Find the normal speed of the governor. 
 
 (6) Find the percentage of variation in speed from no load to full load. 
 (c) If the normal speed is increased 30 per cent and the range of vertical 
 movement of the point A is the same as before, what is the percentage of varia- 
 tion in speed from no load to full load? 
 
 o 
 
 - S/o/oaJ 
 
 - formal 
 
 - - FU///04J 
 
 FIG. Q 
 
 FIG. R 
 
 82. In the cross-armed gravity-balanced spindle governor shown in Fig. R,. 
 the upper arms are 30 inches long and the lower arms are 20 inches long. 
 
 Find the percentage of variation in speed from no load to full load, and 
 compare the result with that of Problem 81. 
 
 83. The governor of Problem 81 is now loaded with a weight of 60 pounds. 
 If the normal speed is now 100 r.p.m., and the vertical movement of the point A 
 is the same as before, what is the percentage of variation of speed from normal? 
 
 84. A Corliss engine is governed by a loaded gravity-balanced spindle 
 governor. The pulley on the governor and pulley on the engine are both 
 10 inches in diameter. It is desired to change the speed of the engine from 
 100 to 120 r.p.m. In what three ways may this be done without affecting 
 the speed regulation? Give your calculations. 
 
234 
 
 ENGINES AND BOILERS 
 
 86. Find the percentage of variation in speed from no load to full load for 
 the governor shown in Fig. S. 
 
 86. Suppose that the spring of a spring-balanced centrifugal governor is 
 fastened directly to a weight of 40 pounds, as shown in Fig. T. If the speed 
 
 FIG. S 
 
 FIG. T 
 
 at no load is 206 r.p.m., and at full load 200 r.p.m., what must be the scale 
 of spring? 
 
 87. If the spring in Problem 86 is replaced by one of 40 pound scale, and 
 the speed at full load is 200 r.p.m., what is the speed at no load? Is the 
 governor stable or unstable? 
 
 88. What scale of spring would make the governor of Problem 86 iso- 
 chronous at a speed of 200 r.p.m.? 
 
 89. The no-load speed of a governor is 300 r.p.m. and the full load speed 
 
 is 290 r.p.m. At no load, the tension 
 in the governor spring is 500 pounds. 
 At full load, the spring is 2 inches shorter 
 than at no load. The scale of spring is 
 100 pounds. 
 
 If the spring is tightened by shorten- 
 ing it up half an inch, what will be the 
 effect on the no-load and full-load speeds? 
 
 90. With the governor of Problem 89, 
 how much would the spring have to be 
 taken up to make the governor isochro- 
 nous? What would the speed then be? 
 
 91. In the steam-turbine governor 
 shown in Fig. U, the weights of 8 pounds 
 each are 4 inches from the center of the 
 spindle at full load when the speed is 600 
 r.p.m. At no load, the weights are 5 inches 
 
 FIG. U 
 
 from the spindle and the speed is 610 r.p.m. The weights are pivoted at 
 points A and A . 
 
 (a) Compute the scale of spring. 
 
 (6) Design the spring, i.e. find the size of spring wire, the diameter of the 
 coil, and the number of turns that will give the correct force and scale. 
 
M512399 TJ255 
 B9 
 Forestry