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TABLES OF
THE PROPERTIES OF STEAM
AND OTHER VAPORS
AND
TEMPERATURE-ENTROPY
TABLE
BY
CECIL H. ,PEABODY
PROFESSOR OF NAVAL ARCHITECTURE AND MARINE ENGINEERING
MASSACHUSETTS INSTITUTE OF TECHNOLOGY
EIGHTH EDITION. REWRITTEN
TOTAL ISSUE FIFTEEN THOUSAND
K
OF THE
UNIVERSITY ;
OF /
NEW YORK
JOHN WILEY & SONS
LONDON: CHAPMAN & HALL, LIMITED
1909
COPYRIGHT, 1888, 1907, 1909,
BY
CECIL H. PEABODY.
Stanhope ipress
F. H. GILSON COMPANY
BOSTON. U.S.A.
PREFACE.
THE Tables of the Properties of Steam were published in 1888, to
accompany the author's " Thermodynamics of the Steam Engine"; in 1907
they were revised, taking advantage of added information then available,
and a Temperature-Entropy Table was added to facilitate calculations
for steam turbines.
The properties of steam have recently been redetermined by new and
refined methods, that are capable of great certainty and precision, so that
computations based upon them show a satisfactory concordance. These
tables have been recomputed with this information, and may, therefore,
be used with confidence and may be expected to have permanence.
The Temperature-Entropy Table gives solutions of all adiabatic prob-
lems (and many others) both for saturated and for superheated steam
with ease and precision, and permits us to make certain determinations
not otherwise possible. For engineering purposes answers to such prob-
lems may in general be read directly from the table; greater refinement
can be had by interpolation when necessary.
Original data are given in the Introduction, and methods of compu-
tation are given with such completeness that each one may decide for
himself the degree of accuracy he shall attribute to the properties and
methods presented.
The author desires to express his appreciation of assistance given by
Mr. H. A. Everett, S.B., in the preparation of material, computation of
tables and reading of proof.
C. H. P.
MAY ist, 1909.
196479
CONTENTS.
INTRODUCTION
Page
i
Table I.
Table II.
Table III.
Table IV.
Table V.
Table VI.
Table VII.
Table VIII.
Table IX.
Table X.
Table XI.
Table XII.
Table XIII.
Table XIV.
Table XV.
STEAM, ENGLISH UNITS, DEGREES 35
STEAM, ENGLISH UNITS, POUNDS 45
STEAM, FRENCH AND ENGLISH UNITS 54
ETHER 66
ALCOHOL 67
CHLOROFORM 68
CARBON BISULPHIDE . 69
CARBON TETRACHLORIDE 70
ACETON 71
AMMONIA 72
SULPHUR DIOXIDE 73
SPECIFIC VOLUMES OF LIQUIDS 74
VOLUMES OF HOT WATER 74
INCHES OF MERCURY AND POUNDS 75
CORRECTIVE FACTORS, SUPERHEATED STEAM 76
TEMPERATURE-ENTROPY TABLE 77
NAPERIAN LOGARITHMS 130
FOUR-PLACE LOGARITHMS 132
OF THE
UNIVERSITY
, OF
PROPERTIES OF STEAM AND OTHER VAPORS.
INTRODUCTION.
FOR engineering purposes steam is generated in a boiler which is
partially filled with water^ and arranged to receive heat from the fire in
the furnace. The ebullition is usually energetic, and more or less water
is mingled with the steam; but if there is a fair allowance of steam space
over the water, and if proper arrangements are provided for withdrawing
the steam, it will be found when tested to contain a small amount of water,
usually between half a per cent and a per cent and a half. Steam which
contains a considerable percentage of water is passed through a sepa-
rator which removes almost all of it. Such steam is considered to be
approximately dry.
If the steam is quite free from water it is said to be dry and saturated;
steam from a boiler with a large steam space and which is making steam
very slowly is nearly if not quite dry.
Steam which is withdrawn from the boiler may be heated to a higher
temperature than that found in the boiler, and is then said to be super- ;
heated.
The physical properties of both saturated and superheated steam have
now been determined by methods susceptible of certainty and precision
so that computations based on them show satisfactory concordance. The
results of these investigations will be quoted directly from the original
authorities, together with their estimate of the degree of precision to be
attributed to their results. This matter should be read with care, so
that each one may determine for himself the confidence he can have in
the following tables and the accuracy of computation made by their aid.
Saturated Steam. The essential properties of saturated steam are
heat of the liquid, heat of vaporization, specific pressure and specific vol-
ume; other properties dependent on these are heat equivalent of external
work, heat equivalent of internal work, entropy of the liquid and entropy
of vaporization. All these properties depend on the temperature only,
and may conveniently be determined and tabulated for use in solving
engineering problems. They are given by Tables I and III for each
2 PROPERTIES OF STEAM AND OTHER VAPORS.
degree Fahrenheit and each degree Centigrade, and by Table II for each
pound per square inch. Properties of some other vapors are given in
Tables IV to XL
Thermometric Scales. Temperatures are commonly measured by
mercurial thermometers which may be graduated on the Fahrenheit or
the centigrade scales. The centigrade scale has its zero at the freezing-
point of water, and the boiling-point is called 100 degrees. The Fahren-
heit thermometer has its freezing-point numbered 32 F., and its boiling-
point 212 degrees. It is clear that
IF = - tc + 3 2 and tc = ~ (h ~ 3 2 )-
o y
Physicists base their heat measurements on a thermodynamic scale,
which is determined from certain theoretical considerations of the proper-
ties of gases. For engineering purposes the difference between this scale
and the scale of the mercurial thermometer is not important.
Standard Temperature. It is customary to refer all calculations for
gases to the standard conditions of the pressure of the atmosphere (760 mm.
of mercury) and to the freezing-point of water. Formerly the freezing-
point was taken as the standard temperature for water and steam as even
now it is the initial point for tables of the properties of saturated vapors.
But the investigation of the mechanical equivalent of heat by Rowland
resulted in a determination of the specific heat of water with much greater
delicacy than is possible by Regnault's method of mixtures, and showed
that the freezing-point is not well adapted for the standard temperature
for water. It is the habit of many physicists to take 15 C. as the standard
temperature, and this corresponds substantially with 62 F., at which the
English units of measure are standard.
Unit of Heat. The unit for the measurement of heat is the amount of
heat required to raise one unit of weight of water one degree from the
standard temperature.
The calorie is the amount of heat required to raise the temperature of
one kilogram of water from 15 to 16 C.
The British Thermal Unit is the amount of heat required to raise the
temperature of one pound of water from 62 to 63 F.
These two definitions lead to a discrepancy of 0.03 of one per cent,
which is insignificant for engineering purposes; in these tables the B.T.U,
is taken as the standard, and the discrepancy noted is ignored.
INTRODUCTION. 3
Some physicists prefer to use for the unit of heat, one hundredth part
of the heat required to raise a kilogram of water from freezing-point to
boiling-point. Such a mean calorie is greater than those defined above,
by 0.2 of one per cent. It requires also that a different value shall be
assigned to the mechanical equivalent of heat than that given in the
following section.
Mechanical Equivalent of Heat. If mechanical energy or work is trans-
formed into heat and applied to heating water, it will be found that 778
foot-pounds of work will be required to heat one pound of water from
62 to 63 F.; in other words, one B.T.U. is equivalent to that number of
foot-pounds. This is known as the mechanical equivalent of heat. The
most authoritative determination of this important constant appears to be
that by Rowland,* who gives the value quoted, namely,
778 foot-pounds.
This is equivalent to
427 metre kilograms
in the metric system. Since his experiments were made, this important
physical constant has been investigated by several experimenters, and
also a recomputation of his results has been made after a recomparison of
his thermometers. The conclusion appears to be that his results may be a
little small, but the differences are not important, and it is not certain
that the conclusion is valid. There seems, therefore, no sufficient reason
for changing the accepted values given above.
Specific Heat is the number of thermal units required to raise a unit of
weight of a given substance one degree of temperature. The specific
heat of water at standard temperature is unity, and any specific heat is
essentially a ratio.
Specific Heat of Water. The most reliable determination of the
specific heat of water is that by Dr. Barnes,f who used an electrical
method devised by Professor Callendar and himself, and who extended
the method to and below freezing-point by carefully cooling water without
the formation of ice to 5 C. This method gives relative results with
great refinement, and gives also a good confirmation of Rowland's deter-
mination of the mechanical equivalent of heat. Dr. Barnes reports values
of the specific heat of water up to 95 C.
* Proc. Am. Acad., vol. xv (N. S. vii), 1879.
f Physical Review, vol. xv, p. 71, 1902.
PROPERTIES OF STEAM AND OTHER VAPORS.
For temperatures above boiling-point values of the specific heat of
water have been determined by the author from Regnault's* experiments
on the heat of the liquid, allowing for the correct specific heat of the
water in his calorimeter from Barnes's work. The probable error of the
heats of the liquid thus obtained, appears to be one-fourth of a per cent.
But the heat of the liquid for temperatures above boiling-point is habit-
ually associated with the heat of vaporization, and the above error is less
than one-tenth per cent of their sum.
In the following table Barnes's results are quoted directly from o to
55 C.; from 55 to 95 degrees his results have been slightly increased to
join with results determined by recomputing Regnault's experiments on
the heat of the liquid for water by allowing for the true specific heat at low
temperature from Dr. Barnes's experiments. The maximum effect of
modifying Dr. Barnes's results is to increase the heat of the liquid at
95 degrees by one-tenth of one per cent.
Temperature.
Temperature.
Temperature.
Specific
Specific
Specific
Heat.
Heat.
Heat.
C.
F.
C.
F.
C.
F.
32
1.0094
45
113
0.99760
90
194
1.00705
5
41
1.00530
50
122
0.99800
95
103
1.00855
10
50
1.00230
55
131
0.99850
100
212
1.01010
15
59
1.00030
60
140
0.99940
120
248
1.01620
20
68
0.99895
65
149
1.00040
140
284
1.02230
25
77
0.99806
70
158
1.00150
160
320
1.02850
30
86
0.99759
75
167
1.00275
180
356
1.03475
35
95
0.99735
80
176
1.00415
200
392
1.04100
40
104
0.99735
85
188
1.00557
220
428
1.0476G
The specific heats of water at high temperatures have been determined
by Dietericif using a method which does not appear to have the certainty
of Barnes's method. His results appear to be systematically larger than
Barnes's results, the discrepancy at 95 C. being four-tenths of a per cent.
Should his specific heats be used to determine the heat of the liquid at
200 C., the results would appear to be four-tenths of a per cent larger
than the tabular values of the heat of the liquid at 200 C., in Table III.
Even so if this be compared with the sum of the heat of the liquid and the
* Memoir es de Vlnstitut de France, etc., tome xxvi.
f Annalen der Physik, vol. 16, part 4, p. 593. 1905.
INTRODUCTION. 5
heat of vaporization, the discrepancy becomes about one-tenth of a
per cent.
Heat of the Liquid. The heat required to raise one unit of weight of
any liquid from freezing-point to a given temperature is called the heat of
the liquid at that temperature.
If the specific heat of water were constant the heat of the liquid would
be found by multiplying the increase of temperature by the specific heat.
An approximate result can be obtained by using the mean specific heat.
For example, the mean specific heat from o to 25 C. may be taken to be
(J X 1.0094 + 1.00530 + 1.00230 + 1.00030 + 0.99895 + J X 0.99806)
= i. 00212,
and 25 X 1.00212 = 25.05,
which in this case corresponds exactly with the tabular value in Table III.
The integral calculus gives for a varying specific heat the expression
<? =
for the heat of the liquid. An equivalent of the operation represented by
this equation is to draw a curve with temperatures and specific heats as
coordinates and to measure the area under that curve. The fact that the
specific heat does not vary much from unity suggests the following method :
Let c = i + k
where k is the difference between the specific heat and unity; it may be
positive or negative as the case may be. Then
= / + fkd,
which leads to a convenient graphical method since k is always small, and
the diagram may be drawn with a large scale for ordinates, and accurate
results can be obtained. The values for the heat of the liquid in the tables
vere obtained in this way.
The following table gives equations for heats of the liquid for various
substances as determined by Regnault:*
* Memoires de Vlnslitut de France, etc., tome xxvi.
6 PROPERTIES OF STEAM AND OTHER VAPORS.
HEAT OF THE LIQUID.
Alcohol q 0.54754 / + o.ooii2i8/ 2 + o.ooooo22o6/ 3
Ether.. q = 0.52901 1 + 0.0002959^
Chloroform q 0.23235 / -f 0.0000507 / 2
Carbon bisulphide q = 0.23523^ + o.oooo8i5/ 2
Carbon tetrachloride q = 0.19798^ + 0.0000906^
Aceton . . . q = 0.50643 1 + 0.0003965^
Heat of Vaporization. If a unit of weight of a liquid be at a certain
temperature and subject to the corresponding pressure, then the amount
of heat required to entirely vaporize it into dry saturated vapor at that
temperature and against that pressure, is called the heat of vaporization.
Henning* gives the following formula for the heat of vaporization of a
kilogram of water in calories,
r =94.210 (365 - t) Q ' 3124 (i)
He gives as the probable error of this equation one-tenth of one per cent.
Other experiments by Dieterici,f Griffiths, { and A. C. Smith are
represented by this equation with nearly the same degree of precision.
The heat of vaporization of one pound of water in B.T.U. is given by
the following equation, obtained by transforming equation (i).
r = 141.124 (689 - /) ' 31249 . (2)
Both of the above equations are applicable from freezing to boiling-
point; equation (i) from o to 100 C., and equation (2) from 32 to
212 F.
Total Heat. The amount of heat required to raise a unit of weight of
a liquid from freezing-point to a given temperature and to vaporize it into
dry saturated vapor against the corresponding temperature is called the
total heat.
The quantity is clearly equal to the sum of the heat of the liquid and the
heat of vaporization; if the first is represented by q and the latter by r,
chen H, the total heat, is given by the following equation,
H - r + q. (3)
Conversely, if H and q are known, the preceding equation will give r.
* Annalen der Physik, vol. 21, part 4, p. 849, 1906.
f Annalen der Physik, vol. 16, part 4, p. 912, 1905.
J Phil. Trans. 186, p. 261, 1895; P- 593> I 95-
Physical Review, vol. xxv, 1907.
INTRODUCTION. 7
From an investigation of certain experiments on the superheating of
steam by throttling, Dr. Harvey N. Davis * gives for the total heat of
steam in B.T.U. per pound,
H = H 212 + 0.3745 (/ - 212) - 0.000550 (t - 2I2) 2 , ( 4 )
in which H 212 is the total heat at boiling point. Equation (2) gives for
the heat of vaporization at boiling-point 969.7, and the method on page 5,
for finding the heat of the liquid, gives 180.3 at that temperature, conse-
quently the above equation may be written, for English units,
H = 1150 + 0.3745 (/ 212) O.OOO550 (/ 2I2) 2 . (5)
For French units the equation takes the form
H = 638.9 + 0.3745 (/ - 100) - 0.00099 (* ioo) 2 . (6)
Dr. Davis gives one-tenth of one per cent for the probable error of this
equation.
For other liquids the heats of vaporization are given by Regnault.
Ether H = 94 -f 0.45* 0.00055556^
Chloroform H = 67 + o. 1375 t
Carbon bisulphide H = 90 + o. 14601 0.0004123^
Carbon tetrachloride H = 52 4- o. 14625 / o. 000172 ^
Aceton. H = 140.5 -f 0.36644^ o.ooo5i6/ 2
Specific Pressure. It is customary to develop theoretical thermody-
namic equations with the specific pressure expressed in pounds per square
foot, for English units. Engineers habitually express pressures in pounds
per square inch.
For French units, specific pressures are expressed in kilograms per
square meter. Engineers use kilograms per square centimeter, and on
the other hand physicists commonly express pressure in millimeters of
mercury.
One cubic decimeter (or one liter) of mercury weighs 13.5959 kilograms,
and a cubic decimeter is one-thousandth of a cubic meter, consequently
the pressure of a column of mercury one millimeter high, on a base
one meter square, is 13.5959 kilograms.
The normal pressure of the atmosphere is taken to be 760 mm. of mer-
cury (at o C.), which is equivalent to 10,333 kilograms per square meter.
* Trans. Am. Soc. Mech. Eng., 1908.
8 PROPERTIES OF STEAM AND OTHER VAPORS.
The normal pressure of the atmosphere is, therefore, 1.0333 kilograms
per square centimeter. It was formerly the custom to graduate pressure
gauges in atmospheres, for use in countries using the metric system.
There is a tendency to confusion of units that are roughly approximate,
and in some cases it is necessary to determine whether a pressure is
intended to be in atmospheres or in kilograms per square centimeter.
Taking the meter to be equivalent to 39.37 inches, and the kilogram to
weigh 2.20462 pounds, then one millimeter of mercury will be equivalent
to
J 3-5959 X 2.20462
39-37
= .019338
of a pound per square inch. The normal pressure of the atmosphere is
760 times this, or 14.696 pounds per square inch. The corresponding
specific pressure is 2116 pounds per square foot.
Pressure of Saturated Steam. Recent determinations of the pressure
of saturated steam have been made by Holborn and Henning* with all the
resources of modern physical methods including the platinum thermometer.
Their results reduced to the thermometric scale are set down in Table III
exactly as given in their original report. Their own tests covered the
range of temperature from 50 C. to 200 C., but they extend their results
to 205 C. The results which they give from freezing-point to 50 C.
were deduced by them from experiments of Thiesen and Scheel. In
Table III the pressures from 205 to 220 C. are extrapolated by the
author by aid of a curve of corrections for Regnault's equation for the
range ioo-to 220 C.
Holborn and Henning attribute to their own experiments a precision of
Tta of a degree Centigrade; this is far beyond technical requirements
for direct application, but is needed in the computation of specific vol-
umes, as will appear later. Thiesen and Scheel's experiments had a less
degree of precision; and the extrapolation from 205 to 220 C. is open to
some doubt.
Pressures of Other Vapors. Regnault determined the pressures of
various vapors and deduced for all of them equations having the form
log/> = a + ba n + c{3 n . (7)
* Annalen der Physik, vol. 26, part 4, p. 83.3,1908.
INTRODUCTION.
The following table gives the special forms of the equation and the
constants for several vapors:
log a.
a.
6.
/ c -
Alcohol
a - ban + c fin
a + ban c fin
a ba n cfin
a ba n cfin
a ban c ($n
5.4562028
5.0286298
5.2253893
5.4011662
12.0962331
4.9809960
0.0002284
2.9531281
3.4405663
9.1375180
0.0485397
3.1906390
0.0668673
0.2857386
1.9674890
Ether . . .
Chloroform
Carbon bisulphide
Carbon tetrachloride. . .
log a.
log/?.
n.
Limits.
Alcohol
Ether
9.99708557-10
0.0145775
9.9974144 -10
9.9977628 -10
9.9997120 -10
9.9409485 -10
9.996877 -10
9.9868176 -10
9.9911997 -10
9.9949780 -10
J+20
t+ 20
t- 20
t+ 20
t+ 20
-20, + 150 C.
- 20, + 120 C.
+ 20, + 164 C.
- 20, + 140 C.
- 20, + 188 C.
Chloroform
Carbon bisulphide
Carbon tetrachloride. . .
Zeuner* gives the following equation for aceton based on Regnault's
work:
log p = a ba n + c$ n \
log ba n = + 0.5312766 0.0026148/5
log c[$ n = 0.9645222 0.0215592 t.
Specific Volume of Saturated Vapor. From the extreme difficulty of
direct experimental determinations of the specific volume of saturated
vapor it has been customary to compute this property by aid of the equation
5 = u + a = -
(8)
dt
where s is the volume of the vapor and a is the volume of the liquid; the
other quantities are r the heat of vaporization, T the absolute tempera-
ture, the mechanical equivalent of heat, and
A dt
the differential coeffi-
cient of the pressure with regard to temperature. A close approximation
to the differential coefficient may be had by the following process : choosing
a temperature (for example iooC), take the pressure at two degrees
* Mechanische Warmetheorie.
10 PROPERTIES OF STEAM AND OTHER VAPORS.
higher (102 C.) and at two degrees lower (98 C.) and divide by 4.
The pressures must be in kilograms per square meter. From Table III
we deduce
A/> 1100.3 061.6
AT 4 = 36 ' 92 '
The pressures are 1000 times the tabular pressures in kilograms per square
centimeter. The expression - is taken to represent an operation of the
nature explained above. This statement is given in hopes that it may
make evident an important method to readers who are not conversant
with calculus.
Equation (8) must be used for all other vapors than steam, and for
steam at temperatures less than 100 C.; it probably gives the best values
for the specific volume of steam at temperatures higher than 100 C., as
will appear in the discussion of experimental results.
Laws of Thermodynamics. Theoretical thermodynamics is based on
two propositions or laws known as the first and second laws. The first law
is stated on page 3, under the heading Mechanical Equivalent of Heat.
The second law cannot be stated so briefly and satisfactorily; it may
perhaps be best represented by one of its consequences, which can be
written
T-T' ' .
where e is the efficiency of an ideal perfect heat engine and T and T' are
absolute temperatures at which the engine receives and rejects heat.
For our present purpose it may be sufficient to define the absolute
temperature by the expressions
r = / + 2 73 C. (10)
T = t + 459-5 F. (n)
Derivation of Equation (8). It is hoped that the folio wing simple deriva-
tion of equation (8) may be evident even to those who are not familiar
with theoretical thermodynamics. Suppose that we have a simple engine
consisting only of a piston moving in a cylinder with a closed end, both
being supposed to be made of a non-conducting substance. Let Fig. i
represent the indicator diagram of a series of operations as follows. First
assume that there is one pound of water at the temperature / in the cylin-
\ X
d T-AT c
INTRODUCTION. 1 1
der at the beginning of operations which can be represented by a; to this
let there be applied the heat r\ it will entirely vaporize the water
at constant pressure and the volume will increase
from o to 5, the increase being
u = s a. (12)
The second operation is an expansion represented by
be. During the third operation, represented by cd,
we must imagine that heat is withdrawn in some
way and that the steam partially condenses. Finally FlG - T -
we have a compression da, which closes the diagram.
The second law of thermodynamics, represented by equation (9), gives
for the efficiency of the diagram
T - (T - AT) *_&T
T T'
for the temperature at which heat is withdrawn is A T degrees less than T.
Consequently the heat changed into work is
rAT
T
But by the first law of thermodynamics this heat is equivalent to the
work represented by the diagram. If is the mechanical equivalent, then
A
the work produced from the heat is
A T
But the pressure is p pounds per square foot during the forward stroke
and p - A/> during the return stroke, so that the effective work is
\p.u,
where u is the increase in volume. For example, the piston might have
one square foot of area and move u feet. Equating the above expressions
Now it can make no difference whether the change of temperature is
measured in the usual way and written A/ or measured as above. There-
fore
12 PROPERTIES OF STEAM AND OTHER VAPORS.
The expression -^ is that discussed on page 10. Those familiar with
calculus will recognize that equation (13) leads to
(14)
Specific Volume of Saturated Steam. The relation of the pressure of
saturated steam to the temperature is given by Holborn and Henning in
the form of a table of results which are quoted directly in Table III, the
pressure being expressed in millimeters of mercury. It is considered that
the best way of dealing with the differential coefficient -~ is to replace it
by the ratio - , as discussed on page 10, using 4 C. for the interval of
temperatures A/.
A number of elements enter into this consideration. If the relation of
the pressure to the temperature could be represented by a second degree
curve, that is, if such a curve were a parabola with its axis vertical, the
ratio -T* for any interval would be precisely equal to -j- . A table that
A/ (it
could be represented by such a curve would have constant second differ-
ences; by second differences are meant the differences of the tabular dif-
ferences as in Table III. An examination of second differences derived
from Table III shows that they increase slowly, but that the increase is
not perceptible for four degrees. For a six-degree interval the increase
is barely perceptible, and for ten degrees it is very apparent. Now the
precision claimed for the measurement of temperature is T &tf of a degree,
so that a four-degree interval appears to give a precision of computation
of ?VT> for a single value of -^ . It may be noted in passing that the
precision of observation of the height of the mercury column is better
than the temperature determinations and therefore does not contribute
to the probable error.
In order to diminish the effect of local variations of the nature of acci-
dental errors, the values of the ratio were computed for each degree
INTRODUCTION. 13
of temperature from o C. to 220 C. The first and second differences
were then computed, and the computed values of ^ were changed when
necessary to the amount of -njW in order to make the second differences
regular. This process is equivalent to drawing a smooth or fair curve
to represent physical properties obtained by observation.
Having values of the ratio - for each degree of temperature, the spe-
cific volumes were computed by equation (8). These values were then
tested for fairness by taking second differences, and again the computed
values were varied when necessary to the extent of yuW to make the
second differences regular. The combined effect of both fairings is
estimated not to exceed -svv, and it is believed that the probable error of
the specific volumes thus determined is not greater than that amount
for the range of temperature 50 C. to 200 C. covered by Holborn and
Henning's experiments. This estimate carries with it the assumption
that the methods of fairing give somewhat greater mean precision than
can be attributed to a single computation of -~
For the range of temperature from o C. to 50 C., and especially for
temperatures less than 30 C. (86 F.), so small a probable error cannot
be claimed for the specific volumes; but that range has less interest for
engineers. For temperatures less than 30 C. the specific volumes were
derived in the following way. In the first place the values Apu given in
Table III were computed from the specific volumes, and a curve was
drawn to represent them; above 30 C. the computed values varied from
the curve less than y^; in only a few cases was the variation greater
than TsW- Below 30 C. it was considered more correct to take values
of Apu from the curve which was there appreciably straight, and
values of the specific volume were obtained for Table III by inver-
sion of the method of computing Apu. In passing it may be said
that all values of Apu in Tables I and III were derived from the curve
mentioned, which gave a greater degree of precision than needed for
that purpose.
Since the pressures corresponding to temperatures above 200* C. are
extrapolated, the specific volumes computed from them are affected by
the same degree of uncertainty that attaches to the pressures.
PROPERTIES OF STEAM AND OTHER VAPORS.
Specific Volumes of Other Vapors. In order to apply equation (8)
to the computation of vapors for which Regnault's equations are given
on page 9, we may derive the differential coefficient in the form
The following table gives values to be used for the factors that appear
in that equation.
SIGN.
LogUa").
LogCB/3").
4 a".
BP n .
Alcohol
+
+
+
+
+
+
+
+
+
+
+
- 1.1720041-0. 0029143 1
-1.3396624-0.0031223*
-1. 3410130-0. 0025856*
-1.4339778-0.0022372*
-1.8611078-0.0002880*
-1.3268535-0.0026148*
t, temperature C.
-2. 9992701-0. 0590515*
-4.4616396+0.0145775*
-2.0667124-0.0131824*
-2.0511078-0.0088003*
-1.3812195-0.0050220*
-1.9064582-0.0215592*
Ether
Chloroform
Carbon bisulphide..
Carbon tetrachloride
Aceton
Experimental Determinations of Specific Volumes. By far the best
direct determinations of the specific volumes of saturated steam are those
reported by Knoblauch,* Linde, and Klebe in connection with their deter-
minations of the properties of superheated steam. These experiments
determined the pressures at constant volume, and the results are so treated
as to give the volume at saturation by extrapolation with great certainty.
In their report they claim for their results, including volumes at satura-
tion, a probable error not greater than
COMPARISON OF EXPERIMENTAL AND COMPUTED VALUES OF THE SPECIFIC
VOLUME OF SATURATED STEAM.
Volumes Cu. M.
Volume Cu. M.
Tempera-
Tempera-
ture.
Experi-
mental.
Computed.
Per Cent
Deviation.
ture.
Experi-
mental.
Computed.
Per Cent
Deviation.
100
1.674
1.671
+ 0.18
145
0.4458
0.4457
+ 0.02
105
1.421
1.419
+ 0.14
150
0.3927
0.3921
+ 0.15
110
1.211
1.209
+ 0.17
155
0.3466
0.3463
+ 0.09
115
1.036
1.036
160
0.3069
0.3063
+ 0.20
120
0.8894
0.8910
-0.18
165
0.2724
0.2729
+ 0.18
125
0.7688
0.7698
-0.13
170
0.2426
0.2423
+ 0.12
130
0.6670
0.6677
-0.10
175
0.2168
0.2164
+ 0.19
135
0.5809
0.5812
-0.05
180
0.1940
0.1941
-0.05
140
0.5080
0.5081
-0.02
* Mitteilungen uber Forschungsarbeiten, etc., Heft 21, S. 33, 1905.
INTRODUCTION. 1 5
These experimenters give 32 determinations of the volume of saturated
steam. In order to make a comparison of these experimental values with
computations in Table III, a large plot was made with temperatures for
abscissae and logarithms of volumes for ordinates, and a fair curve was
drawn ; from this curve the experimental values set down in the preceding
table were deduced; the computed values are taken from Table III.
The greatest deviation is 0.2 of one per cent, which is the probable
error assigned by the experimenters to their work. It may therefore be
concluded that the claim of a probable error not in excess of -gvv for the
computed values of the specific volume of saturated steam, and of a simi-
lar degree of precision for the experimental values, is warranted.
Now equation (8) includes explicitly the heat of vaporization, the
absolute temperature and the mechanical equivalent of heat as well as
the differential coefficient -^-. It also includes the heat of the liquid
implicitly, since the heat of vaporization is derived from the total heat.
Consequently the claim of a precision of -5^ for the specific volume
attributes a like degree of precision to the first three named properties,
and the same effective certainty to the heat of the liquid. It is true that
we may independently attribute a greater precision to the three first
properties named. Thus a probable error of T ^W is claimed for the total
heat by Dr. Davis, and Callendar * claims a probable error of yuVtf or
better for the absolute temperature; the real value of the mechanical
equivalent is even now slightly in question, but the value assigned is
probably in error less than T tfW.
The conclusion appears to be that our knowledge of the properties of
saturated steam is sufficient for engineering purposes, and that tables
computed with available data will not require change.
Specific Volume of Liquids. The coefficient of expansion of most
liquids is large as compared with that of solids, but it is small as compared
with that of gases or vapors. Again, the specific volume of a vapor is
large compared with that of the liquid from which it is formed. Con-
sequently the error of neglecting the increase of volume of a liquid with
the rise of temperature is small in equations relating to the thermo-
dynamics of a saturated vapor, or of a mixture of a liquid and its vapor
when a considerable part by weight of the mixture is vapor. It is, there-
fore, customary to consider the specific volume of a liquid to be constant.
* Phil. Mag., Jan., 1903.
1 6 PROPERTIES OF STEAM AND OTHER VAPORS.
Table XII, giving the specific volumes of various liquids, was taker
from the Phys.-Chem. Tabellen of Landolt and Bornstein.
Volume of Water. Table XIII gives the volumes of water compared
with its volume at 4. From o to 100 C., the values are those given b>
Rossetti. Above 100, the values are those calculated by Hirn's equa-
tion.
Volumes of Liquids. The volumes of liquids at high temperatures,
compared with the volume at freezing-point, are represented by the
following equations given by Him : *
Water 100 C. to 200 C. (vol. at 4 C.= Logs.
unity) v=l + 0.00010867875* 6. 0361445- 1C
+ 0.0000030073653* 2 4. 4781862- 1C
+ . 0000000028730422* 3 1 . 4583419- 1C
-0.0000000000066457031* 4 8. 8225409- 2C
Alcohol 30 C. to 160 C. (vol. at C.=
unity) v=l + 0.00073892265* 6.8685991- 1C
+ 0.00001055235* 2 3. 0233492- 1C
- . 000000092480842* 3 2. 9660517- 1C
+ . 00000000040413567* 4 . 6065278- 1C
Ether 30 C. to 130 C. (vol. at 0C.=
unity) v= 1 + 0. 0013489059* 7. 1299817- 1C
+ 0.0000065537* 2 4. 8164866- 1C
- . 000000034490756* 3 2 . 5377028- 1C
+ . 00000000033772062^ . 5285571 - 1C
Carbon bisulphide 30 to 160 C. (vol. at
0C. = unity) v=l + 0. 0011680559* 7.0674636-10
+ 0.0000016489598* 2 4.2172103-10
-0. 00000000081 119062* 3 0.9091229-10
+ . 000000000060946589* 4 8 . 7849494- 20
Carbon tetrahcloride 30 to 160 C. (vol.
at C.=unity) v= 1 + 0.0010671883* 7.0282409- 10
+ 0.0000035651378* 2 4.5520763-10
- . 000000014949281* 3 2 . 1746202- 10
+ . 000000000085182318* 4 9 . 9303494- 20
Internal and External Latent Heat. The heat of vaporization over-
comes external pressure, and changes the state from liquid to vapor at
constant temperature and pressure. Let the specific volume of the
saturated vapor be s, and that of the liquid be o y then the change of
volume is s a = u, on passing from the liquid to the vaporous state.
The external work is
p(s - a) = pu,
and the corresponding amount of heat, or the external latent heat, is
Ap (s o) = Apu,
A being the reciprocal of the mechanical equivalent of heat.
* Annales de Chimie et de Physique, 1867.
INTRODUCTION. I?
That part of the heat of vaporization which is not used in doing external
work is considered to be used in changing the state from liquid to vapor.
This work required to change the molecular arrangement is called dis-
^gregation work. The heat required to do the disgregation work is rep-
resented by
p = r - Apu. (15)
Quality or Dryness Factor. All the properties of saturated steam,
such as pressure, volume, and heat of vaporization, depend on the tem-
perature only, and are determinable either by direct experiment or by
computation, and are commonly taken from tables like those assembled
in this book.
Many of the problems met in engineering deal with mixtures of liquid
and vapor, such as water and steam. In such problems it is convenient
to represent the proportions of water and steam by a variable known as
the quality or the dryness factor; this factor, x, is defined as that portion
of each pound of the mixture which is steam; the remnant, i x, is
consequently water.
Specific Volume of Wet Steam. If a pound of a homogeneous mixture
of water and steam is x part steam, then the specific volume may be
represented by
v = xs + (i x) a = xu + a,
where u is the increase of volume due to vaporization.
Intrinsic Energy. When heat is applied to a substance, a part is
expended in increasing the temperature, a part is required to do the
external work, and the remainder is considered to be used up in changing
the molecular arrangement or condition. It has been seen that these
three portions can be separated for saturated vapor; they are represented
by #, Apu, and p. In some cases the first and last cannot be separated
and must be treated together; in any case it is convenient to consider them
together. The mechanical equivalent of their sum is called the intrinsic
energy and may be represented by
E - j G + ?) (16)
If only a portion of the liquid is vaporized the external work and the
disgregation work may be obtained by multiplying the proper quantity
by the dryness factor, and the heat equivalents will be
Axpu and xp.
1 8 PROPERTIES OF STEAM AND OTHER VAPORS.
In such case the intrinsic energy is
E = ~(xp + q). (17)
Entropy. In the discussion of steam-engines or other heat engines,
it is convenient to begin by considering the way in which steam (or other
working substance) would behave if the cylinder were made of non-
conducting material. Afterwards the effect of the actual material can
be investigated. The expansion line which an indicator would draw
under such conditions is called an adiabatic line. Calculations for
adiabatic changes of steam can be made by aid of a "special function
devised for the purpose and called entropy. A discussion of adiabatic
actions and of entropy can be found in any text-book on Thermodynamics;
for example, on pages 17 and 31 of the " Thermodynamics of the Steam
Engine " by the author. It is sufficient for our present purpose to con-
sider that entropy can be expressed numerically and that the numerical
values enter into the calculation of certain engineering problems.
It is customary to represent entropy in general by <, but entropy may
be represented by 6 in dealing with a liquid.
To calculate the increase of entropy during any operation we may
divide the heat added by the absolute temperature at which it is added.
This leads to a very simple calculation in the case of vaporization of a
liquid, as will be seen in the next paragraph. If the heat is added at a
varying temperature, an approximation may be had by breaking the heat
into small portions and dividing each by the mean* temperature and
then summing up.
Such an operation can be represented by the expression
> (18)
where dQ represents an infinitesimal amount of heat and T is the abso-
lute temperature at which it is added.
Equation (18) is a consequence of the second law of thermodynamics,
and that law is sometimes said to be represented by it.
Entropy of Vaporization. If a pound of water at the temperature t
(or absolute temperature T) is partially vaporized, the heat expended
is xr. The method of calculating entropy in the preceding paragraph
gives in this case
* - <<> = f; = * ^ ( J 9)
INTRODUCTION. 19
In Tables I, II, and III values of are given for each degree or each
pound.
Entropy of the Liquid. When water is heated the specific heat varies
and the heat is added at a varying temperature. While an approxima-
tion can be had by breaking up the heat into small parts as indicated in
the preceding paragraph, a satisfactory determination of the entropy of
the liquid can be made only by aid of the methods of the integral cal-
culus. These methods give for the entropy of the liquid
'-f-f?- (*>>
It is shown on page 5 that the specific heat of water can be repre-
sented by
c = i + k,
and this expression introduced in the preceding equation gives
t T
in which t and T are the temperature by the thermometer of freezing,
and the corresponding absolute temperature. The first part of the
above expression for the entropy of the liquid can be computed readily,
and the second part (which is small) can be determined graphically with
great precision. This method was used for the tables of the properties
of saturated steam.
To obtain the entropy of any liquid named on page 6, we may first
differentiate the proper equation to obtain dq and then integrate as
indicated by the equation
The values given in Tables IV to IX were determined in this way.
Entropy of a Mixture of a Liquid and its Vapor. The increase in
entropy due to heating a unit of weight of a liquid from freezing-point
to the temperature / and then vaporizing x portion of it is
-f,
2O PROPERTIES OF STEAM AND OTHER VAPORS.
where is the entropy of the liquid, r is the heat of vaporization, and 7
is the absolute temperature. For steam - may be taken from the tables
for other vapors it must usually be calculated.
For any other state, determined by x l and ^ we shall have, for th<
increase of entropy above that of the liquid at freezing-point,
*
The change of entropy in passing from one state to another is
4> - & = ~ + 6 - x -f l - 0,.
1 * 1
When the condition of the mixture of a liquid and its vapor is giver
by the pressure and the value of x, then Table II giving the propertie:
at each pound may be conveniently used for this computation.
Adiabatic Equation for a Liquid and its Vapor. During an adiabati<
change the entropy is constant, so that the preceding equation gives
(?2 . (2a -
1 2
When the initial state, determined by x^ and ^ or p l} is known and the
final temperature t 2 , or the final pressure p 2 , the final value # 2 may b<
found by this equation. The initial and final volumes may be calcu
lated by the equations
v l = XjUi + a and v 2 = x 2 u 2 + a.
Tables of the properties of saturated vapor commonly give the specifi(
volume 5 but
s = u + <7.
The value of a for water is 0.016, and for other liquids will be found ir
Table XII.
For example, one pound of dry steam at 100 pounds absolute has the
following properties found in Table II :
/! = 327. 9 F. - = 1.1273; 0i = 0-4748;
INTRODUCTION. 2 1
If the final pressure is 15 pounds absolute, we have
/ 2 = 2i3.oF. -^-= 1.4409; 02 = 0.3140; s 2 = 26.28,
* 2
whence
i. 6021 = 1.4409* + 0.3140.
.:x 2 = .8939.
The initial and final volumes are
^i = *i = 4-43 2
V 2 = X 2 u 2 + a = 23.43.
Such a problem cannot be solved inversely, that is, we cannot assume
a final volume and determine directly the temperature and pressure cor-
responding. The Temperature-Entropy Table to be explained later will,
however, give an approximate solution directly, and an exact solution
by interpolation.
External Work during Adiabatic Expansion. Since no heat is trans-
mitted during an adiabatic expansion, all of the intrinsic energy lost is
changed into external work, so that
W = E l - E 2 = (?i - ft + oc lPl - x 2 p 2 ). (23)
For example, the external work of one pound of dry steam in expanding
adiabatically from 100 pounds to 15 pounds absolute is
W = 778 (298.5 - 181.3 + i X 805.7 - 0.8939 X 896.2),
W = 121. 8 X 778 = 94,760 foot-pounds.
Attention should be called to the unavoidable defect of this method of
calculation of external work during adiabatic expansion, in that it depends
on taking the difference of quantities which are of the same order of
magnitude. For example, the above calculation appears to give four
places of significant figures, while, as a matter of fact, the total heat H
from which p is derived is affected by a probable error of yAs or perhaps
more. Both the quantities
q l + x^ and q 2 + X 2 p 2
have a numerical value somewhere near 1000, and an error of juW is
nearly equivalent to one thermal unit, so that the probable error of the
above calculation is nearly one per cent. For a wider range of tempera-
ture the error is less ; had the lower pressure been i pound the error would
22 PROPERTIES OF STEAM AND OTHER VAPORS.
have been of a per cent. This matter should be borne in mind in
considering the use of approximate methods of calculation, for example,
by aid of a diagram like the temperature-entropy diagram.
Heat Contents. The heat required to raise one pound of water from
freezing-point to a given temperature t corresponding to a pressure p t
and to vaporize a part x at that pressure, is represented by
xr + q\
this quantity may be called the heat contents.
Rankine's Cycle. An important investigation for the steam-engine
may be made by aid of the accompanying figure which represents the
indicator diagram from a steam-engine without clear-
ance and with a non-conducting cylinder. Steam is
admitted at an absolute pressure p l from a to 6; adia-
batic expansion follows from b to c\ finally the steam
FIG. 2. is exhausted from c to d at the pressure p 2 . The
external work during admission for one pound of steam having the
quality x l is
pM = #!(*i w i + *);
the external work during expansion is
and the external work during exhaust is
P^2 = P 2 0*2^2 + (7),
which must be subtracted since it is done by the piston on the steam.
The effective work of the cycle is
PM + E l - E 2 - p,v,,
or, substituting the proper values,
W = - (& + XM + Ap&Ut - q l - x,p 2
the last term is small and may be dropped.
Remembering that
r = p + Apu,
we have
W = A ^ + * lfl ~~ q * ~
INTRODUCTION. 23
The values of r and q may be taken from Tables I, II, or III, and the
value of x 2 can be determined by aid of the equation
+ 6,.
By the first law of thermodynamics the difference between the heat
supplied to an engine and the heat rejected is equivalent to the work
done, provided there are no losses; therefore,
This most important conclusion can be stated as follows: the heat
changed into work by a steam-engine working on Rankine's cycle is
equal to the difference in the heat contents of the steam supplied to and
exhausted by the engine.
This same expression is found in the discussion of steam-turbines.
Problems of this nature can be solved immediately by aid of the
Temperature-Entropy Table.
Superheated Steam. A dry and saturated vapor, not in contact with
the liquid from which it is formed, may be heated to a temperature greater
than that corresponding to the given pressure for the same vapor when
saturated; such a vapor is said to be superheated. When far removed
from the temperature of saturation, such a vapor follows the laws of
perfect gases very nearly, but near the temperature of saturation the
departure from those laws is too great to allow of calculations by them
for engineering purposes.
All the characteristic equations that have been proposed have been
derived from the equation
pv = RT,
which is very nearly true for the so-called perfect gases at moderate
temperatures and pressures; it is, however, well known that the equa-
tion does not give satisfactory results at very high pressures or very low
temperatures. To adapt this equation to represent superheated steam
a corrective term is added to the right-hand side which may most
conveniently be assumed to be a function of the temperature and pres-
sure, so that calculations by it may be made to join on to those for
saturated steam.
24 PROPERTIES OF STEAM AND OTHER VAPORS.
The most satisfactory characteristic equation of this sort is that given
by Knoblauch,* Linde, and Klebe,
pv = BT-p(i+ap) cY-- D - ( 2 4)
p the pressure is in kilograms per square metre, v is in cubic metres,
and T is the absolute temperature by the Centigrade thermometer.
The constants have the following values:
B = 47.10, a = 0.000002, C = 0.031, D = 0.0052.
In the English system of units, the pressures being in pounds per
square foot, the volumes in cubic feet per pound, and the temperatures
in the Fahrenheit scale, we have
pv= 85.85 T - p (i + 0.00000976 p) ^50,300,000 - 0.0833) (25)
The following equation may be used with the pressure in pounds per
square inch:
pv = o. 59 62T-p(i+o.ooi 4 p) ^50,300,000 _ oo833 J. (26)
The labor of calculation is principally in reducing the corrective term,
and especially in the computation of the factor containing the tempera-
ture. Table XV gives values of this factor for each five degrees from
100 to 600 F. For ordinary use the nearest value in the table may be
selected without interpolation; when this is done the error in calculation
of a volume will not exceed 0.2 of a percent for pressures less than 150;
for higher pressures and near saturation the error may be twice as much.
By interpolation the corrective factor may be obtained with precision
for all conditions.
Knoblauch attributes to his equation a probable error of 0.2 of a
per cent within the range of his experiments which extends from 100 C.
to 1 80 C., and to about 50 C. of superheating. It has been shown
that a special treatment of his experimental values extrapolated to satur-
ation shows at no place a greater discrepancy from the tabular values
of Table III than 0.2 of a per cent. His equation when applied to
saturated steam is nearly as good, the maximum discrepancy within his
* Milteilungen uber Forschungsarbeiten, Heft 21, S. 33, 1905.
INTRODUCTION.
range being one-third of a per cent at 160 C. Below boiling-point the
greatest discrepancy of his equation is half a per cent at 50 C.; toward
freezing-point the discrepancy decreases to zero.
Specific Heat of Superheated Steam. A very laborious investigation
of the specific heat of superheated steam was made by Professor Knob-
lauch * and Dr. Jakob with the special object of avoiding the presence
of moisture in the steam near saturation.
Professor Knoblauch's report gives the results of the investigations
made, under his direction in the form of a table giving specific heats at
various temperatures and pressures and in a diagram, which can be
found in the original memoir, and he also gives a table of mean specific
heats from the temperature of saturation to various temperatures at
several pressures. This latter table is given here in both the metric
system and in the English system of units.
SPECIFIC HEAT OF SUPERHEATED STEAM.
Knoblauch and Jakob.
p Kg. per Sq. Cm.
1
2
4
6
8
10
12
14
16
18
20
p Lbs. per Sq. In.
14.2
28.4
56.9
85.3
113.8
142.2
170.6
199.1
227.5
156.0
284.4
t s Cent.
99
120
143
158
169
179
187
194
200
206
211
t s Fahr.
210
248
289
316-
336
350
368
381
392
403
412
Fahr.
Cent.
212
100
463
302
150
0.462
0.478
515
392
200
462
475
502
530
560
597
635
677
482
250
0.463
0.474
0.495
0.514
0.532
0.552
0.570
0.588
0.609
0.635
0.664
572
300
0.464
0.475
0.492
0.505
0.517
0.530
0.541
0.550
0.561
0.572
0.585
662
350
0.468
0.477
0.492
0.503
0.512
0.522
0.529
0.536
0.543
0.550
0.557
752
400
0.473
0.481
0.494
0.504
0.512
0.520
0.526
0.531
0.537
0.542
0.547
The construction of this table is readily understood from the following
example: Required the heat needed to superheat a kilogram of steam
at 4 kilograms per square centimetre from saturation to 300 C. The
saturation temperature (to the nearest degree) is 143 C.; so that the
steam at 300 degrees is superheated 157 degrees, and for this is required
the heat
157 X 0.492 = 77.2 calories.
The experiments of Professor Knoblauch were made at 2, 4, 6, and 8
kilograms per square centimetre; the remainder of the table was obtained
* Mitteilungen iiber Forschungsarbeiten, Heft 36, s. 109.
26 PROPERTIES OF STEAM AND OTHER VAPORS.
from his diagram, which was extended graphically to the extent indi-
cated. Within the limits of the experimental work the table may be
used with confidence, the greatest error being probably not more than
one-third of one per cent.
Total Heat of Superheated Steam. In the solution of problems that
arise in engineering it is convenient to use the total amount of heat
required to raise one pound of water from freezing-point to the tem-
perature of saturated steam at the given pressure and to vaporize it and
to superheat it at that pressure to the given temperature. This total
heat may be represented by the expression
H = q + r + c p (t - /.), (27)
where t is the temperature of the superheated steam, t s is the temper-
ature of saturated steam at the given pressure />, and q and r are the
corresponding heat of the liquid and heat of vaporization. The mean
specific heat c p may usually be taken from the table on page 25
without interpolation, as a small variation does not have a very large
effect.
The total heats or heat contents of superheated steam in the tempera-
ture-entropy table were obtained by the following method. From
Professor Knoblauch's table of true specific heats as given in his report
a diagram was drawn with degrees of superheating for abscissae and
true specific heats as ordinates; this diagram (which was substantially
equivalent to Knoblauch's diagram) consisted of curves, which gave the
specific heats at various constant pressures from i kilogram per square
centimetre to 20 kilograms. His tabular values were taken directly
for pressures from i kilogram to 10 kilograms, and the resultant dia-
gram was faired by cross-curves, which were also used to extrapolate
curves below i kilogram and above 10 kilograms; but in this extrapola-
tion attention was given to his extrapolation, substantially the same
results being obtained except near saturation for higher pressures. The
diagram constructed, (which was better adapted for extension to satura-
tion than Knoblauch's), indicated, at high pressure, the selection of
smaller values of the specific heat at saturation, and there is reason to
think that such values are more correct. The difference for pressures
below 10 kilograms per square centimetre (140 pounds per square inch)
in the resultant total heat computed by equation (27) is insignificant.
INTRODUCTION. 2/
At 20 kilograms (280 pounds) the difference amounts to one thermal
unit out of about 1200.
The diagram described furnished the basis of a diagram from which
the heat required to superheat the steam at a given pressure and to a
given degree could be obtained graphically for English units. Having
values of the third term in equation (27) the total heat was readily
obtained.
Entropy of Superheated Steam. By the entropy of superheated
steam is meant the increase of entropy due to heating water from freez-
ing-point to the temperature of saturated steam at the given pressure,
to the vaporization and to the superheating at that pressure. This
operation may be represented as follows:
+
F + /
1 t J Tf
in which T is the absolute temperature of the superheated steam and T s
is the temperature of the saturated steam at the given pressure; and
can be taken from Table I. The last term was obtained for the tem-
perature-entropy table by graphical integration of curves plotted with
values of ^ derived from the curves of specific heats at various tempera-
tures just described under the previous section.
Properties of Ammonia and Sulphur Dioxide. One of the most inter-
esting and important applications of the theory of superheated vapors is
found in the approximate calculation of properties of certain volatile
liquids which are used in refrigerating-machines, and for which we have
not sufficient experimental data to construct tables in the manner followed
for the fluids already discussed.
All attempts in this line have followed the example of Ledoux, who
made the first attempt and who took for the basis of his investiga-
tions the form of equation proposed by Zeuner for superheated steam,
namely, pv = BT - Cp a .
Investigations by Knoblauch already discussed show that this equation
can be considered only a crude approximation for steam, and conse-
quently less confidence can be placed on investigations by its aid than
we formerly thought.. Nevertheless, in our present condition and until
28 PROPERTIES OF STEAM AND OTHER VAPORS.
more complete experimental data are available we are constrained to
use some such approximate method, and it does not appear profitable to
recompute tables at this time.
Fortunately Regnault determined the relation of temperature and
pressure, and gave the following equations for pressure in millimetres of
mercury, the temperature being on the Centigrade thermometer.
SULPHUR DIOXIDE. AMMONIA.
log p = a ba n cfi n log p = a - ba n cfi n
a = 5.6663790 a = 11.5043330
b = 3.0146890 b = 7.4503520
c = 0.1465400 c = 0.9499674
log a 9.9972989 10 log a = 9.9996014 10
log /? = 9.9872900 10 log /? = 9.9939729 10
n = t + 28 n = t + 22
Limits, 28, + 62. Limits, 22, + 82.
The corresponding equations for pressures in pounds per square inch
for temperatures Fahrenheit are:
SULPHUR DIOXIDE. AMMONIA.
log p = a ba n cfi n log p = a - ba n - c! n
a = 3.9527847 a = 9.7907380
log b = 0.4792425 log b = 0.8721769 10
log c = 9.1659562 10 log c = 9.9777087 - 10
log a = 9.9984994 10 log a = 9.9997786 10
log /? = 9.99293890 10 log /? = 9.9966516 10
n = t + i8.4F. n = t + 7.6F.'
In the "Thermodynamics of the Steam Engine" by the author, pages
117 to 126, this calculation has been carried out with the best ascertained
properties of the superheated vapors of sulphur dioxide and ammonia
with the following results:
SULPHUR DIOXIDE. AMMONIA.
French units, pv = 14.5 T - 48 />' 22 ; pv = 54.3 T - i42/>i
English units, pv = 26.4 T - 184 />' 22 ; pv = 99 T - 7io/>i
The application of these equations to the vapors when saturated gives
the following results:
INTRODUCTION. 29
HEAT OF VAPORIZATION.
SULPHUR DIOXIDE. AMMONIA.
French units, r =* 98 0.27* r = 300 o.8/
English units, r = 176 0.27 (t 32) r = 540 0.8 (t 32)
SPECIFIC HEAT OF THE LIQUID.
SULPHUR DIOXIDE. AMMONIA.
c = 0.4 c = i.i
Tables X and XI were calculated by aid of the equations written, and
may be of use for approximate calculations, in default of more reliable
tables.
Other Data. For convenience the following data are assembled :
Length of the metre in inches 39-37-
Weight of the kilogram in pounds 2 . 2046.
Weight of i litre (i cubic decimetre) of mercury . . 13.5959 kilos.
One horsepower, in foot-pounds per second 550.
Cheval a vapeur, in kilogrammetres per second 75.
760 mm. of mercury.
I0 >333 kilos per sq. m.
Normal pressure of the atmosphere
14.7 Ibs. per sq. in.
2ii6 Ibs. per sq. ft.
29.921 in. of mercury.
One inch of mercury is equivalent to 0.4912 pound.
273
Absolute temperature of freezing-point
Mechanical equivalent of heat
A
49i- 5 .
427 metre-kilograms.
778 foot-pounds.
Explanation of Tables. Table I gives the properties of saturated
steam for each degree Fahrenheit, in English units. It is in part com-
puted directly and in part derived from Table III by interpolation, but
the interpolation was so guarded that the numerical accuracy is the
same as would be possible by direct computation. The proper degree
of precision to be attributed to any property may be judged from the
3O PROPERTIES OF STEAM AND OTHER VAPORS.
preceding statements of data and transformation. In general, atten-
tion is given to this matter, each property being stated with the precision
considered proper, avoiding superfluous figures. Exceptions are found
Y
in the cases of r, p and , which are sometimes given to five places,
while the data do not warrant more than four; but there are practical
conveniences in keeping one decimal place for those properties.
Table II, which gives properties of steam for each pound pressure,
is made by interpolation from Table I, the interpolation being so done
that it has practically the same degree of accuracy.
Table III is the fundamental table because the pressures are quoted
directly from the original authorities. These pressures in millimetres
of mercury are directly converted into kilograms per square centimetre
and into pounds per square inch. They also serve as the basis of com-
putation 1 of specific volumes which were computed both in cubic metres
and in cubic feet. The degree of precision of interpolation for pressures
at each degree. Fahrenheit was readily made greater than that required in
practice, and the degree of precision for volumes was quite as good as the
data warranted. Consequently all these tables have the same degree
of reliability.
This table gives properties for each degree Centigrade both in French
and in English units, which frequently is of direct convenience. It also
serves as a conversion table.
Tables IV to IX were taken from Zeuner's "Mechanische Warme-
theorie," making a correction for the true value of the mechanical equiv-
alent of heat, instead of Joule's earlier value, and adding columns of
entropy of the liquid.
Tables X and XI for sulphur dioxide and ammonia were calculated by
the approximate method described earlier; though open to a considerable
degree of error they may be used till better information can be obtained.
Tables XII and XIII do not appear to call for comment.
Table XIV has been computed to aid in reducing data from tests where
pressures are recorded in inches of mercury. Pressures measured in
inches of mercury are usually less than that of the atmosphere, and the
reading gives the vacuum, which is to be subtracted from the barometric
reading to find the absolute pressure in inches of mercury. The table
then gives the pressure in pounds per square inch, which can be taken
to Table II to find the properties of steam.
INTRODUCTION. 31
Table XV has been computed to reduce the labor of calculating the
volume of superheated steam. It gives the value of the factor
150,300,000
* Y 3 - 8 33
in Knoblauch's equation on page 24 for English units. By aid of this
table the volume for a given temperature and pressure can be readily
computed. The inverse calculation assuming the volume cannot be
made directly, but such problems can be resolved by trial without much
labor. If the pressure and volume are assumed the temperature can
be found neglecting the correction term, and this will enable us to enter
the table at nearly the right place.
TEMPERATURE-ENTROPY TABLE.
This table has been made to facilitate the solution of problems involv-
ing adiabatic action for steam and some other problems.
It gives for each degree Fahrenheit and for each hundredth of a unit
of entropy the quality, heat contents, and specific volume, both for moist
and for superheated steam. For convenience the pressures correspond-
ing to the temperatures are also given.
The properties named may be more exactly stated as follows:
Moist Steam.
Quality, #; the portion of a pound which is steam.
Heat contents, xr + q.
Specific volume, v = xu + a.
Superheated Steam.
Quality, / - t sat ; the number of degrees of superheating.
Heat contents, r + q + c p (t - t sat ).
Specific volume, v.
The table is arranged in groups of eight triple columns, four on each of
two pages, which face each other. Such a group is continued from the
highest to the lowest temperature; then comes the next group of eight
triple columns, etc. Commonly the solution of a given problem may
be found in a single group or in two successive groups. It is important
to note this feature of arrangement to avoid aimless search.
32 PROPERTIES OF STEAM AND OTHER VAPORS.
For engineering purposes it will be found sufficient to take the nearest
temperature of saturated steam and the nearest column of entropy, and
to take from the corresponding place in the table the required quantities.
At the highest temperature (420 F.), the variation of half a degree of
temperature corresponds to a variation of a pound and a half in pressure ;
the other properties have the following variations: heat contents 0.15 of
a B.T.U., and specific volume 0.008 of a cubic foot, which latter amounts
to half of one per cent. At lower temperature the variation of pressure
is progressively less, but the other two properties named are affected to
about the same degree. Such variations if they were carried into com-
putations and united with others in such a way as to occasion greater
uncertainties would be liable to be inconvenient; but when found in the
final results of computations and their limits known, are not likely to
cause trouble.
On the other hand the variation of half a hundredth of a unit of
entropy will at 400 degrees correspond to 0.5 of a per cent of priming or
moisture in the steam, and will carry a like variation into all of the work.-
This uncertainty of using the table without interpolation will be nearly
the same throughout the table.
Should the variations named be considered to be too large in any case,
greater accuracy can be had by interpolation. Direct interpolation for
temperature or for entropy can be made with facility; cross-interpolation
will be somewhat more troublesome.
The use of the tables can best be illustrated by a few examples.
Example i. Given the pressure by the gauge 150.3 pounds (165
absolute) and the priming 2.0 per cent (x = 0.980), to find the entropy,
heat contents, and specific volume. This condition is found most nearly
on page 80 and gives
(j> = 1.54 ocr + q = 1176.8 v = 2.697.
Example 2. Given the pressure 150.3 pounds by the gauge and the
temperature 508 F., to find the entropy, heat contents, and specific
volume. The temperature of saturated steam corresponding to 165
pounds absolute is 366 F and the superheating is 142. These condi-
tions are found on page 95 and give
< = 1.65 r + q + c p (t - ts) = 1273.3 v = 3-39 6 -
Example 3. Required the amount of heat changed into work per pound
of steam for Rankine's cycle, the initial pressure being 150.3 pounds
/
X
xr + q
V
366
.990
1185.0
2.723
126
.789
899.1
137-
INTRODUCTION. 33
by the gauge and the exhaust being under a vacuum of 26 inches of
mercury. The steam initially has i.o per cent of priming, and the
barometer stands at 30 inches of mercury.
The exhaust pressure is 4 inches of mercury, which by Table XIV
corresponds to 1.96 pound. The initial absolute pressure is found by
adding the equivalent of 30 inches of mercury or
14.7 pounds to 150.3, giving 165.0.
The solution of this problem is found in the column for entropy 1.55.
P
Initial 165
Final, 2
Heat changed into work B.T.U. 285.9
Example 4. Required the velocity of discharge from a nozzle which
takes steam at 150.3 pounds by the gauge and expands down to 26 inches
of vacuum; the initial priming being .01 and the barometer being at
30 inches.
The available heat is the same as that for the previous problem, namely,
285.9 B.T.U. for an adiabatic expansion. The velocity without friction
would be
V =\/2 X 32.2 X 778 X 285.9 = 37 8 6.
If an allowance of ten per cent can be made for friction the velocity
will be
V = v/2 X 32.2 X 778 X 0.90 X 285.9 = 359-
The specific volume at exit can be found as follows: The heat that
would be changed into work with an allowance of ten per cent for friction
will be
0.90 X 285.9 = 257.2 B.T.U.
Subtracting from the initial heat contents leaves
1185 - 257 = 928 B.T.U.
for the heat contents at 126 F. at the discharge, and this property
is found for the entropy 1.60; the corresponding specific volume is
142 cubic feet.
34 PROPERTIES OF STEAM AND OTHER VAPORS.
Example 5. Suppose that the conditions of example 3 are applied
to a steam-turbine which has four pressure stages. For adiabatic expan-
sion the available heat per stage will be
285.9 + 4 = 7I-4B.T.U.
This quantity may be subtracted four times successively from the
initial heat contents and the results will be the heat contents for the
intermediate and final pressures. All the properties are to be located in
the columns for entropy 1.55. The results are as follows:
INITIAL
SECOND
THIRD
FOURTH
DISCHARGE.
STAGE.
STAGE.
STAGE.
STAGE.
Heat contents . . .
II85.0
IH3-5
I042.I
970.6
899.1
Temperatures . . .
3 66
299
237
180
126
Pressures . .
i6<
66.0
23.4
7- ^I
1. 00
A full discussion of this method with allowance for friction and other
losses together with its limitations will be found in the author's Thermo-
dynamics oj the Steam Engine.
TABLE I.
SATURATED STEAM.
ENGLISH UNITS.
Temperature, 1
Decrees
1 :iliicnheit. 1
Pressure,
Pounds per
Square
Inch.
0)
a
fl
|'i
'gJS'd
JJl
1
"o .
I?
i
tig
jH
02
Density,
Pounds per
Cubic Foot.
Temperature,
Degrees
Fahrenheit.
t
P
Q
r
P
Apu
r
tji
9
1
*
J
.5
vl
i/V
s
32
0.0886 7
0.0
1071.7
m
1017.5
54.2
0.0000
2.1804
3308. 9Q
0. 000302. Q
32
33
0.0923 07
1.0
1071.2
1016.9
54.3
0.0021
2.1749
3179jf 7
0.000315:;;
33
34
0.0960 ^
2.0
1070.7
1016.3
54.4
0.0041
2.1695
3062 112
0. 000327 Jg
34
35
0.0999 ..
3.0
1070.2
1015.6
54.6
0.0061
2.1642
2950. nfi
0. 000339. Q
35
36
0.1040 JJ
4.0
1069.7
1015.0
54.7
0.0082
2.1588
2842}"
0.000352.^
36
37
0.1082 ~
5.0
1069.2
1014.4
54.8
0.0102
2.1535
2737}jg
0. 000365 Jj
37
38
39
0.1126 .,
0.1171 T
6.1
7.1
1068.7
1068.2
1013.8
1013.2
54.9
55.0
0.0122
0.0142
2.1481
2.1427
2634 ft
2538^
0.000379.,
0.000394};!
38
39
40
0.1217 *
8.1
1067.6
1012.5
55.1
0.0163
2.1373
244681
0.000409 J ;
40
41
0.1265 , n
9.1
1067.1
1011.9
55.2
0.0183
2.1321
2358 g6
0. 000424. ft
41
42
0.1315
10.1
1066.6
1011.3
55.3
0.0203
2.1267
2272*2
0. 000440 } 7
42
43
0.1367 **
54
11.1
1066.0
1010.6
55.4.
0.0223
2.1214
2190 82
0.000457^
43
44
0.1421 ,,
12.1
1065.5
1010.0
55.5
0.0243
2.1162
2110 7 ,
0. 000474. 7
44
45
0.1476 I*
13.1
1065.0 1009.4
55.6
0.0262
2.1109
2035^
0.000491}'
46
46
' 1533 58
14.1
1064.4
1008.7
55.7
0.0282
2.1057
1963 69
0. 000509 j*
46
47
0.1591 fi .
15.1
1063.9
1008.1
55.8
0.0302
2.1005
1894, A
0. 000528. Q
47
48
0.1652 U,
16.1
1063.4 1007.5
55.9
0.0322
2.0954
1828
0.000547^
48
49
0.1715 JJJ
17.1
1062.8
1006.8
56.0
0.0342
2.0902
1764 61
0.000567^
49
50
0.1780 .,
18.1
1062.3
1006.2
56.1
0.0361
2.0850
1703 ftn
0.000587 9 .
50
51 0.1848
19.1
1061.811005.6
56.2
0.0381
2.0799
1643^
0.00060822
61
52
0.1918 ^
20.1
1061.3
1005.0
56.3
0.0401
2.0748
1586 55
52
53
0.1990
21.1
1060.7
1004.3
56.4
0.0420
2.0697
1531 52
0.000653 9q
53
54 0.2064 L*
22.1
1060.211003.7
56.5
0.0440
2.0647
0.000676rJ
54
55
0.2140 Jj
23.1
1059.7
1003.1
56.6
0.0459
2.0596
H29*>
0.000700^4
55
56
0.2219 Qi
24.1
1059.1
1002.4
56.7
0.0479
2.0546
1381 46
0.000724 9( .
56
57 0.2301 *
25.1
1058.6
1001.7
56.9
0.0498
2.0496
1335;
0.000749^
57
58
0.2385 gj
26.1
1053.1
1001.1
57.0
0.0517
2.0446
1291 44
0.000775^
58
59
0.2471
27.1
1057.6
1000.5
57.1
0.0537
2.0396
1248 41
0. 000801 2?
59
60 0.2561
28.1
1057.0
999.8
57.2
0.0556
2.0347
1207 40
0.000828^0
60
61
0.2654 Jjg
29.1
1056.5
999.2
57.3
0.0575
2.0298
1167 39
0.000857 29
61
62
63
0.2750 Qfi
' 2848 101
30.1
31.1
1056.0
1055.5
998.6
998.0
57.4
57.5
0.0594
0.0614
2.0249
2.0201
^36
0.000887 qft
0.000917^
62
63
35
36
SATURATED STEAM TABLE I.
Temperature,
Degrees
Fahrenheit.
S,
fill
p
0)
's
&
Q
a
r
II-
P
!
l 11
Apu
J
Sj
1
e
3 t
ilg
w
r
T
Is*!
3 S o
a
OQ
s
!l
|ii
I *
i
s
Temperature,
~ Degrees
Fahrenheit. I
64
0.2949 in ,
32.1
1055.0
997.4
57.6
0.0633
2.0152
1056
0.000947, 9
64
65
3054
33.1
1054.4
996.7
57.7
0.0652
2.0103
1021 o
0.000979^
65
66
;3161 m
34.1
1053.9
996.1
57.8
0.0671
2.0055
988 32
0.001012 34
66
67
0.3272^
35.1
1053.4
995.5
57.9
0.0690
2.0007
956 31
0.001046 Q ,
67
68
0.3386}!*
36.1
1052.8
994.8
58.0
0.0709
1.9959
925 29
0.001081!
68
69
0.3505J22
37.1
1052.3
994.2
58.1
0.0728
1.9911
896^
0.001116^
69
70
0.3627 19 ,
38.1
1051.8
993.6
58.2
0.0747
1.9863
868 98
0.001152
70
71
0.3752};;
39.1
1051.2
992.9
58.3
0.0766
1.9816
840 2?
O'o01190 3 n
71
72
- 3879 J33
40.1
1050.7
992.3
58.4
0.0784
1.9769
813 25
0.001230*g
72
73
0.4012 1Q7
41.1
1050.2
991.7
58.5
0.0803
1.9722
788 2 ,
0.001269 49
73
74
0.4149}^
42.1
1049.7
991.1
58.6
0.0822
1.9675
763 24
0.00131K 9
74
75
0.4289}^
43.1
1049.2
990.5
58.7
0.0841
1.9629
7 QQ^4
0.001353^2
75
76
0.4434 1/lft
44.1
1048.7
989.8
58.9
0.0859
1.9583
717 99
0.001395 44
76
77
0.4582}^
45.1
1048.1
989.1
59.0
0.0878
.9536
695 21
0.001439**
77
78
' 4736 158
46.1
1047.6
988.5
59.1
0.0896
.9490
67 *20
0.001484*?
TTO
78
79
0.4894 1R9
47.1
1047".!
987.9
59.2
0.0915
.9444
654 90
0.001529, 8
79
80
0.5056}^:
48.1
1646.5
987.2
59.3
0.0934
.9398
634 2 -
0.001577**
80
81
- 5223 172
49.1
1046.0
986.6
59.4
0.0952
.9352
615} 9
0.001626*2
81
82
0.5395 177
50.1
1045.4
985.9
59.5
0.0971
.9306
596 lg
0.001678, 9
82
83
- 5572 182
51.1
1044.9
985.3
59.6
0.0989
.9261
578 17
0.001730^3
83
84
52.1
1044.4
984.7
59.7
0.1007
.9216
561 17
0.001783 55
84
85
0.5942 1Q9
53.1
1043.9
984.1
59.8
0.1026
1.9171
544 1fi
0.001838, fi
85
86
0.6134}^
54.1
1043.3
983.4
59.9
0.1044
1.9126
528
0.001894^
86
87
0.6332^
55.1
1042.8
982.8
60.0
0.1062
1.9081
513 lso
0.001950 5g
87
88
0.6535 9in
56.1
1042.3
982.2
60.1
0.1081
1.9037
498. QI^
0.002008 fi1
88
89
0.6745 9 }"
57.
1041.7
981.5
60.2
0.1099
1.8992
483.4!*;
0. 002069
89
90
0.6960JJJ
58.
1041.2
980.9
60.3
0.1117
1.8948
469 ' 2 138
0.002131^
DO
90
91
0.7181 997
59.
1040.6
980.2
60.4
0.1135
.8903
455.4 34
0.002196 fifi
91
92
0.7408 f (
60.
1040.1
979.6
60.5
0.1153
.8859
442 - 29
0.002262^
92
93
0^7642 234
61.
1039.5
978.9
60.6
0.1171
.8815
429. l}~
0.002330 7 ^
93
240
1^4
<u
94
0.7882 94fi
62.
1039.0
978.3
60.7
0.1189
.8771
416.7 11Q
0.002400 7n
94
95
8128
63.
1038.5
977.7
60.8
0.1207
.8728
404.8}}^
0.002470 79
95
96
:8381 259
64.
1037.9
977.0
60.9
0.1225
.8684
393.3JJ2
0.002542^
96
97
0.8640 9ft7
65.0
1037.4
976.4
61.0
0.1243
.8641
382.l 1ftR
0.002617 7fi
97
98
0.8907;?;
66.0
1036.8
975.7
61.1
0.1261
.8597
371 .3 ,,
0.002693 7 g
98
99
0.9180 273
67.0
1036.3
975.1
61.2
0.1279
.8554
360.9 1Q1
0.002771 8 *
99
100
0.9461 9Qn
68.0
1035.7
974.4
61.3
0.1297
.8511
350. 8 Q7
0.00285l ft1
100
101
0.9751^
69.0
1035.1
973.7
61.4
0.1314
.8468
341 - ! 95
0.002932^
101
102
1.0047 29
70.0
1034.6
973.0
61.6
0.1332
.8426
331. 6 92
0.003016 86
102
103
1.0351 312
71.0
1034.0
972.3
61.7
0.1350
1.8383
000 A
O4 . *OQ
0.003102 Sfi
103
104
1.0663 322
72.0
1033.5
971.7
61.8
0.1368
1.8341
313. 5 89
0.003190gJ
104
SATURATED STEAM TABLE I.
37
S -5
I
1
a
M
i x g
8.,
o t
|S&
M
h *s
III
fills
5
vl
JrJ
w""5
|l
lie-
!!!'
sis
3^5
|H
rcj;
s 3
g'o
si" 5
gl.8
Is
!
'g |
ill
|H
H
Pk
K
H
K~ c
E
w~
w
OQ
Q
EH
t
P
*
r
P
Apu
8
r
T
8
8
t
105
1.098,,
73.0
1032.9
971.0
61.9
0.1385
1.8298
304. 8 a .
0.003281 Q ,
105
106
i.iiig
74.0
1032.4
970.4
62.0
0.1403
1.8256
296. 4 4
0.003374 Q
106
107
1.165 34
75.0
1031.8
969.7
62.1
0.1421
1.8214
288 ' 2 80
0.003470 9 c
107
108
1.200,,
76.0
1031.2
969.0
62.2
0.1438
1.8172
280.2 7ft
0.003569 QQ
108
109
1 235 36
77.0
1030.7
968.4
62.3
0.1456
1.8130
272.6
0.003668*;
109
110
1.271 3?
78.0
1030.1
967.7
62.4
0.1473
1.8088
265. 2 74
- 003771 105
110
111
1.308 3g
79.0
1029.6
967.1
62.5
0.1491
1.8047
258.0 fiq
0. 003876. n7
111
112
1.347|j
80.0
1029.0
966.4
62.6
0.1508
1.8005
251. iK
0.003983}^
112
113
81.0
1028.4
965.7
62.7
0.1526
1.7963
244 - 4 64
0.004092j^
113
114
1.426..
82.0
1027.8
965.0
62.8
0.1543
1.7922
238.0 fi9
0. 004202. 19
114
115
l^
83.0
1027.2
964.3
62.9
0.1560
1.7881
231.8^?
0.004314}}^
115
116
1.509 42
84.0
1026.7
963.7
63.0
0.1578
1.7840
225.7
0.004430jjJ
116
117
1.552..
85.0
1026.1
963.0
63.1
0.1595
1.7799
219.8.
0. 004550. 9 ,
117
118
1.597*?
86.0
1025.5
962.3
63.2
0.1612
1.7758
214.0?
0.004673} 9 ^
118
119
1.642^
87.0
1025.0
961.7
63.3
0.1630
1.7717
208.4^
0.004798}^
119
120
1 . Oo7 ^ o
88.0
1024.4
961.0
63.4
0.1647
1.7677
203. 0, 9
0. 004926., n
120
121
1.737*g
89.0
1023.8
960.2
63.6
0.1664
1.7637
197.8?f
0.00506., u
121
122
1 785
90.0
1023.2
959.5
63.7
0.1682
1.7597
192.7^
0.00519}^
122
123
1.835,.
91.0
1022.7
958.9
63.8
0.1699
1.7557
187.7. fi
0.00533..
123
124
1.886JJ
92.0
1022.1
958.2
63.9
0.1716
1.7517
182.9^
0.00547} 4
124
125
1.938J 2
93.0
1021.5
957.5
64.0
0.1733
1.7477
178 - 3 45
0.00561J|
125
126
1.992,,
94.0
1021.0
956.9
64.1
0.1750
1.7438
173.8..
0.00575,,
126
127
2 - 047 56
95.0
1020.4
956.2
64.2
0.1767
1.7398
169.4J
0.00590}?
127
128
n -innOO
96.0
1019.8
955.5
64.3
0.1784
1.7359
41
0.00605j^
128
129
2.161,g
97.0
1019.3
954.9
64.4
0.1801
1 . 7320
161. l. n
0.00621..
129
130
2.220^
98.0
1018.7
954.2
64.5
0.1818
1.7281
157.1*
0.00637}?
130
131
2 280
99.0
1018.1
953.5
64.6
0.1835
1 . 7242
153.2!?;
37
0.00653Jg
131
132
2.341 62
100.0
1017.6
952.9
64.7
0.1852
1 . 7204
149. 5, 7
0. 00669. 7
132
133
101.0
1017.0
952.2
64.8
0.1869
1.7165
145.8X1
0.00686} 7
133
134
2:4%
102.0
1016.5
951.6
64.9
0.1886
1.7127
142 - 2 34
0. 00703 J 7
134
135
2.533 67
103.0
1015.9
950.9
65.0
0.1902
.7088
138.8,.
0. 00720. a
135
136
2 600 69
104.0
1015.4
950.3
65.1
0.1919
1.7050
135. 4 34
0.00738}o
136
137
.2.669 7 *
105.0
1014.8
949.6
65.2
0.1936
1.7012
132. I 33
0. 00757 jg
137
138
2.740 72
106.0
1014.2
948.9
65.3
0.1952
1.6974
128. 9 3 ,
0. 00776. Q
138
139
2.812'^
107.0
1013.6
948.2
65.4
0.1969
1.6936
125.8^
0.00795}*
139
140
2.88S 73
108.0
1013.1
947.5
65.6
0.1986
1.6899
122 8
0.00814^*
140
141
2.960 77
109.0
1012.5
946.8
65.7
0.2002
1.6861
119. 9 9R
0.00834 9n
141
142
3.037JJ
110.0
1011.9
946.1
65.8
0.2019
1.6823
117 - 1 28
0.00854;V
142
143
3 ' 116 80
111.0
1011.4
945.5
65.9
0.2036
1.6786
114.3 28
0. 00875^
143
144
3.196 ft9
112.0
1010.8
944.8
66.0
0.2052
1.6749
111.6 26
0.00896 9 .
144
145
3 ' 278 83
113.0
1010.2
944.1
66.1
0.2069
1.6711
109. 25
0.00917 2 ^
145
38
SATURATED STEAM TABLE I.
perature,
:e:rees
,hrenheit.
a
-.2 v
<o~
t- C o3 J
O)
Ii
ft
;|
Si;
l-l
ws|
2s .
JlS-8
W <S
^^
i?
"3
03
lid
iP
~4
as"
& l
rcfa
>.".s
.15 sja
perature,
egrees
ihrenheit.
|
H
t
I&&5
p
*
o>
Q
|o
T
&**
p
|ll
Apu
II
m
e
ft>!
w
r
T
O M ^ -P
gSfcPi
OQ
s
o
Q
1
s
SQfe
t
146
3.361 QA
114.0
1009.6
943.4
66.2
0.2085
1 . 6674
106.5 2 ,
0.00939 99
146
147
3.447^
115.0
1009.0
942.7
66.3
0.2102
1.6636
104.0 f.
0. 00961^,
147
148
3.535^
116.0
1008.4
942.0
66.4
0.2118
1.6599
101.624
0.00984^
148
149
3.624 Q1
117.0
1007.8
941.3
66.5
0.2135
1 . 6563
99.2
0.01008 9 .,
149
150
3.715~
118.0
1007.2
940.6
66.6
0.2151
1.6526
96.9 f
0.01032;;
150
151
3 ' 808 95
119.0
1006.7
940.0
66.7
0.2168
1 . 6490
^1
0.01056^
151
152
3.903 Q7
120.0
1006.1
939.3
66.8
0.2184
1 . 6453
92.5 2
0.01081 9 ,
152
153
4.000JJ
121.0
1005.5
938.6
66.9
0.2200
1.6416
90.4 f
0. 01106R
153
154
4 -"?oi
122.0
1004.9
937.9
67.0
0.2217
1.6380
88.4 fjj
0.01131^
154
155
4.200 inQ
123.0
1004.3
937.2
67.1
0.2233
1 . 6344
86.4 -
0.01157 9fi
155
156
4.303^
124.0
1003.7
936.5
67.2
0.2249
1.6307
84.5 \l
0.01183 9 o
156
157
4.409^
125.0
1003.1
935.8
67.3
0.2265
1.6271
82.6 \l
0.01211^
157
158
4.517 tftQ
126.0
1002.5
935.1
67.4
0.2282
1.6235
80.7 1R
0.01239 9Q
158
159
,, COC 109
4.626 n 10
127.0
1002.0
934.4
67.6
0.2298
1 . 6200
78.9 }
0.01267^
159
160
4 - 738 H4
128.0
1001.4
933.7
67.7
0.2314
1.6164
77.2 \l
0.01296*5
160
161
4.852 117
129.0
1000.8
933.0
67.8
0.2330
1.6129
75.4
0.013260,
161
162
4.969 }}l
130.0
1000.2
932.3
67.9
0.2347
1 . 6093
73.7 }l
0.01357^
162
163
5 - 088 122
131.0
999.6
931.6
68.0
0.2363
1 . 6058
72.1 {I
0.01387 3 g
163
164
5.210 19 ,,
132.0
999.0
930.9
68.1
0.2379
1 . 6023
70.6 -.
0.01417o ft
164
165
5 - 334 12fi
133.0
998.4
930.2
68.2
0.2395
1.5988
69.1 \l
0.01447,"
165
166
5 A cr >uo
.460 129
134.0
997.9
929.6
68.3
0.2411
1.5953
67.7 H
0.01477^
166
167
5.589 iqi
135.0
997.3
928.9
68.4
0.2427
.5918
66.2 1A
O.OlSlOoo
167
168
5.720},i
136.0
996.7
928.2
68.5
0.2443
.5884
RA 14
64.8 ,,
0.01543^
168
169
5.853| 33
137.0
996.1
927.5
68.6
0.2459
.5849
63-4 | 4
0.01577o
36
169
170
5.990^0
138.0
995.5
926.8
68.7
0.2475
.5814
62.0 14
0.01613 q7
170
171
6.129}^
139.0
994.9
926.1
68.8
0.2491
.5780
60.6 \*
0.01650?!
171
172
6 ' 270 H5
140.0
994.3
925.4
68.9
0.2506
.5745
59.3 g
0.01686^
172
173
6.415 H8
141.0
993.7
924.7
69.0
0.2522
.5711
58.1
0.01722 qfi
173
174
6 . 563 1 r-i
142.0
993.1
924.0
69.1
0.2538
.5677
56.9 "
0. 01758^
174
175
R >7 14 1O1
6.714 154
143.0
992.5
923.3
69.2
0.2554
1.5643
55.7 H
0.01795^
175
176
6.868 ir . 7
144.0
991.9
922.6
69.3
0.2570
1.5609
54.5 n
0.01834o Q
176
177
7.025j.l
145.0
991.3
921.9
69.4
0.2585
1.5575
53.4 {{
0.01873^
177
178
7 18^ 160
7.185 161
146.0
990.7
921.2
69.5
0.2601
1.5541
52.3 }}
0.01912^
178
179
7.346 1R4
147.0
990.1
920.5
69.6
0.2617
.5507
51.2 in
0.01953 40
179
180
7 5in 164
' - O1 V 1 fiQ
148.0
989.5
919.8
69.7
0.2633
.5474
50.2 }g
0.01993^ 9
180
181
7.678^ 8
149.0
988.9
919.1
69.8
0.2648
.5440
4Q IV"'
4y.id 1Q2
0.02035^
181
182
7.849 17 ,
150.1
988.3
918.4
69.9
0.2664
.5406
48.11 QQ
0.02078 44
182
183
8.024};s
151.1
987.7
917.7
70.0
0.2680
.5373
47.12XJ
0.02122^
183
184
o 9n9 178
8.202 lgl
152.1
987.1
917.0
70.1
0.2696
.5340
46 ' 17 94
0.02166 4 *
184
185
8.383 1Q ,
153.1
986.5
916.3
70.2
0.2711
1.5307
45.23 Qft
0.02211.,
185
186
o c c o J- ^ c
8.568 18g
154.1
985.9
915.6
70.3
0.2727
1.5273
44 ' 33 88
0.02256^
186
SATURATED STEAM TABLE I.,
39
Temperature,
. Dcirn'r-
Fahrenheit.
I
t -f 2
p
i
9
Heat of VapJ
orization.
pi
P
^ Heat Equiva-
e leatofLxter-
c nal Work.
e
Entropy of
h Vaporiza-
tion.
fill
OQ
S
Density,
eo i H- Pounds per
Cubic Foot.
Temperature, I
<- Degrees
Fahrenheit. |
187
8.756 1Q1
155.1
985.3
914.9
70.4
0.2742
.5240
43.45 Q ,
0. 02301. 7
187
188
8 ' 947 194
156.1
984.7
914.2
70.5
0.2758
.5207
42.59^
0.02348T'
188
189
157.1
984.0
913.4
70.6
0.2773
.5174
41. 75 84
0.02395 4 g
189
190
9 339
'158.1
983.4
912.7
70.7
0.2789
.5141
40.92 Q1
0. 02444.
190
191
9 . 541 n/\f
159.1
982.8
912.0
70.8
0.2805
.5108
40 - n 80
0.02493~
191
192
Q 74fi
160.1
982.2
911.3
70.9
0.2820
.5076
' 78
0.02544 51
192
193
9 955 213
161.1
981.5
910.5
71.0
0.2835
.5043
38.53 7 ,
0.02595, 9
193
194
162.1
980.9
909.8
71.1
0.2851
.5010
37.77^
0.02647^
194
195
l^lll
163.1
980.3
909.1
71.2
0.2866
.4978
37.03
0.02700^
195
196
10.605 225
164.1
979.7
908.4
71.3
0.2882
1.4946
36.31 7n
0.02754..
196
197
165.1
979.1
907.7
71.4
0.2897
1.4913
35.61
0.02808?*
197
198
n - 059 232
166.2
978.4
906.9
71.5
0.2912
1.4881
34 ' 93 66
0.02863^
198
199
11.291 9 , 7
167.2
977.8
906.2
71.6
0.2928
1.4849
34.27,,
0.02918,,
199
200
n - 528 240
168.2
977.2
905.5
71.7
0.2943
1.4817
33.62^,
0. 02974^ 7
200
201
11 . 768 . ,
169.2
976.6
904.8
71.8
0.2958
1.4786
, QQ 63
OA . UU /*(\
O.OSOSni
201
245
62
58
202
12.013 9 . ft
170.2
976.0
904.1
71.9
0.2973
.4754
32.37, 9
0.03089 60
202
203
12 261
171.2
975.4
903.4
72.0
0.2989
.4723
31.75^
203
204
12:514^
172.2
974.7
902.6
72.1
0.3004
.4691
31.15
0.03210^
204
205
12.771 9 , 9
173.2
974.1
901.9
72.2
0.3019
.4659
30.56, fi
0.03272,,
205
206
13.033;^
174.2
973.5
901.2
72.3
0.3034
.4628
29.98^
0.03335^
206
207
13.299"
175.2
972.8
900.4
72.4
0.3049
.4596
29 ' 41 55
0.03399gg
207
208
13.570 97 ,
176.2
972.2
899.7
72.5
0.3064
.4565
28.86,.
0.03465,,
208
209
13.845;'*
177.2
971.6
899.0
72.6
0.3079
.4534
28.32^
0.03531
209
210
14.125 280
178.3
970.9
898.3
72.6
0.3095
.4502
27.80^2
0.03597
210
211
14.409 9QQ
179.
970.3
897.6
72.7
0.3110
.4471
27.29,!
0.03664 7ft
211
212
14.698;*
180.
969.7
896.9
72.8
0.3125
.4441
26. 78^0.
0.03734^
212
213
14 992
181.
969.1
896.2
72.9
0.3140
.4410
26.29 49
213
214
215
15.291 30 .
15.595^
182.
183.
968.5
967.8
895.5
894.7
73.0
73.1
0.3155
0.3170
.4380
.4349
25.81 4?
25.34 4 g
0.03874 79
0.03946 7 ,
214
215
216
15 903 308
U<3 314
184.
967.2
894.0
73.2
0.3185
.4318
0.04019^
216
217
16.217, 10
185.
966.5
893.2
73.3
0.3200
.4287
24.43..
0.04093 7 ,
217
218
16.536^
186.
965.9
892.5
73.4
0.3215
.4257
23.99*,
0.04168 7
218
219
16 859
187.4
965.2
891.7
73.5
0.3230
.4226
23.56 4 2
0.04244^
219
220
17.188,0s
188.4
964.6
891.0
73.6
0.3244
.4196
23. 14.,
0.04321 7Q
220
221
17.523^
189.4
964.0
890.3
73.7
0.3259
.4165
22.73 4 J
0. 04399.1Q
221
222
17.863^
190.4
963.3
889.5
73.8
0.3274
.4135
04478
222
223
18.208,, n
191.4
962.7
888.8
73.9
0.3289
.4105
21.93
0.04560 Q ,
223
224
18.558^"
192.4
962.0
888.1
73.9
0.3304
.4075
21 ^54 39
0. 04643*,
224
225
18.914^?
ool
193.4
961.4
887.4
74.0
0.3319
.4045
21 ' 16 38
83
225
226
19.275,, fi
194.4
960.7
886.6
74.1
0.3333
.4015
20.78,,
0.04811 Q ,
226
227
19 ' 643 375
195.4
960.1
885.9
74.2
0.3348
.3985
20 ' 42 35
0.04897*
227
SATURATED STEAM TABLE I.
-i
I
1
*.
li.
H"O
83
*,
jgp
M
t 'S
le
. ro <D
*-^
^ o
3^-g
'y^_^
o 1
9
gfo
-5^"^
8 I
Oil
"o'B
.2"
li
11|
111
o'a,
1-
if!
"r*^" +3
!jj|
|||
gli
|s?-s
Sftfe
jp
w
m
W
1
CO
1
5
*
p
q
r
P
Apu
e
r
T
a
1
s
t
228
20.02 QQ
196.5
959.4
885.1
74.3
0.3363
1.3955
20.07 Q ,
0.04983 Q7
228
229
20.40^
197.5
958.7
884.3
74.4
0.3378
1.3925
19.72^
0.0507 I 1
229
230
20 - 78 39
198.5
958.1
883.6
74.5
0.3392
1.3895
19 ' 37 33
0.0516 ^
230
231
21.17 4Q
199.5
957.4
882.8
74.6
0.3407
1.3866
19.04 QQ
0.0525 Q
231
232
200.5
956.8
882.1
74.7
0.3422
1.3836
18.71X2
0.0534^
232
233
2l:97 4
201.5
956.1
881.3
74.8
0.3436
1.3806
18.39 32
0.0544 1 "
y
233
234
22.38 41
202.5
955.4
880.6
74.8
0.3451
1.3777
18.08.,.
0.0553. n
234
235
22.79*i
203.6
954.8
879.9
74.9
0.3466
1.3748
17.77^}
0.0563}"
235
236
23.21*3
204.6
954.1
879.1
75.0
0.3480
1.3718
17.46 3 J
0.0573^
236
237
23.64...
205.6
953.4
878.3
75.1
0.3495
1.3689
17.16 9Q
0.0583. n
237
238
24.08*!
206.6
952.8
877.6
75.2
0.3509
1.3660
16.87^
0.0593. 1 "
238
239
24.52 44
207.6
952.1
876.8
75.3
0.3524
1.3631
16.59 2
0.0603JQ
239
240
24.97 4 ,
208.6
951.4
876.0
75.4
0.3538
1.3602
16.31 97
0.0613. n
240
241
25 ' 42 46
209.6
950.8
875.4
75.4
0.3553
1.3573
16.04;;
0623}V
241
242
25.88*5
210.7
950.1
874.6
75.5
0.3567
1.3544
15.77 27
0.0634JJ
242
243
26.35. e
211.7
949.4
873.8
75.6
0.3582
1.3515
15.51 9 ,
0.0645. n
243
244
26.83!*
212.7
948.7
873.0
75.7
0.3596
1.3486
15.26 9 ?
0.0655}V
244
245
27 - 31 49
213.7
948.1
872.3
75.8
0.3611
1.3457
15.01^
0.0666JJ
245
246
27.80 4q
214.7
947.4
871.5
75.9
0.3625
1.3429
14.77 9 ,
0.0677.
246
247
28.29S
215.7
946.7
870.7
76.0
0.3639
1.3401
14.52fJ
0.0689}:
247
248
28.79J?"
216.7
946.0
870.0
76.0
0.3654
1.3372
14 - 28 23
0.0700^2
248
249
29.30, 9
217.7
945.4
869.3
76.1
0.3668
1.3343
14.05 9Q
0.0712 19
249
250
29.82?*
218.8
944.7
868.5
76.2
0.3683
1.3315
13.82^
0.0724};
250
251
30 - 35 53
219.8
944.0
867.7
76.3
0.3697
1.3286
13. 59 23
0. 0736^2
251
252
30.88,.
220.8
943.3
866.9
76.4
0.3711
1.3258
13.37 9 .
0.0748. 9
252
253
31- 42* 4
221.8
942.6
866.1
76.5
0.3726
1.3229
13 ' 16 22
0.0760jg
253
254
31 " 97 56
222.8
941.9
865.3
76.6
0.3740
1.3201
12.94 22
0.0773 12
254
255
32.53, ft
223.8
941.2
864.5
76.7
0.3754
1.3173
12.73 9n
0.0785.,
255
256
33.09?H
224.9
940.5
863.7
76.8
0.3768
1.3145
12.53^
0.0798}:?
256
257
OO GG& '
33.66 5g
225.9
939.8
863.0
76.8
0.3782
1.3117
O.OSllJg
257
258
34.24, q
226.9
939.1
862.2
76.9
0.3797
1.3089
12.13 1Q
0.0824
258
259
34.83^0
227.9
938.4
861.4
77.0
0.3811
1.3062
11 .94
0^0837} 3
259
260
35 - 42 60
229.0
937.8
860.7
77.1
0.3825
1.3034
n ' 75 18
0.0851J*
260
261
36.02, 9
230.0
937.1
859.9
77.2
0.3839
1.3006
11.57. s
0.0864..
261
262
36.64^ 9
231.0
936.4
859.2
77.2
0.3853
1.2978
11 39
0.0878}*
262
263
37 - 26 63
232.0
935.7
858.4
77.3
0.3867
1.2950
n: 2 i} 8
0.0892J*
263
264
37.89 fi4
233.0
935.0
857.6
77.4
0.3881
1.2923
11.04 17
0.0906..
264
265
Qft ,ot)4
234.0
934.3
856.8
77.5
0.3895
1.2895
10.87};
0.0920J*
265
266
39:17"
235.0
933.6
856.0
77.6
0.3909
1.2868
10.70^
266
267
39.83,..,
236.1
932.9
855.3
77.6
0.3923
1.2840
10.53 16
0.0950..
267
268
237.1
932.1
854.4
77.7
0.3937
1.2813
10.37 16
0.0964} 4
268
SATURATED STEAM TABLE I.
cT .ti
3 r .S
1
1
|,
!L
II.
3 K^X
"o .
i
*e
Bj
5- 2
M
job
1 '
| 8 -
ii r
aT"3 2
*o^2
"s'^
o*^ o
OW Q
*!
^n
*d
^"e
!!l
So o* a
+,&
*l
o
j5*
11^
1-s
Ih
g>'5
*2"3
J <D o
: ----
.^3
cc O 3
^o
|H
s
K
H
K~ G
S~ G
w~
1
&
H
f
P
Q
r
p
Apu
f
r
l *
t
269
41.16
238.1
931.4
853.6
77.8
0.3951
1.2786
10.21 lfi
0.0979 16
269
270
41.84^
239.1
930.7
852.8
77.9
0.3965
1.2758
10.05
0.0995}^
270
271
42.54 7
240.2
930.0
852.0
78.0
0.3979
1.2731
Q om
y.yui 152
271
272
43.24.
241.2
929.3
851.3
78.0
0.3993
1.2704
9.749 15Q
0.1026 16
272
273
43.95i 9
242.2
928.6
850.5
78.1
0.4007
1.2677
9.599^
0.1042jg
273
274
^T]
243.2
927.9
849.7
78.2
0.4021
1.2650
9.453 H4
0.1058 16
274
275
45.39 ?4
244.2
927.2
848.9
78.3
0.4035
.2623
9.309 14ft
0.1074 1R
275
276
245.3
926.5
848.1
78.4
0.4049
.2596
9.169}*"
0.1090 17
276
277
S:Sjj
246.3
925.7
847.3
78.4
0.4063
.2569
9 - 033 133
0.1107^
277
278
47.64 ?7
247.3
925.0
846.5
78.5
0.4077
.2542
8.900 n2
0.1124 17
278
279
48 - 41 78
248.3
924.3
845.7
78.6
0.4091
.2516
8.768 ^
0.1141};
279
280
49. 19 78
249.4
923.6
844.9
78.7
0.4104
1.2489
8 - 639 128
0.1158J;
280
281
49.98 7Q
250.4
922.9
844.2
78.7
0.4118
1.2463
8.5ll 19fi
0.1175 1Q
281
282
50.77
251.4
922.1
843.3
78.8
0.4132
.2436
8.385} 9 ?
0.1193}
282
283
51.588}
252.4
921.4
842.5
78.9
0.4146
.2409
8.261 121
0.1211J8
283
284
52.39 CQ
253.4
920.7
841.7
79.0
0.4160
.2383
8.140 11Q
0.1229 1Q
284
285
53.22;?
254.5
920.0
841.0
79.0
0.4173
.2356
8 - 021 iie
0.1247}
285
286
54 ' 06 86
255.5
919.2
840.1
79.1
0.4187
.2330
7.903}}
110
286
287
54.92 8fi
256.5
918.5
839.3
79.2
0.4201
.2304
7.788 1H
0.1284 1Q
287
288
55.78?
257.5
917.7
838.5
79.2
0.4215
.2277
0.1303}^
288
289
56 - 65 88
258.6
917.0
837.7
79.3
0.4228
1.2251
rllllll
0.1322} 9
289
290
57.53 fiQ
259.6
916.3
836.9
79.4
0.4242
1.2225
7.454 1Q7
0.1341 9n
290
291
58.428 9
260.6
915.5
836.0
79.5
0.4255
1.2199
0.1361;"
291
292
59.33 gi
261.6
914.8
835.3
79.5
0.4269
1.2173
7 - 242 103
0.1381^
292
293
60.24 Q7
262.7
914.1
834.5
79.6
0.4283
1.2147
7.l39 1ft9
0.1401 on
293
294
61.17
263.7
913.3
833.6
79.7
0.4297
1.2121
7 - 037 loo
0.1421;"
294
295
62. II 94
264.7
912.6
832.8
79.8
0.4310
1.2095
0.14412J
295
296
63.07 QR
265.7
911.8
832.0
79.8
0.4324
1.2070
6.839 Q7
0.1462 91
296
297
64.03
266.7
911.1
831.2
79.9
0.4337
1 . 2044
6.742 Q'
0.1483^}
297
298
65 -98
267.8
910.4
830.4
80.0
0.4351
1.2018
6.647 9 ^
0.1504^
298
299
65.98 inn
268.8
909.6
829.6
80.0
0.4364
1.1992
6.554 Q9
0.1526 91
299
300
66 - 98 ioi
269.8
908.9
828.8
80.1
0.4378
1.1967
6.462 Jf
0.1547 9 ;
300
301
67.99 1Q2
270.8
908.1
827.9
80.2
0.4391
1.1942
6.371 g 9
0.156923
301
302
69.01 1Q3
271.9
907.4
827.1
80.3
0.4405
1.1916
6.282 Q7
0.1592 99
302
303
70 - 04 05
272.9
906.6
826.3
80.3
0.4418
1.1891
6.195 J
0.1614^
303
304
71 no
71 - uy 106
273.9
905.9
825.5
80.4
0.4432
1.1865
6.109 85
0.163723
304
305
72.15 in7
274.9
905.1
824.7
80.4
0.4445
1.1840
6.024 QQ
0.1660 9 ,
305
306
73.22 "J
276.0
904.4
823.9
80.5
0.4458
1.1814
5.941
1683
306
307
74.3o}"j
277.0
903.6
823.0
80.6
0.4472
1.1788
5.859 J
o.noj 24
307
308
75.40 in
278.0
902.9
822.2
80.7
0.4485
1.1763
5.778 7Q
0.1731 9A
308
309
76.5lJ} 2
279.1
902.1
821.4
80.7
0.4499
1.1738
5.699 79
0.1755^
309
42
SATURATED STEAM TABLE I.
Temperature,
Degrees
Fahrenheit.
Pressure,
Pounds per
Square
Inch.
B
43. S*
w
5
c.
>.i
sj
1
r
'ytJM
Uj- c
p
|ll
Apu
0|
0*
II
c "*"
W
e
Entropy of
^h Vaporiza-
tion.
02
&
^1|
&
1
s
Temperature, 1
-* Degrees
Fahrenheit. |
310
77.63 n ,
280.1
901.3
820.5
80.8
0.4512
1.1713
5.622 7fi
0.1779 9 .
310
311
78 ' 76 115
281.1
900.5
819.7
80.8
0.4525
1.1688
5.546,12
0.1803 9 ^
311
312
79 - 91 U6
282.1
899.8
818.9
80.9
0.4538
1.1663
S.472 74
- 1827 25
312
313
81.07 11(
283.2
899.1
818.1
81.0
0.4552
1.1639
5.399 7Q
0.1852 9 ,
313
314
82.25}}
284.2
898.3
817.3
81.0
0.4565
1.1614
5. 326 '
0.1877^
314
315
83.44m
285.2
897.6
816.5
81.1
0.4578
1.1589
5.254
0.1903^
315
316
84.64
286.2
896.8
815.6
81.2
0.4592
1.1564
5.182 7Q
0.1929 97
316
317
85.86};*
287.3
896.0
814.8
81.2
0.4605
1.1539
5.112;
0.1956 97
317
318
S7.09}23
288.3
895.2
813.9
81.3
0.4618
1.1514
K 04-r 9
&>0455 69
0.19832 7
318
319
88.33 19fi
289.3
894.5
813.1
81.4
0.4631
1.1490
4.974 67
0.2010 9ft
319
320
89.59}^
290.4
893.7
812.3
81.4
0.4644
1.1465
4 - 907 fifi
0.2038 97
320
321
QQ Q7128
291.4
892.9
811.4
81.5
0.4658
1.1440
4 " 841 64
0.206528
321
322
92.16^0
292.4
892.2
810.6
81.6
0.4671
1.1416
4.777 fi ,
0.2093 9Q
322
323
93.46}^ 9
293.4
891.4
809.8
81.6
0.4684
1.1392
4 714i
0.2121 9
323
324
94 ' 78 134
294.5
890.6
808.9
81.7
0.4697
1.1367
i.653|J
0.2149^
324
325
96.12 10 .
295.5
889.8
808.1
81.7
0.4710
1.1343
4.594, 7
0.2177 97
325
326
97 46
296.5
889.0
807.2
81.8
0.4723
1.1318
4 ' 537 57
0.2204 9 '
326
327
98.S2HI
297.5
888.3
806.4
81.9
0.4736
1.1294
4 " 480 56
0.2232^
327
328
100.20 1QQ
298.6
887.5
805.6
81.9
0.4749
1.1269
4.424
0.2260 29
328
329
I01.58J2
299.6
886.7
804.7
82.0
0.4762
1.1245
4 -368^
. 22o9<jA
329
330
300.6
885.9
803.8
82.1
0.4775
1.1221
4.312^6
0.2319^
330
331
104. 40. .
301.7
885.1
803.0
82.1
0.4789
1.1197
4.257, fi
0.2349,!
331
332
105.84JS
302.7
884.3
802.1
82.2
0.4802
1.1173
4.20lf!
0.2380o 9
332
333
107.30}
303.7
883.5
801.3
82.2
0.4815
1.1149
4 ' 146 54
- 2412 32
333
334
I08.77 1/r
304.8
882.8
800.5
82.3
0.4828
1.1125
4.092,,
0.2444, 9
334
335
110. 25? 4 ;
305.8
882.0
799.6
82.4
0.4841
1.1101
4.038?!
0.2476?*
335
336
111.74} 49
306.8
881.2
798.8
82.4
0.4854
1.1077
3.98551
- 2509 33
336
337
113.26 1KQ
307.9
880.4
797.9
82.5
0.4867
1.1053
3.934^
0.2542, Q
337
338
114 79
308.9
879.6
797.1
82.5
0.4880
1.1029
3.883^
0.2575^
338
339
116 ' 34 157
309.9
878.8
796.2
82.6
0.4892
1.1006
000^"
0.2609^
339
340
117.91
310.9
878.0
795.3
82.7
0.4905
1.0982
3.784 47
0.2642,.
340
341
H9-50}^
312.0
877.2
794.5
82.7
0.4918
1.0958
S.737 4 '
0.2676o
341
342
1O1 1 A-"-V)l
121.10 161
313.0
876.4
793.6
82.8
0.4931
1.0934
3.691 4 ^
0^2709^
342
343
I22.7l 1ft ,
314.0
875.6
792.8
82.8
0.4944
1.0911
3.645 46
0.2743 Q ,
343
344
124.35JJJ;
315.1
874.8
791.9
82.9
0.4957
1.0887
3.599 4
0.2778^
344
345
316.1
874.0
791.0
83.0
0.4970
1.0864
3.554 44
0.2813^
06
345
346
I27.67 1fis
317.1
873.2
790.2
83.0
0.4982
1.0840
3.510.,
0.2849,,
346
347
129.35}?
318.2
872.4
789.3
83.1
0.4995
1.0817
3 467
0.2884^
347
348
131.06}
319.2
871.6
783.5
83.1
0.5008
1.0793
-S
0.2920X5
36
348
349
132.78 174
320.2
870.8
787.6
83.2
0.5021
1.0770
3.383 41
0.2956, fi
349
350
134.52} 7 ,
321.3
870.0
786.8
83.2
0.5034
1.0747
3.342 4 J
0.2992^
36
350
SATURATED STEAM TABLE I.
43
-5
1
i";
c.
is
Si
&J
"o ,
IP
| 3
*
3 2
tb
5*3
> i
*1
fcl
WS
wJg
Jf
4-
> d ^
^11
||1
r ~~~
!J!l
i
n
pi
pi
P
!>!
111!
i||
Bftl
H
p^
K
S
W
w
e
Q
H
*
'
9
r
'
Apu
e
r
f
s
1
s
t
351
136.27 177
322.3
869.2
785.9
83.3
0.5047
1.0724
3.302, Q
0.3028, 7
351
352
138.04}
323.3
868.3
785.0
83.3
0.5059
1.0700
3.263^
0.3065, 7
352
353
139.83} 79
324.4
867.5
784.1
83.4
0.5072
1.0677
, oox" y
' 3102 38
353
354
141.64 1R9
325.4
866.7
783.3
83.4
0.5085
1.0654
3.185, ft
0.3140, 8
354
355
143 ' 46 184
326.4
865:9
782.4
83.5
0.5097 1.0631
3.147 38
0.3178,Q
355
356
145.30 18?
327.5
865.1
781.5
83.6
0.5110
1.0608
3.109 38
' 3217 39
356
357
147.17 18 ,
328.5
864.3
780.7
83.6
0.5123
1.0585
3.071 00
0.3256 41
357
358
149 ' 05 191
329.5
863.5
779.8
83.7 0.51351.0562 3.033^
0.3297*}
358
359
150.96 193
330.6
862.6
778.9
83.7
0.5148
1.0539
2.996-
0.3338*J
359
360
152.89 1Q ,
331.6
861.8
778.1
83.7
0.5161
1.0516
2.960,,
0.3378 41
360
361
154 83
332.6
861.0
777.2
83.8
0.5173
1.0493
2.925^?
0.3419*}
361
362
156: 78 l98
333.7
860.2
776.3
83.9
0.5186
1.0470
2.890^
0.3460 42
362
363
158.76 200
334.7
859.3
775.4
83.9
0.5199
1.0448
2.856,,
0.3502,,
363
364
160 - 76 201
335.7
858.5
774.6
83.9
0.5211
1.0425 2.821^
0.3545*^
364
365
162.77 2Q4
336.8
857.7
773.7
84.0
0.5224
1.0403
2.787^
0.3688JJ
365
366
164.81 9n7
337.8
856.8
772.8
84.0
0.5236
1.0380
2.754,,
0.3631,,
366
367
166. 88 2 , 07
338.8
856.0
771.9
84.1
0.52491.0357
2.721X2
0.3675**
367
368
168.96 2 ? 8
339.9
855.2
771.0
84.2
0.5261
1.0335
2.689 32
0.3719**
44
368
369
171.06 911
340.9
854.4
770.2
84.2
0.5274
1.0312
2.657 Q1
0.3763,,
369
370
173 17
341.9
853.5
769.3
84.2
0.5286 1.0289
2.626^
0.3808*^
370
371
175!3l2J 4
343.0
852.7
768.4
84.3
0.5299
1.0267
2.596
0.3852**
371
372
177.47 918
344.0
851.8
767.5
84.3
0.5311
1.0245
2.566, Q
0.3897, fi
372
373
179. 65
345.0
851.0
766.6
84.4
0.5324
1.0222
2.536 9 "
0.3943*^
373
374
181 - 85 223
346.1
850.2
765.8
84.4
0.5336
1.0200
2.507 29
0.3989^
374
375
184.08 99
347.1
849.3
764.9
84.4
0.5349
1.0178
2.478 9ft
0.4035, 7
375
376
377
186.32;;*
188.60J5JJ
348.2
349.2
848.5
847.6
764.0
763.1
84.5
84.5
0.5361
0.5374
1.0156
1.0134
2 - 450 2S
2.422 28
0.4082*7
0.4129 47
376
377
378
190. 88,,,,
350.2
846.8
762.2
84.6
0.5386
1.0112
2.394 9a
0.4177,
378
379
193 19
351.3! 846.0
761.4
84.6
0.5398
1.0089
2.366 97
0.4226*Q
379
380
19 5 :52 233
352.3 845.1
760.5
84.6
0.5411
1.0066
2.339 2 y
0.4275 49
380
381
197.87
353.3
844.3
759.6
84.7
0.5423
1.0045
2.312 27
0.4325 K1
381
382
200.25 9 ^
354.4
843.4
758.7
84.7
0.5435' 1.0022
2.285 9
0.4376?^
382
383
202.64 24 j
355.4
842.5
757.7
84.8
0.5448
1.0000
2 ' 259 25
" 4426 50
383
384
205. 05 9 ,,
356.5
841.7
756.9
84.8
0.5460
0.9978
2.234 ,
0.4476,,
384
385
207.49;**
357.5; 840.8
756.0
84.8
0.547310.99571 2.209^
4527
385
386
209.96JJJ
358.5
840.0
755.1
84.9
0.5485
0.9935
2.184-
0:4579^2
386
387
388
212. 45 2
214.96;?]
359.6
360.6
839.1
838.3
754.2
753.3
84.9
85.0
0.5497
0.5509
0.9913
0.9891
2.160 94
2.136 9 *
0.4630, 9
0.4682?,
387
388
389
217 ' 50 255
361.7
837.4
752.4
85.0
0.5522
0.9869
2 - 112 24
0.4735^
389
390
220.05 25g
362.7
836.6
751.6
85.0
0.5534
0.9848
2.088 94
0.4789, R
390
391
363.7
835.7
750.6
85.1
0.5546J0.9826
2.064 24
- 4845 55
391
44
SATURATED STEAM TABLE I.
2 -1
2 03^3
1
0)
a
JJK
II-
1
"o
<J3
> 3 *
||
l
elS-
"SS
-S
t!
rfS^
&3
o. i
"*i5
111
^MJjj
If
3
-^.2*
+J .
o^
o^
ftw
o" Q e
lall
.tJ s2
H
I **
a
is
111
iJl
!*
H
OQ
gPnO
H
1
p
g
r
p
Apu
e
r
T
S
1
s
I
392
225. 2 97
364.8
834.8
749.7
85.1
0.5558
0.9804
2.041 99
0.490,
392
393
227.9;'
365.8
834.0
748.9
85.1
0.5571
0.9783
2.019??
0.495^
393
394
230.5*7
366.9
833.1
747.9
85.2
0.5583
0.9761
1.99722
0.501^
394
395
233. 2 97
367.9
832.2
747.0
85.2
0.5595
0.9740
1.975 99
0.506 ft
395
396
235. 9 9 '
368.9
831.4
746.2
85.2
0.5607
0.9718
1.953 22
0.512^
396
397
238 - 6 28
370.0
830.5
745.2
85.3
0.5619
0.9696
1.931 21
0.518^
397
398
241. 4 27
371.0
829.7
744.4
85.3
0.5632
0.9675
1.910 21
0.524,
398
399
244. i;'
372.0
828.8
743.5
85.3
0.5644
0.9654
1.889,}
0.529^
399
400
246.9 2
373.1
827.9
742.6
85.3
0.5656
0.9633
1.868 2 J
0.535g
400
401
249. 7 9Q
374.1
827.0
741.6
85.4
0.5668
0.9611
.847 91
0.541 7
401
402
252.6;*
375.2
826.1
740.7
85.4
0.5680
0.9589
.826^
0.548'
402
403
255.S 2 , 9
376.2
825.2
739.8
85.4
0.5692
0.9568
.806*!
0.554g
403
404
258. 4 2q
377.3
824.4
739.0
85.4
0.5704
0.9547
.786 9n
0.560 R
404
405
261. 3^
378.3
823.5
738.1
85.4
0.5716
0.9525
.766:"
0.566^
405
406
264 ' 3 30
379.4
822.6
737.1
85.5
0.5728
0.9504
747 9
0.572^
406
407
267.3, ft
380.4
821.7
736.2
85.5
0.5741
0.9483
1.728 1Q
0.579 fi
407
408
270.3^"
381.4
820.8
735.3
85.5
0.5753
0.9462
1.709Jg
0.585^
408
409
273.3^
382.5
820.0
734.5
85.5
0.5765
0.9441
1.691 lg
0.591J
409
410
276.30,
383.5
819.1
733.6
85.5
0.5777
0.9420
l.673 1fi
0.598 fi
410
411
279.4^!
384.6
818.2
732.7
85.5
0.5789
0.9399
1.655}
0.604 7
411
412
282.5 3 2-
385.6
817.3
731.7
85.6
0.5801
0.9378
1.637 lg
0.611^
412
413
285. 7 Q9
386.7
816.4
730.8
85.6
0.5813
0.9357
1.619 1S
0.618 7
413
414
288. 9,f
387.7
815.5
729.9
85.6
0.5825
0.9336
1 601
0.625'
414
415
292 -32
388.7
814.6
729.0
85.6
0.5837
0.9315
iimg
0.631^
415
416
295. 2
389.8
813.7
728.1
85.6
0.5849
0.9294
1.567 17
0.638 7
416
417
298. 5^
390.8
812.8
727.2
85.6
0.5861
0.9273
1.550} 7
0.645'
417
418
301.8^
391.9
811.9
726.3
85.6
0.5873
0.9253
1.533^
0.652'
o
418
419
305. lo.
392.9
811.0
725.4
85.6
0.5885
0.9232
1.516 17
0.660 7
419
420
808..5S
394.0
810.1
724.5
85.6
0.5896
0.9211
1.499}'
0.667'
420
421
Q1 1 Q""
911.834
395.0
809.2
723.6
85.6
0.5908
0.9191
1.483JJ
0.674^
421
422
315.2,.
396.1
808.3
722.7
85.6
0.5920
0.9170
l.467 1t .
0.682 7
422
423
318.6^
397.1
807.4
721.8
85.6
0.5932
0.9149
l':452,X
0.689 7
423
424
322. lf 5
398.2
806.5
720.9
85.6
0.5944
0.9128
M36j
0.696^
424
425
325. 6 q ,
399.2
805.6
720.0
85.6
0.5955
0.9108
1.421,,
0.704 7
425
426
329.1^
400.3
804.7
719.1
85.6
0.5967
0.9088
1 ' 406 15
0.711'
426
427
332 - 6 36
401.3
803.8
718.2
85.6
0.5979
0.9067
1.391 15
0.719 8
427
428
336.2
402.3
802.9
717.3
85.6
0.5991
0.9047
1.376
0.727
428
TABLE II.
SATURATED STEAM
ENGLISH DNITS.
jj
?
V
e.
H
ts .
*i
"o
i|S
y
sj
til
IB
"=1
Sj
SI
'g X^i
2*^
|
||=
iii!
rtl
|w
g3
So
S S"^
g C *83
3
g>'5
SfePU
{S<5
^x
PH
H
H
K
E"~ c
M"" c
H
W
QQ
Q
PH
P
f
i
r
p
Apu
e
r
8
1
P
f\
t
f f
sEi
8
'
1
101.84 9 JQ
69.8
1034.7
973.1
61.6
0.1329
1.8433
333. lif>nn
0.00300 97fi
1
2
126 15,co7
94.2
1021.9
957.8
64.1
0.1753
1.7432
173. i 1 SI:
0.00578 9fi7
2
3
ftu.ag5
109.6
1012.2
946.4
65.8
0.2011
1.6841
118.4 2 gQ
0.00845 2 g|
3
4
153.00 09A
121.0
1005.5
938.6
66.9
0.2200
1.6416
90.4 171
0.01106 9 . Q
4
5
162.26 7 ?
130.3
1000.0
932.1
67.9
0.2351
1 . 6084
73.3 [{I
0.01364 ;J
5
6
i ~n 07
138.1
995.5
926.8
68.7
0.2476
1.5812
61.9 g 3
0.01616 2 ^Q
6
7
176.84 An9
144.9
991.4
922.0
69.4
0.2583
1.5580
53 ' 6 63
0.01866 9 , n
7
8
182.86 Si
150.9
987.8
917.8
70.00.26781.5378
A7 Oft
0.02116 9 J"
8
9
188.27 94
156.4
984.5
914.0
70.5
0.2762
1.5198
42.36 39Q
0.02362 ^
9
10
11
12
193.21 ,
197.74 f\
201.95 ^
161.3
165.9
170.1
981.4
978.6
976.0
910.4
907.1
904.1
71.0
71.5
71.9
0.2838
0.2908
0.2972
1 . 5036
1.4889
1.4756
38.37, 9fi
35. II 32 ?
32.40 2 ^
0.02606 949
0.02848 5*5
0.03088 239
10
11
12
13
14
205.87 QAC
209.55 3
174.1
177.8
973.6
971.2
901.3
898.6
72.3
72.6
0.3032
0.3088
1.4632
1.4516
30.06 203
28.03^
0.03327 24Q
0.03567 9 *X
13
14
15
213.03 32 g
181.3
969.1
896.2
72.9
0.3140
1 . 4409
26 ' 28 154
0.03805 2 g
15
16
216.31 19
184.6
967.0
893.8
73.2
0.3189
1 . 4308
24.74 1QR
0.04042 ,
16
17
219.43 9Q7
187.8
965.0
891.5
73.5
0.3236
1.4213
23. 38 }J? 0.04277 ^
17
18
222.40 HI
190.8
963.1
889.3
73.8
0.3280
1.4123
22. ITffi 0.04511 i\l
111) ^oO
18
19
225.24 971
193.7
961.2
887.2
74.0
0.3322
1.4038
21.07 Jo. 04746 OQO
19
20
227.95 9 'f
196.4
959.4
885.1
74.3
0.3362
1.3957
20.09 l\
0.04978""
20
21
230.56 2 ^}
199.1
957.7
883.1
74.6
0.3401
1.3879
in in yi
iy.iy 82
0.0521 23
21
22
233.07 9 ,,
201.6
956.0
881.2
74.8
0.3438
1.3804
18.37 75
0.0544 24
22
23
235.50 9 , 9
204.1
954.4
879.4
75.0
0.3473
1.3733
1 7^,62 7
0.0568;*
23
24
237.82 ^
206.4
952.9
877.7
75.2
0.3507
1.3665
16.92
0.0591^
24
25
240.07 91Q
208.7
951.4
876.0
75.4
0.3539
1.3600
16.29 - Q
0.0614 9 ,
25
26
242.26 "9
210.9
949.9
874.4
75.5
0.3571
1.3536
15.70
0.0637;
26
27
244 ' 36 205
213.0
948.5
872.8
75.7
0.3601
1.3475
15.17 ^
0.0659^
27
28
246.41 9nn
215.1
947.1
871.2
75.9
0.3631
1.3417
14.67 .,
0.0682 9 ,
28
29
248.41 :"!;
217.2
945.8
869.7
76.1
0.3660
1.3360
14-19 H
0705 9 o
29
30
250.34 Jgj:
219.1
944.4
868.2
76.2
0.3687
1.3305
13.74 g
0.0728^
30
31
252.22 1ft ,
221.0
943.1
866.7
76.4
0.3714
1.3252
13.32 , Q
0.0751 99
31
32
254.05 }*
222.9
941.8
865.2
76.6
0.3740
1.3200
12.93 37
0.0773 23
32
45
4 6
SATURATED STEAM TABLE II.
I
<u ."
J-i o>
A
a
ij
*i
"3
o
~||
N
u-S
3 _J3
> C
'5 E**-^*
'3 jd
|
jj
r^
^H
|||g
~cj * c
III
w.2 1
1
w^l
r^O
*l
P
!}<
'S S *> o
'| C 3
*^2 <i^
c Jj-
1&
QJ fV CCt^
|CtM
o ^
fl? O
03 *C3
g"3
C "*^
->'
"PMcc
H
K
w
K~ G
X~ a
02
|
1
P
t
q
r
>
Apu
e
r
f
S
1
S
P
33
255.84 17 ,
224.7
940.6
863.8
76.8
0.3766
1.3149
12.56 .
0.0796 9 ,
33
34
257.59!'*
226.5
939.4
862.5
76.9
0.3791
1.3101
12.21
0.0819 9 ^
34
35
259.29$
228.2
938.2
861.2
77.0
0.3815
1.3054
11.88 gQ
0.0842J2
35
36
260.96 1fi9
229.9
937.1
859.9
77.2
0.3838
1.3007
11.58 9Q
0.0864 99
36
37
262.58}^
231.6
935.9
858.6
77.3
0.3861
1.2962
11.29
0.0886 99
37
38
264 ' 17 156
233.2
934.8
857.4
77.4
0.3883
1.2918
11.01 28
0.0908 22
38
39
265.73 1f . Q
234.8
933.7
856.2
77.5
0.3905
1.2875
10.75 9fi
0.0930 OQ
39
40
267.26}^
236.4
932.6
855.0
77.6
0.3927
1.2833
10.49 9
n no^^
40
41
268. 76 I*"
237.9
931.6
853.8
77.8
0.3948
1.2792
10.25 23
0'.0976 2 ^
41
42
270.23 1AQ
239.4
930.6
852.7
77.9
0.3968
1.2752
10.02 go
0.0998 99
42
43
271.66}!?
240.8
929.5
851.5
78.0
0.39.88
1.2713
9.801 9 ^ 9
0. 1020o
43
44
273. 07} 4 ]
242.3
928.5
850.4
78.1
0.4008
1.2675
9,589^
O.'l043 22
44
45
274.40,00
243.7
927.5
849.3
78.2
0.4027
1.2638
9.387 1Q9
0.1065 99
45
46
275.82}*
245.1
926.6
848.2
78.4
0.4046
1.2601
9.195}^
0.1087 9 ;
46
47
277.16}oi
246.4
925.6
847.2
78.4
0.4065
1.2565
9.012}?^
0.1109 99
47
131
174
w&
48
278.47
247.8
924.7
846.2
78.5
0.4083
1.2530
8 838! ftc
0.1131 99
48
49
279.76};;
249.1
923.8
845.1
78.7
0.4101
1.2496
8.670}"
o.iissf;
49
50
281.03} 9 '
250.4
922.8
844.1
78.7
0.4119
1.2462
8.507} 7
0.1176 99
50
125
157
22
51
282. 28, 9 ,
251.7
921.9
843.1
78.8
0.4136
1.2428
8.350^2
0.1198 22
51
52
283 - 52 122
253.0
921.0
842.1
78.9
0.4153
1.2395
8. 198}?f
- 1220 22
52
53
284.74 11Q
254.2
920.1
841.1
79.0
0.4170
1.2363
8.052 HO
- 1242 22
53
54
285.93 11fi
255.4
919.3
840.2
79.1
0.4186
1.2332
7.912.0,
0.1264 99
54
55
287.09}}
256.6
918.4
839.2
79.2
0.4202
1.2302
7-.778.JJ:
0.1286 9 ;
55
56
288.25}}
257.8
917.6
838.3
79.3
0.4218
1.2271
7 ' 647 128
0.1308^
56
57
289.40 t1 o
259.0
916.7
837.4
79.3
0.4233
1.2241
7.519 199
0.1330 99
57
58
290.53}}?
260.1
915.9
836.5
79.4
0.4249
1.2211
7. 397
0.1352 99
58
59
291 - 64 no
261.3
915.1
835.6
79.5
0.4264
1.2182
7.280 n4
0.1374^
59
60
292.74 g
262.4
914.3
834.7
79.6
0.4279
1.2154
7.166 m
0.1395 99
60
61
293.82}[j
263.5
913.5
833.8
79.7
0.4294
1.2126
7 - 055 106
- 1417 22
61
62
294.88 1Q5
264.6
912.7
832.9
79.8
0.4308
1.2099
6.949 1Q3
0.1439^
62
63
295.93 1Q4
265.7
911.9
832.1
79.8
0.4323
1.2072
6.846 1Q1
0.1461 22
63
64
296 ' 97 03
266.7
911.1
831.2
79.9
0.4337
1.2045
A 7 /I d
0. 1483^
64
65
298.00}62
267.8
910.4
830.4
80.0
0.4351
1.2018
6:647 95
0.1504*2
65
66
299.02 inn
268.8
909.6
829.6
80.0
0.4365
1.1992
6.552 Q9
0.1526 99
66
67
300.02 QQ
269.8
908.9
828.8
80.1
0.4378
1.1966
6.460 ^
0.1548 9 ;
67
68
301.01 jjg
270.9
908.1
827.9
80.2
0.4391
1.1942
6.370 9 ?
0.1570^
68
69
301.99 Q7
271.9
907.4
827.1
80.3
0.4405
1.1917
6.283 R
0.1592 9 '
69
70
302.96 fti
272.9
906.6
826.3
80.3
0.4418
1.1892
6.199 " 9
o.ieis;;
70
71
303.91 11
273.8
905.9
825.5
80.4
0.4430
1.1867
6.117 82
0.1635^
71
72
304.86 Q ~
274.8
905.2
824.8
80.4
0.4443
1.1843
6.036 7R
0.1657 91
72
73
305.79 93275.8
904.5
824.0
80.5
0.4456
1.1819
5.958 ^
0.1678^
73
UNIVERSITY
F
SATURATED STEAM TABLE II.
47
M
-5
0)
3
c.
S
4
fh
"833
"3 ,
in
N
|1
3 m jj
"trf & S
i 1 h z
M
^
tjj
tt
O o>
4a
> 3
fa
fef.2
.ti 3J2
^
PI
T? y
- f.
a
g3
il
g|-3
1^1
1
!>-j
life ft
g O 3
f. = r
gfiHOQ
EH
S
n
E c
K- c
m
GO
Q
P
t
q
r
p
Apu
e
r
T
3
1
s
p
74
306.72 Q9
276.7
903.8
823.2
80.6
0.4468
1.1795
5.882 7 ,
0.1700 22
74
75
307.64^
277.7
903.1
822.4
80.7
0.4480
1.1772
5 807
0.1722 99
75
76
308.54 9
278.6
902.4
821.7
80.7
0/4492
1.1750
5:735*3
0.1744^
76
77
309.44 8g
279.5
901.8
821.0
80.8
0.4504
1.1727
5.665 6g
0.1765 99
77
78
310.33
280.4
901.1
820.3
80.8
0.4516
1.1705
e KQ7o
0.1787 9 f
78
79
ui:ii
281.3
900.4
819.6
80.8
0.4528
1.1683
S^SO^
0.1808^}
7ff
80
312.08 Sfi
282.2
899.8
818.9
80.9
0.4540
1.1661
5.466 fi ,
0.1829 22
80
81
312.94
283.1
899.1
818.1
81.0
0.4551
1.1640
5.403X7
81
82
313.79 g4
283.9
898.5
817.4
81.1
0.4562
1.1619
5.342*}
; 1872^
82
83
314.63 fi ,
284.8
897.8
816.7
81.1
0.4573
.1598
5.281 61
0.1894 99
83
84
315.47,
285.7
897.2
816.1
81.1
0.4584
.1577
5.220^1
o.i9ie;;
84
85
316.30J2
286.5
896.6
815.4
81.2
0.4595
.1557
5.161$
0.193821
85
86
317.12 R1
287.4
895.9
814.7
81.2
0.4606
.1536
5-104 g
0.1959 99
86
87
317.93*
288.2
895.3
814.0
81.3
0.4617
.1516
5.048^
0.1981 99
87
88
318773*
289.0
894.7
813.3
81.4
0.4628
.1496
4-993^
0.2003^2
88
89
90
319.53-q
320.32^
289.9
290.7
894.1
893.5
812.7
812.1
4H-
0.4638
0.4649
1.1477
1.1457
4.939,,
4.886;??
0.2025 99
0.2047 9 f
89
90
91
321.10}!
291.5
892.9
811.4
81.5
0.4659
1.1438
*' 835 50
0.206822
91
92
321.88 77
292.3
892.3
810.7
81.6
0.4669
1.1419
4.785, Q
0.2090 90
92
93
322.65''
293.1
891.7
810.1
81.6
0.4679
1.1400
4.736*^
0.2112?;
93
94
323.41
293.9
891.1
809.5
81.6
0.4689
1.1382
4.6S9* 7
0.2133^
94
95
324. 16 7 ,
294.6
890.5
808.8
81.7
0.4699
1.1363
4,644
0.2153 91
95
96
324. 91 7 ?
295.4
889.9
808.2
81.7
0.4709
1.1345
4.599*j
0.2174;}
96
97
325.66^
296.2
889.3
807.5
81.8
0.4719
1.1327
4.556^
0.2195^
97
98
326. 40 7 ,
296.9
888.7
806.9
81.8
0.4729
1 . 1309
4.514,.
0.2215 91
98
99
327.13',
297.7
888.2
806.3
81.9
0.4738
1.1291
4.473*
0.2236;*
99
100
327.8672
298.5
887.6
805.7
81.9
0.4748
1.1273
4.432*}
0.225621
100
101
328.58 79
299.2
887.0
805.1
81.9
0.4757
1.1255
4.391 4Q
0.2277 91
101
102
329. 30 7 T
299.9
886.5
804.5
82.0
0.4766
1.1238
4.351*
0.2298 9 i
102
103
330.017J
300.6
885.9
803.8
82.1
0.4776
1.1221
4.311*
0.2320^1
103
104
330.72 7f)
301.4
885.3
803.2
82.1
0.4785
1.1204
4.272, 9
0.2341 21
104
105
331.42^"
302.1
884.8
802.7
82.1
0.4794 1.1187
4.233,^
2362
105
106
332.11gg
302.8
884.3
802.1
82.2
0.4803
1.1170
*' 195 38
0. 2384^
106
107
332.79 fiQ
303.5
883.7
801.5
82.2
0.4812
.1154
4.157, 7
0.2406 91
107
108
333.48
304.2
883.2
800.9
82.3
0.4821
.1137
4.120^;
0.2427;i
108
109
334. 16g
304.9
882.6
800.3
82.3
0.4830
.1121
4.083 37
0.2449^2
109
110
334.83 ft7
305.6
882.1
799.7
82.4
0.4838
.1105
4.047, R
0.2471 99
110
111
335.50'
306.3
881.6
799 .*2
82.4
0.4847
.1089
4.011 3 ^
0.2493;;
111
112
336 ' 17 66
307.0
881.0
798.6
82.4
0.4856
.1073
3 - 976 33
0.2515^
112
113
336.83-,
307.7
880.5
798.0
82.5
0.4864
1.1057
3.943,,
0.2536 99
113
114
337 -* 8 66
308.3
880.0
797.5
82.5
0.4873
1.1041
3.909 3 *
0.2558^
114
48
SATURATED STEAM TABLE II.
Pressure,
ti Pounds per
Square Inch.
Temperature,
Degrees
Fahrenheit.
fl}
s
S2
*s
^
Q
Ij
s'-s
fl
r
is.
m
pi
p
?l .
9
i
Apu
^S
'^
ll
H
8
*
ft
W
r
T
n i .
mi
*3fcOH
OJ
s
Density,
1 M Pounds per
Cubic Foot.
t--^
SI
111
m 3 g
m o a 1
P4C
p
115
338.14 fi ,
309 .t)
879.5
797.0
82.5
0.4881
1.1026
3.876oo
0.2580 91
115
116
338.78^
309.7
879.0
796.4
82.6
0.4890
1.1011
3.844**
0.26015*
116
117
339. 42g*
310.3
878.5
795.9
82.6
0.4898
1.0996
3.812 32
0.262321
117
118
340.06 A o
311.0
878.0
795.3
82.7
0.4906
1.0981
3.781 9q
0.2644 91
118
119
340.69^
311.7
877.4
794.7
82.7
0.4914
1.0966
3.752^
0.2665 9 |
119
120
341 ' 31 63
312.3
876.9
794.2
82.7
0.4922
1.0951
3.723^
0.26862}
120
121
341.94 fi9
312.9
876.4
793.6
82.8
0.4930
1.0936
3.694 2g
0.2707 22
121
122
342.56^ 9
313.6
875.9
793.1
82.8
0.4938
1.0921
3.665 9 *
0.2729;:
122
123
343. 18<; 2
314.2
875.4
792.6
82.8
0.4946
1.0907
3.637'f
0.2750^}
123
124
343.79 fin
314.8
875.0
792.1
82.9
0.4954
1.0892
3.609 9R
0.2771 99
124
125
344.39V
315.5
874.5
791.6
82.9
0.4962
1.0878
3.581*
0.2793;:
125
126
345.00^
316.1
874.0
791.0
83.0
0.4970
1.0864
3.554*}
0.2814*}
126
127
345.60 fin
316.7
873.5
790.5
83.0
0.4977
1.0850
3.527 9fi
0.2835 91
127
128
346.20^"
317.3
873.0
790.0
83.0
0.4985
1.0836
3.501^
0.2856 9 !
128
129
346 ' 79 59
317.9
872.6
789.5
83.1
0.4993
1.0822
3 - 476 25
0.2877^}
129
130
347.38, fi
318.6
872.1
789.0
83.1
0.5000
1.0808
3.451 24
0.2898 90
130
131
347.96^
319.2
871.6
788.5
83.1
0.5008
1.0794
3 - 427 25
o.29is;y
131
132
348.55^
319.8
871.1
788.0
83 ..1
0.5015
1.0780
3.402^
0.29392}
132
133
349.13, 7
320.4
870.7
787.5
83.2
0.5023
1.0767
3.378 24
0.2960 91
133
134
349.70^'
320.9
870.2
787.0
83.2
0.5030
1.0754
3.354^
0.2981 9 !
134
135
350.27^
321.5
869.8
786.5
83.3
0.5037
1.0741
3.33l|
0.3002^}
135
136
350.84, 7
322.1
869.3
786.0
83.3
0.5044
1.0728
3.308 99
0.3023 9n
136
137
351. 4lJ'
322.7
868.8
785.5
83.3
0.5052
1.0714
3 - 286 22
0.3043 9 "
137
138
OKI QQ'
51.98 5 g
323.3
868.3
785.0
83.3
0.5059
1.0701
3 - 264 22
0.3064*}
138
139
352.54,,
323.9
867.9
784.5
83.4
0.5066
1.0688
3.242 99
0.3085 91
139
140
353.09^
324.4
867.4
784.0
83.4
0.5073
1.0675
3.220 9 f
0.3106 9 ;>
140
141
353.65^
325.0
867.0
783.6
83.4
0.5080
1.0662
3.19922
0.31262"
141
142
354.20,,
325.6
866.5
783.1
83.4
0.5087
1.0649
3.177 2 i
0.3147 21
142
143
354.75^
326.2
866.1
782.6
83.5
0.5094
1.0637
3.156^
0.3168 9 !
143
144
355.29^
326.7
865.6
782.1
83.5
0.5101
1.0624
3.13621
0.31892}
144
145
355.83,,
327.3
865.2
781.6
83.6
0.5108
1.0612
3.115 Q
0.3210 91
145
146
356.37^
327.8
864.8
781.2
83.6
0.5115
1.0599
3.095;"
0.323i;i
146
147
356 ' 91 53
328.4
864.3
780.7
83.6
0.5122
1.0587
3.074 2 J
0.325321
147
148
357.44,,
328.9
863.9
780.3
83.6
0.5128
1.0575
3.054 20
0.3274 22
148
149
357. 97^
329.5
863.5
779.8
83.7
0.5135
1.0563
3.034;"
0.3296 99
149
150
358.50g2
330.0
863.0
779.3
83.7
0.5142
1.0551
3-()H 2 <>
0.3318'j
150
151
359.02, 9
330.6
862.6
778.9
83.7
0.5148
1.0539
2.995 lg
0.3339 9n
151
152
359.54^ 9
331.1
862.2
778.5
83.7
0.5155
1.0527
2.977}
0.3359 9 i
152
153
360.06^1
331.6
861.8
778.1
83.7
0.5162
1.0515
2.958J9
0.3380 2 }
153
154
360.57, 9
332.2
861.3
777.6
83.7
0.5168
1.0503
2.940 lg
0.3401 91
154
155
361.09^
332.7
860.9
777.1
83.8
0.5175
1.0491
2.922J8
0.3422JJ
155
SATURATED STEAM TABLE II.
49
M
|
1
i.
|L
ia|
3-j
*o
til
M
.|
sll
13 1
>i
o'|
5
o 1
&
4=
> a 4
.i||
ni
l&s
|2
gl
|i
pi
ill
II
ra~
ill
fill
in
r-4
H
K
H
n
E
W
w
QQ
w
^
P
1
9
r
p
Apu
e
r
T
3
8
p
156
361.60,,
333.2
860.5
776.6
83.9
0.5181
1.0479
2.904, e
0.3444 91
156
157
362.11*}
333.8
860.1
776.2
83.9
0.5187 1.0468
2. 886}?
0.3465 9 }
157
158
362.62 5Q
334.3
859.6
775.7
83.9
0.5194
1.0456
2.869}}
0.34863}
158
159
363.12, n
334.8
859.2
775.3
83.9
0.5200
1.0445
2.852, Q
0.3507 91
159
160
161
363.62)?"
364.12
335.3
335.9
858.8
858.4
774.9
774.5
83.9
83.9
0.5206
0.5213
1.0434
1.0422
2.834}?
2.817} 7
0.3528 9 i
0.3550^
160
161
162
364.62, Q
336.4
858.0
774.0
84.0
0.5219
1.0411
2.800 17
0.3571 99
162
163
365.11*Q
336.9
857.6
773.6
84.0
0.5225
1.0400
2.783"
0.3593 9 f
163
164
365.60*5
337.4
857.2
773.2
84.0
0.5231
1.0389
2.767}*
0.3614^}
164
165
366.09, Q
337.9
856.8
.772.8
84.0
0.5237
.0378
2.751 lfi
0.3635 91
165
166
366.58*g
338.4
856.4
772.3
84.1
0.5244
.0367
2.735}
0.3656 9 }
166
167
367.06*g
338.9
856.0
771.9
84.1
0.5250
.0356
0.36772}
167
168
367. 54, 8
339.4
855.6
771.4
84.2
0.5256
.0345
2.704, fi
0.3698 99
168
169
368.02*g
339.9
855.2
771.0
84.2
0.5262
.0335
2.688}
0.3720 9 f
169
170
368.50JJ
340.4
854.8
770.6
84.2
0.5268
.0324
2.673};!
0.3741^}
170
171
368. 97, Q
340.9
854.4
770.2
84.2
0.5273
.0313
2.658,,
0.3762 99
171
172
369.45*
341.4
854.0
769.8
84.2
0.5279
.0302
2.643 e
0.3784;f
172
173
369.92*}
341.8
853.6
769.4
84.2
0.5285
1.0291
2.628 H
O.SSOSg}
173
174
370. 39, 7
342.3
853.2
769.0
84.2
0.5291
1.0280
2.614,,
0.3826 9n
174
175
370.86*'
342.8
852.8
768.5
84.3
0.5297
.0270
2.600}*
0.3846 9 "
175
176
371.32*
343.3
852.4
768.1
84.3
0.5303
.0260
2.586}*
0.3867^
176
177
371.78.-
343.8
852.0
767.7
84.3
0.5309
.0250
2.573,,
0.3887 91
177
178
372.24*
344.2
851.6
767.3
84.3
0.5314
.0239
2.559}*
0.3908 9 }
178
179
372.70*
344.7
851.3
766.9
84.4
0.5320
.0229
0.392922
179
180
373.16.,
345.2
850.9
766.5
84.4
0.5326
.0219
2.531,,
0.3951 91
180
181
373.61*?
345.7
850.5
766.1
84.4
0.5331
.0209
2.518}:?
0.3972^
181
182
374.07*
346.2
850.1
765.7
84.4
0.5337
.0199
2.505}!]
0.399221
182
183
374.52..
346.6
849.7
765.3
84.4
0.5343
.0189
2.492,,
0.4013 2 ,
183
184
374.96**
347.1
849.4
764.9
84.5
0.5348
.0179
2.479 19
0.4034;;,
184
185
375.41*;!
347.5
849.0
764.5
84.5
0.5354
.0169
2.467J2
0.405421
185
186
375.86.,
348.0
848.6
764.1
84.5
0.5359
1.0159
2.454, 9
0.4075 20
186
187
376.30,*
348.5
848.2
763.7
84.5
0.5365
1.0149
2.442};
0.4095S
187
188
376.74**
348.9
847.8
763.3
84.5
0.5370
1.0140
2.429}*
0.41162}
188
189
377.. 18,,
349.4
847.5
763.0
84.5
0.5376
.0130
2.417 2
0.4137 91
189
190
377.61*;?
349.8
847.1
762.6
84.5
0.5381
.0121
2.405};
0.4158 9 }
190
191
378.05*^
350.3
846.8
762.2
84.6
0.5387
.0111
2.393J2
- 4179 22
191
192
378.49.,
350.7
846.4
761.8
84.6
0.5392
.0101
2.380 19
0.4201 91
192
193
378.92*,
351.2
846.0
761.4
84.6
0.5397
.0091
2.368{i
0.4222 9 }
193
194
379.35*:?
^C
351.6
845.7
761.1
84.6
0.5403
.0081
2.357 12
0.4243^}
194
195
379. 78, 9
352.1
845.3
760.7
84.6
0.5408
.0071
2.345 1t
0.4264 9 ,
195
196
380.20*'
352.5
844.9
760.3
84.6
0.5413
.0062
2.334}^
0.42852}
196
SATURATED STEAM TABLE II.
11
1 3
1.
s .
iJ
"o-;
"e
Lt
||a
W
KJ
ill
111
=1
2 1
*|
|r|
= ^;
'3
g7
3
Hi
fill
DDfo
*M O D
111
SpkOQ
Q&<
$3
i
ii"*
III
"c **
%>*
<U 3tt,Pt
gfPjO 1
H
w
w
R~~
W
W
0,
Q
p
t
Q.
r
p
Apu
8
r
T
s
1
s
197
380. 63, 9
353.0
844.6
759.9
84.7
0.5418
1.0053
2.322
0.4306 91
197
198
381.05
353.4
844.2
759.5
84.7
0.5424
1.0044
2Q 1 1
. Ol 1 i 9
- 4327 22
198
199
381.47
353.8
843.9
759.2
84.7
0.5429
1.0034
2.299J 2
0.4349 22
199
200
381. 89, 9
354.3
843.5
758.8
84.7
0.5434
1.0025
2.288 n
0.4371 91
200
201
382.31* 9
354.7
843.1
758.4
84.7
0.5439
1.0015
2.277J!
0.4392 9 !
201
202
382.73*2
355.1
842.8
758.0
84.8
0.5444
1.0006
2.266JJ
0.4413^}
202
203
383.15,,
355.6
842.4
757.6
84.8
0.5450
0.9997
2.255 1Q
0.4434
203
204
383.56* 9
356.0
842.1
757.3
84.8
0.5455
0.9988
2.245
0.4454;"
204
205
383. 98* j
356.4
841.7
756.9
84.8
0.5460
0.9979
2.235J"
0. 4475g }
205
206
384.39,1
356.9
841.3
756.5
84.8
0.5465
0.9970
2.224
0.4496 91
206
207
384.80*!
357.3
841.0
756.2
84.8
0.5470
0.9961
2.214
- 4517 20
207
208
385.21*J
357.7
840.7
755.8
84.9
0.5475
0.9952
2.204|
0.4537 2
208
209
385.61,.
358.1
840.3
755.4
84.9
0.5480
0.9944
2.194
0.4558 91
209
210
386.02*,!.
358.6
840.0
755.1
84.9
0.5485
0.9935
2 ' 184 10
0.4579;!
210
211
386.42*
359.0
839.6
754.7
84.9
0.5490
0.9926
2.174 1Q
0. 4600^ 1
211
212
386.82,
359.4
839.3
754.4
84.9
0.5495
0.9917
2.164
0.4621 90
212
213
387.22*"
359.8
839.0
754.1
84.9
0.5500
0.9908
2.155*
0. 4641 9 V
213
214
387.62*|J
360.2
838.6
753.7
84.9
0.5505
0.9899
2.145^
0.4662^J
214
215
388.02, Q
360.6
838.3
753.3
85.0
0.5510
0.9891
2.136 1Q
0.4682 91
215
216
388.41$
361.0
837.9
752.9
85.0
0.5514
0.9882
2.126!
0.4703 9 !
216
217
388. 80 Jjj
361.4
837.6
752.6
85.0
0.5519
0.9873
2 ' 117 10
- 4724 22
217
218
389.20, Q
361.9
837.2
752.2
85.0
0.5524
0.9865
2.107 Q
0.4746 91
218
219
389.59$
362.3
836.9
751.9
85.0
0.5529
0.9857
2.098"
0.4767;;
219
220
389.98 3g
362.7
836.6
751.6
85.0
0.5534
0.9848
2.088^
0.4789^
220
221
390.37, Q
363.1
836.2
751.2
85.0
0.5538
0.9840
2.079 Q
0.4810 91
221
222
390.76,e
363.5
835.9
750.8
85.1
0.5543
0.9831
2.070 Q
0.4831 9 !
222
223
391 " 14 39
363.9
835.6
750.5
85.1
0.5548
0.9823
2.061 J
0.4852^
223
224
391.53, a
364.3
835.2
750.1
85.1
0.5553
0.9814
2.052 Q
0.4873 91
224
225
391.91gg
364.7
834.9
749.8
85.1
0.5557
0.9806
2.043 I
0.4894;. 1 .
225
226
392.29 3g
365.1
834.6
749.5
85.1
0.5562
0.9798
2.035 Q
y
0.4914^
226
227
392.67,.
365.5
834.3
749.2
85.1
0.5566
0.9790
2.026 Q
0.4935 91
227
228
393.04,'
365.9
833.9
748.8
85.1
0.5571
0.9782
2.018 *
0.4956^
228
229
393.42 3 g
366.2
833.6
748.5
85.1
0.5576
0.9774
2.010 g
0.4976^
229
230
393.80, fi
366.6
833.3
748.1
85.2
0.5580
0.9765
2.001 R
0.4997 9
230
231
394.18^
367.0
832.9
747.7
85.2
0.5585
0.9757
1.993 Q
0.502 9
231
232
394.56, 7
6i
367.4
832.6
747.4
85.2
0.5590
0.9749
1.985
0.504 ^
232
233
394.93, 7
367.8
832.3
747.1
85.2
0.5594
0.9741
1.977 Q
0.506 9
233
234
395.30^;
368.2
832.0
746.8
85.2
0.5598
0.9733
1.968 ^
0.508 9
234
235
395.67^
61
368.6
831.7
746.5
85.2
0.5603
0.9725
1.960
0.510 ^
235
236
396.04, 7
369.0
831.3
746.1
85.2
0.5608
0.9717
1.952 R
0.512 9
236
237
396.41^
369.4
831.0
745.8
85.2
0.5612
0.9709
1.944 *
0.514 3
237
SATURATED STEAM TABLE II.
tl
'S
2
k-.
IL
&i
*'
*
m
ii
Si
S-l
>
"5 ^
9
i
u
c;
lit
111
ill
"o's
a"
i 3
i\
I'i
iii
ill
E
t!
fill
til
gp^o
ill
III
HH
K
H
w- c
n
W **
w
02
Q
p
t
Q
r
'
Apu
e
r
T
S
1
8
P
238
396.78
369.7
830.7
745.4
85.3
0.5617
0.9701
.936 a
0.517 9
238
239
397.14
370.1
830.4
745.1
85.3
0.5621
0.9693
.928 7
0.519;
239
240
397.50
370.5
830.1
744.8
85.3
0.5625
0.9686
.921'
0.521^
240
241
397.86
370.9
829.8
744.5
85.3
0.5630
0.9678
.913 C
0.523
241
242
398.22
371.2
829.5
744.2
85.3
0.5634
0.9670
.905?
0.525;
242
243
398.59^
371.6
829.1
743.8
85.3
0.5639
0.9663
.898?
0.527^
243
244
398.96
372.0
828.8
743.5
85.3
0.5643
0.9655
.890 a
0.529 9
244
245
399.32
372.4
828.5
743.2
85.3
0.5648
0.9647
.882 7
0.531;
245
246
399.68
36
372.8
828.2
742.9
85.3
0.5652
0.9640
.875 8 7
0.533g
246
247
400.04,,
373.1
827.8
742.5
85.3
0.5656
0.9632
.867-
0.536 9
247
248
400.39
373.5
827.5
742.2
85.3
0.5661
0.9624
.860'
0.538 9
248
249
400.75
373.9
827.2
741.8
85.4
0.5665
0.9617
.852*
0.5402
249
250
401.10,,
374.2
826.9
741.5
85.4
0.5669'0.9609
.845-
0.542 9
250
251
401.45
374.6
826.6
741.2 85.4
0.56730.9601
.838'
0.544^
251
252
401 ' 79 35
375.0
826.3
740.9
85.4
0.5678
0.9594
.830
252
253
402.14,.
375.3
826.0
740.6
85.4
0.5682
0.9586
.823-
0.549 9
253
254
402.48,*
375.7
825.7
740.3 85.4
0.5686 ! 0.9579
.816-
0.5512
254
255
402.83g4
376.0
825.4
740.0
85.4
0.5690
0.9572
.809?
255
256
403.17,,.
376.4
825.1
739.7
85.4
0.5694
0.9564
.803-
0.555 9
256
257
403.52
376.8
824.8
739.4 85.4
0.5699
0.9557
.796 7
0.557 9
257
258
403 " 86 35
377.1
824.5
739.1
85.4
0.5703
0.9550
.789^
0.5592
258
259
404.21,,
377.5
824.2
738.8
85.4
0.5707
0.9542
1.782.
0.561 9
259
260
404. 55*!
377.8
823.9
738.5
85.4
0.5711
0.9535
1.775-
0.563,
260
261
404.89^
378.2
823.6
738.2
85.4
0.5715
0.9527
1.768 7
0.5662
261
262
405.23,,
378.5
823.3
737.9
85.4
0.5719
0.9520
1.762-
0.568 9
262
263
405.57,,
378.9
823.0
737.5
85.5
0.5723
0.9513
1.755'
0.570 9
263
264
405.90^
379.2
822.7
737.2
85.5
0.5727
0.9506
1.749^
0.572^
264
265
406.23,,
379.6
822.4
736.9
85.5
0.5731
0.9499
1.743-
0.574 9
265
266
406.57,,
379.9
822.1
736.6
85.5
0.5735
0.9492
1.736'
0.576 9
266
267
406.90
380.3
821.8
736.3
85.5
0.5739
0.9485
1.730^
0.5783
267
268
407.23,,
380.6
821.5
736.0
85.5
0.5743
0.9478
1 . 724-
0.580 2
268
269
407.57^
381.0
821.2
735.7
85.5
0.5747
0.9471
1.717J
0.582;
269
270
407.9033
381.3
820.9
735.4
85.5
0.5751
0.9464
1.711 6
0.5843
270
271
408.23,,
381.7
820.6
735.1
85.5
0.5755
0.9457
1 . 705 A
0.587 9
271
272
408.57,,
382.0
820.3
734.8
85.5
0.57590.9450
1.699^
0.589 9
272
273
408.90^
382.4
820.1
734.6
85.5
0.5763
0.9443
l.Wj
0.591^
273
274
409. 23.
382.7
819.8
734.3
85.5
0.5767
0.9436
1.687 R
0.593
274
275 409.57?*
383.1
819.5
734.0
85.5
0.5771
0.9429
1.68H
0.595;
275
276
409.90
383.4
819.2
733.7
85.5
0.5775
0.9422
i.ml
0.597^
276
277
410.23, 9
383.8
818.9
733.4
85.5
0.5779
0.9415
1 . 669 A
0.599 9
277
278
410.5532 384.1
818.6
733.1
85.5
0.5783
0.9408
1.663^
0.6012
278
SATURATED STEAM TABLE II.
If
s i
Sri
1
j>d
|L
Pi
'3
.2*
"8
t
iP
|
||
I'll
a||
+,&
Jl
^1-
-^ C -i
Pi
liil
|||
H
1^
go
W
|Jc
sS""
"c "- 1
W
jpfePH
&
|^c
*
t
Q
r
>
Apu
9
r
T
S
1
s
P
279
410.87, 9
384.4
818.3
732.8
85.5
0.5787
0.9402
1.657,
0.603 9
279
280
411.19*,
384.8
818.0
732.5
85.5
0.5791
0.9395
1.652
0.605,
280
281
411.5233
385.1
817.7
732.1
85.6
0.5795
0.9388
6
0.608^
281
282
411.84, 9
385.4
817.4
731.8
85.6
0.5799
0.9381
1.640 ft
0.610
282
283
412.16*f
385.8
817.2
731.6
85.6
0.5803
0.9375
1.634?
0.612^
283
284
412.47JJ}
386.1
816.9
731.3
85.6
0.5806
0.9368
1.629g
0.614^
284
285
412.78,,
386.4
816.6
731.0
85.6
0.5810
0.9362
1.623,
0.616 9
285
286
413.09*i
386.7
816.3
730.7
85.6
0.5814
0.9355
1/617*
O.eiSg
286
287
413.4132
387.1
816.0
730.4
85.6
0.5818
0.9348
1.612*
0.620 3
287
288
413.72 Q1
387.4
815.8
730.2
85.6
0.5821
0.9342
1.606 ft
0.623 9
288
289
414.03**
387.7
815.5
729.9
85.6
0.5825
0.9335
1.600
0.625 9
289
290
414.35*2
388.1
815.2
729.6
85.6
0.5829
0.9329
1.595 6
0.627^
290
291
414.68, 9
388.4
814.9
729.3
85.6
0.5833
0.9322
1.589,
0.629 9
291
292
415.00*f
388.7
814.6
729.0
85.6
0.5837
0.9315
1.584?
0.631 9
292
293
415.31*1
389.1
814.3
728.7
85.6
0.5840
0.9308
1.579JJ
0.633^
293
294
415.63 Q1
389.4
814.1
728.5
85.6
0.5844
0.9302
1.573,
0.636 9
294
295
415.94**
389.7
813.8
728.2
85.6
0.5848
0.9295
1.568?
0.638 9
295
296
416.24^
390.0
813.5
727.9
85.6
0.5852
0.9289
1.563?
o
0.640^
296
297
416.55
390.4
813.2
727.6
85.6
0.5855
0.9282
1.558,
0.642 9
297
298
416.85*"
390.7
813.0
727.4
85.6
0.5859
0.9276
1.553*
0.644;
298
299
417.1530
391.0
812.7
727.1
85.6
0.5862
0.9270
1.5476
0.646^
299
300
417.45^
391.3
812.4
726.8
85.6
0.5866
0.9264
1.542,
0.649 9
300
301
417.76**
391.6
812.1
726.5
85.6
0.5870
0.9258
1.537?
0.651 9
301
302
418.06*"
391.9
811.9
726.3
85.6
0.5873
0.9252
1.532?
0.653^
302
303
418.36 Q1
392.3
811.6
726.0
85.6
0.5877
0.9245
1.527,
0.655 9
303
304
418.67**
392.6
811.3
725.7
85.6
0.5881
0.9239
1.522*
0.657 9
304
305
418 - 97 29
392.9
811.1
725.5
85.6
0.5884
0.9233
1.517 5
0.659^
305
306
419.26
393.2
810.8
725.2
"85.6
0.5888
0.9227
1.512,
0.661 Q
306
307
419.56*0
393.5
810.5
724.9
85.6
0.5891
0.9220
1.507?
0.664*
307
308
419.85^
393.8
810.3
724.7
85.6
0.5895
0.9214
1- 502 5
0.6662
308
309
420.15
394.1
810.0
724.4
85.6
0.5898
0.9208
1.497,
0.668 9
309
310
420.45*"
394.4
809.7
724.1
85.6
0.5902
0.9202
1.492?
0.670 9
310
311
420.7631
394.8
809.5
723.9
85.6
0.5905
0.9196
1.487?
o
0.672^
311
312
421.06 9Q
395.1
809.2
723.6
85.6
0.5909
0.9190
1.482,
0.675 9
312
313
421.35
395.4
808.9
723.3
85.6
0.5912
0.9184
1.477*
0.677;;
313
314
421.6530
395.7
808.7
723.1
85.6
0.5916
0.9177
1.473:
o
0.679^
314
315
421.94 n
396.0
808.4
722.8
85.6
0.5919
0.9171
1.468,
0.681 9
315
316
422.24*"
396.3
808.1
722.5
85.6
0.5923
0.9165
1.463?
O.eSSg
316
317
422. 53JJ
396.6
807.9
722.3
85.6
0.5926
0.9159
1.459*
317
318
422.82
396.9
807.6
722.0
85.6
0.5930
0.9153
1.455,
0.687,
318
319
423.1129
397.2
807.3
721.7
85.6
0.5933
0.9147
1.450*
0.690*
319
SATURATED STEAM TABLE II.
53
d
-s
3 aJj
|
Q.
> C '
&*
gS.*'
2
3
*,
.iP
11
11
3 C 3
~ uJs
Si
s|
K?|
wS|
f
*1 =
*!
Sfj
P"
joJcH
SGfa
0)""
g'3
is
2g^
8 1*3
t
C^
&*
iimlH
fS5
>*
H
A
S
K
W~"
H
W
02
p
p
I
*
r
P
Apu
e
r
T
8
^
p
320
321
322
423.40 2Q
423. 69~
423.97^
397.5
397.8
398.1
807". 1
806.8
806.6
721.5
721.2
721.0
85.6
85.6
85.6
0.5937
0.5940
0.5943
0.9141
0.9135
0.9129
.446,
441 5
.436^
0.692 9
0.694;
0.696 2
320
321
322
323
324
325
424.26 9R
424. 54JJ
424.83**
398.4
398.7
399.0
806.3
806.0
805.8
720.7
720.4
720.2
85.6
85.6
85.6
0.5947
0.5950
0.5953
0.9123
0.9117
0.9111
.432.
.428*
.424*
0.698 9
0.700;
0.702^
323
324
325
326
327
328
425.11 2g
425.40JJ
399.3
399.6
399.9
805.5
805.3
805.0
719.9
719.7
719.4
85.6
85.6
85.6
0.5957
0.5960
0.5964
0.9106
0.9100
0.9094
1.419.
1-.415J
1.411 5
0.705 9
0.707;
0.709 2
326
327
328
329
330
331
425.97 2q
426.26;*
428.54*;
400.2
400.5
400.8
804.7
804.5
804.2
719.1
718.9
718.6
85.6
85.6
85.6
0.5967
0.5970
0.5974
0.9089
0.9083
0.9077
.406,
.402*
.398*
0.711 9
0.713 9
0.715^
329
330
331
332
333
334
426.83 9fi
427.n;
427.39 2
401.1
401.4
401.7
804.0
803.7
803.5
718.4
718.1
717.9
85.6
85.6
85.6
0.5977
0.5980
0.5984
0.9071
0.9065
0.9059
.394,
.389^
.385*
0.717,
0.720 9
0.722^
332
333
334
335
336
427.67 97
427. 94^ '
402.0
402.2
803.2
803.0
717.6
717.4
85.6
85.6
0.5987
0.5990
0.9054
0.9048
1.381,
1.377*
0.724 9
0.726
335
336
TABLE III.
SATURATED STEAM.
FRENCH AND ENGLISH CONVERSION TABLES."
j
PRESSURE.
HEAT OF
THE LIQUID.
HEAT OF
VAPORIZATION.
LENT OF IN-
TERNAL WORK.
s -'
c
3
e$s
m
n.
03
'
5 <-S
tf
,.
c5 c3 '43 <3
03 03 j
.
[D
$
p
.2
&
8
s&S
jLg
j) ,_, 3 C -g
^ ^0
Q
4
o
EH
j>
H
a 4?-^
^ 8
|Q&
1
3
ed
3
PQ
6
H
'
p
P
P
q
q
r
r
'
P
t
4.579 ,,,
0.00623 .-
0.0886 fifi
0.00
0.0
595.4
1071.7
565.3
1017.5
32
i
4.924 ^
0.00670 la
0.0952 7 ^
1.01
1.8
594.9
1070.8
564.7
1016.4
33.8
2
^' 391
0.00719 g 3
0.1023 7 g
2.02
3.6
594.4
1069.9
564,0
1015.3
35.6
3
5.681 , 1fi
0.00772 , 7
0.1099 ftn
3.03
5.5
593.9
1069.0
563.4
1014.2
37.4
4
6.097 ;JJ
0.00829 ^
0.1179 "
4.03
7.3
593.3
1068.0
562.8
1013.1
39.2
5
6.541 gj
0.00889 g]J
0.1265 9 j
5.04
9.1
592.8
1067.1
562.2
1011.9
41
6
7-011 , nn
0.00953 AR
0.1356 Q7
6.04
10.9
592.3
1066.1
561.5
1010.7
42.8
7
7.511 "
0.01021 Xo
- 1453 102
7.05
12.7
591.8
1065.2
560.9
1009.6
44.6
8
8-042 JJJ
0.01093 77
8.05
14.5
591.2
1064.2
560.2
1008.5
46.4
9
8.606 , QQ
0.01170 Q9
0.1664 U6
9.05
16.3
590.7
1063.3
559.6
1007.4
48.2
10
9.205 JOE
0.01252 ^
. 17oO. fjq
10.06
18.1
590.2
1062.3
559.0
1006.2
50
11
9.840 "^
0.01338 ll
0.1903} 23
11.06
19.9
589.6
1061.3
558.3
1005.0
51.8
12
10.513 71 ,
0.01429 Q .
0.2033 1Q8
12.06
21.7
589.1
1060.4
557.7
1003.9
53.6
13
11.226 it]
0.01526^'
0.2171 If
13.06
23.5
588.6
1059.4
557.1
1002.7
55.4
14
11.980 79 <j
0.01629Jo
' 2317 154
14.06
25.3
588.1
1058.5
556.5
1001.6
57.2
15
12.779 fi .,.
0. 01737, ,,
0.2471
15.06
27.1
587.6
1057.6
555.9
1000.5
59
16
13.624 J^
0.0185fijiS
0.2635}?;
16.06
28.9
587.0
1056.6
555.2
999.4
60.8
17
14.517
0.01974 12g
0.2807} 72
17.06
30.7
586.5
1055.7
554.6
998.3
62.6
18
15.460 Qqfi
0.02102 1Q .
0.2990 192
18.06
32.5
585.9
1054.7
553.9
997.1
64.4
19
16 456
0.02237}^
0.3182i^
19.06
34.3
585.4
1053.8
553.3
996.0
66.2
20
17.51 m
0. 02381 J^J
0.3386*^
20.06
36.1
584.9
1052.8
552.7
994.8
68
21
22
23
18.62 n7
19.79"!
21 ' 02 130
0.02532.' Q
0.02691}^
0.02858j5 7
0.3601 99fi
0.3827^
0.4065 23
21.06
22.06
23.06
37.9
39.7
41.5
584.4
583.9
583.3
1051.9
1051.0
1050.0
552.1
551.5
550.8
993.7
992.6
991.4
69.8
71.6
73.4
24
22.32^
0. 03035. aft
0.4316 9fi ,
24.06
43.3
582.8
1049.1
550.2
990.3
75.2
25
23.69J44
0.03221}^
0.4581
25.05
45.1
582.3
1048.1
549.5
989.1
77
26
0. 03417S?
o!4860 2 ^
26.05
46.9
581.8
1047.2
548.9
988.0
78.8
152
206
294
27
26 65
0.03623 21g
0.5154o no
27.05
48.7
581.2
1046.2
548.2
986.9
80.6
28
28 ' 25 !fiQ
0.5463^;
28.05
50.5
580.7
1045.2
547.6
985.7
82.4
29
oq Q4 169
J9.94 m
- 04071 24C
5790
29.04
52.3
580.2
1044.3
547.0
984.6
84.2
30
31.71 186
0.04311 253
0.6132 360
30.04
54.1
579.6
1043.3
546.3
983.4
86
* NOTE: This table gives the Metric values for one kilogram and the English values for one pound at
corresponding temperatures.
54
TABLE III.
SATURATED STEAM.
FRENCH AND ENGLISH CONVERSION TABLES.
HEAT EQUIVA-
LENT OF EX-
01
SPECIFIC VOLUME.
DENSITY.
J
TERNAL WORK.
~
I
*
-
3
|
.
ll
"SJ
E^
1 i
ly
I
III
III
S
"5
H
fl
P
ill
*
Jol
111
III
H
O
1
w
d
IOA,
M
1
h
Apu
Apu
e
r
T
8
i
s
1
s
t
30.1
54.2
0.0000
2.1804
206.3 10 ~
3304 917
0.00485 04
0.000303 91
32
1
2
30.2
30.4
54.4
54.6
0.0037
0.0074
2.1706
2.1609
192.7}
180.0J 27
3087 203
9884 Uti
2884 190
0.00519 , 7
0.00556 jjj
0.000324^
0.000347^
33.8
35.6
3
30.5
54.8
0.0110
2.1513
168.2 1in
2694 1?6
0.00595 41
0.000371 9R
37.4
4
30.5
54.9
0.0146
2.1416
157.2
0.00636 *i
0.000397 97
39.2
5
30.6
55.2
0.0183
2.1320
147.1 oJ
^OOD-j - r\
0.00680 ^
0.000424;;
41
94
150
/y
6
30.8
55.4
0.0219
2.1225
137.7 87
2206, ,
0.00726 , (
0.000453,,
42.8
7
30.9
55.6
0.0256
2.1130
129.0
2067}^
0.00775
0.000484^ 9
44.6
8
31.0
55.7
0.0290
2.1036
120.9 8 *
1Q o 7 l30
937 121
0.00827 ^
0.000516^
46.4
9
31.1
55.9
0.0326
2.0943
113.4 71
1816 11Q
0.00882 , Q
0.000551o R
48.2
10
31.2
56.1
0.0361
2.0850
106.3 'i
1703 ^
0.00941 H*
0.000587^
50
11
31.3
56.3
0.0397
2.0758
99.8 gj
icqo 1 04
9 97
0.01002 JJ
DO
0.000625^
51.8
12
31.4
56.5
0.0433
2.0667
93.7 , ft
1502 Q1
0.01067 RQ
0.000666,,
53.6
13
31.5
56.7
0.0467
2.0576
88.1
1411 Q!
0.01135 ?
0. 000709 J?
55.4
14
31.6
56.9
0.0502
2.0486
82 ' 9 50
1327 84
0.01206 7 J
0.000754^
57.2
15
31.7
57.1
0.0537
2.0396
77.9 Al
1248 74
0.01283 c
0.000801,,
59
16
31.8
57.3
0.0571
2.0308
73.3 *
1174 'Q
0.01364 ^
0.000852^
60.8
17
31.9
57.4
0.0607
2.0220
AQ 1 ^
1 40
,105
0.01447 g 9
0.000905 56
62.6
18
32.0
57.6
0.0641
2.0132
65.1 oo
1041 CQ
0.01536 ,
0.000961 57
64.4
19
32.1
57.8
0.0675
2.0045
61.3
982
0.01631 I
66.2
20
32.2
58.0
0.0709
1.9959
57.8 3*
926
06
- 01730 105
o!ooio8o5 2
DO
68
21
32.3
58.2
0.0743
1.9873
54.5 Qn
873 4Q
0.0l835 1ft7
0.001145, Q
69.8
22
32.4
58.4
0.0776
1.9788
51.5 30
824 :;
0.01942}"^
0.001214?;
71.6
23
32.5
58.6
0.0811
1.9703
48 ' 60 268
778 4 ^
0. 02058}^
0.001286^
73.4
24
25
26
32.6
32.8
32.9
58.8
59.0
59.2
0.0845
0.0878
0.0911
1.9620
1.9536
1.9453
45.92 252
43 ' 40 235
41.05 23 *
735 , ft
695
657 35
0.02178 126
0.02304!^
0.02436}^
0.001361 7C
0.001439^
0.001522^
75.2
77
78.8
27
33.0
59.3
0.0945
1.9370
38.83
622
0.02575 H7
0.001608 Qft
80.6
28
33.1
59.5
0.0978 1.9288
" 1 Of
589
0.001698o 7
82.4
29
33.2
59.7
0.1011
1.9207
S4.78|S
557 ^
O'.S^ 3
0.001795^
84.2
30
33.3
59.9
0.1044
1.9126
32.95 in
528 2?
0.03035 166
0.001894 102
86
* NOTE : This table gives the Metric values for one kilogram and the English values for one pound
at corresponding temperatures. If refinement is desired Table I should be used.
55
SATURATED STEAM -TABLE III.
a
g
PRESSURE.
HEAT OF
THE LIQUID.
HEAT OF
VAPORIZATION.
HEAT EQUIVA-
LENT OF IN-
TERNAL WORK.
Temperature,
Degrees
Fahrenheit.
+j o>
;.-<- 3
~ O O
3
1
o
3
H
PQ
o
3
p
H
J3
ta
H
PQ
1
p
P
p
Q
q
r
r
p
P
t
31
32
33
33.57 1Qfi
35 - 53 206
0.04564 266
oiosiii^
0.6492 37Q
- 6871 398
0.7269 3 ? 8
31.04
32.04
33.04
55.9
57.7
59.5
579.1
578.6
578.0
1042.4
1041.4
1040.4
545.7
545.1
544.4
982.2
981.0
979.9
87.8
89.6
91.4
34
35
36
39.75 997
j c\ AO^^ *
44 ' 40 250
0.05404 30Q
0.05713;
- 06037 339
0.7687 43Q
- 8126 460
0.8586^
34.03
35.03
36.03
61.3
63.1
64.9
577.4
576.9
576.4
1039.4
1038.5
1037.5
543.7
543.1
542.5
978.7
977.6
976.4
93.2
95
96.8
37
38
39
46.90 9fi1
49 ' 51 275
52.26 27 7 '
}:06731 3 ^
0.07105 374
0.9068, ftfi
0.9574^
1.0105^
37.02
38.02
39.02
66.6
68.4
70.2
575.8
575.3
574.7
1036.5
1035.5
1034.5
541.8
541.2
540.5
975.2
974.0
972.8
98.6
100.4
102.2
40
41
42
55.13 3Q1
58.14 3 ?!
-*g|
0.07495 41Q
0.07905*2g
1.0661, 8 o
1.1243^:
1.1854^
40.02
41.01
42.01
72.0
73.8
'75.6
574.2
573.6
573.1
1033.5
1032.5
1031.5
539.9
539.2
538.6
971.7
970.5
969.3
104
105.8
107.6
43
44
45
64.59,^
68 ' 05 361
71.66 3?7
0.08782 470
0:09743^ 9 J
1.2492 fifi7
1 ' 3159 699
43.01
44.01
45.00
77.4
79.2
81.0
572.5
571.9
571.3
1030.5
1029.4
1028.4
537.9
537.2
536.5
968.2
966.9
965.7
109.4
111.2
113
46
47
48
75.43 395
83:50 4 4 J 2
0.10256 536
0.10792^
0.11353JJHJ
1.4587 7R o
1.5360IK
1fi1 /(7 ' " '
6147 832
46.00
47.00
48.00
82.8
84.6
86.4
570.8
570.2
569.6
1027.4
1026.4
1025.3
535.8
535.1
534.4
964.5
963.3
962.0
114.8
116.6
118.4
49
50
51
87.80 45Q
92- 30 4 ^
0.11937 612
1.6979 S7n
1 ' 7849 907
48.99
49.99
50.99
88.2
90.0
91.8
569.0
568.4
567.8
1024.3
1023.2
1022.2
533.7
533.0
532.3
960.8
959.6
958.4
120.2
122
123.8
52
53
54
101.88,,,
106. 99^!
112 " 30 555
0.13852 6Q4
0.14546?;*
0.15268 7 ^
1.9701 Q oo
2.0689^
2.172 J^ 7
51.99
52.99
53.98
93.6
95.4
97.2
567.3
566.8
566.2
1021.2
1020.2
1019.1
531.7
531.1
530.4
957.2
956.0
954. 7
125.6
127.4
129.2
55
56
57
117.85, 7R
123.61 A 'o
129.63^ 2
0.16023 7CQ
0.16806^
- 17624 851
2.279 t11
2.390 }"
2.506 J 2 J
54.98
55.98
56.98
99.0
100.8
102.6
565.6
565.1
564.5
1018.
1017.
1016.
529.7
529.1
528.4
953.5
952.3
951.1
131
132.8
134.6
58
59
60
135.89 R , 9
142.41 R7 g
149 ' 19 ?05
0.18475 sft7
0.19362;
0.20284^
2.627 197
2.754 },:
2.885 J 3 g
57.98
58.97
59.97
104.4
106.2
108.0
563.9
563.4
562.8
1015.
1014.
1013.
527.7
527.1
526.4
949.9
948.7
947.5
136.4
138.2
140
61
62
63
156.24 7Q ,,
163.58:!?
171.20 2
0.21242 inft
0.2224 fr;
0.2328 {JJ*
3.021 ,, 9
3.163 \^L
3.310 J^ 4
60.97
61.97
62.97
109.8
111.6
113.4
562.2
561.7
561.1
1012.0
1011.0
1009.9
525.7
525.1
524.4
946.3
945.1
943.8
141.8
143.6
145.4
64
65
66
179.13,
187 ' 36 856
195 " 92 888
0.2435 119
0.2547 }};
0.2664 J 2 Q
3.464 1( . Q
3.623 } RR
3.789 J 7 J
63.98
64.98
65.98
115.2
117.0
118.8
560.5
559.9
559.3
1008.9
1007.8
1006.8
523.7
523.0
522.3
942.6
941.3
940.1
147.2
149
150.8
67
68
69
204.80 Q99
214 ' 02 956
223 ' 58 995
0.2784 19fi
0.2910 f
0.3040 J 3 ;
3.960 17g
4 ' 324 192
66.98
67.98
68.98
120.6
122.4
124.2
558.8
558.2
557.6
1005.8
1004.7
1003.6
521.7
521.0
520.3
938.9
937.6
936.3
152.6
154.4
156.2
70
233.53 1Q3
0.3175 14Q
4.516 1Q9
69.98
126.0
556.9
1002.5
519.5
935.0
158
SATURATED STEAM TABLE III.
57
HEAT
EQUIVALENT
O
SPECIFIC VOLUME.
DENSITY.
.
OF EXTER-
1
c
^
1 "i
NAL WORK.
~ii
^
k
'3
a|S
"^
O N
<D
ft
s
III
H
1
P
>>3
P
IS
r
ea
ill
1
Jl.
jll
111
t
Apu
Apu
e
r
T
8
'
1
a
1
8
t
31
33.4
60.2
0.1077
1.9046
31.24 lfi9
501
0. 03201 17 ,
0.001996..
87.8
32
33.5
60.4
0.1110
1.8966
29.62}^
474.7 26
0.03376}')?
0.002107}} 7
89.6
33
33.6
60.5
0.1142
1.8886
28 - 08 H6
449 ' 7 232
0. 03561 }jj
0. 002224 J 2 J
91.4
34
35
33.7
33.8
60.7
60.9
0.1175
0.1207
1.8806
1.8728
26.62 137
25.25 27
426.5 218
404 ' 7 205
0.03757 2Q3
0. 002345. 9fi
0. 00247l},X
93.2
95
36
33.9
61.1
0.1239
1.8650
23.98J 27
384.2 1Q3
- 04170 220
0. 002603 J 37
96.8
37
38
34.0
34.1
61.3
61.5
0.1272
0.1304
1.8572
1.8494
22.78..,
21.66";
364.9 181
346.8J{
0.04390 22q
0.04619^
0.002740.,
0.002884}*;
98.6
100.4
39
34.2
61.7
0.1336J1.8417
90 58
101
329.7 162
0.04859^
0. 003033 Jg 7
102.2
40
34.3
61.8
0.13681.8341
19.57 Qft
313.5.,,
0.0511o*
0.003190. fift
104
41
34.4
62.0
0.1399 1.8265
18.61 Q
298.o}2 7 !o.0537 9 g
0.003356};^
105.8
42
34.5
62.2
0.1431
1.8189
17.69 gy
283.3J 47 J0.0565^
0.003530jgj
107.6
43
34.6
62.3
0.1463
1.8113
16.82 fi
269.5.^
0.0595, n
0.003711 1Q
109.4
44
34.7
62.5
0.1494
1.8038
16.01 7 *
256.5 30
0.0625,"
0.003899}!
111.2
45
34.8
62.7
0.1526
1.7963
15.25 j;
244 - 4 m
0.0656 32
0.004092^3
113
46
35.0
62.9
0.1557
1.7889
14.54 fifi
233-0.00
0.0688 ,
0.004292 9in
114.8
47
35.1
63.1
0.1588
1.7815
13.86 55
222.l}"^0.0722o1
0.004502;;"
116.6
48
35.2
63.3
0.1619
1.7742
13 21 b5
11 61
211 ' 7 98
0.0757^
0.004724^
118.4
49
35.3
63.5
0.1650
1.7669
12.60 .,
201.9 Q ,
0.0794, Q
0.00495 9 .
120.2
50
35.4
63.6
0.1682
1.7597
12.02 11
192.6 JJ
0.0832^
00519
122
51
35.5
63.8
0.1713
1.7525
11.47 11
183.8 11
0.0872
0!00544 25 5
123.8
52
35.6
64.0
0.1743
.7454
10.96 , Q
175.5 7C
0.0912
0.00570 9R
125.6
53
35.7
64.2
0.1774
.7383
10.47 * 7
167.7 i
0.0955 4 3
0.00596 28
127 .4
54
35.8
64.4
0.1804
.7312
10.00 *
160.3 J!
0.1000*^
129.2
44
71
46
29
55
35.9
64.6
0.1835
.7242
9.56 . 9
153.2 fi7
0.1046.Q
0.00653,o
131
56
36.0
64.8
0.1865
.7173
9.14 J*
146.5 5
0.1094*^
0.00683,"
132.8
57
36.1
65.0
0.1895
.7104
8.74
140.1 4
' 1144 52
0.00713 33
134.6
58
36.2
65.2
0.1925
. 7035
8.36 , fi
134.0 , 7
0.1196,.
0.00746,,
136.4
59
36.3
65.4
0.1955
.6967
8.00 3
128.3 r:
0.1250^
0.00779,^
138.2
60
36.4
65.6
0.1986
.6899
7 ' 66 32
122.8 II
0.1305^
0.00814,
oo
140
61
36.5
65.7
0.2016
.6831
7.34 ,,
117.6 .
0.1362 An
0.00850, 7
141.8
62
36.6
65.9
0.2046
.6764
7.03 ^
112.7 4 ;
1422
0.00887,'
143.6
63
36.7
66.1
0.2075
.6696
6.74 11
108.0 :'
<M484 62
0.00926^
145.4
28
45
64
40
64
36.8
66.3
0.2105
.6629
6.46 97
103.5 .,
0.1548 ft7
0. 00966. 9
147.2
65
36.9
66.5
0.2135
.6563
6.19 I 7 ,
99.2 *J
0.1615^
0.01008*,
149
66
37.0
66.7
0.2164
.6497
5.94 ~*
95,1 3g
0.1684^
0.01051*^
150.8
67
37.1
66.9
0.2194
1.6431
5.70 9 ,
91.3 , 7
0.1754 71
0.01095. 7
152.6
68
37.2
67.1
0.2223
1.6366
5.47
87.6 H
0.1828 77
0.01142* 7
154.4
69
37.3
67.3
0.2253
1.6300
5.25 21
84.1
0.1905^
0.01189 47
156.2
70
37.4
67.4
0.2282
1.6235
5.04 2Q
80.7 32
0.1984 83
0.01239 51
158
SATURATED STB AM TABLE III.
HEAT EQUIVA-
PRESSURE.
HEAT OF
THE LIQUID.
HEAT OF
VAPORIZATION.
LENT OF IN-
TERNAL WORK.
14
u
2i
tn
V
05
S
a gj. c
L
1
P
.1
p
.1
p
III
lot
Illll
"SB'S
gft
O
3
3
o
3
s
III
E-t
^
M
AH
H
t
P
p
P
q
q
r
r
>
p
t.
71
243. 8. n -
0.3315^,
4 715
70.98
127.8
556.4
1001.5
518.8
933.9
159.8
72
254.5 07
o.346o:f:
4.921 9 ?|
71.99
129.6
555.8
1000.4
518.1
932.6
161.6
73
R C lll
265.6 n5
' 3611 156
5 - 136 222
72.99
131.4
555.2
999.4
517.4
931.4
163.4
74
277.1 11Q
0.3767 162
5.358 9<n
73.99
133.2
554.6
998.3
516.7
930.1
165.2
75
289 -123
5 589
74.99
135.0
554.0
997.3
516.0
928.8
167
76
301.3 127
o!4096J 7 !
5.826 246
76.00
136.8
553.4
996.2
515.3
927.6
168.8
77
78
314.
327.2}*;
0.4269 18()
0.4449}
6.072 2 .
6.327^?
77.00
78.00
138.6
140.4
552.9
552.3
995.2
994.1
514.7
514.0
926.4
925.2
170.6
172.4
79
OAn q lt5 '
40.9 U2
0.4635j!
6 ' 592 275
79.01
142.2
551.7
993.0
513.3
923.9
174.2
80
355.1
0.4828 19g
6.867 9CQ
80.01
144.0
551.1
991.9
512.6
922.6
176
81
369 i?! 4 !;
7.150^
81.02
145.8
55tf.5
990.8
511.9
921.3
177.8
82
oo 4 Q 152
84>9 156
o' 5233^2
7 443 293
7.44d 302
82.02
147.6
549.9
989.8
511.2
920.1
179.6
83
84
85
400.5
A 1 A IT**
433'5 168
0.5445 99n
0.5665^
- 5894 235
7.745 313
8.058 3 ^
8 ' 383 334
83.03
84.03
85.04
1*9.4
151.
153.
549.3
548.7
548.1
988.7
987.6
986.5
510.5
509.8
509.1
918.8
917.6
916.3
181.4
183.2
185
86
450. 8, 7Q
0.6129 242
8-717,..
86.04
154.
547.4
985.4
508.3
915.0
186.8
87
468.6}'
9.062^*2
87.05
156.
546.8
984.3
507.6
913.7
188.6
88
487. l} 8 *
S: 6623^
9 ' 419 368
88.06
158.
546.2
983.2
506.9
912.5
190.4
89
506.1 197
0.6881 9ftc
9.787, an
89.06
160.
545.6
982.1
506.2
911.2
192.2
90
0.7149^8
10.167^!:
90.07
162.
544.9
980.9
505.4
909.9
194
91
546. I 2 ? 3
' 7425 285
10.560 393
91.08
163.
544.3
979.8
504.7
908.5
195.8
92
567.l 91ft
0.7710 9Q4
I0.966.. 1fi
92.08
165.
543.7
978.7
504.0
907.2
197.6
93
588 ' 7 223
0.8004^
11.3842i?
93.09
167.
543.1
977.6
503.3
906.0
199.4
94
611 '230
0.8307^
n ' 815 445
94.10
169.
542.5
976.5
502.6
904.7
201 2
95
634.0 9Q7
8620
12. 260., Q
95.11
171.
541.9
975.4
501.9
903.4
203
96
657.7^1
) 8942
12 718
96.12
173.0
541.2
974.2
501.1
902.1
204.8
97
-4g
0.9274 342
13.190 488
97.12
174.8
540.6
973.1
500.4
900.8
206.6
98
707.3 OAn
0.9616 354
13.678, no
98.13
176.6
539.9
971.9
499.6
899.4
208.4
99
733.3^0
14.180^? 2
99.14
178.5
539.3
970.8
498.9
898.2
210.2
100
760. O 267
[0333
14.697|i;
100.2
180.3
538.7
969.7
498.2
896.9
212
275
374
532
101
787.5 9fi ,
1.0707o SR
15.229,, Q
101.2
182.1
538.1
968.5
497.5
895.5
213.8
102
815.9
1093
.5.778
102.2
183.9
537.4
967.3
496.8
894.1
215.6
103
845.1 30Q
1.-1490 397
16 ' 342 581
103.2
185.7
536.8
966.2
496.1
892.9
217.4
104
875 1
1.1898., 91
16.923.QQ
104.2
187.6
536.2
965.1
495.4
891.6
219.2
105
906 ' 1 318
1.23192,;
17.522^
105.2
189.4
535.6
964.0
494.7
890.3
221
106
1.275222'
18.137^
106.2
191.2
534.9
962.8
493.9
889.0
222.8
327
444
632
107
108
109
970.6,,.
1004.3,^
1038 - 8 35?
1.3196 457
11?23 470
1.41^ 485
18.769,,,
19.420^J
20,089^ 9
107.2
08.2
09.3
193.0
194.8
196.7
534.2
533.6
532.9
961.6
960.5
959.3
493.1
492.4
491.6
887.6
886.3
885.0
224.6
226.4
228.2
110
1074.5 366
1.4608 498
20.777 7()9
10.3
198.5
532.3
958.1
490.9
883.6
230
SATURATED STEAM TABLE III.
59
HEAT
EQUIVALENT
_
SPECIFIC VOLUME.
DENSITY.
OF EXTER-
~
Q
.
1 i
NAL WORK.
"83
- ^3
_^
u
I 1
III
&-
1
P
II
oj
c
! i
11
I.,,
~^2 O
ill
E->
o
3
H
"c
a
W
ill
!&
|il
M
J
t
Apu
Apu
s
r
T
s
3
i
s
1
S
t
71
37.6
67.6
0.2311
1.6171
4.838 1Q1
775
0.2067 c .
0.01290 ,.
159.8
72
37.7
67.8
0.2340
1.6107
4.647
74 ' 4 29
0.2152 ;
0.01344 J;
161.6
73
37.8
68.0
0.2369
1 . 6044
4 - 466 m
71.5 2?
0.2239 ^
0.01398 g*
163.4
74
37.9
68.2
0.2398
1.5981
4.294 1R ,
68.8 0ft
0.2329 Q9
0.01453
165.2
75
38.0
68.5
0.2427
1.5918
4 - 130 157
66.2;
0.2421 I
0.01510 R( l
167
76
38.1
68.6
0.2456
1.5856
3.973 151
63 - 7 25
0.2517 11
0.01570 g 4
168.8
77
38.2
68.8
0.2484
1.5793
3.822..,,
61.2
0.2616 Q
0.01634 R
170.6
78
38.3
68.9
0.2513
1.5731
3.676!*
58 - 8 22
0.2720j" 7
0.01700 R7
172.4
79
38.4
69.1
0.2541
1.5670
3 " 537 l33
56.6 22
0. 2827^J
0.01767 gg
174.2
80
38.5
69.3
0.2570
1 . 5609
3.404
54.5 2Q
0.2938
0.01835 7n
176
81
38.6
69.5
0.2598
1.5548
3 ' 277 121
en e*U
0.3052 HI
0.01905 7 "
177.8
82
38.7
69.7
0.2626
1.5487
3 ' 156 H6
5 :6 i9
0.3168J 2 J
0.01976 ifi
179.6
83
84
38.8
38.9
69.9
70.0
0.2654
0.2682
1.5426
1.5366
3.040 m
2.929 05
48.71 17Q
46.92j R Q
0.3289 2
0.3414 If
0.02053 7fi
0.02131 '*
181.4
183.2
85
39.0
70.2
0.2711
1.5307
2 - 824 loi
45 23
' 161
0.3541} 27
0.02211 ^
185
86
39.1
70.4
0.2739
1.5247
2.723 OR
43.62 t , 4
0.3672 17 ,
0.02293 a ,
186.8
87
39.2
70.6
0.2767
1.5187
2.627 I
42 ' 08 149
3807|oQ
0.02376 g 7
188.6
88
39.3
70.7
0.2795
1.5128
2.534 H
40.59 H4
0.3946} 3 ^
0.02463 9 |
190.4
89
39.4
70.9
0.2823
1.5069
2.444 8fi
39.15 1QQ
0.4091 1( . ft
0.02554 QA
192.2
90
39.5
71.0
0.2851
1.5010
2.358 !
37.77;, 9
0.4241 ^
0.02648 11
194
91
39.6
71.3
0.2879
1.4952
2.275 |
36.45} 32
0.4395}^
0.02743 99
195.8
92
39.7
71.5
0.2906
1.4894
2.197 7 ,
35.19 110
0.4552
0.02842 QQ
197.6
93
39.8
71.6
0.2934
1.4836
2.122 79
34 -OOl14
0.4713}^
0.02941^
199.4
94
39.9
71.8
0.2961
1.4779
2.050 7 g
32.S6}} 4
0.4878j^
- 03043 lo6
201.2
95
96
40.0
40.1
72.0
72.1
0.2989
0.3016
1.4723
1.4666
1.980 A7
.913 H
31.75 1Q8
30 - 67 04
0.505,'
0.523:^
0.03149 1V
0.03260};!
203
204.8
97
40.2
72.3
0.3043
1.4609
.849 ,
29.63^ 4
0.54l} 8
0.03375JJ?
206.6
62
yy
iy
117
98
40.3
72.5
0.3070
1.4552
.787 , Q
28.64 Q ,
0.560 ig
0.03492
208.4
99
40.4
72.6
0.3097
1.4496
.728 ;
27.69 Q
0.579!^
0.0361l}i^
210.2
100
40.5
72.8
0.3125
1;4441
ATI 91
671 nA
26.78 01
0.598^
0.03734j;^
212
O4
oo
Ml
127
101
40.6
73.0
0.3152
1.4386
-617
25.90 fi
0.618 91
0.03861 19Q
213.8
102
40.6
73.2
0.3179
1.4330
.564 "
25.06 J
0.639;^
03990
215.6
103
40.7
73.3
0.3205
1.4275
K1A 5U
514 4g
24.25 8 g
0.661 22
0:04124} 34
217.4
104
40.8
73.5
0.3232
1.4220
.465 Al
23.47 74
0.683 99
0. 04261 ,
219.2
105
40.9
73.7
0.3259
1.4165
.419 ll
22.73 79
0.705;;
0. 04400 J 4 g
221
106
41.0
73.8
0.3286
1.4111
.374 4 g
22.01 72
0.728 23
0.04543 H9
222.8
107
41.1
74.0
0.3312
1.4057
.331 , 9
21.31 R -
0.751 9 ,
0. 04692.
224.6
108
41.2
74.2
0.3339
1.4003
.289 4 f
20.64 R '
0.776^
0. 04845 J, 7
226 4
109
41.3
74.3
0.3365
1.3949
248 39
19.99 g 2
0.801 2 ^
o n"on
228.2
110
41.4
74.5
0.3392
1.3895
1.209 3?
19.37 6Q
0.827 26
0.0516 17
230
6o
SATURATED STEAM TABLE III.
HEAT EQUIVA-
PRESSURE .
HEAT OF
HEAT OF
LENT OF IN-
i
THE LIQUID.
VAPORIZATION.
TERNAL WORK.
"5
s 4
f
I|S
ll
1 5* &
|
2
,j
|
.
4
.
|)1
Is
M <-> 2, 55 "
Ip
S
Ejj
'o
H
E
o
& si-fi
Spo
3*3 o
^S^oS
1^5
a
m
3
ri
3
PQ
So
S
S
M
w
h
t
P
p
p
5
Q.
r
r
p
p
t
111
112
1148!7?oS
1-5106 K11
,/> 1 nOi i
.5617,07
22'2H 728
111.3
112.3
200.3
202.1
531.6
530.9
956.9
955.7
490.2
489.4
882.3
880.9
231.8
233.6
113
1187 ' 4 397
C1 ., ,527
6144 540
22:%2 ?67
113.3
203.9
530.3
954.5
488.7
879.5
235.4
114
115
1227. W
1267. 9 4 ? 8
6684
.7238??*
23.729 78Q
24.518 8 *Q
114.3
115.3
205.8
207.6
529.6
528.9
953.3
952.1
487.9
487.1
878.2
876.8
237.2
239
116
1309. 8*
.7808^
116.4
209.4
528.2
950.8
486.3
875.4
240.8
430
585
832
117
1352. 8..0
8393 600
26.160 Q ,,
117.4
211.2
527.5
949.5
485.5
873.9
242.6
118
1397. 442
27 - 015 878
118.4
213.0
526.9
948.4
484.8
872.6
244.4
119
1442 ^65
liSSigj
27 ' 893 899
119.4
214.9
526.2
947.2
484.0
871.3
246.2
120
121
1488. 9 477
1536.6*''
2.0243 R , 8
2 ' 0891 665
28 ' 792 923
120.4
121.4
216.7
218.5
525.6
524. P
946.0
944.8
483.4
482.6
870.0
868.6
248
249.8
122
1585 ' 7 503
3 :664 973
122.5
220.4
524.2
943.5
481.8
867.1
251.6
123
1636.0,^
2.2241 7n9
31.637 inn
123.5
222.2
523.5
942.3
481.0
865.8
253.4
124
1687. 5^
2.2943 72 jj
32 64
124.5
224.1
522.8
941.0
480.2
864.3
255.2
125
!740.5>
2.3663 738
33 - 66 105
125.5
225.9
522.1
939.8
479.4
863.0
257
126
1794.7
2.4401 7 ,,
34.71 In7
126.5
227.7
521.4
938.6
478.6
861.6
258.8
127
1850 '3^
2.5156 77 ;?
35.78 JV1
127.5
229.5
520.7
937.3
477.8
860.2
260.6
128
1907 - 3 585
2 ' 5931 795
36.88 JJ 3
128.6
231.4
520.0
936.1
477.0
858.8
262.4
129
1965. 8, QQ
2.6726 C1 ,
38.01 11ft
129.6
233.3
519.3
934.8
476.3
857.4
264.2
130
2025. 6gj 3
2.7540*^*
39.17 {;J
130.6
235.1
518.6
933.6
475.5
856.0
266
131
' 629
2.8373 g54
40.36 HI
131.6
236.9
517.9
932.3
474.7
854.6
267.8
132
2149. 8 A ,
2.9227^.
41.57 194
132.6
238.7
517.3
931.1
474.0
853.2
269.6
133
2214. O^ 42
3.0101*'*
42.81 {go
133.7
240.6
516.6
929.8
473.3
851.8
271.4
134
2280.0^5
3.0999JJJJ
44.09 J 3
134.7
242.4
515.9
928.5
472.5
850.4
273.2
135
2347. 5 6qo
3.1916 QQS
45.39 1Q ,
135.7
244.2
515.1
927.2
471.6
848.9
275
136
2416. 5 7 ^g
3.2854^*
46.73 JJ!
136.7
246.0
514.4
925.9
470.8
847.5
276.8
137
2487.3
3.3816 985
48.10 } 3 J
137.7
247.9
513.7
924.6
470.1
846.1
278.6
138
2559. 7 7A1
3.480l 1ft1
49.50 ,
138.8
249.7
513.0
923.3
469.3
844.6
280.4
139
2633.8;*i
3.581 }JJi
50.93 }^
139.8
251.6
512.3
922.1
468.5
843.3
282.2
140
2709.5
3.684 }g3
52.39 J*Q
140.8
253.4
511.5
920.7
467.6
841.8
284
141
2787. 1 7Q ,
3.789 1nfi
53.89 .,,
141.8
255.3
510.7
919.3
466.8
840.2
285.8
142
2866.4'
3.897 Jr,
55.43 f^ 7
142.8
257.1
510.1
918.1
466.1
838.9
287.6
143
004.7 nolo
;y47.7 828
4.008 JJg
57.00 JgQ
143.9
259.0
509.3
916.7
465.3
837.4
289.4
144
3030. 5 8 ,,
4.121 1t ,
58.60 1A .
144.9
260.8
508.6
915.4
464.4
835.9
291.2
145
3115. 3 84 ;
4.236 }}
60.24 {JJ
145.9
262.7
507.8
914.1
463.6
834.5
293
146
3202.1^8
,, oc/ , 118
4.354 12Q
61.92 }J
146.9
264.5
507.1
912.8
462.8
833.1
294.8
147
3290. 8 Qft ,
4.474 19
63.64 17 ,
148.0
266.4
506.4
911.5
462.0
831.6
296.6
148
3381.32x2
4.597 JS
65.39 };J
149.0
268.2
505.6
910.1
461.2
830.1
298.4
149
3474 -947
4.723 J26
67.18 Jgg
150.0
270.1
504.9
908.8
460.4
828.7
300.2
150
3568. 7 Q66
4.852 132
69.01 187
151.0
271.9
504.1
907.4
459.5
827.2
302
SATURATED STEAM TABLE III.
6l
EQUIVALENT
0)
SPECIFIC VOLUME.
DENSITY.
OF EXTER-
c
-r *i
-S
NAL WORK.
*- -
*2
-5
Temperatu
Degrees
Centigram
1
p
F
1
W
i"
Ij
I 8 *
JuS
ill
&
3 w^S
til
J*
1
Apu
Apu
r
f
8
1
i
8
t
111
112
41.4
41.5
74.6
74.8
0.3418
0.3445
.3842
.3789
.172, fi
136 S5
18.77 .
18.20^'
0.853 97
0.880 9 i
0.0533 17
0.0550} 7
231.8
233.6
113
41.6
75.0
0.3471
.3736
tn-t <JU
17 ' 64 54
0.908^
0.0567jg
235.4
114
41.7
75.1
0.3498
.3683
.068 q9
17.10.,
0.936 9Q
0.0585 ia
237.2
115
41.8
75.3
0.3524
.3631
036of
16. WS
0.965 3 J
0.0603}
239
116
41.9
75.4
0.3550
1.3579
i: 05 30
16.09
0.995 31
0.0622j 9
240.8
117
42.0
75.6
0.3576
1.3527
0.9746 286
15.61 4 ,
026 31
0.0641 18
242.6
118
42.1
75.8
0.3602
1.3475
0.9460 9 ;
15 16^
057 32
0.0659 9 ^
244.4
119
42.2
75.9
0.3628
1.3423
0.9183 277
14-72"
89 33
0.0679^
246.2
120
42.2
76.0
0.3654
.3372
0.8914 6
14.28,,
.122
0.0700 21
248
121
42.3
76.2
0.3680
.3321
- 8653 252
13 ' 88 40
156ot
0.0721 99
249.8
122
42.4
76.4
0.3705
.3269
- 8401 243
13.46*"
i<
0.074322
251.6
123
42.5
76.5
0.3731
.3218
0.8158 2 o 4
13.07
226
0.0765 23
253.4
124
125
42.6
42.7
76.7
76.8
0.3756
0.3782
.3167
.3117
- 7924 22fi
0.7698^
12 ^69 38
12 ' 33 35
:262 37
299 38
Hsii^ 3
255 2
257
126
42.8
77.0
0.3807
.3067
0.7479 212
11.98,,
1.337 M
0.0835 94
258.8
127
42.9
77.1
0.3833
.3017
0.7267 2( ^
11.64, 9
1.376^
0.0859 9 ?
260 6
128
43.0
77.3
0.3858
.2967
0.7063 1%
11.32 32
1.416 4Q
0.0883^
262.4
129
130
43.0
43.1
77.4
77.6
0.3884
0.3909
.2917
.2868
0.6867 1Qn
0.6677J^
n.oo 30
10. 70?
1.456 42
1.498];
0.0909 9r
0.0935 9 "
264.2
266
131
43.2
77.7
0.3934
.2818
0.6493 1?8
10.40 30 8
1.540 42
0.0961^
267.8
132
43.3
77.9
0.3959
.2769
0.6315 173
10.12 9Q
1.583.,
0.0988 9a
269 6
133
43.3
78.0
0.3985
.2720
9.839;?.
1 . 628 4 g
0.1016 9
271 4
134
43.4
78.1
0.4010
.2672
0.5974J|j 8
9 569
260
1.674 4?
0.1045 29
273 2
135
136
137
43.5
43.6
43.6
78.3
78.4
78.5
0.4035
0.4060
0.4085
.2623
.2574
.2526
0.5812 6
0.5656|?
0.5506J 4 ;
9.309 24q
9 - 060 240
8820 233
1.721 47
1 - 768 48
1.816 48
0.1074 3Q
- 1104 30
0.1134^
275
276.8
278 6
138
43.7
78.7
0.4110
.2479
0.5361 1/19
8.587 997
1.865 K1
0.1165
280 4
139
43.8
78.8
0.4135
.2431
0.5219!^
8.360 99/ 1
1.W6JJ
O'll96 3 l
282.2
140
43.9
78.9
0.4160
.2383
0.508lJ 3 !
8 - 140 2H
0.1229 33
284
141
43.9
79.1
0.4185
.2335
0.4948 19Q
7.926 on7
2.02U.
1262
285.8
142
44.0
79.2
0.4209
.2288
0.4819| 9 "
7 - 719 9nn
2.075^
1296
287 6
143
44.0
79.3
0.4234
.2241
- 4694 l20
7 ' 519 ?93
2 13055
:i330 34
289 4
291.2
144
44.2
79.5
0.4259
1.2194
0.4574, 17
7.326 1Q7
2.186, Q
1365
145
146
44.2
44.3
79.6
79.7
0.4283
0.4307
1.2147
1.2100
0.4457 |
0.4343JJ
7.139 \ll
6.957J;J
2 ' 244 59
2 ' 303 60
0.1 40 1 3 !!
' 1437 38
293
294.8
147
44.4
79.9
0.4332
1.2054
0.4232 in7
6.780 171
2.363 A1
0.1475 QC
296 6
148
44.4
80.0
0.4356
1 . 2008
0.4125:;;'
6 609 166
2.424^
o isn
298.4
149
44.5
80.1
0.4380
1.1962
0.4022 1"?
2.486^
0-1552 39
300.2
lUJ
161
64
40
150
44.6
80.2
0.4405
1.1916
0.3921 g -
6.282 1M
2.550..
0.1592, n
302
150 DO
40
62
SATURATED STEAM TABLE III.
cl
PRESSURE.
HEAT OF
THE LIQUID.
HEAT OF
VAPORIZATION.
HEAT EQUIVA-
LENT OF IN-
TERNAL WORK.
gj -s
3
ll
{I.
1 S-is
SI
1
P
I
1
p
III
a^
J
3*0
l^oS
m
o
3
E-!
PQ
o
6
EH'
PQ
o
3
o
S
ll
i
p
p
p
3
5
r
r
p
P
t
151
3665.3 QQQ
4.984 n4
70.88 1Q1
152.1
273.8
503.4
906.1
458.7
825.7
303.8
152
3764.1^
5.118}^ 7
72.79}^
153.1
275.6
502.6
904.7
457.9
824.2
305.6
153
5.255^
74.74} 9 9 5
154.1
277.4
501.9
903.3
457.1
822.7
307.4
154
3968
5.395
76.73
155.1
279.2
501.1
901.9
456.3
821.2
309.2
155
4073 108
5.538J
/o./ UOAO
156.2
281.1
500.3
900.5
455.4
819.6
311
156
4181 log
5.684}
on o/208
80.84 212
157.2
283.0
499.6
899.2
454.6
818.2
312.8
157
4290. 19
5.833 1f;9
82.96 216
158.2
284.8
498.8
897.8
453.8
816.7
314.6
158
4402}}^
5.985}^
159.3
286.7
498.1
896.5
453.0
815.3
316.4
159
4517115
fi U1 156
6.141 159
87 - 33 226
160.3
288.5
497.3
895.1
452.1
813.7
318.2
160
4633 11Q
6.300 1fi9
89.59 9Qn
161.3
290.4
496.5
893.7
451.2
812.2
320
161
4752} 99
6.462}^
91 ' 89 236
162.3
292.2
495.7
892.3
450.4
810.7
321.8
162
74}
6.628}68
94.25 24Q
163.4
294.1
494.9
890.9
449.5
809.2
323.6
163
4998 19ft
6.796 171
96.65 , 4
164.4
295.9
494.2
889.5
448.7
807.7
325.4
164
5124
ft Oft7 171
6.967 17 -
99.09*;;
165.4
297.7
493.4
888.1
447.9
806.2
327.2
165
5253 131
7.142} 7 *
101 ' 58 253
166.5
299.6
492.6
886.7
447.0
804.7
329
166
167
5384
5518} 34
7.320 189
7 - 502 186
104.11 2fi0
106.71*S
167.5
168.5
301.5
303.3
491.9
491.1
885.4
883.9
446.3
445.4
803.3
801.7
330 8
332.6
168
5655
7 . 688 1 Q n
109.35^Q
169.5
305.1
490.3
882.5
444.6
800.1
334.4
139
189
269
169
5794
7.877
112.04 97 ,
170.6
307.0
489.5
881.0
443.7
798.5
336.2
170
5937} 4 ^
8.07l}o 7
114 79
171.6
308.9
488.7
879.6
442.8
797.0
338
171
608l} 44
o 9fiQ iy '
8.268 2Q1
m ;59 286
172.6
310.7
487.9
878.3
441.9
795.6
339.8
172
173
6229
6379 \ll
8.469 4
8 ' 673 209
120.45
123.36 29 J
173.7
174.7
312.6
314.5
487.1
486.3
876.9
875.4
441.1
440.2
794.1
792.5
341.6
343.4
174
Rfill *
33 156
8.882 212
126.33 3Q2
175.7
316.3
485.5
873.9
439.4
790.9
345.2
175
6689 15g
9.094 91fi
129.35. n8
176.8
318.2
484.7
872.4
438.5
789.3
347
176
1 fi9
9 310
132.43 r
177.8
320.0
483.9
871.0
437.7
787.8
348.8
177
7010}<J 2
9:53l221
135 ' 56 3ic
178.8
321.8
483.1
869.5
436.8
786.2
350.6
178
7l75 1fiQ
9.755 22g
138.75 Q9 ,
179.9
323.7
482.3
868.1
436.0
784.7
352.4
179
7343jf|
142 00
180.9
325.6
481.4
866.6
435.0
783.1
354.2
180
7514 m
lolie 2 , 33
145^30 33 7
do/
181.9
327.5
480.6
865.1
434.2
781.5
356
181
182
183
7688 7
7866 180
8046} 8 '
10.453 9/10
10. 695^
10 - 940 249
148.67 44
152 ' 11 349
155.60 349
183.0
184.0
185.0
329.3
331.2
333.0
479.8
479.0
478.2
863.6
862.2
860.7
433.3
432.5
431.6
779.9
778.4
776.9
357.8
359.6
361.4
184
8230 1Q7
11.189
159.15 qfi9
186.1
334.9
477.4
859.2
430.8
775.3
363.2
185
04-1 7 lO 1
11 .444
162. 77
187.1
336.8
476.6
857.7
429.9
773.7
365
186
8608 194
n - 703 264
166.46 3?5
188.1
338.6
475.7
856.3
429.0
772.2
366.8
187
8802 1Q7
11.967 9ft8
170.21 3gl
189.
340.5
474.8
854.7
428.0
770.5
368.6
188
8999
12.235
190.
342.4
474.0
853.2
427.2
768.9
370.4
189
9200 204
12.508 27g
H7'.90 388
191.
344.2
473.2
851.7
426.3
767.4
372.2
190
9404 2Q8
12.786 282
181.85 4Q2
192.
346.1
472.3
850.2
425.4
765.8
374
SATURATED STEAM TABLE III.
HEAT
3
EQUIVALEN-T
o
SPECIFIC VOLUME.
DENSITY.
.J
OF EXTER-
5
c
. _j
pw
NAL WORK.
"OTJ
~'^
a
S
'Z
III
1
pj
.S
P
H
o
is
5*fc
li
.11
a
|||
|||
Q ui
o
T2
H
a
!>
l
2 cA
.SoS
Qfci
H
3
PQ
H
5
w
f2
H
1
i
1
Apu
Apu
e
f
s
s
s
s
t
151
152
44.6
44.7
80.4
80.5
0.4429
0.4453
1.1870
1.1824
0.3824 5
0.3729
6.126 152
5 ' 974 48
2.615 R7
2.682
0.1632
0.1674^
303.8
305.6
153
44.8
80.6
0.4477
1.1778
0.3637JJJ
5 ' 826 H3
2.750 g
0.1716 42
307.4
154
44.8
80.7
0.4501
1.1733
0.3548 Q ,
5.6831,,,
2.818 ?0
0.1759..
309.2
155
44.9
80.9
0.4525
1.1688
0.3463!?
5 ' 546 133
2.888 'V
0.1803^
311
156
45.0
81.0
0.4549
1.1644
0.3380^
5.413 131
2.959 J*
0.1847 44
312.8
157
158
45.0
45.1
81.1
81.2
0.4573
0.4596
1.1599
1.1554
0.3298 sn
0.3218 7 "
5.282 _
5 ' 154 25
3.032 7fi
3.108 5
0.1893. 7
0.1940^g
314.6
316.4
159
45.2
81.4
0.4620
1.1509
0.3140}
5 - 029 l23
3.185 77
0.1988 5Q
318.2
160
45.3
81.5
0.4644
1.1465
0.3063 7 .
4.906 117
3.265 cn
0.2038, ft
320
161
45.3
81.6
0.4668
1.1421
0.2989'*
4.789}} 2
3.345 [{
0.2088^"
321.8
162
45.4
81.7
0.4692
1.1377
0.2920
DO
4.677 1Q6
3.425 80
0.2138^
323.6
163
45.5
81.8
0.4715
1.1333
0.2855 6 .
4.571 in9
3.503 7Q
0.2188, n
325.4
164
45.5
81.9
0.4739
1.1289
0.2792^
4 - 469 101
3.582 ' 9
0.2238^
327.2
165
45.6
82.0
0.4763
1.1245
0.2729^
63
4.368 1QO
3.664 **
0.2289^
329
166
45.6
82.1
0.4786
1.1202
0.2666 ft ,
4.268 1on
3.751 Q1
0.2343, fi
330.8
167
45.7
82.2
0.4810
1.1159
0.2603^,
4.168 10
3.842 Ji
2399^?
332 6
168
45.7
82.4
0.4833
1.1115
- 2540 60
4.070 9 5
3.937 9 g
' 2457 59
334.4
169
45.8
82.5
0.4857
1.1072
0.2480, 7
3.975 Q9
4.032
0.2516, Q
336.2
170
45.9
82.6
0.4880
1.1029
0.2423?'
3.883 g* 9
4.127 Q
0.2575^
338
171
46.0
82.7
0.4903
1.0987
0.2368JJJ
4.223 99
0,2036"
339.8
172
46.0
82.8
0.4926
1.0944
0.2314, 9
3.709 8 ,
4.322 qq
0.2696 ft9
341.6
173
46.1
82.9
0.4949
1.0901
0.2262?;:
3.626 a?
4.421
0.2758,
343.4
174
46.1
83.0
0.4972
1.0859
0.2212
3.545 g
4.521 1QO
2821
345.2
175
176
46.2
46.2
83.1
83.2
0.4995
0.5018
1.0817
1.0775
0.2164. 7
0.2117*'
3.467 7fi
3.391 7 ,
4.621
4.724 ^
0.2884 A ,
0.2949^
347
348.8
177
46.3
83.3
0.5041
1.0733
0.2072
3.318 }j
4.826^2
0.3014^
350.6
45
10i
DO
178
46.3
83.4
0.5064
1.0691
0.2027..
3.247 7ft
4.933 no
0.3080 ftc
352.4
179
46.4
83.5
0.5087
1.0649
0.1983* 9
3.177 '"
5. 04^
0.3148^
354.2
180
46.4
83.6
0.5110
1.0608
0.1941
3.109^8
5.15 12
0.3217JJ
356
181
46.5
83.7
0.5133
1.0567
0.1899. 9
3.041 fi7
5.27 n
0.3288 7 .
357.8
182
46.5
83.8
0.5156
1.0525
0-1857-
2.974 ^,
5.38j 2
0.3362',
359.6
183
46.6
83.8
0.5178
1.0484
' 1817 39
2.911 ^
5.50 12
0.3435^
361.4
184
46.6
83.9
0.5201
1.0443
0.1778, ft
2.849 fi9
5.62 3
0.3510 78
363.2
185
46.7
84.0
0.5224
1.0403
A i 7/in
2.787 ^
5 ' 75 13
0.3588 7 Q
365
186
46.7
84.1
0.5246
1.0362
:1702 36
2.727
0.3667^
366.8
187
46.8
84.2
0.5269
1.0321
0.1666,.
2.669 ,,
6.00,,
0.3746 ft
368.6
188
46.8
84.3
0.5291
1.0280
0.1632,*
2.614
6.13"
0.3826 1 ^
370.4
189
46.9
84.3
0.5314
1.0240
0.1598^ 4
2.560 g 3
6 ' 26 13
n Qonft,
372.2
190
46.9
84.4
0.5336
1.0200
0.1565 32
2.507 M
6.39 13
0.3989 g3
374
6 4
SATURATED STEAM TABLE III.
PRESSURE.
HEAT OF
THE LIQUID.
HEAT OF
VAPORIZATION.
HEAT EQUIVA-
LENT OF INTER-
NAL WORK.
.
H
*
|y|
l!i
|bf,fi|
hj
j
t>
H
i
p
E-!
J
ti
til
cQ ti
~*O W
CUBO
'aQtS
"3
PQ
3
PQ
<s
CQ
SO&H
H
9
N
AH
w
H
I
p
p
P
q
q
r
r
P
p
t
191
192
193
9612 2n
9823 2 15
10038 2 }*
13.068 9a7
13 - 355 292
13.647 292
185.87 4Q
189.96 4 ^
193.3
194.4
195.4
347.9
349.8
351.7
471.5
470.6
469.8
848.7
847.1
845.6
424.5
423.6
422.8
764.2
762.5
761.0
375.8
377.6
379.4
194
195
196
10256 99 ,
10479 226
10705 229
13.944
14 ' 247 307
14.554 3 ? 7
202^64 43 J
207. 01 J^
196.4
197.5
198.5
353.5
355.4
357.3
468.9
468.1
467.2
844.1
842.5
841.0
421.9
421.0
420.1
759.4
757.7
756.1
381.2
383
384.8
197
10934 9Q ,
14.866
211.45,,,
199.5
359.2
466.4
839.5
419.2
754.6
386.6
198
11168 238
15^184 3 J 8
2i5.96:xi
200.6
361.1
465.6
838.0
418.4
753.0
388.4
199
11406 241
15.507 323
220.56 4 ^
201.6
362.9
464.7
836.4
417.4
751.3
390.2
200
11647
15.835
225.23
202.7
364.8
463.8
834.8
416.5
749.7
392
201
11893 24Q
lo 1 o9 DO
229^98 47 9
203.7
366.7
462.9
833.3
415.6
748.1
393.8
202
12142 253
16:508^9
234.80 4 gj
204.7
368.5
462.1
831.8
414.8
746.6
395.6
203
204
12395 2 -
12653 2fi2
}?&"
1 1 . UnEj
239.71 49g
205.8
206.8
370.4
372.3
461.2
460.3
830.2
828.6
413.8
412.9
744.9
743.3
397.4
399.2
205
12915
17.558^
249^75^
207.9
374.1
459.4
827.0
412.0
741.6
401
266
OOo
514
206
207
208
13181 971
13452;;*
13727 2?9
17.921
18.289^?
18.663 374
254.89
260.13^;
265 ' 45 540
208.9
210.0
211.0
376.0
377.9
379.8
458.6
457.7
456.8
825.4
823.8
822.2
411.1
410.2
409.3
740.0
738.3
736.7
402.8
404.6
406.4
209
210
211
14006 2
14290 98fi
14578 288
19.042, RR
19 ' 428 3Q2
19.820 392
2 2 7 7 6l4 549
28i:91 566
212.0
213.1
214.1
381.6
383.5
385.4
455.9
455.0
454.1
820.6
819.1
817.4
408.4
407.5
406.6
735.1
733.6
731.9
408.2
410
411.8
212
213
214
14871 297
20.218
20.622 4 J 4
21.033;"
287.57 7
293.31^*
299.16S2
215.2
216.2
217.3
387.3
389.2
391.1
453.2
452.4
451.5
815.8
814.3
812.7
405.7
404.9
404.0
730.2
728.7
727.1
413.6
415.4
417.2
308
4iy
594
215
216
217
15778 -m
16090!^
16406 322
21.452 4
21 ' 876 430
22.306^
305.10 ftn .
311 ' 14 6?2
317 ' 26 622
218.3
219..3
220.4
392.9
394.8
396.7
450.6
449.6
448.7
811.0
809.3
807.7
403.1
402.1
401.2
725.4
723.7
722.1
419
420.8
422.6
218
219
16728 Q97
17065?;'
22.743 4
23.188 4 gJ
323 ; 48 633
221.4
222.5
398.5
400.4
447.8
446.9
806.1
804.5
400.3
399.4
720.5
718.9
424.4
426.2
220
17387 6
23.639
336. 24 643
223.5
402.3
446.0
802.9
398.5
717.3
428
SATURATED STEAM TABLE III.
HK ~
-.3
EQUIVALENT
SPECIFIC VOLUME.
DENSITY.
J
OF EXTER-
NAL \VORK.
5
g
B
fed
s|
A
1
u
i
ill
111
|
t*
P
a
!
t i
in
Hi
I|l
H
c3
P
m
tT
Q
i
M
2
H
1
Apu
Apu
e
r
T
8
i
i
1
191
192
193
47.0
47.0
47.0
84.5
84.6
84.6
0.5358
0.5381
0.5403
.0160
.0120
.0080
0.1533, 9
o.ison:
- 1470 30
2.456,.
2 ' 405 50
i.awg
6.52
6.66 4
6-80} 4
0.4072 C ,
0.4158
0.4246 88
375 8
377 6
379 4
194
195
196
47.0
47.1
47.1
84.7
84.8
84.9
0.5426
0.5448
0.5470
.0040
.0000
0.9961
0.1440 29
0.1411$
0.1382
2.306, 7
2.259%.
2 ' 214 45
6.94
7 7 :23J 4
0.4336 9Q
- 4426 90
0.4516^
381 2
383
384 8
197
198
47.2
47.2
84.9
85.0
0.5492
0.5514
0.9922
0.9882
0.1354 97
0.1327 97
2.169 43
2.126 4 *
7.38 H
7 ' 53 16
0.4610 g4
386 6
388.4
199
47.3
85.1
0.5536
0.9843
o.iaoog
9 fiCQ
7.69 15
o'.mill
390 2
200
201
47.3
47.3
85.1
85.2
0.5558
0.5580
0.9804
0.9765
0.1274 2 ,
0.1249 9 ?
2.041
2.00C"
7.84 1fi
8 00:?
0-4998 98
392
393 8
202
47.3
85.2
0.5602
0.9727
0.122524
1 962
8.16{ 7 6
0.510 J 8
395 6
203
47.4
85.3
0.5624
0.9688
0.1201 24
923
8.33 17
0.520 1t
397.4
204
47.4
85.3
0.5646
0.9650
- 1177 24
885 38
8.50 1 ;
0.531 f*
399 2
205
47.4
85.4
0.5668
0.9611
0.115323
.847 37
8.67} 7
0.541 J"
401
206
207
208
47.5
47.5
47.5
85.4
85.5
85.5
0.5690
0.5712
0.5733
0.9572
0.9534
0.9496
0.1130 99
0.110822
. O lUo/j
774 ^
739 34
8.85 lg
9.03j
0.552 2
0.564 \*
0.575
402.8
404 6
406.4
209
210
47.5
47.5
85.5
85.5
0.5755
0.5777
0.9458
0.9420
0.1065 91
0.1044;*
.705
.673^
9.39 9
9.58J5
0.587 .
0.598 "
408.2
410
211
47.5
85.5
0.5799
0.9382
0.1024$
640 32
9.77 19
0.610 ||
411.8
212
47.5
85.6
0.5820
0.9344
0.1004 9n
1 608
9.96 9n
0.622 19
413.6
213
47.5
85.6
0.5842
0.9307
0.0984f"
1 577 31
10 - 16 9n
0.634 "
415.4
214
47.5
85.6
0.5863
0.9269
0.0965J9
10.36$
0.647 J 3
417.2
215
47.5
85.6
0.5885
0.9232
0.0947 1Q
.516^
10 56 22
0.660 1Q
419
216
47.5
85.6
0.5906
0.9195
0.0928Jg
.486^
0.673 J^
420 8
217
47.5
85.6
0.5927
0.9157
0.0910 1?
^ KC 28
458 28
w^Il
0.686 ^
422 6
218
47.5
85.6
0.5948
0.9120
0.0893 17
430 97
11 20 21
0.699 .
424.4
219
220
47.5
47.5
85.6
85.6
0.59690.9084
0.5991 0.9047
0.0876!'
0.0860 10
- 403 27
1.376 27
0.713 } 4
0.727 *
26 2
428
66
PROPERTIES OF STEAM AND OTHER VAPORS.
TABLE IY.
SATURATED VAPOR OF ETHER.
FRENCH UNITS.
"S
j
g
3
i
Density.
53
1 |
j
^
I
11
||
S
3
2 |
f<
2 fl5
^ "^
?|
1
si
3 J3 .
|| |
if
1
S 8 S
III
S Q fee
3-3
"i 2
3
"i ^
1 oj
H "S ^
-^ ^
'g
- s 3 6 s
S Q bjb
H
fi
n
H
w
i
w
i
S
1
P
3
H
r
p
Apu
9
s
V
t
184.39
0.00
94.00
94.00
86.45
7.55
.0000
1.278
0.728
10
286.83
5.32
98.44
93.12
85.37
7.75
0.01909
0.8440
1.185
10
20
432.78
10.70
102.78
92.08
84.13
7.95
0.03772
0.5741
1.742
20
30
634.80
16.14
107.00
90.86
82.72
8.14
0.05593
0.4013
2.492
30
40
907.04
21.63
111.11
89.48
81.15
8.33
0.07374
0.2877
3.746
40
50
1264.8
27.19
115.11
87.92
79.41
8.51
0.09117
0.2108
4.744
50
60
1725.0
32.80
119.00
86.20
77.53
8.67
0.1083
0.1580
6.329
60
70
2304 .9
38.48
122.78
84.30
75.49
8.81
0.1250
0.1203
8.313
70
80
3022.8
44.21
126.44
82.23
73.32
8.91
0.1415
0.0932
10.73
80
90
3898.3
50.00
130.00
80.00
71.03
8.97
0.1576
0.0731
13.68
90
100
4953 .3
55.86
133.44
77.58
68.62
8.96
0.1735
0.0577
17.33
100
110
6214.6
61.77
136.78
75.01
66.13
8.88
0.1891
0.0459
21.79
110
120
7719.2
67.74
140.00
72.26
63.57
8.69
.2045
0.0364
27.47
120
PROPERTIES OF STEAM AND OTHER VAPORS.
6 7
TABLE V.
SATURATED VAPOR OF ALCOHOL.
FRENCH UNITS.
Jj
j
1
J*"
|
Density.
i
J
2 >>
s'
t
"eS "3
"3
a
3
-. -2
o
H r-
III
ill
1
g
*f
1JN
> S
if
"3
Jl'i
1"
I"
r
1
m
l ?l
r*
I 5
1
CQ
|9g*
1
'
P
a
H
r
>
Apu
8
Y
t
12.70
0.00
236.5
236.50
223 .38
13.12
.0000
32.21
0.03105
10
24.23
5.59
244.4
238.81
225 .29
13.52
0.01996
17.39
.05750
10
20
44.46
11.42
252.0
240.58
226.56
14.02
.04003
9.847
0.1016
20
30
78.52
17.49
258.0
240.51
226 .03
14.48
.06029
5.753
0.1738
30
40
133.69
23.71
262.0
238.29
223 .44
14.85
0.08073
3.465
0.2886
40
50
219.90
30.21
264.0
233 .79
218.59
15.10
0.1014
2.143
0.4666
50
60
350.21
37.37
265.0
227 .63
212.38
15.25
0.1223
1.359
.7358
60
70
541.15
44.58
265.2
220 .62
205 .28
15.34
0.1435
.8855
1.129
70
80
812.91
52.11
265.2
213.09
197.69
15.40
0.1650
0.5921
1.689
80
90
1189.3
59.97
266.0
206 .03
190.54
15.49
0.1868
.4073
2.455
90
100
1697.6
68.18
267.3
199.12
183.54
15.58
.2090
.2874
3.479
100
110
2367.6
76.74
269.6
192.86
177.15
15.71
0.2315
0.2083
4.801
110
120
3231.7
85.67
272.5
186.83
170.97
15.86
.2544
0.1544
6.477
120
130
4323 .0
94.98
276.0
181.02
164.99
16.03
.2776
0.1170
8.547
130
140
5674.6
104.70
280.5
175.80
159.55
16.25
0.3013
.0905
11.05
140
150
7318.4
114.82
285.3
170.48
154.03
16.45
.3254
0.0714
14.01
150
68
PROPERTIES OF STEAM AND OTHER VAPORS.
TABLE VI.
SATURATED VAPOR OF CHLOROFORM.
FRENCH UNITS.
.A
j
,
c
o5
Density.
5$
if
*!f
*U-
I
I
'3 fe .
||
a
"o <
"o
||
S "- 1 'S
o ^
i ii
1
B
1
ssi
wig
8
o
J |
,
S Q feb
i *o
1? ^
.*
"1 **
3 *o ^
"el *O ^
> 0)
'S 2 o s
S Q tJo
H
w
s
W
n
tS
&
i
^
H
t
p
9
JET
r
p
A P u
e
s
Y
t
59.72
0.00
67.00
67.00
62.45
4.55
.00000
2.377
.4207
10
100.47
2.33
68.38
66.04
61.29
4.75
0.00836
1.475
0.6780
10
20
160.47
4.67
69.75
65.08
60.14
4.94
0.01646
0.9601
1.042
20
30
247.51
7.02
71.12
64.10
59.00
5.10
.02432
0.6437
1.554
30
40
369 .26
9.37
72.50
63.13
57.87
5.26
0.03196
0.4449
2.248
40
50
535 .05
11.74
73.87
62.13
56.73
5.40
.03940
0.3155
3.170
50
60
755 .44
14.12
75.25
61.13
55.60
5.53
0.04664
0.2291
4.356
60
70
1042.1
16.51
76.62
60.11
54.45
5.66
0.05369
0.1700
5.88
70
80
1407.6
18.91
78.00
59.09
53.31
5.78
0.06057
0.1286
7.78
80
90
1865.2
21.32
79.37
58.05
52.16
5.89
0.06729
0.0991
10.09
90
100
2428 .5
23.74
80.75
57.01
51.01
6.00
0.07386
0.0777
12.87
100
110
3111.0
26.17
82.12
55.95
49.84
6.11
.08027
0.0618
16.18
110
120
3925.7
28.61
83.50
54.89
48.67
6.22
0.08655
0.0500
20.00
120
130
4885.1
31.06
84.87
53.81
47 .48
6.33
.09270
0.0410
24.39
130
140
6000.2
33.52
86.25
52.73
46.30
6.43
0.09872
0.0340
29.4
140
150
7280.6
35.99
87.62
51.63
45.10
6.53
0.10462
0.0286
35.0
150
160
8734.2
38.47
89.00
50.53
43.90
6.63
0.11041
0.0243
41.2
160
PROPERTIES OF STEAM AND OTHER VAPORS.
69
TABLE VIL
SATURATED VAPOR OP CARBON BISULPHIDE.
FRENCH U1SITS.
a
d
^
G
d
Density.
j<
|i
Jb
- 2*
^
o
J
> c
2*3
- g
> c
sl
j3
3
a o|
||i
3 S
I
|l
|||
3 *
O <D
i
g o s
fill
j||
i
I
W
H
a
W
W
c *^
w
i
S
i
p
q
H
r
p
A P u
6
8
Y
t
127.91
0.00
90.00
90.00
82.76
7.24
.00000
1.766
0.5662
10
198.46
2.36
91.42
89.06
81.58
7.48
.00847
1.177
0.8496
10
20
298 .03
4.74
92.76
88.02
80.31
7.71
0.01670
0.8071
1.239
20
30
434.62
7.13
94.01
86.88
78.97
7.91
.02472
0.5684
1.759
30
40
617.53
9.54
95.18
85.64
77.54
8.10
0.03252
.4098
2.440
40
50
857.07
11.96
96.27
84.31
76.04
8.27
0.04013
0.3017
3.315
50
60
1164.5
14.41
97.28
82.87
74.45
8.42
.04756
0.2264
4.417
60
70
1552.1
16.86
98.20
81.34
72.78
8.56
.05482
0.1726
5.794
70
80
2032 .5
19.34
99.04
79.70
71.03
8.67
0.06192
0.1338
7.473
80
90
2619.1
21.83
99.80
77.97
69.20
8.77
.06886
0.1052
9.51
90
100
3325.2
24.34
100.48
76.14
67.29
8.85
0.07566
0.0837
11.95
100
110
4164.1
26.86
101 .07
74.21
65.31
8.90
.08233
0.0674
14.84
110
120
5148.8
29.40
101.58
72.18
63.24
8.94
.08886
0.0549
18.21
120
130
6291 .6
31.96
102.01
70.05
61.09
8.96
.09527
.0452
22.12
130
140
7604 .0
34.53
102.36
67.83
58.88
8.95
0.10157
0.0375
26.7
140
150
9095 .9
37.12
102.62
65.50
56.58
8.92
0.10775
0.0314
31.8
150
PROPERTIES OF STEAM AND OTHER VAPORS.
TABLE VIII.
SATURATED VAPOR OF CARBON TETRACHLORIDE.
FRENCH UNITS.
Density.
i
2
1
la
11
a
1
j3
gl
3 w
3
I
1
1
S, I
_>
s|
.2 o 3
2 S
1 !
aJ" S <3
^ S
si
n
"8 8,
s" -H
B -s
j3
eg
- o gj
| |^
so g
jl*
*J O*
I 3
3
X
w
w
i
1
S JB
fall
|S6
^
P
q
H
r
P
Apu
S
v
t
fit*
32.95
0.00
52.00
52.00
48.54
3.46
.00000
3.272
.3056
10
55.97
1.99
53.44
51.45
47.85
3.60
0.00714
2.005
0.4987
10
20
90.99
3.99
54.86
50.87
47.13
3.74
0.01409
1.283
0.7794
20
30
142.27
6.02
56.23
50.21
46.33
3.88
0.02087
0.8510
1.175
30
40
214.81
8.06
57.58
49.52
45.51
4.01
.02749
0.5831
1.715
40
50
314.38
10.12
58.88
48.76
44.62
4.14
0.03396
0.4109
2.434
50
60
447 .43
12.20
60.16
47.96
43.69
4.25
.04028
.2969
3.368
60
70
621.15
14.30
61.40
47.10
42.75
4.35
.04648
0.2192
4.562
70
80
843 .29
16.42
62.60
46.18
41.74
4.44
.04255
0.1650
6.061
80
90
1122.3
18.55
63.77
45.22
40.50
4.72
0.05849
0.1263
7.92
90
100
1467.1
20.70
64.90
44.20
39.62
4.58
0.06433
0.0980
10.20
100
110
1887.4
22.87
66.01
43.14
38.52
4.62
.07006
0.0770
12.99
110
120
2393.7
25.06
67.07
42.01
37.36
4.65
0.07569
0.0611
16.37
120
130
2996.9
27.27
68.10
40.83
36.18
4.65
0.08122
,0490
20.41
130
140
3709 .0
29.49
69.10
39.61
34.95
4.63
0.08666
0.0395
25.3
140
150
4543.1
31.73
70.07
38.34
33.75
4.59
0.09201
0.0321
31.2
150
160
5513.1
34.00
71.00
37.00
32.47
4.53
.09729
.0262
38.2
160
PROPERTIES OF STEAM AND OTHER VAPORS.
TABLE IX.
SATURATED VAPOR OF ACBTON.
FRENCH UNITS.
-
Density.
I
2 b
d
"a
ll
- TJ
3
1
- 0}
"5 3
5-d
"3
B
1 c
| |
* 1
"o
S *o S
=3
ill
ill
*1
a
= 1
11 1
tS-g
*". 3'
ill
in &
83*
is
3
i >
i * ^
**
1
s 3 o s
S Q )
S
fi
K
H
H
1
B
1
$
1
P
5
H
r
P
*
6
8
y
t
63.33
0.00
140 .50
140 .50
131 .82
8.68
.00000
4.275
.2339
10
110.32
5.10
144.11
139.01
129.51
9.50
0.01832
2.686
0.3723
10
20
180.08
10.29
147.62
137.33
127.16
10.17
0.03627
1.758
0.5688
20
30
280 .05
15.55
151.03
135.48
124.83
10.65
.05389
1.187
.8425
30
40
419.35
20.89
154.33
133.44
121.39
11.05
0.07119
0.8227
1.215
40
50
608.81
26.31
157.53
131.22
119.86
11.36
.08820
0.5830
1.715
50
60
860.96
31.81
160.63
128.82
117.22
11.60
0.1049
0.4215
2.372
60
70
1189.9
37.39
163.62
126.23
114.43
11.80
0.1214
0.3106
3.220
70
80
1611.1
43.05
166.51
123.46
111.49
11.97
0.1376
0.2328
4.296
80
90
2140.8
48.79
169.30
120.51
108.41
12.10
0.1536
0.1773
5.640
90
100
2796.2
54.61
171.98
117.37
105.17
12.20
0.1694
0.1372
7.289
100
110
3594.3
60.50
174.56
114.06
101.78
12 -.28
0.1850
0.1076
9.294
110
120
4552.0
66.48
177.04
110.56
98.23
12.33
.2004
0.0856
11.68
120
130
5684.9
72.54
179.42
106 .88
94.53
12.35
0.2156
.0689
14.51
130
140
7007 .6
78.67
181.69
103.02
90.67
12.35
0.2306
0.0561
17.83
140
PROPERTIES OF STEAM AND OTHER VAPORS.
TABLE X.
SATURATED VAPOR OF AMMONIA.
ENGLISH UNITS.
(
d
0)
aJ
Density.
,
M
M pfl
.2
.a
ifl
1 8 *
*
03
tl
1
11
IE
S .
I
.2 1!
3~ w
if 1
il
1
A
3 <3 .
ffg-g
3 .
Il
o
ca
{-H r-j (D Q
1 1
SO 1
pi
1
1 1>
1 o ^
1 o |l
P
I
ill!
E P
H
1
w
B
jiq
H
02
^
H
'
p
g.
H
r
p
Apu
6
s
y
t
-40
9.93
-79
519
598
550
48
-0.1737
26.1
0.0383
-40
-35
11.53
-74
520
594
546
48
-0.1607
22.6
.0442
-35
-30
13.36
-68
522
590
541
49
-0.1482
19.7
0.0507
-30
-25
15.40
-63
523
586
537
49
-0.1354
17.3
0.0580
-25
-20
17.70
-57
525
582
532
50
-0.1229
15.2
0.0660
-20
-15
20.25
-52
526
578
528
50
-0.1102
13.3
0.0750
-15
-10
23.10
-46
528
574
524
50
-0.0982
11.8
.0848
-10
-5
26.25
-41
529
570
519
51
-0.0859
10.5
0.0956
-5
29.74
-35
531
566
515
51
-0.0738
9.32
0.108
5
33.58
-30
532
562
511
51
-0.0619
8.31
0.120
5
10
37.80
-24
534
558
506
52
-0.0501
7.44
0.134
10
15
42.43
-19
535
554
502
52
-0.0386
6.68
0.150
15
20
47.49
-13
537
550
497
53
-0.0271
6.02
0.166
20
25
53.01
-8
538
546
493
53
-0.0157
5.43
0.184
25
30
59.01
-2
540
542
489
53
-0.0044
4.92
0.203
30
35
65.53
3
541
538
484
54
.0067
4.46
0.225 .
35
40
72.59
9
543
534
480
54
0.0177
4.06
0.247
40
45
80.21
14
544
530
475
55
.0287
3.70
0.270
45
50
88.44
20
546
526
471
55
0.0395
3.38
0.296
50
55
97.30
25
547
522
467
55
0.0502
3.09
0.323
55
60
106.82
31
549
518
462
56
.0608
2.84
0.352
60
65
117.04
36
550
514
458
56
0.0713
2.61
0.383
65
70
'127.98
42
552
510
454
56
0.0817
2.40
0.416
70
75
139.67
47
553
506
449
57
0.0921
2.22
.451
75
80
152.15
53
555
502
445
57
0.1023
2.05
0.488
80
85
165.47
58
556
498
441
57
0.1124
1.90
0.527
85
90
179.64
64
558
494
436
58
0.1224
1.76
0.568
90
95
194.70
69
559
490
432
58
0.1324
1.63
0.612
95
100
210.70
75
561
486
428
58
0.1423
1.52
0.657
100
PROPERTIES OF STEAM AND OTHER VAPORS.
73
TABLE XI.
SATURATED VAPOR OP SULPHUR DIOXIDR
ENGLISH UNITS.
JB
1
1
i
Density.
.a
&i
jB
3
1
Is
11
"8
5 0-2
-.0
|* i
P I 'I
1 J |
?!
1
if
3 fc .
srS-g
IjN
a
Is
-^
g If
HQ!
ill
if
1
i*
*a
"o 1 ^
H
1
IIII
l(t|
H
w
H
H
H
W
3
in
s
t
p
<7
H
r
p
Apu
8
y
1
-40
3.14
-29
166
195
182
13
-0.0632
23.0
.0434
-40
-35
3.70
-27
167
194
180
14
-0.0584
19.7
.0507
-35
-30
4.34
-25
168
193
179
14
-0.0539
17.0
.0590
-30
-25
5.07
-23
168
191
177
14
-0.0492
14.7
.0682
-25
-20
5.90
-21
169
190
176
14
-0.0447
12.7
.0785
-20
-15
6.83
-19
170
189
175
14
-0.0401
11.1
.0901
-15
-10
7.88
-17
170
187
173
14
-0.0357
9.73
0.103
-10
-5
9.05
-15
171
186
172
14
-0.0312
8.56
0.117
-5
10.35
-13
172
185
170
15
-0.0268
7.54
0.133
5
11.81
-11
172
183
168
15
-0.0225
6.67
0.450
5
10
13.41
-9
173
182
167
15
0.0182
5.93
0.169
10
15
15.19
-7
174
181
166
15
-0.0140
5.29
0.189
15
20
17.15
-5
174
179
164
15
-0.0098
4.72
0.212
20
25
19.30
-3
175
178
163
15
-0.0057
4.23
0.236
25
30
21.66
-1
176
177
162
15
-0.0016
3.81
0.263
30
35
24.24
1
176
175
160
15
.0024
3.43
0.291
35
40
27.06
3
177
174
158
16
.0064
3.10
0.322
40
45
30.12
5
177
172
156
16
0.0104
2.81
0.356
45
50
33.45
7
178
171
155
16
0.0144
2.58
0.390
50
55
37.07
9
179
170
154
16
0.0182
2.32
0.430
55
60
40.98
11
179
168
152
16
0.0221
2.11
0.473
60
65
45.20
13
180
167
151
16
.0259
1.94
0.516
65
70
49.75
15
181
166
150
16
.0297
1.78
0.563
70
75
54.64
17
181
164
148
16
.0334
1.63
0.614
75
80
59.90
19
182
163
146
17
.0372
1.50
0.668
80
85
65.54
21
183
162
145
17
.0409
1.38
0.725
85
90
71.57
23
183
160
143
17
.0445
1.27
0.786
90
95
78.02
25
184
159
142
17
.0482
1.18
0.849
95
100
84.90
27
185
158
141
17
0.0518
1.09
0.917
100
74
PROPERTIES OF STEAM AND OTHER VAPORS.
TABLE XII.
SPECIFIC GRAVITY AND SPECIFIC VOLUME OF LIQUIDS.
Name of Liquid.
Specific Gravity, compared with Water
at 4 C.
Specific Volume.
Cubic Meters
per Kilo.
Alcohol, C 2 H O . .
.80625
0.736
1.527
1 .2922
1 .6320
0.81
1 .4336
0.6364
'Mendelejeff, 1869] . .
"Kopp, 1860]
0.001240
0.001358
.000655
.000774
0.000613
0.00123
.0006981
0.001571
Ether, C 4 H 10 O
Chloroform
Thorpe, 1880] . . .
Thorpe, 1880] . . .
Thorpe, 1880] . . .
"Zander, 1882] . . .
"Andre'eff, 1859] . . .
"Andreeff, 1859] . . .
Carbon bisulphide, CS 2 ....
Carbon tetrachloride, CC1 4 . .
Aceton, CgtLO
Sulphur Dioxide, SO 2
Ammonia NH 3
TABLE XIII.
VOLUME OF 'WATER
Vol. at 4 C. =1.
[Rossetti, 1871] and [Him, 1867].
Temper-
ature .
Volume.
Temper-
ature.
Volume.
Temper-
ature.
Volume.
Temper-
ature.
Volume.
10
1 .000253
60
1.01691
110
1 .0512
160
.1018
20
1 .001744
70
1 .02256
120
1 .0599
170
.1139
30
1 .00425
80
1 .02887
130
1 .0694
180
.1268
40
1 .00770
90
1 .03567
140
1 .0795
190
.1403
50
1.01195
100
1 .04312
150
1 .0903
200
.1544
PROPERTIES OF STEAM AND OTHER VAPORS.
75
TABLE XIV.
CONVERSION TABLE.
INCHES OF MERCURY AND POUNDS PER SQUARE INCH.
1
2
3
4
5
6
7
8
9
1
2
0.00
0.49
0.98
0.05
0.54
1.03
0.10
0.59
1.08
0.15
0.64
1.13
0.20
0.69
1.18
0.25
0.74
1.23
0.29
0.79
1.28
0.34
0.84
1.33
0.39
0.88
1.38
0.44
0.93
1.42
3
4
5
1.47
1.96
2.46
1.52
2.01
2.51
1.57
2.06
2.55
1.62
2.11
2.60
1.67
2.16
2.65
1.72
2.21
2.70
1.77
2.26
2.75
1.82
2.31
2.80
1.87
2.36
2.85
1.91
2.41
2.90
e
7
8
2.95
3.44
3.93
3.00
3.49
3.98
3.05
3.54
4.03
3.09
3.59
4.08
3.14
3.63
4.13
3.19
3.68
4.18
3.24
3.73
4.22
3.29
3.78
4.27
3.34
3.83
4.32
3.39
3.88
4.37
9
10
11
4.42
4.91
5.40
4.47
4.96
5.45
4.52
5.01
5.50
4.57
5.06
5.55
4.62
5.11
5.60
4.67
5.16
5.65
4.72
5.21
5.70
4.76
5.26
5.75
4.81
5.30
5.80
4.86
5.35
5.85
12
13
14
5/89
6.39
6.88
5.94
6.43
6.93
5.99
6.48
6.97
6.04
6.53
7.02
6.09
6.58
7.07
6.14
6.63
7.12
6.19
6.68
7.17
6.24
6.73
7.22
6.29
6.78
7.27
6.34
-6.83
7.32
15
16
17
7.37
7.86
8.35
7.42
7.91
8.40
7.47
7.96
8.45
7.52
8.01
8.50
7.56
8.06
8.55
7.61
8.10
8.60
7.66
8.15
8.64
7.71
8.20
8.69
7.76
8.25
8.74
7.81
8.30
8.79
18
19
20
8.84
9.33
9.82
8.89
9.38
9.87
8.94
9.43
9.92
8.99
9.48
9.97
9.04
9.53
10.02
9.09
9.58
10.07
9.14
9.63
10.12
9.19
9.68
10.17
9.23
9.73
10.22
9.28
9.77
10.27
21
22
23
10.32
16.81
11.30
10.37
10.86
11.35
10.41
10.90
11.40
10.46
10.95
11.44
10.51
11.00
11.49
10.56
11.05
11.54
10.61
11.10
11.59
10.66
11.15
11.64
10.71
11.20
11.69
10.76
11.25
11.74
24
25
26
11.79
12.28
12.77
11.84
12.33
12.82
11.89
12.38
12.87
11.94
12.43
12.92
11.99
12.48
12.97
12.03
12.53
13.02
12.08
12.57
13.07
12.13
12.62
13.11
12.18
12.67
13.16
12.23
12.72
13.21
27
28
29
13.26
13.75
14.24
13.31
13.80
14.29
13.36
13.85
14.34
13.41
13.90
14.39
13.46
13.95
14.44
13.51
14.00
14.49
13.56
14.05
14.54
13.61
14.10
14.59
13.66
14.15
14.64
13.70
14.20
14.69
30
14.74
14.78
14.83
14.88
14.93
14.98
15.03
15.08
15.13
15.18
7 6
PROPERTIES OF STEAM AND OTHER VAPORS-
TABLE XV.
CORRECTIVE FACTORS FOR SUPERHEATED STEAM.
Values of the factor 150 ' 3 W' OOQ - 0.0833.
Temperature.
Value,
of
Factor.
Temperature.
Value,
of
Factor.
Temperature.
Value
of
Factor.
Fahr.
Abs.
Fahr.
Abs.
Fahr.
Abs.
200
659.5
0.441
335
794.5
0.216
470
929.5
0.104
205
664.5
0.429
340
799.5
0.211
475
934.5
0.101
210
669.5
0.417
345
804.5
0.205
480
939.5
0.098
215
674.5
0.405
350
809.5
0.200
485
944.5
0.095
220
679.5
0.395
355
814.5
0.195
490
949.5
0.092
225
684.5
0.385
360
819.5
0.190
495
954.5
0.090
230
689.5
0.375
365
824.5
0.185
500
959.5
0.087
235
694.5
0.365
370
829.5
0.180
505
964.5
0.084
240
699.5
0.356
375
834.5
0.175
510
969.5
0.082
245
704.5
0.347
380
839.5
0.171
515
974.5
0.079
250
709.5
0.338
385
844.5
0.166
520
979.5
0.077
255
714.5
0.329
390
849.5
0.162
525
984.5
0.074
260
719.5
0.320
395
854.5
0.158
530
989.5
0.072
265
724.5
0.312
400
859.5
0.153
535
994.5
0.070
270
729.5
0.304
405
864.5
0.149
540
999.5
0.067
275
734.5
0.296
410
869.5
0.145
545
1004.5
0.065
280
739.5
0.288
415
874.5
0.141
550
1009 .5
0.063
285
744.5
0.281
420
879.5
0.138
555
1014.5
0.061
290
749.5
0.274
425
884.5
0.134
560
1019.5
0.059
295
754.5
0.267
430
889.5
0.131
565
1024.5
0.057
300
759.5
0.260
435
894.5
0.127
570
1029 .5
0.055
305
764.5
0.253
440
899.5
0.123
575
1034.5
0.053
310
769.5
0.247
445
904.5
0.120
580
1039.5
0.051
315
774.5
'0.240
450
909.5
0.117
585
1044.5
0.049
320
779.5
0.234
455
914.5
0.113
590
1049 .5
0.047
325
784.5
0.228
460
919.5
0.110
595
1054.5
0.045
330
789.5
0.222
465
924.5
0.107
TEMPERATURE-ENTROPY TABLE
THIS table gives the properties of moist and of superheated steam at
each degree of temperature Fahrenheit, and for each hundredth of a unit
of entropy.
At the left hand of each page are given the temperatures and the corre-
sponding pressures of saturated steam; the lines across the tables are,
therefore, constant pressure lines, and for moist steam are also constant
temperature lines.
The table is divided by a broken line which corresponds roughly to the
saturation line; properties to the left of that line are for moist steam and
to the right are for superheated steam.
The triple-columns are headed with the entropy, and are constant
entropy lines; they can be used for solving problems concerning adiabatic
operations in a closed cylinder, and similar problems.
At any point in the table, determined by the entropy and the pressure
(or the corresponding temperature of saturated steam), there are given
three properties :
(1) The quality, which for moist steam is the proportion of a pound
that is steam, and for superheated steam is the number of degrees of super-
heating.
(2) The heat contents, or the number of thermal units required to change
a pound of water at freezing into steam at the given pressure and with the
given quality.
(3) The specific volume in cubic feet per pound.
For examples, solved by aid of the table, see page 32.
77
TEMPERATURE-ENTROPY TABLE.
tj
TJ
c
1.52
1.53
1.54
1.55
oJ 3
g 1 ^
O u
ft, *
S
_ 3
c
d
c
g
a
&
I
|*^
a I
|
o 42
I i
>>
II
o g
< 1
I&5
23
03
m
23
i^
1
23
>
1
23
8,^"
H
5
B
OQ
a
B
$
0"
W
02
o-
H
co
420
308.5
10.7
1212.5
1.535
23.1
1221.2
1.569
36.5
1230.4
1.609
50.7
1239.6
1.651
419
305.1
9.7
1211.5
1.548
22.0
1220.3
1.584
35.4
1229.4
1.622
49.6
1238.5
1.665
418
301.8
8.6
1210.5
1.562
21.0
1219.3
1.599
34.3
1228.4
1.637
48.4
1237.5
1.679
417
298.5
7.6
1209.5
1.576
19.9
1218.4
1.612
33.1
1227.4
1.652
47.2
1236.5
1.694
416
295.2
6.6
1208.6
1.589
18.8
1217.5
1.626
32.0
1226.4
1.667
45.9
1235.5
1.709
415
292.0
5.5
1207.6
1.603
17.7
1216.5
1.640
30.8
1225.4
1.681
44.7
1234.5
1.723
414
288.9
4.5
1206.6
1.617
16.6
1215.5
.655
29.7
1224.4
1.696
43.5
1233.5
1.738
413
285.7
3.4
1205.6
1.632
15.4
1214.4
.670
28.5
1223.4
1.711
42.3
1232.5
1.753
412
282.5
2.4
1204.7
1.645
14.3
1213.4
.685
27.3
1222.4
1.724
41.2
1231.5
1.768
411
279.4
1.3
1203.8
1.660
13.2
1212.4
.700
26.2
1221.5
1.740
40.0
1230.5
1.783
410
276.3
0.3
1202.9
1.674
12.2
1211.5
.715
25.1
1220.5
1.754
38.8
1229.5
1.799
409
273.3
9994
1201.9
1.690
11.1
1210.5
1.730
23.9
1219.5
1.770
37.6
1228.4
1.814
403
270.3
9984
1201.0
1.706
10.0
1209.6
1.745
22.7
1218.5
1.786
36.4
1227.4
1.830
407
267.3
9974
1200.0
1.723
9.0
1208.7
1.760
21.6
1217.5
1.802
35.1
1226.4
1.845
406
264.3
9966
1199.2
1.741
7.9
1207.7
1.776
20.5
1216.5
1.819
33.9
1225.4
1.861
405
261.3
9956
1198.2
1.759
6.8
1206.7
1.791
19.3
1215.5
1.834
32.7
1224.4
1.877
404
258.4
9947
1197.3
1.777
5.7
1205.7
1.808
18.2
1214.6
1.850
31.5
1223.4
1.894
403
255.5
9937
1196.3
1.795
4.6
1204.7
1.823
17.1
1213.7
1.865
30.3
1222.4
1.910
402
252.6
9928
1195.3
1.813
3.5
1203.8
1.839
16.0
1212.7
1.882
29.1
1221.4
1.927
401
249.7
9918
1194.3
1.832
2.4
1202.9
1.856
14.9
1211.8
1.899
27.9
1220.4
1.944
400
246.9
9907
1193.4
1.851
1.3
1202.0
1.873
13.8
1210.8
1.915
26.7
1219.4
1.961
399
244.1
9899
1192.4
1.870
0.2
1201.0
1.890
12.7
1209.8
1.931
25.5
1218.4
1.978
398
241.4
9889
1191.5
1.889
9993
1200.0
1.909
11.5
1208.8
1.950
24.3
1217.4
1.995
397
238.6
9881
1190.6
1.908
9984
1199.1
1.928
10.4
1207.9
1.968
23.1
1216.4
2.013
396
235.9
9871
1189.6
1.928
9974
1198.1
1.948
93
1206.9
1.985
21.9
1215.4
2.030
395
233.2
9862
1188.6
1.948
9965
1197.2
1.968
8.1
1206.0
2.002
20.7
1214.4
2.049
394
230.5
9852
1187.7
1.967
9955
1196.3
1.988
7.0
1205.0
2.020
19.5
1213.4
2.068
393
227.9
9843
1186.7
1.987
9945
1195.3
2.008
5.9
1204.0
2.039
18.3
1212.4
2.087
392
225.2
9835
1185.8
2.007
9937
1194.3
2.028
4.8
1203.0
2.058
17.1
1211.4
2.105
391
222.6
9825
1184.8
2.028
9927
1193.3
2.049
3.7
1202.0
2.076
15.9
1210.4
2.124
390
220.1
9816
1183.9
2.049
9917
1192.3
2.071
2.6
1201.0
2.095
14.7
1209.3
2.144
389
217.5
9806
1182.9
2.071
9907
1191.4
2.092
1.5
1200.0
2.115
13.5
1208.3
2.163
388
215.0
9798
1181.9
2.093
9899
1190.4
2.114
0.3
1198.9
2.135
12.3
1207.3
2.183
387
212.5
9788
1180.9
2.114
9889
1189.4
2.136
9990
1197.8
2.158
11.1
1206.3
2.203
386
210.0
9779
1179.9
2.136
9879
1188.4
2.158
9980
2.180
9.9
1205.3
2.223
385
207.5
9769
1179.0
2.158
9870
1187.4
2.180
9970
1195^8
2.202
8.7
1204.3
2.244
384
205.1
9761
1178.0
2.181
9861
1186.5
2.203
9962
1194.8
2.225
7.5
1203.3
2.265
383
202.6
9752
1177.1
2.203
9852
1185.5
2.226
9952
1193.9
2.248
6.3
1202.3
2.286
382
200.3
9743
1176.1
2.226
9843
1184.4
2.249
9943
1192.9
2.272
5.1
1201.3
2.308
381
197.9
9734
1175.1
2.251
9833
1183.5
2.274
9933
1191.9
2.297
3.9
1200.3
2.329
380
195.5
9724
1174.2
2.274
9823
1182.6
2.298
9923
1190.9
2.321
2.7
1199.3
2.351
379
193.2
9716
1173.2
2.299
9815
1181.6
2.322
9914
1190.0
2.346
1.5
1198.3
2.373
378
190.9
9705
1172.2
2.323
9804
1180.6
2.347
9903
1189.0
2.371
0.3
1197.3
2.394
377
188.6
9696
1171.2
2.348
9795
1179.6
2.372
9893
1188.0
2.396
9992
1196.3
2.420
376
186.3
9687
1170.2
2.374
9786
1178.6
2.397
9884
1187.0
2.422
9983
1195.3
2.446
375
184.1
9679
1169.2
2.399
9777
1177.5
2.423
9876
1185.9
2.447
9974
1194.2
2.472
374
181.9
9671
1168.3
2.426
9769
1176.5
2.449
9867
1184.9
2.474
9965
1193.2
2.498
373
179.7
9661
1167.3
2.451
9759
1175.5
2.475
9857
1183.9
2.500
9955
1192.2
2.524
TEMPERATURE-ENTROPY TABLE.
Temperatures,
Degrees Fahr. |
1
|
*a
E b 5
gSLS
1.56
1.57
1.58
1.59
>>
1
6 3
jj
,1
>
1
63
JJ
il
do
1
<
6 3
*j O
|J
,1
I*
OQ
>>
a
a
6 3
11
n
|J
||
02
420
419
418
308.5
305.1
301.8
66.1
64.9
63.6
1248.8
1247.7
1246.7
1.692
1.705
1.720
82.7
81.4
80.0
1258.3
1257.2
1256.2
1.739
1.753
1.768
100.5
99.0
97.5
1267.8
1266.7
1265.6
1.784
1.799
1.814
118.9
117.4
115.9
1277.7
1276.6
1275.6
1.830
1.845
1.861
417
416
415
298.5
295.2
292.0
62.3
61.0
59.7
1245.6
1244.6
1243.5
1.735
1.750
1.765
78.7
77.3
76.0
1255.1
1254.1
1253.1
1.783
1.799
1.814
96.0
94.6
93.1
1264.5
1263.4
1262.3
1.829
1.844
1.859
114.4
112.9
111.4
1274.5
1273.5
1272.4
1.877
1.893
1.909
414
413
412
288.9
285.7
282.5
58.4
57.1
55.9
1242.5
1241.5
1240.5
1.781
1.796
1.812
74.7
73.3
72.0
1252.0
1251.0
1250.0
1.829
1.844
1.859
91.7
90.3
88.9
1261.3
1260.3
1259.3
1.875
1.890
1.906
109.9
108.3
106.8
1271.3
1270.2
1269.1
.926
.942
.958
411
410
409
279.4
276.3
273.3
54.6
53.3
52.1
1239.5
1238.4
1237.4
1.827
1.843
1.858
70.7
69.4
68.0
1248.9
1247.9
1246.9
1.875
1.891
1.906
87.4
86.0
84.6
1258.2
1257.2
1256.1
1.922
1.939
1.954
105.3
103.9
102.4
1268.1
1267.1
1266.0
.975
.992
2.009
408
407
406
270.3
267.3
264.3
50.8
49.5
48.3
1236.4
1235.4
1234.4
1.874
1.891
1.907
66.6
65.3
64.0
1245.8
1244.8
1243.8
1.923
1.940
1.956
83.2
81.8
80.3
1255.1
1254.1
1253.1
1.971
1.988
2.003
100.9
99.4
97.9
1264.9
1263.8
1262.7
2.025
2.043
2.060
405
404
403
261.3
258.4
255.5
46.9
45.6
44.4
1233.4
1232.3
1231.3
1.924
1.940
1.957
62.6
61.3
59.9
1242.6
1241.5
1240.4
1.972
1.989
2.006
78.9
77.5
76.0
1252.1
1250.9
1249.7
2.021
2.039
2.056
96.4
94.9
93.4
1261.6
1260.5
1259.4
2.078
2.095
2.113
402
401
400
252.6
249.7
246.9
43.1
41.8
40.6
1230.3
1229.3
1228.3
1.974
1.991
2.009
58.5
57.1
55.8
1239.4
1238.3
1237.3
2.023
2.040
2.058
74.5
73.0
71.6
1248.6
1247.5
1246.4
2.074
2.093
2.110
91.9
90.4
88.9
1258.4
1257.3
1256.2
2.131
2.150
2.168
399
398
397
244.1
241.4
238.6
39.3
38.0
36.7
1227.2
1226.2
1225.1
2.027
2.045
2.064
54.5
53.1
51.8
1236.3
1235.2
1234.2
2.077
2.095
2.113
70.3
68.9
67.5
1245.3
1244.3
1243.3
2.129
2.148
2.167
87.5
86.0
84.5
1255.2
1254.1
1253.0
2.187
2.205
2.224
396
395
394
235.9
233.2
230.5
35.5
34.3
33.0
1224.
1223.
1222.
2.082
2.101
2.120
50.4
49.1
47.8
1233-2
1232.1
1231.0
2.131
2.150
2.169
66.0
64.7
63.3
1242.3
1241.2
1240.2
2.186
2.205
2.224
83.0
81.5
80.1
1251.9
1250.8
1249.7
2.243
2.263
2.282
393
392
391
227.9
225.2
222.6
31.8
30.6
29.3
1221.
1220.
1219.0
2.138
2.157
2.178
46.4
45.0
43.7
1230.0
1229.0
1227.9
2.188
2.208
2.227
61.9
60.5
59.2
1239.1
1238.0
1237.0
2.244
2.263
2.283
78.6
77.1
75.7
1248.6
1247.5
1246.4
2.303
2.323
2.343
390
389
388
220.1
217.5
215.0
28.0
26.7
25.5
1218.0
1217.0
1216.0
2.198
2.217
2.236
42.4
41.1
39.8
1226.9
1225.9
1224.8
2.247
2.268
2.289
57.9
56.5
55.0
1235.9
1234.8
1233.8
2.304
2.325
2.346
74.2
72.7
71.2
1245.3
1244.2
1243.1
2.363
2.384
2.405
387
386
385
212.5
210.0
207.5
24.3
23.0
21.8
1215.0
1213.9
1212.8
2.257
2.278
2.299
38.4
37.0
35.7
1223.7
1222.7
1221.6
2.310
2.331
2.352
53.6
52.3
50.9
1232.7
1231.6
1230.6
2.367
2.389
2.410
69.8
68.3
66.8
1242.0
1240.9
1239.8
2.427
- 2.449
2.470
384
383
382
205.1
202.6
200.3
20.5
19.3
18.0
1211.8
1210.8
1209.8
2.320
2.341
2.362
34.4
33.0
31.7
1220.5
1219.5
1218.4
2.374
2.395
2.418
49.6
48.1
46.7
1229.6
1228.5
1227 .4
2.432
2.454
2.476
65.3
63.8
62.3
1238.7
1237.6
1236.5
2.493
2.516
2.539
381
380
379
197.9
195.5
193.2
16.8
15.6
14.3
1208.7
1207.7
1206.7
2.384
2.406
2.429
30.4
29.1
27.8
1217.4
1216.3
1215.3
2.440
2.463
2.486
45.4
43.9
42.6
1226.4
1225,3
1224.2
2.500
2.523
2.546
60.8
59.4
57.9
1235.4
1234.3
1233.2
2.561
2.585
2.609
378
377
376
190.9
188.6
186.3
13.0
11.8
10.5
1205.6
1204.6
1203.6
2.452
2.474
2.497
26.4
25.1
23.8
1214.2
1213.1
1212.1
2.509
2.533
2.557
41.3
39.9
38.5
1223.2
1222.1
1221.0
2.570
2.594
2.619
56.4
55.0
53.5
1232.1
1230.9
1229.7
2.633
2.658
2.682
375
374
373
184.1
181.9
179.7
9.3
8.0
6.8
1202.6
1201.6
1200.6
2.520
2.544
2.568
22.5
21.1
19.8
1211.1
1210.1
1209.0
2.581
2.605
2.630
37.1
35.7
34.3
1219.9
1218.8
1217.6
2.643
2.668
2.694
52.0
50.6
49.1
1228.6
1227.5
1226.4
2.707
2.732
2.758
80
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
i-ih-iv-i Pressure, Pounds!
^3 & Square
to CO Or
1.52
1.53
1.54
1.55
j>>
1
li
2
B
<v
s!
F
02
>,
<
la
^ a
2*
aj
si
F
OQ
>,
Of
la
-j a
23
d
ll
||
GO
_>.
1
J*
11
W
4
3 2.
l>
CQ
372
371
370
9653
9644
9635
1166.3
1165.3
1164.3
2.478
2.504
2.531
9751
9741
9732
1174.6
1173.6
1172.6
2.502
2.529
2.556
9848
9838
9830
1182.9
1181.9
1180.9
2.527
2.554
2.581
9946
9936
9927
1191.2
1190.2
1189.1
2 . 552
2.579
2.607
369
368
367
171.1
169.0
166.9
9626
9617
9608
1163.3
1162.3
1161.3
2.559
2.587
2.615
9723
9714
9705
1171.6
1170.6
1169.
2.583
2.612
2.641
9820
9811
9801
1179.9
1178.9
1177.8
2.609
2.638
2.667
9917
9908
9898
1188.1
1187.1
1186.0
2.635
2.664
2.693
366
365
364
164.8
162.8
160.8
9600
9590
9582
1160.3
1159.3
1158.3
2.645
2.674
2.704
9696
9686
9678
1168.
1167.
1166.
2.670
2.701
2.731
9792
9783
9774
1176.8
1175.8
1174.8
2.697
2.726
2.757
9889
9879
9870
1185.0
1184.0
1183.0
2.723
2.753
2.784
363
362
361
158.8
156.8
154.8
9572
9564
9556
1157.3
1156.3
1155.3
2.735
2.765
2.796
9668
9660
9651
1165.
1164.
1163.
2.762
2.793
2.824
9764
9755
9746
1173.7
1172.7
1171.7
2.789
2.819
2.851
9860
9851
9841
1182.0
1181.0
1179.9
2.816
2.847
2.879
360
359
358
152.9
151.0
149.1
9546
9538
9529
1154.3
1153.3
1152.3
2.826
2.859
2.891
9641
9633
9624
1162.
1161.
1160.
2.855
2.887
2.920
9736
9728
9719
1170.7
1169.7
1168.6
2.883
2.914
2.948
9832
9823
9813
1178.9
1177.9
1176.8
2.910
2.943
2.976
357
356
355
147.2
145.3
143.5
9520
9512
9503
1151.3
1150.3
1149.3
2.925
2.958
2.992
9614
9606
9597
1159.
1158.
1157.
2.954
2.987
3.021
9709
9700
9692
1167.6
1166.6
1165.6
2.982
3.016
3.050
9803
9795
9786
1175.8
1174.7
1173.7
3.011
3.045
3.080
354
353
352
141.6
139.8
138.0
9494
9486
9477
1148.3
1147.3
1146.2
3.025
3.059
3.093
9588
9579
9571
1156.
1155.
1154.
3.055
3.089
3.124
9682
9673
9664
1164.6
1163.
1162.
3.085
3.120
3.154
9776
9767
9758
1172.7
1171.7
1170.6
3.114
3.149
3.184
351
350
349
136.3
134.5
132.8
9468
9459
9451
1145.2
1144.2
1143.2
3.127
3.162
3.198
9561
9552
9544
1153.
1152.
1151.
3.158
3.193
3.230
9654
9645
9637
1161.
1160.
1159.
3.189
3.224
3.261
9748
9739
9730
1169.5
1168.5
1167.4
3.219
3.254
3.291
348
347
346
131.1
129.4
127.7
9443
9434
9426
1142.2
1141.2
1140.2
3.235
3.272
3.310
9535
9527
9518
1150.
1149.
1148.
3.267
3.304
3.342
9628
9619
9611
1158.
1157.
1156.
3.299
3.336
3.374
9721
9712
9703
1166.4
1165.4
1164.3
3.329
3.367
3.406
345
344
343
126.0
124.4
122.7
9417
9408
9400
1139.1
1138.1
1137.1
3.348
3.387
3.427
9509
9500
9492
1147.
1146.
1145.1
3.380
3.420
3.461
9601
9592
9583
1155.
1154.
1153.1
3.413
3.453
3.494
9693
9684
9675
1163.2
1162.2
1161.1
3.445
3.486
3.527
342
341
340
121.1
119.5
117.9
9391
9383
9375
1136.1
1135.0
1134.0
3.467
3.507
3.548
9483
9474
9466
1144.1
1143.0
1142.0
3.501
3.542
3.583
9574
9566
9557
1152.1
1151.0
1150.0
3.535
3.576
3.617
9666
9657
9648
1160.1
1159.0
1158.0
3.569
3.610
3.652
339
338
337
116.3
114.8
113.3
9366
9357
9349
1133.0
1131.9
1130.9
3.591
3.634
3.679
9457
9448
9439
1140.9
1139.9
1138.8
3.626
3.669
3.714
9548
9538
9530
1148.9
1147.9
1146.8
3.661
3.705
3.750
9639
9629
9620
1156.9
1155.8
1154.8
3.696
3.740
3.786
336
335
334
111.7
110.3
108.8
9340
9332
9323
1129.8
1128.8
1127.8
3.723
3.769
3.8-16
9430
9422
9413
1137.8
1136.8
1135.8
3.759
3.805
3.853
9521
9512
9503
1145.7
1144.7
1143.7
3.795
3.842
3.890
9611
9602
9593
1153.7
1152.6
1151.6
3.831
3.878
3.926
333
332
331
107.3
105.8
104.4
9315
9306
9298
1126.7
1125.7
1124.7
3.863
3.911
3.959
9405
9396
9387
1134.7
1133.6
1132.6
3.900
3.948
3.997
9494
9485
9477
1142.6
1141.5
1140.5
3.937
3.986
4.035
9584
9575
9566
1150.5
1149.4
1148.4
3.975
4.023
4.073
330
329
328
103.0
101.6
100.2
9291
9282
9274
1123.7
1122.6
1121.6
4.007
4.055
4.104
9380
9370
9363
1131.5
1130.5
1129.5
4.046
4.094
4.143
9469
9459
9451
1139.4
1138.4
1137.4
4.084
4.133
4.182
9558
9548
9540
1147.3
1146.2
1145.2
4.122
4.172
4.222
327
326
325
98.8
97.5
96.1
9265
9257
9248
1120.5
1119.5
1118.4
4.152
4.201
4.250
9354
9345
9337
1128.4
1127.3
1126.3
4.192
4.241
4.290
9442
9434
9425
1136.3
1135.2
1134.1
4.231
4.281
4.331
9531
9522
9513
1144.1
1143.0
1142.0
4.271
4.321
4.371
TEMPERATURE-ENTROPY TABLE.
8l
il
jt
372
371
370
Is
ft
I s * 2
1.56
1.57
1.58
1.69
>,
a
l|
11
H
1
>,
I
If
15
,1
l>
m
I
1
la
|l
eg!
*S
1
J
IS
ii
t
177.5
175.3
173.2
5.5
4.2
3.0
1199.5
1198.5
1197.4
2.592
2.616
2.640
18.5
17.2
15.9
1207.9
1206.8
1205.8
2.655
2.680
2.706
32.9
31.5
30.0
1216.5
1215.4
1214.3
2.720
2.746
2.772
47.7
46.1
44.7
1225.3
1224.1
1222.9
2.783
2.810
2.836
369
368
367
366
365
364
171.1
169.0
166.9
164.8
162.8
160.8
1.7
0.4
1196.4
1195.4
2.665
2.690
14.6
13.3
12.0
10.7
9.4
8.1
1204.7
1203.7
1202.7
1201.6
1200.5
1199.5
2.732
2.759
2.785
2.811
2.838
2.865
28.6
27.3
25.9
24.5
23.2
21.8
1213.2
1212.2
1211.1
1210.0
1209.0
1207.9
2.798
2.824
2.852
2.879
2.906
2.935
43.3
41.8
40.4
39.0
37.5
36.1
1221.9
1220.8
1219.7
1218.6
1217.5
1216.4
2.864
2.891
2.919
2.946
2.974
3.002
9994
9985
9975
9966
1194.3
1193.3
1192.3
1191.2
2.719
2.750
2.780
2.811
363
362
361
158.8
156.8
154.8
9955
9946
9937
1190.2
1189.2
1188.1
2.843
2.874
2.906
6.8
5.5
4.2
1198.4
1197.4
1196.4
2.894
2.920
2.949
20.4
19.0
17.6
1206.7
1205.6
1204.5
2.964
2.993
3.021
34.6
33.2
31.8
1215.3
1214.2
1213.0
3.030
3.060
3.089
360
359
358
357
356
355
152.9
151.0
149.1
147.2
145.3
143.5
9927
9917
9908
9898
9889
9880
1187.1
1186.1
1185.0
1183.9
1182.9
1181.9
2.938
2.971
3.005
3.040
3.074
3.109
2.9
1.6
0.4
1195.3
1194.3
1193.3
2.978
3.007
3.037
16.3
14.9
13.6
12.2
10.9
9.5
1203.4
1202.3
1201.2
1200.2
1199.1
1198.1
3.050
3.081
3.111
3.141
3.171
3.201
30.3
28.9
27.4
26.0
24.6
23.2
1211.9
1210.9
1209.8
1208.7
1207.6
1206.5
3.119
3.148
3.178
3.209
3.240
3.270
9992
9983
9974
1192.23.069
1191.1 3.104
1190.03.139
354
353
352
141.6
139.8
138.0
9870
9860
9851
1180.9
1179.8
1178.7
3.143
3.179
3.215
9963
9954
9945
1189.03.173
1187.93.209
1186.83.245
8.1
6.8
5.4
1197.0
1196.0
1195.0
3.232
3.264
3.296
21.8
20.4
19.0
1205.4
1204.3
1203.3
3.302
3.334
3.367
351
350
349
348
347
346
136.3
134.5
132.8
131.1
129.4
127.7
9841
9832
9822
9813
9804
9795
1177.6
1176.6
1175.5
1174.5
1173.5
1172.4
3.249
3.286
3.323
3.361
3.399
3.438
9934
9925
9915
9906
9897
9887
1185.7
1184.7
1183.6
1182.6
1181.6
1180.5
3.280
3.317
3.354
3.393
3.431
3.470
4.0
2.7
1 3
1193.9
1192.8
1191.7
3.328
3.360
3.392
17.5
16.0
14.6
13.2
11.8
10.4
1202.1
1201.0
1199.9
1198.8
1197.7
1196.7
3.400
3.433
3.466
3.499
3.534
3.570
9999
9989
9979
1190.6
1189.6
1188.5
3.425
3.463
3.503
345
344
343
126.0
124.4
122.7
9785
9776
9766
1171.3
1170.3
1169.2
3.477
3.518
3.561
9877
9868
9858
1179.4
1178.3
1177.2
3.510
3.551
3.593
9969
9959
9950
1187.4
1186.3
1185.2
5.543
3.584
3.627
8.9
7.5
6.0
1195.5
1194.4
1193.3
3.606
3.641
3.679
342
341
340
121.1
119.5
117.9
9757
9748
9739
1168.1
1167.1
1166.0
3.601
3.643
3.685
9849
9839
9830
1176.1
1175.1
1174.0
3.635
3.677
3.720
9940
9931
9921
1184.1
1183.0
1182.0
3.669
3.711
3.754
4.6
3.2
1.8
1192.2
1191.1
1190.1
3.716
3.754
3.792
339
338
337
116.3
114.8
113.3
9730
9720
9710
1164.9
1163.8
1162.7
3.729
3.774
3.820
9820
9810
9801
1172.9
1171.8
1170.7
3.764
3.809
3.856
9911
9901
9891
1180.9
1179.8
1178.7
3.799
3.845
3.891
0.3
1189.0
3.832
9992
9982
1187.8
1186.7
3.880
3.927
336
335
334
111.7
110.3
108.8
9701
9692
9683
1161.6
1160.6
1159.6
3.866
3.914
3.963
9791
9782
9773
1169.6
1168.5
1167.5
3.902
3.950
3.999
9882
9872
9863
1177.6
1176.5
1175.4
3.938
3.986
4.036
9972
9962
9953
1185.6
1184.5
1183.4
3.974
4.023
4.073
333
332
331
107.3
105.8
104.4
9674
9664
9655
1158.5
1157.4
1156.3
.012
.061
.111
9763
9754
9745
1166.4
1165.3
1164.2
4.048
4.098
4.148
9853
9843
9834
1174.3
1173.2
1172.1
4.085
4.135
4.186
9943
9933
9923
1182.3
1181.1
1180.0
4.122
4.173
4.224
330
329
328
103.0
101.6
100.2
9646
9637
9629
1155.2
1154.1
1153.1
.161
.211
.261
9736
9726
9718
1163.1
1162.1
1161.0
4.198
4.249
4.299
9825
9815*
9806
1171.0
1170.0
1168.9
4.237
4.287
4.338
9914
9904
9895
1178.9
1177.8
1176.7
4.275
4.326
4.378
327
326
325
98.8
97.5
96.1
9620
9610
9601
1152,0
1150.9
1149.8
4.311
4.361
4.412
9708
9699
9689
1159.9
1158.8
1157.7
4.349
4.400
4.451
9797
9787
9777
1167.8
1166.6
1165.5
4.389
4.440
4.492
9885
9876
9866
1175.6
1174.5
1173.4
4.429
4.481
4.532
82
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
ii
o 1
S^-a
m *>
So a
* H
1.52
1.53
1.54
1.55
>,
a
6 J2
g J
v
||
I>
QQ
jj
1
l|
1*
!
-
^
QQ
tj
"3
O 1
J*
I 1
|j
!>
02
15
1
i,ii
_ a
g
B
!
'5 =>
i*
OQ
324
323
322
94.8
93.5
92.2
9239
9231
9223
1117.3
1116.3
1115.2
4.300
4.352
4.407
9327
9319
9311
1125.2
1124.1
1123.1
:4.341
14.394
4.449
9415
9407
9398
1133.0
1131.9
1130.9
4.382
4.435
4.491
9503
9495
9486
1140.8
1139.8
1138.7
4.423
4.477
4.532
321
320
319
90.9
89.6
88.3
9215
9207
9199
1114.2
1113.2
1112.1
4.462
4.519
4.576
9302
9294
9286
1122.0
1121.0
1119.9
4.504
4.562
4.620
9389
9382
9373
1129.8
1128.8
1127.7
4.546
4.605
4.663
9477
9469
9460
1137.6
1136.6
1135.5
4.589
4.647
4.706
318
317
316
87.1
85.9
84.6
9190
9182
9173
1111.1
1110.0
1108.9
4.636
4.695
4.755
9277
9269
9260
1118.8
1117.8
1116.6
4.679
4.739
4.799
9364
9355
9346
1126.6
1125.5
1124.4
4.723
4.783
4.844
9451
9442
9433
1134.4
1133.3
1132.1
4.767
4.828
4.889
315
314
313
83.4
82.3
81.1
9166
9157
9149
1107.9
1106.8
1105.8
4.817
4.878
4.941
9252
9243
9235
1115.6
1114.6
1113.5
4.862
4.924
4.987
9338
9330
9321
1123.4
1122.3
1121.2
4.907
4.970
5.033
9425
9416
9407
1131.1
1130.0
1128.9
4.953
5.016
5.080
312
311
310
79.9
78.8
77.6
9141
9133
9125
1104.7
1103.6
1102.5
5.003
5.066
5.131
9227
9219
9210
1112.4
1111.3
1110.2
5.050
5.114
5.179
9313
9304
9295
1120.1
1119.0
1117.9
5.097
5.161
5.227
9399
9390
9381
1127.8
1126.7
1125.6
5.144
5.209
5.275
309
308
307
76.5
75.4
74.3
9116
9109
9100
1101.5
1100.4
1099.3
5.196
5.264
5.333
9201
9194
9185
1109.2
1108.1
1107.0
5.245
5.313
5.383
9287
9279
9270
1116.8
1115.7
1114.6
5.293
5.362
5.432
9372
9364
9355
1124.5
1123.4
1122.3
5.342
5.411
5.482
306
305
304
73.2
72.2
71.1
9093
9084
9076
1098.2
1097.1
1096.0
5.403
5.473
5.545
9177
9169
9160
1106.0
1104.8
1103.7
5.453
5.524
5.597
9262
9253
9244
1113.6
1112.4
1111.3
5.503
5.575
5.648
9347
9337
9329
1121.3
1120.1
1118.9
5.554
5.626
5.700
303
302
301
70.0
69.0
68.0
9068
9059
9052
1095.0
1093.9
1092.8
5.620
5.693
5.769
9152
9143
9136
1102.7
1101.6
1100.4
5.671
5.745
5.821
9236
9227
9219
1110.3
1109.2
1108.0
5.723
5.798
5.875
9320
9311
9303
1117.9
1116.8
1115.6
5.775
5.850
5.928
300
299
298
67.0
66.0
65.0
9043
9036
9027
1091.7
1090.7
1089.6
5.846
5.924
6.002
9127
9119
9111
1099.3
1098.3
1097.2
5.899
5.978
6.057
9210
9203
9194
1106.9
1105.9
1104.8
5.953
6.032
6.112
9294
9286
9277
1114.5
1113.5
1112.3
6.007
6.087
6.167
297
296
295
64.0
63.1
62.1
9020
9011
9004
1088.5
1087.4
1086.3
6.083
6.165
6.248
9103
9094
9086
1096.1
1095.0
1093.9
6.138
6.220
6.304
9186
9177
9169
1103.7
1102.5
1101.4
6.194
6.277
6.361
9269
9260
9252
1111.2
1110.0
1108.9
6.250
6.334
6.419
294
293
292
61.2
60.2
59.3
8995
8987
8980
1085.2
1084.1
1083.1
6.332
6.418
6.505
9077
9070
9062
1092.8
1091.7
1090.6
6.389
6.476
6.564
9160
9152
9144
1100.3
1099.2
1098.1
6.447
6.535
6.623
9242
9234
9226
1107.8
1106.7
1105.6
6.505
6.593
6.682
291
290
289
58.4
57.5
56.7
8972
8963
8956
1082.0
1080.9
1079.8
6.594
6.683
6.775
9054
9045
9037
1089.5
088.4
087.3
6.654
6.744
6.837
9136
9127
9119
1097.0
1095.9
1094.8
6.713
6.804
6.898
9218
9209
9201
1104.5
1103.4
1102.2
6.773
6.865
6.959
288
287
286
55.8
54.9
54.1
8947
8940
8932
1078.7
1077.6
1076.5
6.868
6.964
7.061
9029
9021
9013
086.2
085.1
084.0
6.931
7.027
7.125
9110
9102
9094
1093.6
1092.5
1091.4
6.992
7.090
7.188
9192
9183
9175
1101.1 7.055
1100.0,7.153
1098.97.252
285
284
283
53.2
52.4
51.6
8924
8916
8908
1075.4
1074.3
1073.2
7.160
7.259
7.361
9005
8996
8988
082.9
081.7
080.6
7.225
7.325
7.427
9086
9077
9069
1090.3
1089.1
1088.0
7.289
7.390
7.493
9167
9158
9150
1097.7
1096.5
1095.4
7.354
7.455
7.559
282
281
280
50.8
50.0
49.19
8900
8892
8885
1072.1
1071.0
069.9
7.465
7.570
7.677
8980
8973
8965
079.5
078.4
077.3
7.532
7.639
7.746
9061
9053
9045
1086.9
1085.8
1084.7
7.600
7.7C7
7.816
9141
9133
9125
1094.3
1093.21
1092.1
7.666
7.774
7.884
279
278
277
48.41
47.64
46.88
8876
8868
8860
068.8
067.6
066.5
7.784
7.895
8.006
8956
8948
8940
076.2
075.0
073.9
7.854
7.966
8.077
9036
9028
9020
1083.6
1082.4
1081.3
7.924
8.037
8.149
9116
9107
9099
1090.97.994
1089.78.106
1088.68.220
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
Ji
$X 4
ju
1.56
1.57
1.58
1.59
>,
1
*l
H
K
-5
tn 2
l>
03
f
ll
2*
jj
5
1*
- a
23
|J
1*
<
jj
|!
o5
*J
P
cc
324
323
322
94.8
93.5
92.2
9591
9583
9573
1148.7
1147.6
1146.5
4.464
4.518
4.574
9679
9670
9661
1156.5
1155.4
1154.3
4.505
4.559
4.616
9767
9758
9749
1164.3
1163.2
1162.1
4.545
4.600
4.657
9855
9846
9836
1172.2
1171.1
1169.9
4.586
4.641
4.699
321
320
319
90.9
89.6
88.3
9564
9556
9547
1145.4
1144.4
1143.2
4.631
4.690
4.750
9652
9643
9634
1153.2
1152.2
1151.0
4.673
4.733
4.793
9739
9730
9721
1161.0
1160.0
1158.8
4.715
4.775
4.835
9827
9818
9808
1168.8
1167.8
1166.6
4.757
4.818
4.879
318
317
316
87.1
85.9
84.6
9538
9528
9519
1142.2
1141.0
1139.9
4.811
4.872
4.934
9625
9615
9606
1149.9
1148.8
1147.6
4.855
4.916
4.979
9711
9702
9692
1157.7
1156.6
1155.4
4.897
4.960
5.022
9798
9788
9779
1165.5
1164.4
1163.1
4.941
5 . 004
5.067
315
314
313
83.4
82.3
81.1
9511
9502
9493
1138.9
1137.8
1136.7
4.998
5.062
5.126
9597
9588
9579
1146.65.043
1145.55.108
1144.45.172
9684
9674
9665
1154.3
1153.2
1152.1
5.088
5.152
5.218
9770
9760
9750
1162.1
1161.0
1159.8
5.133
5.198
5.264
312
311
310
79.9
78.8
77.6
9484
9475
9466
1135.5
1134.4
1133.3
5.191
5.256
5.323
9570
9561
9552
1143.2
1142.1
1141.0
5.238
5.303
5.370
9656
9646
9637
1151.0
1149.8
1148.7
5.284
5.350
5.419
9742
9732
9722
1158.7
1157.5
1156.4
5.331
5.397
5.466
309
308
307
76.5
75.4
74.3
9457
9449
9439
1132.2
1131.1
1130.0
5.391
5.460
5.532
9542
9534
9524
1139.9
1138.8
1137.6
5.439
5.510
5.581
9627
9619
9609
1147.6
1146.4
1145.3
5.488
5.559
5.631
9713
9704
9694
1155.3
1154.1
1153.0
5.535
5.607
5.680
306
305
304
73.2
72.2
71.1
9431
9422
9413
1128.9
1127.7
1126.6
5.604
5.677
5.751
9516
9506
9497
1136.6
1135.3
1134.2
5.654
5.728
5.803
9600
9591
9581
1144.2
1143.0
1141.8
5.705
5.779
5.854
9685
9675
9666
1151.9
1150.6
1149.5
5.755
5.829
5.906
303
302
301
70.0
69.0
68.0
9404
9395
9387
1125.5
1124.4
1123.2
5.827
5.903
5.981
9488
9479
9471
1133.2
1132.0
1130.8
5.879
5.956
6.035
9573
9563
9554
1140.8
1139.6
1138.5
5.931
6.008
6.088
9657
9647
9638
1148.4
1147.2
1146.1
5.983
6.061
6.141
300
299
298
67.0
66.0
65.0
9378
9369
9360
1122.1
1121.1
1119.9
6.061
6.142
6.223
9461
9453
9443
1129.7
1128.6
1127.5
6.115
6.196
6.278
9545
9536
9527
1137.3
1136.2
1135.0
6.169
6.251
6.333
9628
9620
9610
1144.96.223
1143.86.306
1142.66.389
297
296
295
64.0
63.1
62.1
9352
9343
9334
1118.8
1117.6
1116.5
6.306
6.390
6.476
9435
9426
9417
1126.4
1125.2
1124.1
6.362
6.447
6.534
9518
9508
9500
1133.9
1132.7
1131.6
6.418
6.504
6.591
9601
9591
9582
1141.56.474
1140.36.560
1139.1 6.648
294
293
292
61.2
60.2
59.3
9325
9317
9308
1115.4
1114.3
1113.1
6.563
6.652
6.742
9407
9399
9390
1122.9
1121.8
1120.6
6.621
6.711
6.801
9490
9481
9473
1130.5
1129.4
1128.2
6.679
6.770
6.861
9572
9564
9555
1138.06.737
1136.96.828
1135.76.920
291
290
289
58.4
57.5
56.7
9300
9291
9282
1112.0
1110.9
1109.7
6.834
6.926
7.021
9382
9372
9364
1119.5
1118.4
1117.2
6.894
6.987
7.083
9464
9454
9445
1127.1
1125.9
1124.7
6.954
7.048
7.145
9546
9536
9527
1134.6
1133.4
1132.2
7.014
7.109
7.206
288
287
286
55.8
54.9
54.1
9273
9265
9256
1108.5
1107.4
1106.3
7.117
7.216
7.316
9355
9346
9337
1116.0
1114.9
1113.8
7.180
7.280j
7.380
9436
9427
9418
1123.5
1122.4
1121.2
7.242
7.343
7.444
9517
9508
9499
1131.0
1129.9
1128.7
7.305
7.406
7.508
285
284
283
53.2
52.4
51.6
9248
9239
9230
1105.2
1104.0
1102.9
7.419
7.521
7.626
9329
9319
9311
1112.6
1111.4
1110.3
7.483
7.587
7.693
9410
9400
9391
1120.0
1118.9
1117.7
7.548
7.653
7.759
9490
9481
9472
1127.5 7.613
1126.37.718
1125.27.826
282
281
280
50.8
50.0
49.19
9222
9213
9205
1101.8
1100.7
1099.5
7.733
7.842
7.953
9302
9293
9285
1109.27.801
1108.1 7.911
1106.98.022
9382
9374
9365
1116.6
1115.5
1114.3
7.868
7.979
8.091
9463
9454
9445
1124.0
1122.9
1121.7
7.936
8.047
8.161
279
278
277
48.41
47.64
46.88
9195
9187
9179
1098.28.064
1097. 118. 177
1096.08.292
9275
9267
9258
1105.78.134
1104.58.248
1103.3^.364
9355
9347
9338
1113.1
1111.9
1110.7
8.204
8.319
8.436
9435
9426
9417
1120.5
1119.2
1118.0
8.274
8.390
8.508
84
TEMPERATURE-ENTROPY TABLE.
to to to 1 Temperature,
33 1 Degrees Fahr. 1
1
PH
d
IsJ
c
PI
46.13
45.39
44.67
1.52
1.53
1.54
1.55
>>
Jji
-u O
23
B
ll
8 >
U)
to
"c
3
a
Ifl
* c
8J
ll
'5
D ^
02
>>
<y
J|
ll
n
ij
|
n 2.
'
OQ
jj
1
l|
ll
<o
||
1?
8853
8845
8837
1065.4
1064.3
1063.2
8.119
8.236
8.356
8932
8924
8916
1072.8
1071.7
1070.5
8.192
8.310
8.431
9011
9003
8995
1080.2
1079.0
1077.8
8.265
8.383
8.505
9091
9083
9074
1087.5
1086.4
1085.2
8.336
8.456
8.579
273
272
271
43.95
43.24
42.54
8829
8822
8814
1062.1
1061.0
1059.9
8.477
8.602
8.728
8908
8900
8892
1069.4
1068.3
1067.2
8.553
8.679
8.806
8987
8979
8971
1076.7
1075.6
1074.5
8.629
8.756
8.884
9066
9058
9049
1084.1
1082.9
1081.8
8.704
8.832
8.962
270
269
268
41.84
41.16
40.49
8806
8798
8790
1058.7
1057.6
1056.5
8.852
8.985
9.117
8884
8876
8868
1066.0
1064.9
1063.8
8.931
9.065
9.198
8963
8955
8946
1073.3
1072.2
1071.0
9.009
9.144
9.279
9041
9033
9024
1080.6
1079.5
1078.3
9.088
9.224
9.360
267
266
265
39.83
39.17
38.53
8782
8774
8767
1055.4
1054.2
1053.1
9.250
9.390
9.532
8860
8851
8844
1062.6
1061.4
1060.3
9.332
9.473
9.616
8938
8929
8922
1069.9
1068.7
1067.6
9.414
9.556
9.700
9016
9007
8999
1077.1
1075.9
1074.8
9.496
9.639
9.784
264
263
262
37.89
37.26
36.64
8759
8751
8743
1051.9
1050.8
1049.7
9.672
9.812
9.961
8836
8828
8820
1059.2
1058.1
1056.9
9.757
9.899
10.05
8914
8906
8897
1066.4
1065.3
1064.1
9.843
9.985
10.13
8991
8983
8975
1073.6
1072.5
1071.3
9.928
10.07
10.22
261
260
259
36.02
35.42
34.83
8735
8728
8720
1048.6
1047.4
1046.3
10.11
10.25
10.41
8812
8804
8796
1055.8
1054.6
1053.4
10.20
10.35
10.50
8889
8881
8873
1063.0
1061.8
1060.6
10.28
10.44
10.59
8966
8958
8949
1070.2
1069.0
1067.8
10.37
10.53
10.69
258
257
256
34.24
33.66
33.09
8712
8705
8697
1045.1
1044.0
1042.9
10.57
10.73
10.90
8788
8781
8773
1052.2
1051.1
1050.0
10.66
10.83
10.99
8865
8857
8849
1059.4
1058.3
1057.2
10.75
10.92
11.09
8941
8933
8925
1066.6
1065.5
1064.3
10.85
11.01
11.18
255
254
253
32.53
31.97
31.42
8689
8681
8673
1041.7
1040.5
1039.4
11.06
11.23
11.41
8765
8757
8749
1048.8
1047.6
1046.5
11.16
11.33
11.51
8841
8832
8824
1056.0
1054.7
1053.6
11.25
11.43
11.61
8917
8908
8900
1063.1
1061.9
1060.8
11.35
11.53
11.71
252
251
250
30.88
30.35
29.82
8666
8658
8650
1038.2
1037.1
1035.9
11.59
11.77
11.95
8741
8733
8725
1045.4
1044.2
1043.0
11.69
11.87
12.06
8817
8808
8800
1052.5
1051.3
1050.1
11.79
11.97
12.16
8892
8884
8875
1059.6
1058.4
1057.2
11.89
12.07
12.27
249
248
247
29.30
28.79
28.29
8643
8635
8628
1034.8
1033.6
1032.5
12.14
12.33
12.53
8718
8710
8702
1041.9
1040.7
1039.6
12.25
12.44
12.64
8792
8784
8777
1048.9
1047.7
1046.6
12.35
12.54
12.74
8867
8859
8851
1056.0
1054.8
1053.7
12.46
12.65
12.85
246
245
244
27.80
27.31
26.83
8620
8612
8604
1031.3
1030.2
1029.0
12.73
12.93
13.13
8694
8686
8679
1038.4
1037.3
1036.1
12.84
13.04
13.24
8768
8760
8753
1045.4
1044.3
1043.1
12.95
13.15
13.36
8843
8835
8827
1052.5
1051.3
1050.1
13.06
13.26
13.47
243
242
241
26.35
25.88
25.42
8597
8589
8581
1027.9
1026.8
1025.6
13.33
13.55
13.76
8671
8663
8655
1035.0
1033.8
1032.6
13.45
13.66
13.88
8745
8737
8729
1042.0
1040.8
1039.6
13.56
13.78
14.00
8819
8811
8802
1049.0
1047.8
1046.6
13.68
13.89
14.12
240
239
238
24.97
24.52
24.08
8574
8566
8559
1024.4
1023.2
1022.0
13.98
14.21
14.44
8647
8639
8632
1031.4
1030.2
1029.0
14.10
14.33
14.56
8721
8713
8705
1038.3
1037.2
1036.0
14.22
14.45
14.69
8794
8786
8778
1045.3
1044.2
1043.0
14.34
14.58
14.81
237
236
235
23.64
23.21
22.79
8551
8543
8535
1020.9
1019.7
1018.5
14.67
14.92
15.17
8624
8616
8608
1027.9
1026.7
1025.5
14.80
15.04
15.30
8697
8689
8681
1034.8
1033.6
1032.4
14.92
15.17
15.43
8770
8762
8754
1041.8
1040.6
1039.4
15.05
15.30
15.56
234
233
232
22.38
21.97
21.57
8528
8521
8513
1017.3
1016.1
1014.9
15.42
15.67
15.93
8601
8593
8585
1024.2
1023.1
1021.9
15.55
15.80
16.06
8673
8666
8657
1031.2
1030.0
1028.8
15.68
15.94
16.20
8746
8738
8729
1038.1
1036.9
1035.7
15.81
15.07
16.33
231
230
229
21.17
20.78
20.40
8505
8498
8490
1013.8
1012.7
1011.4
16.19
16.46
16.74
8577
8570
8562
1020.8
1019.6
1018-3
16.33
16.60
16.88
8649
8642
8633
1027.7
1026.5
1025.2
16.47
16.74
17.02
8722
8714
8705
1034.5
1033.3
1032.1
16.61
16.88
17.17
TEMPERATURE-ENTROPY TABLE.
A
-r
e
3 a>
1.56
1.57
1.58
1.59
Cfic<
^ flS
c b.
ft
c
6s
i
^
Is
i
^
3s
aj
$
Is
c
ll
ill
1
- C
J'"i
'%
3
11
|
3
il
'|
1
*i a
H
Of
a
E
a
a
B
GQ
a
*"
CO
276
46.13
9170
1094.9
3.409
9250
1102.2
8.482
9329
1109.6
8.555
9408
1116.9
8.628
275
45.39J 9162
1093.7
8.530
9241
1101.1
8.604
9320
1108.4
8.677
9400
1115.7
8.751
274
44.67
9153
1092.5
8.654
9232
1099.9
8.729
9312
1107.2
8.803
9391
1114.5
8.878
273
43.95
9145
1091.4
8.779
9224
1098.8
8.855
9303
1106.1
8.931
9382
1113.4
9.006
272
43.24
9136
1090.3
8.908
9215
1097.6
8.985
9294
1104.9
9.062
9373
1112.2
9.138
271
42.54
9128
1089.1
9.039
9206
1096.4
9.116
9285
1103.7
9.194
9364
1111.0
9.272
270
41.84
9119
1087.9
9.166
9198
1095.2
9.245
9276
1102.5
9.324
9355
1109.8
9.402
269
41.161 9111
1086.8
9.303
9189
1094.1
9.383
9267
1101.3
9.463
9346
1108.6
9.543
268
40.49
9102
1085.6
9.439
9180
1092.9
9.520
9258
1100.1
9.601
9336
1107.4
9.682
267
39.83
9094
1084.4
9.577
9172
1091.7
9.659
9250
1098.9
9.741
9328
1106.2
9.823
266
39.17
9085
1083.2
9.721
9162
1090.4
9.805
9240
1097.7
9.888
9318
1104.9
9.971
265
38.53
9077
1082.1
9.868
9155
1089.3
9.952
9232
1096.5
10.04
9310
1103.8
10.12
264! 37.89
9069
1080.9
10.01
9146
1088.1
10.10
9223
1095.3
10.18
9301
1102.6
10.27
263 37.26 9060 ! 1079. 7
10.16
9137
1087.0
10.24
9215
1094.2
10.33
9292
1101.4
10.42
262
36.64
9052
1078.5
10.31
9129
1085.8
10.40
9206
1093.0
10.49
9283
1100.2
10.57
261
36.02
9043
1077.4
10.46
9120
1084.6
10.55
9197
1091.8
10.64
9274
1099.0
10.73
260
35.42
9035
1076.2
10.62
9111
1083.4
10.71
9188
1090.6
10.80
9265
1097.8
10.89
259
34.83
9026
1075.0
10.78
9103
1082.2
10.87
9179
1089.4
10.96
9256
1096.6
11.05
258
34.24
9017
1073.8
10.94
9094
1080.9
11.03
9170
1088.1
11.12
9247
1095.3
11.22
257
33.66
9010
1072.7
11.11
9086
1079.8
11.20
9162
1087.0
11.30
9238
1094.1
11.39
256
33.09
9001
1071.5
11.28
9077
1078.6
11.37
9153
1085.8
11.47
9229
1092.9
11.56
255
32.53
8993
1070.3
11.45
9068
1077.4
11.54
9144
1084.6
11.64
9220
1091.7
11.74
254
31.97! 8984
1069.0
11.63
9060
1076.1
11.72
9135
1083.3
11.82
9211
1090.4
11.92
253
31.42
8975
1067.9
11.81
9051
1075.0
11.91
9127
1082.1
12.01
9202
1089.2
12.11
252
30.88
8967
1066.7
11.99
9043
1073.8
12.09
9118
1080.9
12.19
9194
1088.0
12.29
251
30.35! 8959
1065.5
12.18
9034
1072.6
12.28
'9109
1079.7
12.38
9185
1086.8 12.48
250
29.82
8950
1064.3
12.37
9025
1071.4
12.47
9101
1078.5
12.58
9176
1085.6
12.68
249
29.30
8942
1063.1
12.56
9017
1070.2
12.67
9092
1077.3
12.77
9167
1084.4
12.88
248
28.79
8934
1061.9
12.76
9009
1069.0
12.86
9084
1076.0
12.97
9158
1083.1 13.08
247
28.29
8926
1060.7
12.96
9001
1067.8
13.07
9075
1074.8
13.18
9150
1081.9 13.29
246
27.80
8917
1059.5
13.17
8992
1066.6
13.28
9066
1073.6
13.39
9141
1080.7
13.50
245
27.31
8909
1058.4
13.37
8983
1065.4
13.48
9058
1072.5
13.60
9132
1079.5
13.71
244
26.83
8901
1057.2
13.58
8975
1064.2
13.70
9049
1071.3
13.81
9124
1078.3
13.92
243
26.35
8893
1056.0
13.79
8967
1063.0
13.91
9041
1070.1
14.02
9114
1077.1
14.14
242
25.881 8885
1054.8
14.01
8958
1061.8
14.13
9032
1068.8
14.24
9106
1075.9
14.36
241
25.42
8876
1053.6
14.24
8950
1060.6
14.36
9023
1067.6
14.47
9097
1074.6
14.59
240
24.97
8868
1052.3
14.46
8942
1059.3
14.58
9015
1066.3
14.70
9089
1073.3
14.82
239
24.52
8859
1051.1
14.70
8933
1058.1
14.82
9006
1065.1
14.94
9080
1072.1
15.06
238
24.08
8851
1049.9
14.93
8925
1056.9
15.06
8998
1063.9
15.18
9071
1070.9
15.30
237
23.64
8843
1048.7
15.17
8916
1055.7
15.30
8989
1062.7
15.42
9062
1069.7
15.55
236
23.21
8835
1047.5
15.43
8908
1054.5
15.55
8981
1061.5
15.68
9054
1068.4
15.81
235
22.79
8826
1046.3
15.68
8899
1053.3
15.81
8972
1060.2
15.94
9044
1067.1
16.07
234
22.38
8818
1045.0
15.94
8891
1052.0
16.07
8963
1058,9
16.21
9036
1065.8
16.34
233
21.97
8810
1043.8
16.20
8883
1050.8
16.34
8955
1057.7
16.47
9028
1064.6
16.60
232
21.57
8802
1042.6
16.47
8874
1049.5
16.60
8946
1056.4
16.74
9018
1063.3
16.87
231
21.17
8794
1041.4
16.74
8866
1048.3
16.88
8938
1055.2
17.02
9010.
1062.1
17.16
230 20.78 8786 1040.2
17.02
8858
1047.1
17.16
8930
1054.0
17.30
9002
1060.9
17.44
229 20.40 8777 1 1039.0
17.31
8849
1045.9
17.45
8921
1052.817.59
8992
1059.6
17.73
86
TEMPERATURE-ENTROPY TABLE.
bObObO 1 Temperatures,
g^g | Degrees Fahr.
t-'ifco Pressure, Pounds
o?op per Square
tooio Inch.
oo>*>-to 1
1.52
1.53
1.54
1.55
>,
0"
J* j
|l
6
3 3.
'3 o
>
&
ii
Jl
1
c 5.
8
I
>,
!
JJ
|!
!
\>
VI
t
!
l|
ll
Oi
ll
3 S>
I*
VI
8482
8475
8468
1010.2
1009.1
1007.9
17.02
17.31
17.60
8553
8546
8540
1017.1
1015.9
1014.7
17.17
17.45
17.75
8625
8618
8611
1024.0
1022.8
1021.6
17.31
17.60
17.89
8697
8689
8682
1030.8
1029.6
1028.4
17.45
17.74
18.04
225
224
223
18.91
18.56
18.21
8459
8452
8445
1006.7
1005.5
1004.4
17.90
18.21
18.52
8531
8523
8515
1013.5
1012.3
1011.2
18.05
18.36
18.67
8602
8594
8586
1020.4
1019.2
1018.0
18.20
18.51
18.83
8673
8665
8657
1027.2
1026.0
1024.8
18.35
18.66
18.99
222
221
220
17.86
17.52
17.19
8437
8430
8422
1003.2
1002.0
1000.8
18.84
19.16
19.49
8508
8500
8493
1010.0
1008.8
1007.6
19.00
19.32
19.65
8579
8571
8563
1016.8
1015.6
1014.4
19.16
19.48
19.81
8649
8642
8634
1023.6
1022.4
1021.2
19.31
19.64
19.98
219
218
217
16.86
16.54
16.22
8414
8406
8399
999.6
998.3
997.1
19.82
20.17
20.52
8484
8477
8469
1006.4
1005.1
1003.9
19.99
20.34
20.69
8555
8547
8539
1013.1
1011.8
1010.6
20.15
20.50
20.86
8625
8617
8609
1019.9
1018.6
1017.4
20.32
20.67
21.03
216
215
214
15.90
15.60
15.29
8392
8384
8377
995.9
994.7
993.5
20.88
21.25
21.62
8461
8454
8446
1002.7
1001.5
1000.3
21.05
21.42
21.80
8531
8524
8516
1009.4
1008.2
1007.0
21.23
21.60
21.98
8601
8593
8585
1016.2
1015.0
1013.7
21.40
21.78
22.16
213
212
211
14.99
14.70
14.41
8369
8361
8354
992.3
991.1
989.9
22.00
22.39
22.80
8438
8431
8424
999.1
997.9
996.7
22.18
22.58
22.99
8508
8500
8493
1005.8
1004.6
1003.4
22.37
22.76
23.18
8577
8569
8562
1012.5
1011.3
1010.1
22.55
22.95
23.36
210
209
208
14.13
13.85
13.57
8347
8340
8332
988.7
987.5
986.3
23.20
23.62
24.05
8416
8409
8401
995.4
994.2
993.0
23.40
23.81
24.25
8485
8478
8470
1002.1
1000.9
999.6
23.59
24.01
24.44
8554
8546
8538
1008.8
1007.5
1006.3
23.78
24.20
24.64
207
206
205
13.30
13.03
12.77
8325
8317
8309
985.1
983.8
982.6
24.48
24.93
25.39
8393
8385
8378
991.7
990.5
989.3
24.68
25.14
25.60
8462
8454
8446
998.4
997.2
995.9
24.89
25.34
25.81
8530
8522
8514
1005.1
1003.8
1002.6
25.09
25.55
26.02
204
203
202
12.51
12.26
12.01
8302
8294
8287
981.4
980.2
979.0
25.86
26.33
26.83
8370
8362
8355
988.0
986.8
985.6
26.07
26.55
27.05
8438
8430
8423
994.7
993.4
992.2
26.28
26.76
27.26
8506
8498
8491
1001.3
1000.1
998.9
26.50
26.98
27.48
201
200
199
11.77
11.53
11.29
8280
8272
8265
977.8
976.5
975.3
27.31
27.81
28.32
8347
8340
8332
984.4
983.1
981.9
27.54
28.04
28.55
8415
8407
8399
991.0
989.7
988.5
27.76
28.26
28.78
8483
8475
8467
997.6
996.3
995.1
27.98
28.49
29.01
198
197
196
11.06
10.83
10.61
8257
8250
8242
974.1
972.8
971.5
28.84
29.38
29.93
8325
8317
8309
980.7
979.4
978.1
29.08
29.62
30.17
8392
8384
8376
987.3
985.9
984.7
29.31
29.85
30.41
8459
8451
8443
993.9
992.5
991.2
29.55
30.09
30.65
195
194
193
10.39
10.17
9.96
8235.
8227
8220
970.4
969.1
967.9
30.49
31.07
31.67
8302
8294
8286
976.9
975.6
974.4
30.74
31.33
31.93
8368
8360
8353
983.4
982.2
981.0
30.99
31.58
32.18
8435
8427
8419
990.0
988.7
987.5
31.24
31.83
32.44
192
191
190
9.75
9.54
9.34
8212
8204
8197
966.7
965.4
964.2
32.28
32.91
33.54
8278
8270
8263
973.2
971.9
970.7
32.54
33.17
33.81
8345
8336
8329
979.7
978.4
977.2
32.80
33.44
34.08
8411
8403
8395
986.2
984.9
983.7
33.06
33.70
34.35
189
188
187
9.14
8.95
8.76
8190
8182
8174
963.0
961.7
960.5
34.19
34.85
35.52
8256
8247
8240
969.5
968.2
967.0
34.47
35.13
35.80
8321
8313
8306
976.0
974.7
973.4
34.74
35.41
36.09
8387
8379
8371
982.4
981.1
979.9
35.02
35.69
36.37
186
185
184
8.57
8.38
8.20
8166
8159
8151
95 '.2
958.0
956.7
36.20
36.90
37.63
8232
8224
8216
965.7
964.5
963.2
36.49
37.20
37.93
8297
8290
8282
972.1
970.9
969.6
36.78
37.49
38.24
8363
8355
8347
978.6
977.4
976.0
37.07
37.79
38.54
183
182
181
8.02
7.85
7.68
8144
8137
8130
955.5
954.3
953.0
38.37
39.15
39.94
8209
8202
8194
961.9
960.7
959.4
38.68
39.46
40.26
8274
8267
8259
968.4
967.1
965.8
38.99
39.77
40.58
8339
8332
8324
974.8
973.5
972.2
39.29
40.08
40.90
TEMPERATURE-ENTROPY TABLE.
d
= .
1.56
1.57
1.58
1.59
Efe
3
j
,
j
^
d
0*
g 1
Sco^j
>;
J $
||
>,
6 &
! J
c5 3
1 J
>;
i
|
H
ill
I
J O
I
K "*
CO
1
I 1
CO
1
5
ii
H
00
228
20.02
8768
1037.7
17.60
8840
1044.6
17.74
8912
1051.5
17.89
8983
1058.3
18.03
227
19.64
8761
1036.5
17.89
8832
1043.4
18.04
8904
1050.3
18.18
8975
1057.1
18.33
226
19.28
8754
1035.3
18.19
8825
1042.2
18.34
8896
1049.0
18.49
8968
1055.9
18.63
225
18.91
8744
1034.1
18.50
8815
1041.0
18.65
8887
1047.8
18.80
8958
1054.6
18.95
224
18.56
8736
1032.8
18.82
8807
1039.7
18.97
8878
1046.5
19.12
8949
1053.3
19.28
223
18.21
8728
1031.6
19.14
8799
1038.5
19.30
8870
1045.3
19.45
8941
1052.1
19.61
222
17.86
8720
1030.4
19.47
8791
1037.2
19.63
8862
1044.0
19.79
8932
1050.9
19.95
221
17.52
8712
1029.2
19.80
8783
1036.019.96
8853
1042.8
20.12
8924
1049.7
20.28
220
17.49
8704
1028.0
20.14
8774
1034.8
20.30
8845
1041.6
20.47
8915
1048.4
20.63
219
16.86
8695
1026.7
20.49
8765
1033.5
20.65
8836
1040.3
20.82
8906
1047.1
20.98
218
16.54
8687
1025.4
20.84
8757
1032.2
21.01
8827
1039.0
21.18
8897
1045.8
21.34
217
16.22
8679
1024.2
21.20
8749
1031.0
21.37
8819
1037.7
21.54
8889
1044.5
21.72
216
15.90
8671
1022.9
21.57
8741
1029.7
21.75
8811
1036.4
21.92
8880
1043.2
22.09
215
15.60
8663
1021.7
21.95
8733
1028.5
22.13
8802
1035.222.30
8872
1042.0
22.48
214
15.29
8655
1020.5
22.34
8724
1027.2
22.52
8794
1033.922.70
8863
1040.7
22.88
213
14.99
8647
1019.3
22.73
8716
1026.0
22.91
8785
1032.7 ! 23.10
8855
1039.4
23.28
212
14.70
8638
1018.023.13
8708
1024.7
23.32
8777
1031.423.50
8846
1038.1
23.69
211
14.41
8631
1016.8
23.55
8700
1023.5
23.74
8769
1030.223.93
8838
1036.9
24.12
210
14.13
8623
1015.5
23.97
8692
1022.2
24.16
8761
1028.924.35
8830
1035.6
24.55
209
13.85
8615
1014.2
24.40
8684
1020.9 24.59
8753
1027.624.79
8822
1034.3
24.98
208
13.57
8607
1013.0
24.84
8676
1019.7
25.04
8744
1026.325.24
8813
1033.0
25.43
207
13.30
8599
1011.7
25.29
8667
1018.4
25.49
8736
1025.1 25.69
8804
1031.7
25.89
206
13.03
8590
1010.5
25.75
8659
1017.1
25.96
8727
1023.826.16
8796
1030.4
26.37
205
12.77
8582
1009.2
26.23
8651
1015.9
26.44
8719
1022.5
26.64
8787
1029.1
26.85
204
12.51
8574
1007.9
26.71
8642
1014.6
26.92
8710
1021.2
27.13
8778
1027.8
27.34
203
12.26
8566
1006.7
27.20
8634
1013.3
27.41
8702
1019.9
27.63
8770
1026.6
27.84
202
12.01
8558
1005.5
27.70
8626
1012.1
27.92
8694
1018.7
28.14
8762
1025.3
28.36
201
11.77
8550
1004.2
28.21
8618
1010.8
28.43
8685
1017.4
28.65
8753
1024.0
28.88
200
11.53
8542
1002.9
28.72
8610
1009.5
28.94
8677
1016.1
29.17
8745
1022.7
29.40
199
11.29
8534
1001.7
29.25
8601
1008.3
29.48
8669
1014.8
29.71
8736
1021.4
29.94
198
11.06
8526
1000.4
29.78
8593
1007.0
30.02
8661
1013.6
30.25
8728
1020.2
30.49
197
10.83
8518
999.1
30.33
8585
1005.6
30.57
8652
1012.2
30.81
8719
1018.7
31.05
196
10.61
8509
997.8
30.90
'8576
1004.3
31.14
8643
1010.9
31.38
8710
1017.4
31.63
195
10.39
8502
996.5
31.48
8569
1003.1
31.73
8635
1009.6
31.98
8702
1016.2
32.22
194
10.17
8494
995.2
32.08
8560
1001.8
32.33
8627
1008.3
32.58
8693
1014.9
32.83
193
9.96
8486
994.0
32.70
8552
1000.5
32.95
8619
1007.1
33.21
8685
1013.6
33.46
192
9.75
8477
992.7
33.32
8544
999.2
33.58
8610
1005.7
33.85
8676
1012.3
34.11
191
9.54
8469
991.4
33.97
8535
997.9
34.23
8601
1004.4
34.50
8667
1010.9
34.76
190
9.34
8461
990.2
34.62
8527
996.7
34.89
8593
1003.2
35.16
8659
1009.7
35.43
189
9.14
8453
988.9
35.29
8519
995.4
35.57
8585
1001.9
35.84
8651
1008.4
36.12
188
8.95
8445
987.6
35.97
8510
994.1136.25
8576
1000.6
36.53
8642
1007.036.81
187
8.76
8437
986.4
36.66
8502
992.8
36.94
8568
999.3
37.23
8634
1005.8
37.51
186
8.57
8428
985.1
37.36
8494
991.5
37.65
8559
998.0
37.94
8625
1004.4
38.23
185
8.38
8420
983.8
38.08
8486
990.238.38
8551
996.7
38.68
8616
1003.1
38.97
184
8.20
8412
982.5
38.84
8477
988.939.14
8542
995.3
39.44
8607
1001.8
39.74
183
8.02
8404
981.2
39.60
8469
987.639.91
8534
994.1
40.21
8599
1000.5
40.52
182
7.85
8397
979.9
40.40
8461
986.440.71
8526
992.8
41.02
8591
999.2
41.33
181
7.68
8389
978.6
41.21
8453
985.041.53 8518
991.4
41.85
8583
997.8
42.17
88
TEMPERATURE-ENTROPY TABLE.
n
TJ
a
1.52
1.53
1.54
1.55
|fi
PH os
I!
. 3
&
li
i i
^
8*
ll
^
1 j
0)
ll
a
s i
P
02 02 C
1
11
'i 1
15
3
11
1
-^ c
i*
1
ll
'C *
H
5
w
CB
5
w
e
5
tn
QQ
0"
W
OQ
180
7.51
8122
951.
40.77
8186
958.1
41.0
8251
964,
41.42
8316
970.
41.74
179
7.35
8114
950.
41.55
8178
956.8
41.8
8243
963.
42.21
8308
969.
42.54
178
7.19
8107
949.
42. 4C
8171
955.6
42.7
8236
961.
43.07
8300
968.
43.41
177
7.03
8100
947.
43.25
8164
954.3
43.5
8228
960.
43.94
8292
967.
44.28
176
6.87
8092
946.
44. 1C
8156
953.0
44.4
8220
959.
44.80
8284
965.
45.15
175
6.71
8084
945.
45.03
8148
951.7
45.3
8212
958.
45.74
8276
964.
46.10
174
6.56
8077
944.
45.96
8141
950.5
46.3
8205
956.
46.68
8268
963.
47.05
173
6.42
8070
942.
46.88
8133
949.2
47.2
8197
955.
47.62
8261
961.
47.99
172
6.27
8062
941.
47.81
8126
947.9
48.19
8189
954.
48.56
8253
960.
48.94
171
6.13
8054
940.3
48.81
8117
946.6
49.19
8181
952.9
49.58
8244
959.
49.96
170
5.99
8047
939.0
49.89
8110
945.3
50.3
8173
951.6
50.7
8236
957.9
51.1
169
5.85
8039
937.8
51.0
8102
944.1
51.4
8165
950.3
51.8
8228
956.6
52.2
168
5.72
8032
936.5
52.0
8095
942.8
52.5
8158
949.1
52.9
8221
955.3
53.3
167
5.59
8024
935.2
53.1
8087
941.5
53.5
8150
947.8
54.0
8212
954.0
54.4
166
5.46
8017
934.0
54.3
8079
940.2
54.7
8142
946.5
55.1
8205
952.7
55.5
165
5.33
8009
932.7
55.3
8072
938.9
55.8
8134
945.2
56.2
8197
951.4
56.6
164
5.21
8002
931.4
56.5
8064
937.6
56.9
8127
943.9
57.4
8189
950.1
57.8
163
5.09
7994
930.1
57.6
8057
936.3
58.1
8119
942.6
58.5
8181
948.8
59.0
162
4.969
7987
928.8
58.9
8049
935.0
59.3
8111
941.2
59.8
8173
947.5
60.2
161
4.852
7979
927.6
60.2
8041
933.8
60.6
8103
940.0
61.1
8165
946.2
61.6
160
4.738
7972
926.3
61.5
8034
932.5
62.0
8096
938.7
62.5
8157
944.9
63.0
159
4.626
7964
925.0
62.8
8026
931.2
63.3
8088
937.4
63.8
8150
943.5
64.3
158
4.517
7957
923.7
64.2
8018
929.9
64.7
8080
936.0
65.2
8142
942.2
65.7
157
4.409
7950
922.4
65.7
8011
928.6
66.2
072
934.8
66.7
8134
940.9
67.2
156
4.303
7942
921.1
67.1
8003
927.3
67.6
065
933.4
68.1
8126
939.6
68.7
155
4.200
7934
919.8
68.5
.7995
926.0
69.1
056
932.1
69.6
8118
938.3
70.1
154
4.099
7926
918.5
70.1
7987
924.6
70.6
048
930.8
71.1
8109
936.9
71.7
153
4.000
7919
917.2
71.6
7980
923.4
72.1
041
929.5
72.7
8102
935.6
73.2
152
3.903
7911
915.9
73.2
7972
922.0
73.7
033
928.2
74.3
8093
934.3
74.9
151
3.808
7903
914.6
74.8
7964
920.7
75.4
024
926.8
76.0
8085
932.9
76.6
150
3.715
7896
913.3
76.5
7957
919.4
77.1
017
925.5
77.7
8078
931.6
78.3
149
3.624
7888
912.0
78.3
7949
918.1
78.8
009
924.2
79.4
8069
930.3
80.0
148
3.535
7881
910.7
80.1
7941
916.8
80.7
002
922.9
81.3
8062
929.0
81.9
147
3.447
7873
909.4
81.9
7933
915.5
82.5
993
921.5
83.1
8053
927.6
83.8
146
3.361
7866
908.1
83.8
7926
914.2
84.4
986
920.2
85.0
8046
926.3
85.7
145
3.278
7858
906.8
85.6
7917
912.8
86.3
977
918.9
87.0
8037
924.9
87.6
144
3.196
7850
905.5
87.6
7910
911.5
88.3
970
917.6
88.9
8029
923.6
89.6
143
3.116
7842
904.1
89.6
7902
910.2
90.3
961
916.2
91.0
8021
922.2
91.7
142
3.037
7835
902.8
91.7
7894
908.9
92.4
954
914.9
93.1
8013
920.9
93.8
141
2.960
7827
901.5
93.9
7887
907.5
94.6
946
913.5
95.3
8005
919.6
96.0
140
2.885
7820
900.2
96.0
7879
906.2
96.8
938
912.2
97.5
7997
918.2
98.2
139
2.812
7812
898.9
98.3
7871
904.9
99.0
930
910.8
99.8
7989
916.8
00.5
138
2.740
7805
897.6
00.6
7864
903.5
101.4
923
909.5
102.1
7982
915.5
02.9
137
2.669
7797
896.2
03.0
7855
902.2
103.8
914
908.1
104.5
7973
914.1
05.3
136
2.600
7789
894.9
05.5
7848
900.8
106.3
907
906.8
L07.1
7965
912.7
07.8
135
2.533
7782
893.6
08.0
7840
899.5
108. 8
899
905.5
109.6
7957
911.4
10.4
134
2.467
7774
892.2
10.5
7832
898.1
111.4
890
904.1
L12.2
7949
910.0
13.0
133
2.403
7766
890.9
13.2
7825
896.8
L14.1
883
902.7
L14.9
7941
908.6
15.8
i
TEMPERATURE-ENTROPY TABLE.
8 9
J
1
o
1.56
1.57
1.58
1.59
CGh
|1
eg
c
4
i
V
a
,
oJ
- r
r fc
UMj
>,
6|
n 3
6s
c a
>>
Ss
! J
>,
3
en i
a
Ij=
"5
m
J'"l
I
U
1^
"3
11
13
II
||
H
S
=
&
tzj
w
<
H
%
E
i
180
7.51
8380
977.2
42.07
8445
983.6
42.39
8509
990.0
42.72
8574
996.4
43.04
179
7.35
8372
976.0
42.87
8437
982.3
43.20
8501
988.7
43.53
8566
995.1
43.86
178
7.19
8364
974.7
43.75
8429
981.1
44.08
8493
987.4
44.42
8557
993.8
44.76
177
7.03
8357
973.4
44.62
8421
979.8
44.97
8485
986.1
45.31
8549
992.5
45.65
176
6.87
8348
972.1
45.50
8412
978.4
45.85
8476
984.8
46.19
8540
991.1
46.54
175
6.71
8340
970.8
46.45
8404
977.1
46.81
8468
983.5
47.17
8532
989.8
47.52
174
6.56
8332
969.5
47.41
8396
975.8
47.77
8460
982.1
48.14
8524
988.5
48.50
173
6.42
8324
968.2
48.36
8388
974.5
48.73
8452
980.8
49.10
8515
987.2
49.47
172
6.27
8316
966.9
49.32
8380
973.2
49.69
8443
979.5
50.1
8507
985.8
50.4
171
6.13
8308
965.5
50.3
8371
971.8
50.7
8434
978.1
51.1
8498
984.4
51.5
170
5.99
8300
964.2
51.5
8363
970.5
51.8
8426
976.8
52.2
8489
983.1
52.6
169
5.85
8291
962.9
52.6
8355
969.2
53.0
8418
975.5
53.4
8481
981.8
53.8
168
5.72
8284
961.6
53.7
8347
967.9
54.1
8410
974.2
54.5
8473
980.4
54.9
167
5.59
8275
960.3
54.8
8338
966.6
55.2
8401
972.8
55.6
8464
979.1
56.0
166
5.46
8267
959.0
56.0
8330
965.2
56.4
8393
971.5
56.8
8455
977.7
57.2
165
5.33
8259
957.7
57.1
8322
963.9
57'. 5
8385
970.1
57.9
8447
976.4
58.4
164
5.21
8251
956.3
58.3
8314
962.6
58.7
8376
968.8
59.1
8439
975.0
59.6
163
5.09
8243
955.0
59.4
8306
961.2
59.9
8368
967.5
60.3
8430
973.7
60.8
162
4.969
8235
953.7
60.7
8297
959.9
61.2
8359
966.1
61.6
8421
972.3
62.1
161
4.852
8227
952.4
62.0
8289
958.6
62.5
8351
964.8
63.0
8413
971.0
63.4
160
4.738
8219
951.1
63.5
8281
957.3
63.9
8343
963.5
64.4
8405
969.7
64.9
159
4.626
8211
949.7
64.8
8273
955.9
65.3
8335
962.1
65.8
8396
968.3
66.2
158
4.517
8203
948.4
66.2
8265
954.6
66.7
8326
960.7
67.2
8388
966.9
67.7
157
4.409
8195
947.1
67.7
8257
953.3
68.2
8318
959.4
68.7
8380
965.6
69.2
156
4.303
8187
945.8
69.2
8248
951.9
69.7
8310
958.1
70.2
8371
964.2
70.7
155
4.200
8179
944.4
70.7
8240
950.571.2
8301
956.7
71.7
8362
962.8
72.3
154
4.099
8170
943.0
72.2
8231
949.2
72.8
8293
955.3
73.3
8354
961.5
73.8
153
4.000
8163
941.7
73.8
8224
947.9
74.3
8284
954.0
74.9
8345
960.1
75.4
152
3.903
8154
940.4
75.4
8215
946.5
76.0
8276
952.6
76.5
8336
958.7
77.1
151
3.808
8146
939.0
77.1
8206
945.1
77.7
8267
951.2
78.3
8328
957.3
78.9
150
3.715
8138
937.7
78.9
8199
943.8
79.4
8259
949.9
80.0
8320
956.0
80.6
149 3.624
8130
936.3
80.6
8190
942.4
81.2
8250
948.5
81.8
8311
954.6
82.4
148
3.535
8122
935.0
82.5
8182
941.1
83.1
8243
947.2
83.7
8303
953.3
84.4
147
3.447
,8114
933.7
84.4
8174
939.7
85.0
8234
945.8
85.6
8294
951.8
86.3
146 3.361
8106
932.3
86.3
8165
938.4187.0
8225
944.4
87.6
8285
950.5
88.2
145
3.278
8097
930.9
88.3
8157
937.0
88.9
8217
943.0
89.6
8276
949.1
90.2
144
3.196
8089
929.6
90.3
8149
935.7
90.9
8208
941.7
91.6
8268
947.7
92.3
143
3.116
8081
928.2
92.4
8140
934.3
93.0
8200
940.3
93.7
8259
946.3
94.4
142
3.037
8073
926.9
94.5
8132
932.9
95.2
8192
938.9
95.9
8251
944.9
96.6
141
2.960
8065
925.6
96.7
8124
931.6
97.4
8183
937.6
98.1
8243
943.6
98.8
140 2.885
8056
924.2
98.9
8115
930.299.7
8175
936.1
100.4
8234
942.1
101.1
139
2.812
8048
922.8
101.3
8107
928.8
102.0
8166
934.8
102.8
8226
940.8
103.5
138
2.740
8041
921.5
103.6
8099
927.4
104.4
8158
933.4
105.2
8217
939.4
105.9
137 2.669
8032
920.1
106.1
8091
926.0
106.9
8149
932.0
107.7
8208
938.0
108.4
136 2.600
8024
918.7
108.6
8083
924.7
109.4
8141
930.6
110.2
8200
936.6
111.0
135 2.533
8016
917.3
111.3
8075
923.3
112.1
8133
929.2
112.9
8192
935.2
113.7
134 2.467
8007
915.9
113.9
8066
921.9
114.7
8124
927.8
115.5
8182
933.7
116.4
133 2.403
7999
914.6
116. 6
8058
920.5
117. S
8116
926.4
118.3
8174
932.3119.2
90
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
1
2
gjj
d
III
1.52
1.53
1.54
1.55
>>
1
p
O"
69
H
m
I
5 ,5
o
l>
CO
|
I
||
ll
W
^j
^
CO
>
c
6 9
^ o
c
0) -^
m
ll
!>
CO
|
1
Ij
I 1
a!
lJ
P
CO
132
131
130
2.341
2.280
2.220
7759
7751
7744
889.5
888.2
886.9
116.0
118.7
121.7
7817
7809
7802
895.4
894.1
892.8
116.9
119.6
122.6
7875
7867
7860
901.4
900.0
898.7
117.7
120.5
123.5
7933
7925
7917
907.3
905.9
904.6
118.6
121.4
124.4
129
128
127
2.161
2.103
2.047
7736
7729
7721
885.5
884.2
882.9
124.6
127.7
130.8
7794
7786
7778
891.4
890.1
888.8
125.6
128.6
131.8
7852
7844
7836
897.3
895.9
894.6
126.5
129.6
132.7
7909
7901
7893
903.2
901.8
900.5
127.4
130.5
133.7
126
125
124
1.992
1.938
1.886
7713
7705
7698
881.5
880.2
878.8
134.1
137.4
140.8
7770
7763
7755
887.4
886.1
884.6
135.0
138.4
141.8
7828
7820
7812
893.2
891.9
890.5
136.0
139.4
142.9
7885
7877
7869
899.1
897.8
896.3
137.0
140.4
143.9
123
122
121
1.835
1.785
1.737
7690
7682
7675
877.5
876.1
874.8
144.3
148.0
151.8
7747
7739
7732
883.3
881.9
880.6
145.4
149.1
152.9
7804
7796
7788
889.1
887.7
886.4
146.5
150.2
154.1
7861
7853
7845
895.0
893.5
892.2
147.5
151.3
155.2
120
119
118
1.689
1.642
1.597
7667
7659
7652
873.4
872.1
870.7
155.6
159.6
163.7
7724
7716
7708
879.2
877.9
876.5
156.8
160.8
164.9
7780
7772
7764
885.0
883.7
882.3
157.9
162.0
166.2
7837
7828
7821
890.8
889.4
888.0
159.1
163.1
167.4
117
116
115
1.552
1.509
1.467
7644
7636
7628
869.3
867.9
866.6
168.0
172.3
176.8
7700
7692
7684
875.1
873.7
872.4
169.2
173.6
178.1
7756
7748
7740
880.9
879.4
878.1
170.5
174.9
179.4
7812
7804
7796
886.6
885.2
883.8
171.7
176.1
180.7
114
113
112
1.426
1.386
1.347
7620
7612
7605
865.2
863.9
862.5
181.4
186.0
190.9
7676
7668
7660
871.0
869.6
868.2
182.7
187.4
192.3
7732
7724
7716
876.7
875.3
873.9
184.0
188.8
193.7
7788
7779
7771
882.4
881.0
879.6
185.3
190.1
195.1
111
110
109
1.308
1.271
1.235
7597
7589
7581
861.2
859.8
858.4
196.0
201.3
206.7
7652
7644
7636
866.8
865.4
864.1
207.4
202.7
208.2
7707
7699
7691
872.5
871.1
869.7
198.8
204.2
209.7
7763
7755
7746
878.2
876.8
875.4
200.3
205.7
211.2
108
107
106
1.200
1.165
1.131
7573
7565
7558
857.0
855.6
854.2
212.2
218.0
224.0
7629
7620
7612
862.7
861.3
859.9
213.7
219.6
225.6
7684
7675
7667
868.3
866.9
865.5
215.
221.
227.
7739
7730
7722
874.0
872.6
871.2
216.8
222.8
228.9
105
104
103
1.098
1.066
1.035
7550
7542
7534
852.8
851.4
850.1
230.1
236.4
242.9
7605
7596
7589
858! 5
857.1
855.7
231.8
238.1
244.7
7659
7651
7643
864.1
862.7
861.3
233.
239.
246.
7714
7705
7697
869.8
868.3
866.9
235.1
241.5
248.2
102
101
100
1.005
0.975
0.946
7526
7519
7511
848.7
847.3
845.9
249.6
256.5
263.5
7581
7573
7565
854.3
852.9
851.5
251.4
258.3
265.4
7635
7627
7619
859.9
858.5
857.1
253.
260.
267.
7689
7681
7673
865.5
864.1
862.7
255.0
262.0
269.2
99
98
97
0.918
0.891
0.864
7503
7495
7487
844.5
843.1
841.8
270.8
278.3
286.1
7557
7549
7541
850.1
848.7
847.4
272.7
280.3
288.1
7611
7603
7595
855.7
854.2
852.9
274.
282.
290.
7665
7656
7648
861.3
859.8
858.5
276.6
284.3
292.2
96
95
94
0.838
0.813
0.788
7480
7472
7464
840.4
839.0
837.6
294.2
302.5
311.0
7533
7525
7517
846.0
844.6
843.1
296.3
304.6
313.2
7587
7579
7571
851.5
850.1
848.7
298.4
306.8
315.5
7640
7632
7624
857.1
855.7
854.2
300.5
308.9
317.7
93
92
91
0.764
0.741
0.718
7456
7448
7440
836.2
834.8
833.4
319.9
329.2
338.8
7509
7501
7493
841.7
840.3
838.9
322.2
331.6
341.2
7563
7554
7546
847.3
845.8
844.4
324.5
333.9
343.7
7616
7607
7599
852.8
851.3
849.9
326.8
336.2
346.1
90
89
88
0.696
0.675
0.654
7433
7425
7417
832.0
830.6
829.1
348.7
358.9
369.4
7485
7477
7469
837.5
836.1
834.6
351.2
361.5
372.0
7538
7530
7522
843.0
841.6
840.1
353.7
364.0
374.6
7591
7583
7574
848.4
847.0
845.5
356.2
366.5
377.2
87
86
85
0.633
0.613
0.594
7409
7401
7393
827.7
826.3
824.9
380.1
390.8
402.2
7462
7454
7446
833.2
831.8
830.3
382.8
393.5
405.0
7514
7506
7498
838.7
837.2
835.8
385.5
396.3
407.9
7567
7558
7550
844.1
842.7
841.2
388.2
399.1
410.7
TEMPERATURE-ENTROPY TABLE.
1
Pressure, Pounds
i>er Square
ncli.
1.56
1.57
1.58
1.59
1
i !
||
1
6 |
l|
r
1
a
a
3s
JJ
! J
1
|l
|l
GQ
132
131
130
2.341
2.280
2.220
7991
7983
7975
913.2
911.8
910.4
119.5
122.3
125.3
8049
8041
8033
919.1
917.7
916.3
120.3
123.2
126.2
8108
8099
8091
925.0
923.6
922.2
121.2
124.1
127.1
8166
8157
8149
930.9
929.5
928.1
122.1
125.0
128.0
129 2.161
128 2.103
127 2.047
7967
7959
7951
909.1
907.7
906.3
128.3
131.5
134.7
8025
8017
8008
915.0
913.6
912.2
129.3
132.4
135.7
8083
8074
8066
920.8
919.4
918.0
130.2
133.4
136.6
8140
8132
8123
926.7
925.3
923.9
131.1
134.3
137.6
126 1.992
125 1.938
124 1.886
7942
7934
7926
904.9
903.6
902.1
138.0
141.5
145.0
8000
7991
7983
910.8
909.4
908.0
139.0
142.5
146.0
8057
8049
8040
916.6
915.3
913.8
140.0
143.5
147.1
8115
8106
8097
922.5
921.1
919.6
141.0
144.5
148.1
123
122
121
.835
.785
.737
7918
7910
7902
900.8
899.3
898.0
148.6
152.4
156.3
7975
7966
7958
906.6
905.1
903.8
149.7
153.5
157.4
8032
8023
8015
912.5
911.0
909.6
150.8
154.6
158.5
8088
8080
8072
918.3
916.8
915.4
151.8
155.7
159.7
120 .689
119 .642
118J .597
7893
7885
7877
896.6
895.2
893.8
160.2
164.3
168.6
7950
7941
7933
902.4
901.0
899.6
161.4
165.5
169.8
8007
7998
7990
908.2
906.8
905.4
162.5
166.7
171.0
8063
8054
8046
914.0
912.6
911.1
163.7
167.8
172.2
117
116
115
.552
.509
.467
7869
7860
7852
892.4
890.9
889.6
172.9
177.4
182.0
7925
7916
7908
898.2
896.7
895.3
174.2
178.7
183.3
7981
7972
7964
903.9
902.4
901.0
175.4
179.9
184.6
8037
8028
8020
909.7
908.2
906.8
176.7
181.2
185.9
114
113
112
.426
.386
.347
7843
7835
7827
888.2
886.8
885.4
186.7
191.5
196.5
7899
7891
7882
893.9
892.5
891.1
188.0
192.8
197.9
7955
7946
7938
899.6
898.2
896.8
189.
194.
199.
8011
8002
7993
905.4
904.0
902.5
190.7
195.6
200.7
111
110
109
.308
.271
.235
7818
7810
7801
884.0
882.5
881.1
201.7
207.1
212.7
7874
7866
7857
889.7
888.2
886.8
203.1
208.6
214.2
7929
7921
7912
895.4
893.9
892.5
204.
210.
215.
7984
7976
7967
901.1
899.6
898.2
206.0
211.5
217.2
108
107
106
1.200
1.165
1.131
7794
7785
7777
879.7
878.3
876.8
218.4
224.4
230.5
7849
7840
7831
885.4
884.0
882.5
219.9
225.9
232.1
7904
7895
7886
891.0
889.6
888.1
221.
227.
233.
7959
7950
7941
896.7
895.3
893.8
223.0
229.1
235.4
105
104
103
1.098
1.066
1.035
7769
7760
7752
875.4
874.0
872.6
236.8
243.3
249.9
7823
7814
7806
881.1
879.6
878.2
238.4
245.0
251.7
7878
7869
7861
886.7
885.2
883.8
240.1
246.7
253.4
7933
7923
7915
892.4
890.9
889.5
241.8
248.4
255.2
102
101
100
1.005
0.975
0.946
7744
7735
7727
871.1
869.7
868.3
256.8
263.9
271.0
7798
7790
7781
876.8
875.3
873.8
258.6
265.7
272.9
7852
7844
7835
882.4
880.9
879.4
260.4
267.5
274.8
7906
7898
7889
888.0
886.5
885.0
262.2
269.4
276.7
99
98
97
0.918
0.891
0.864
7718
7710
7702
866.9
865.4
864.0
278.6
286.3
294.3
7772
7764
7756
872.4
871.0
869.6
280.5
288.3
296.3
7826
7818
7809
878.0
876.5
875.1
282.5
290.3
298.4
7880
7872
7863
883.6
882.1
880.7
284.4
292.3
300.4
96
95
94
0.838
0.813
0.788
7694
7685
7677
862.6
861.2
859.7
302.6
311.1
319.9
7747
7739
7730
868.2
866.8
865.3
304.7
313.3
322.1
7801
7792
7784
873.7
872.3
870.8
306.8
315.4
324.3
7854
7846
7837
879.3
877.9
876.4
308.9
317.6
326.6
93
92
91
0.764
0.741
0.718
7669
7660
7652
858.3
856.9
855.4
329.1
338.6
348.5
7722
7713
7705
863.9
862.4
860.9
331.4
340.9
350.9
7775
7766
7758
869.4
867.9
866.4
333.6
343.3
353.3
7828
7819
7811
874.9
873.4
871.9
335.9
345.6
355.7
90
89
88
0.696
0.675
0.654
7644
7635
7627
853.9
852.5
851.0
358.6
369.1
379.8
7696
7688
7679
859.4
858.0
856.5
361.1
371.6
382.4
7749
7741
7732
864.9
863.5
862.0
363.6
374.2
385.0
7802
7793
7785
870.4
868.9
867.4
366.0
376.7
387.7
87
86
85
0.633
0.613
0.594
7619
7610
7602
849.5
848.1
846.7
390.9
401.8
413.5
7671
7663
7654
855.1
853.6
852.1
393.5
404.6
416.4
7724
7715
7706
860.5
859.0
857.5
396.2
407.4
419.2
7776
7767
7759
866.0
864.5
863.0
398.9
410.1
422.1
TEMPERATURE-ENTROPY TABLE.
13
a
1.60
1.61
1.62
1.63
02 C3
3
s
"*^ S
,3
c
Q)
G
4)
a
O
L
B
II
03 O*
g*-S
8s
c 3
>>
1
8s
>,
8s
|
B
1
11
1^
1
11
1^
3
11
1^
I
1!
1?
H
5
s
cc
5
w
O"
w
OQ
w
420
308.5
138.3
1287.8
1.881
158.4
1298.3
1.931
179.8
1309.0
1.983
201.4
1320.0
2.031
419
305.1
136.6
1286.7
1.895
156.7
1297.1
1.946
178.0
1307.8
2.000
199.5
1318.7
2.048
418
301.8
135.0
1285.6
1.912
155.0
1295.9
1.963
176.2
1306.7
2.016
197.7
1317.5
2.065
417
298.5
133.4
1284.5
1.927
153.4
1294.7
1.979
174.5
1305.5
2.033
195.9
1316.2
2.082
416
295.2
131.9
1283.4
1.944
151.8
1293.6
1.996
172.7
1304.3
2.050
194.0
1315.0
2.099
415
292.0
130.3
1282.3
1.959
150.1
1292.5
2.013
171.0
1303.1
2.066
192.2
1313.7
2.116
414
288.9
128.7
1281.2
1.975
148.4
1291.3
2.030
169.2
1301.9
2.084
190.4
1312.5
2.133
413
285.7
127.1
1280.1
1.991
146.7
1290.2
2.047
167.5
1300.7
2.100
188.6
1311.3
2.150
412
282.5
1-25.5
1279.0
2.008
145.0
1289.0
2.064
165.8
1299.6
2.118
186.8
1310.2
2.168
411
279.4
124.0
1277.9
2.025
143.4
1287.9
2.081
164.0
1298.4
2.135
184.9
1308.9
2.187
410
276.3
122.3
1276.7
2.043
141.7
1286.7
2.098
162.2
1297.2
2.154
183.0
1307.7
2.205
409
273.3
120.8
1275.5
2.060
140.1
1285.6
2.116
160.5
1296.0
2.172
181.2
1306.5
2.224
408
270.3
119.2
1274.4
2.077
138.4
1284.5
2.133
158.7
1294.8
2.190
179.4
1305.3
2.243
407
267.3
117.7
1273.3
2.095
136.8
1283.3
2.152
157.0
1293.6
2.208
177.6
1304.0
2.261
406
264.3
116.1
1272.2
2.112
135.1
1282.1
2.170
155.3
1292.4
2.226
175.7
1302.8
2.280
405
261.3
114.5
1271.1
2.130
133.4
1281.0
2.188
153.5 1291.3
2.244
174.0
1301.6
2.299
404
258.4
112.9
1270.0
2.148
131.8
1279.9
2.206
151.8
1290.1
2.263
172.2
1300.4
2.318
403
255.5
111.3
1268.9
2.167
130.1
1278.7
2.225
150.0
1288.9
2.282
170.3
1299.1
2.337
402
252.6
109.7
1267.8
2.185
128.6
1277.6
2.243
148.3
1287.8
2.302
168.5
1297.9
2.356
401
249.7
108.2
1266.7
2.203
126.9
1276.4
2.261
146.6
1286.6
2.321
166.8
1296.7
2.377
400
246.9
106.7
1265.6
2.223
125.3
1275.3
2.280
144.9
1285.4
2.340
164.9
1295.5
2.398
399
244.1
105.2
1264.4
2.241
123.6
1274.2
2.301
143.0
1284.2
2.360
163.1
1294.3
2.418
398
241.4
103.6
1263.3
2.260
122.0
1273.1
2.320
141.4
1283.0
2.380
161.3
1293.1
2.438
397
238.6
102.0
1262.2
2.279
120.4
1271.9
2.340
139.6
1281.8
2.400
159.5
1291.9
2.459
396
235.9
100.5
1261.1
2.300
118.6
1270.7
2.360
137.9
1280.7
2.420
157.7
1290.7
2.479
395
233.2
99.0
1260.1
2.320
117.0
1269.6
2.380
136.1
1279.4
2.440
155.9
1289.6
2.500
394
230.5
97.5
1259.0
2.340
115.4
1268.4
2.400
134.5
1278.3
2.461
154.1
1288.4
2.521
393
227.9
95.9
1257.9
2.361
113.8
1267.3
2.421
132.9
1277.1
2.482
152.3
1287.2
2.543
392
225.2
94.4
1256.8
2.382
112.2
1266.1
2.441
131.1
1276.0
2.504
150.6
1286.0
2.565
391
222.6
92.8
1255.6
2.403
110.5
1265.0
2.462
129.4
1274.8
2.525
148.8
1284.8
2.587
390
220.1
91.3
1254.5
2.424
108.9
1263.9
2.483
127.7
1273.6
2.546
147.0
1283.6
2.610
389
217.5
89.8
1253.4
2.444
107.3
1262.8
2.505
126.0
1272.5
2.569
145.2
1282.4
2.632
388
215.0
88.2
1252.3
2.466
105.7
1261.6
2.527
124.3
1271.3
2.591
143.4
1281.2
2.654
387
212.5
86.6
1251.2
2.488
104.1
1260.4
2.546
122.5
1270.1
2.613
141.6
1280.0
2.677
386
210.0
85.0
1250.0
2.510
102.4
1259.2
2.571
120.9
1268.9
2.636
139.9
1278.8
2.701
385
207.5
83.5
1248.9
2.532
100.8
1258.1
2.594
119.1
1267.7
2.660
138.1
1277.6
2.725
384
205.1
81.9
1247.8
2.554
99.2
1257.0
2.617
117.5
1266.5
2.684
136.3
1276.3
2.750
383
202.6
80.4
1246.6
2.577
97.6
1255.8
2.640
115.7
1265.4
2.707
134.5
1275.0
2.773
382
200.3
78.9
1245.4
2.600
95.9
1254.6
2.664
114.0
1264.2
2.730
132.6
1273.8
2.799
381
197.9
77.4
1244.3
2.623
94.3
1253.4
2.688
112.3
1263.0
2.755
130.9
1272.6
2.823
380
195.5
75.8
1243.2
2.646
92.6
1252.3
2.713
110.7
1261.8
2.780
129.1
1271.4
2.849
379
193.2
74.3
1242.1
2.671
91.0
1251.1
2.737
109J.O
1260.6
2.805
127.3
1270.2
2.873
378
190.9
72.7
1241.0
2.696
89.4
1249.9
2.761
107.3
1259.5
2.830
125.5
1268.9
2.899
377
188.6
71.2
1239.9
2.720
87.8
1248.7
2.787
105.7
1258.4
2.856
123.7
1267.7
2.925
376
186.3
69.7
1238.7
2.745
86.1
1247.5
2.813
104.0
1257.2
2.883
122.0
1266.5
2.952
375
184.1
68.1
1237.5
2.770
84.5
1246.4
2.839
102.3
1256.0
2.909
120.1
1265.3
2.979
374
181.9
66.6
1236.3
2.795
83.0
1245.3
2.864
100.7
1254.8
2.935
118.4
1264.1
3.005
373
179.7
65.0
1235.2
2.821
81.4
1244.2
2.891
99.0
1253.6
2.962
116.7
1262.9
3.033
TEMPERATURE-ENTROPY TABLE.
93
Temperature,
Degrees Fahr. |
1
c
C|
g*d
m u U
!*5
1.64
1.65
1.66
1.67
>
1
1 <$
jl
o 1
ll
I 5 *
03
>>
I
l|
1*
V
*!
I*
02
i
3
Of
6 3
J!
!
l>
1
1
J*
I 1
<u
o
11
l>
OQ
420
419
418
308.5
305.1
301.8
223.6
221.7
219.8
1331.1
1329.9
1328.6
2.086
2.103
2.120
245.1
243.2
241.3
1341.7
1340.4
1339.2
2.140
2.157
2.174
267.4
265.4
263.4
1353.3
1352.0
1350.6
2.193
2.210
2.229
289.7
287.7
285.7
1364.4
1363.1
1361.8
2.243
2.261
2.280
417
416
415
298.5
295.2
292.0
217.9
216.0
214.1
1327.3
1326.0
1324.7
2.138
2.156
2.174
239.4
237.5
235.5
1337.9
1336.7
1335.5
2.191
2.210
2.228
261.4
259.4
257.4
1349.2
1347.8
1346.6
2.246
2.264
2.282
283.8
281.9
279.9
1360.5
1359.2
1357.9
2.299'
2.318
2.337
414
413
412
288.9
28.7
282.5
212.2
210.3
208.4
1323.5
1322.3
1321.0
2.191
2.209
2.227
233.6
231.7
229.8
1334.2
1333.0
1331.7
2.246
2.263
2.282
255.4
253.5
251.5
1345.3
1344.0
1342.6
2.300
2.319
2.338
277.9
275.9
273.9
1356.6
1355.3
1354.0
2.356
2.375
2.394
411
410
409
279.4
276.3
273.3
206.5
204.6
202.7
1319.8
1318.5
1317.3
2.245
2.263
2.282
227.9
226.0
224.0
1330.5
1329.2
1327.9
2.301
2.320
2.339
249.5
247.5
245.6
1341.3
1340.1
1338.8
2.356
2.376
2.395
271.9
269.9
267.9
1352.7
1351.4
1350.0
2.414
2.433
2.454
408
407
406
270.3
267.3
264.3
200.8
198.9
197.0
1316.1
1314.8
1313.6
2.301
2.320
2.339
222.0
220.1
218.2
1326.7
1325.4
1324.2
2.358
2.377
2.396
243.7
241.8
239.9
1337.5
1336.3
1335.0
2.414
2.434
2.455
265.9
263.9
261.9
1348.7
1347.4
1346.1
2.474
2.494
2.514
405
404
403
261.3
258.4
255.5
195.1
193.2
191.4
1312.3
1311.0
1309.8
2.359
2.378
2.398
216.3
214.4
212.5
1322.9
1321.6
1320.3
2.415
2.435
2.456
237.9
235.9
233.9
1333.7
1332.4
1331.1
2.475
2.495
2.516
259.9
257.9
255.9
1344.8
1343.4
1342.1
2.535
2.556
2.577
402
401
400
252.6
249.7
246.9
189.5
187.6
185.7
1308.5
1307.3
1306.0
2.418
2.437
2.457
210.5
208.5
206.6
1319.0
1317.7
1316.4
2.477
2.497
2.518
231.9
230.0
228.0
1329.8
1328.5
1327.2
2.536
2.558
2.580
253.9
251.9
249.9
1340.9
1339.6
1338.3
2.599
2.620
2.642
399
398
397
244.1
241.4
238.6
183.8
182.0
180.1
1304.8
1303.5
1302.3
2.478
2.499
2.520
204.7
202.8
200.9
1315.1
1313.9
1312.6
2.538
2.560
2.581
226.0
224.0
222.0
1325.9
1324.6
1323.3
2.601
2.623
2.645
248.0
246.0
244.0
1337.0
1335.7
1334.4
2.664
2.687
2.709
396
395
394
235.9
233.2
230.5
178.2
176.3
174.5
1301.0
1299.7
1298.5
2.541
2.563
2.585
199.0
197.1
195.2
1311.4
1310.1
1308.9
2.603
2.625
2.648
220.0
218.0
216.0
1321.9
1320.6
1319.3
2.667
2.690
2.713
242.0
240.0
238.0
1333.1
1331.8
1330.4
2.731
2.755
2.779
393
392
391
227.9
225.2
222.6
172.7
170.8
168.9
1297.3
1296.0
1294.8
2.607
2.630
2.652
193.3
191.4
189.5
1307.7
1306.5
1305.2
2.670
2.694
2.718
214.1
212.1
210.1
1318.0
1316.7
1315.3
2.736
2.759
2.784
236.0
234.0
232.0
1329.1
1327.8
1326.5
2.803
2.827
2.851
390
389
388
220.1
217.5
215.0
167.0
165.2
163.3
1293.6
1292.4
1291.2
2.675
2.699
2.721
187.6
185.6
183.7
1304.0
1302.7
1301.4
2.741
2.764
2.789
208.2
206.3
204.4
1314.1
1312.8
1311.6
2.808
2.832
2.856
230.0
228.0
225.9
1325.1
1323.8
1322.5
2.876
2.901
2.927
387
386
385
212.5
210.0
207.5
161.4
159.6
157.7
1289.9
1288.6
1287.4
2.746
2.769
2.793
181.8
179.9
178.0
1300.1
1298.8
1297.5
2.813
2.839
2.863
202.4
200.4
198.4
1310.3
1309.1
1307.8
2.881
2.907
2.931
223.9
221.9
219.9
1321.2
1319.9
1318.5
2.951
2.978
3.003
384
383
382
205.1
202.6
200.3
155.9
154.0
152.2
1286.1
1284.9
1283.7
2.819
2.843
2.869
176.1
174.1
172.2
1296.3
1295.0
1293.7
2.888
2.914
2.940
196.5
194.5
192.6
1306.5
1305.2
1303.9
2.958
2.984
3.010
217.9
215.9
213.9
1317.2
1315.9
1314.6
3.030
3.057
3.084
381
380
379
197.9
195.5
193.2
150.3
148.5
146.6
1282.5
1281.2
1280.0
2.893
2.920
2.946
170.3
168.4
166.5
1292.4
1291.1
1289.9
2.967
2.994
3.020
190.7
188.8
186.9
1302.6
1301.4
1300.2
3.037
3.065
3.093
211.9
209.8
207.7
1313.2
1311.9
1310.5
3.111
3.139
3.167
378
377
376
190.9
188.6
186.3
144.8
143.0
141.2
1278.8
1277.6
1276.4
2.973
2.999
3.026
164.6
162.7
160.9
1288.6
1287.4
1286.1
3.046
3.074
3.102
184.9
183.0
181.0
1298.9
1297.6
1296.3
3.120
3.148
3.176
205.7
203.7
201.7
1309.2
1307.9
1306.6
3.195
3.223
3.251
375
374
373
184.1
181.9
179.7
139.4
137.6
135.8
1275.23.053
1273. 9i3.081
1272.73.109
159.0
157.1
155.2
1284.9
1283.6
1282.3
3.130
3.158
3.187
179.1
177.2
175.3
1295.0
1293.7
1292.4
3.204
3.233
3.261
199.7
197.7
195.7
1305.3
1304.0
1302.7
3.281
3.311
3.340
94
TEMPERATURE-ENTROPY TABLE.
jj
-a
a
1.60
1.61
1.62
1.63
oE
3
5
1|
. s
Jj
!
Jjs
aJ
g
6s
to
w S
tn 2,
1 3
9
J
EQ
i UH
|
1 I
* o
"3
1 5
13
1 I
' 1
+j a
'3
<
M
00
02
5
ffi
CO
<y
^
372
177.5
63.6
1234.1
2.848
79.8
1243.0
2.919
97.3
1252.3
2.989
115.0
1261.6
3.061
371
175.3
62.0
1233.0
2.874
78.2
1241.8
2.945
95.7
1251.2
3.018
113.
1260.3
3.090
370
173.2
60.6
1231.9
2.901
76.6
1240.6
2.974
94.0
1250.0
3.045
111.
1259.1
3.118
369
171.1
59.0
1230.8
2.930
75.0
1239.5
3.000
92.3
1248.8
3.073
109.
1257.9
3.147
368
169.0
57.5
1229.6
2.956
73.3
1238.3
3.030
90.6
1247.6
3.102
108.
1256.7
3.175
367
166.9
56.0
1228.5
2.983
71.7
1237.1
3.059
88.9
1246.4
3.130
106.
1255.5
3.205
366
164.8
54.5
1227.4
3.012
70.1
1235.9
3.087
87.2
1245.2
3.160
104.
1254.3
3.235
365
162.8
53.0
1226.2
3.041
68.6
1234.7
3.116
85.6
1244.0
3.190
102.
1253.0
3.265
364
160.8
51.4
1225.1
3.070
67.0
1233.6
3.145
83.9
1242.8
3.220
101.
1251.8
3.295
363
158.8
49.9
1224.0
3.100
65.4
1232.4
3.175
82.2
1241.6
3.250
99.
1250.6
3.325
362
156.8
48.4
1222.9
3.130
63.9
1231.3
3.205
80.6
1240.4
3.280
97.
1249.4
3 . 357
361
154.8
46.9
1221.7
3.160
62.2
1230.1
3.236
78.9
1239.2
3.312
95.
1248.2
3.389
360
152.9
45.4
1220.6
3.190
60.6
1228.9
3.267
77.2
1238.0
3.343
94.
1247.0
3.421
359
151.0
43.9
1219.5
3.221
59.0
1227.7
3.299
75.6
1236.9
3.375
92.
1245.7
3.453
358
149.1
42.3
1218.3
3.252
57.5
1226.6
3.330
74.0
1235.7
3.407
90.
1244.5
3.486
357
147.2
40.9
1217.2
3.285
56.0
1225.5
3.362
72.4
1234.5
3.440
89.
1243.3
3.519
356
145.3
39.5
1216.1
3.317
54.4
1224.3
3.395
70.7
1233.3
3.474
87.4
1242.0
3.554
355
143.5
37.
1215.0
3.350
52.8
1223.1
3.428
69.0
1232.2
3.507
85.8
1240.8
3.588
354
141.6
36.4
1213.9
3.382
51.2
1222.0
3.461
67.4
1231.0
3.540
84.0
1239.6
3.622
353
139.8
34.9
1212.8
3.417
49.6
1220.8
3.495
65.8
1229.8
3.576
82.4
1238.4
3.658
352
138.0
33.4
1211.7
3.450
48.0
1219.6
3.530
64.2
1228.6
3.610
80.8
1237.3
3.693
351
136.3
31.9
1210.6
3.484
46.4
1218.4
3.564
62.6
1227.5
3.648
79.1
1236.2
3.730
350
134.5
30.4
1209.4
3.520
44.9
1217.3
3.599
61.0
1226.3
3.685
77.6
1235.0
3.766
349
132.8
29.0
1208.3
3.555
43.4
1216.2
3.636
59.4
1225.1
3.720
75.9
1233.8
3.804
348
131.1
27.5
1207:2
3.590
41.9
1215.1
3.672
57.7
1223.9
3.758
74.2
1232.6
3.842
347
129.4
26.0
1206.1
3.626
40.4
1214.0
3.710
56.1
1222.7
3.796
72.5
1231.4
3.881
346
127.7
24.5
1205.0
3.663
38.9
1212.8
3.748
54.5
1221.5
3.834
70.9
1230.2
3.920
345
126.0
23.0
1203.9
3.700
37.4
1211.6
3.786
52.9
1220.3
3.874
69.3
1229.0
3.960
344
124.4
21.5
1202.8
3.738
35.9
1210.5
3.824
51.3
1219.2
3.914
67.6
1227.9
4.000
343
122.7
20.0
1201.6
3.776
34.3
1209.4
3.863
49.7
1218.1
3.954
66.0
1226.7
4.. 042
342
121.1
18.5
1200.5
3.815
32.7
1208.3
3.903
48.0
1216.9
3.995
64.4
1225.6
4.085
341
119.5
17.0
1199.3
3.853
31.2
1207.1
3.943
46.5
1215.8
4.036
62.6
1224.4
4.128
340
117.9
15.5
1198.2
3.893
29.7
1206.0
3.984
44.9
1214.7
4.079
61.0
1223.2
4.171
339
116.3
14.0
1197.1
3.933
28.1
1204.8
4.026
43.3
1213.5
4.120
59.3
1222.0
4.215
338
114.8
12.5
1196.0
3.973
26.5
1203.7
4.067
41.7
1212.4
4.164
57.7
1220.8
4.260
337
113.3
11.0
1194.8
4.014
25.0
1202.6
4.110
40.1
1211.2
4.207
56.0
1219.6
4.304
336
111.7
9.6
1193.7
.056
23.4
1201.4
4.151
38.5
1210.0
4.250
54.3
1218.4
4.350
335
110.3
8.1
1192 5
.098
21.9
1200.2
4.194
36.9
1208.9
4.294
52.7
1217.2
4.395
334
108.8
6.6
1191.4
.140
20.3
1199.0
4.238
35.4
1207.6
4.339
51.0
1216.0
4.442
333
107.3
5.1
1190.3
.181
18.8
1197.9
4.283
33.8
1206.4
4.383
49.3
1214.7
4.489
332
105.8
3.6
1189.2
.225
17.3
1196.8
4.328
32.2
1205.2
4.429
47.7
1213.5
4.536
331
104.4
2.1
1188.1
4.268
15.7
1195.6
4.372
30.5
1204.1
4.473
46.0
1212.4
4.584
330
103.0
0.5
1186.9
4.312
14.2
1194.5
4.417
28.9
1203.0
4.520
44.3
1211.2
4.631
329
101.6
9993
1185.7
.365
12.7
1193.4
4.461
27.3
1201.8
4.566
42.7
1210.0
4.680
328
100.2
9984
1184.5
.417
11.1
1192.3
4.509
25.7
1200.6
4.613
41.0
1208.8
4.730
327
98.8
9974
1183.4
.468
9.6
1191.1
4.557
24.1
1199.4
4.661
39.3
1207.6
4.780
326
97.5
9964
1182.3
.521
8.0
1190.0
4.603
22.5
1198.2
4.710
37.7
1206.4
4.830
325
96.1
9954
1181.2
.573
6.5
1189.0
4.650
20.9
1197.0
4.760
36.0
1205.3
4.880
TEMPERATURE-ENTROPY TABLE.
95
WWW 1 Temperature,
^^^ | Degrees Fahr.
1
11
*&*
iU
1.64
1.65
1.66
1.67
>
5
Jj
I s
*!
i#
02
i
a
J*
11
n
!
l>
CQ
6
<
6 3
*i a
23
W
<!
l>
^j
J<2
I 1
!
!>
CQ
177. 1
175.3
173.2
133.9
132.1
130.3
1271.4
1270.1
1268.9
3.138
3.167
3.196
153.3
151.4
149.5
1281.0
1279.8
1278.5
3.215
3.245
3.275
173.4
171.5
169.6
1291.2
1289.9
1288.6
3.293
3.323
3.354
193.7
191.7
189.7
1301.4
1300.1
1298.8
3.370
3.400
3.432
369
368
367
171.1
169.0
166.9
128.5
126.7
124.9
1267.7
1266.5
1265.3
3.225
3.254
3.284
147.6
145.7
143.8
1277.2
1275.9
1274.6
3.305
3.335
3.365
167.7
165.7
163.8
1287.4
1286.1
1284.8
3.384
3.415
3.447
187.7
185.7
183.7
1297.5
1296.2
1294.9
3.464
3.495
3.527
366
365
364
164.8
162.8
160.8
^23.1
121.3
119.5
1264.0
1262.8
1261.6
3.314
3.344
3.376
142.0
140.0
138.2
1273.3
1272.1
1270.9
3.396
3.428
3.460
161.9
160.0
158.0
1283.5
1282.2
1280.9
3.479
3.511
3,. 545
181.7
179.7
177.7
1293.6
1292.3
1291.0
3.559
13.593
3.626
363
362
361
158.8
156.8
154.8
117.7
115.9
114.1
1260.3
1259.0
1257.8
3.408
3.440
3.472
136.3
134.4
132.5
1269.6
1268.3
1267.0
3.490
3.524
3.557
156.0
154.0
152.0
1279.6
1278.3
1277.0
3.579
3.612
3.647
175.7
173.8
171.8
1289.7
1288.4
1287.0
3.660
3.695
3.730
360
359
358
152.9
151.0
149.1
112.3
110.5
108.8
1256.6
1255.3
1254.1
3.504
3.537
3.570
130.6
128.8
127.0
1265.7
1264.5
1263.2
3.590
3.624
3.660
150.0
148.1
146.2
1275.7
1274.4
1273.1
3.682
3.716
3.750
169.8
167.9
166.0
1285.63.765
1284.33.801
1283.03.839
357
356
355
147.2
145.3
143.5
107.1
105.3
103.6
1252.9
1251.7
1250.5
3.605
3.640
3.675
125.1
123.2
121.4
1262.0
1260.7
1259.4
3.695
3.730
3.765
144.3
142.4
140.5
1271.8
1270.5
1269.2
3.786
3.822
3.860
164.0
162.0
160.0
1281.73.874
1280.43.913
1279.03.950
354
353
352
141.6
139.8
138.0
101.8
100.1
98.4
1249.3
1248.0
1246.8
3.713
3.749
3.787
119.6
117.8
115.9
1258.2
1257.0
1255.8
3.803
3.840
3.878
138.7
136.9
135.0
1268.0
1266.7
1265.4
3.898
3.936
3.975
158.0
156.0
154.0
1277.7
1276.4
1275.0
3.990
4.029
4.068
351
350
349
136.3
134.5
132.8
96.5
94.7
93.0
1245.6
1244.3
1243.0
3.824
3.861
3.900
114.1
112.4
110.6
1254.6
1253.3
1252.0
3.915
3.955
3.994
133.1
131.2
129.4
1264.2
1262.9
1261.6
4.014
4.052
4.091
152.0
150.1
148.2
1273.7
1272.4
1271.1
4.108
4.149
4.190
348
347
346
131.1
129.4
127.7
91.3
89.5
87.8
1241.8
1240.6
1239.3
3.940
3.980
4.020
108.8
107.0
105.1
1250.8
1249.6
1248.3
4.033
4.075
4.115
127.5
125.6
123.7
1260.3
1259.0
1257.8
4.132
4.172
4.213
146.2
144.2
142.2
1269.8
1268.5
1267.2
4.230
4.273
4.314
345
344
343
126.0
124.4
122.7
86.0
84.1
82.4
1238.0
1236.8
1235.6
4.062
4.104
4.148
103.3
101.5
99.7
1247.0
1245.8
1244.6
4.157
4.200
4.241
121.9
120.0
118.0
1256.5
1255.2
1253.9
4.255
4.297
4.340
140.3
138.4
136.4
1265.8
1264.5
1263.2
4.357
4.400
4.443
342
341
340
121.1
119.5
117.9
80.7
79.0
77.1
1234.3
1233.0
1231.8
4.190
4.232
4.276
97.9
96.1
94.3
1243.3
1242.0
1240.8
4.285
4.329
4.373
116.1
114.2
112.3
1252.6
1251.3
1250.0
4.384
4.428
4.473
134.5
132.5
130.6
1261.9
1260.6
1259.3
4.488
4.533
4.579
339
338
337
116.3
114.8
113.3
75.4
73.6
71.9
1230.6
1229.3
1228.0
4.320
4.364
4.409
92.5
90.7
89.0
1239.6
1238.3
1237.0
4.417
4.461
4.507
110.4
108.6
106.7
1248.8
1247.5
1246.3
4.519
4.564
4.610
128.7
126.7
124.8
1258.0
1256.7
1255.4
4.625
4.672
4.720
336
335
334
111.7
110.3
108.8
70.1
68.4
66.7
1226.8
1225.6
1224.3
4.455
4.500
4.548
87.2
85.4
83.7
1235.8
1234.6
1233.3
4.553
4.599
4.648
104.8
103.0
101.1
1245.0
1243.7
1242.4
4.657
4.705
4.754
122.9
120.9
119.0
1254.1
1252.7
1251.4
4.768
4.817
4.865
333
332
331
107.3
105.8
104.4
65.0
63.2
61.4
1223.1
1221.9
1220.7
4.595
4.642
4.692
81.9
80.2
78.4
1232.1
1230.9
1229.7
4.697
4.744
4.793
99.3
97.4
95.6
1241.1
1239.8
1238.6
4.803
4.850
4.900
117.0
115.0
113.0
1250.1
1248.7
1247.4
4.916
4.967
5.019
330
329
328
103.0
101.6
100.2
59.8
58.0
56.3
1219.4
1218.2
1217.0
4.740
4.790
4.840
76.6
74.9
73.1
1228.4
1227.2
1226.0
4.845
4.895
4.947
93.7
91.9
90.0
1237.3
1236.0
1234.7
4.953
.005
.057
111.1
109.2
107.3
1246.0
1244.7
1243.4
5.070
5.123
5.180
327
326
325
98.8
97.5
96.1
54.6
52.9
51.1
1215.7
1214.5
1213.2
4.890
4.941
4.994
71.4
69.5
67.7
1224.7
1223.5
1222.2
4.998
5.050
5.105
88.1
86.3
84.5
1233.4
1232.1
1230.7
.109
.163
.218
105.4
103.5
101.7
1242.1
1240.8
1239.5
5.233
5.290
5.345
9 6
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
Pressure, Pounds!
per Square
Inch.
1.60
1.61
1.62
1.63
<
1*
J!
CO
1
c
+j o
1
I 1
"rt
3
a
a
6 $
85
oJ
CO
J 42
jJ
ll
CO
324
323
322
94.8
93.5
92.2
9943
9934
9924
1180.0
1178.9
1177.8
4.626
4.683
4.741
5.0
3.5
1.9
1187.9
1186.7
1185.5
4.700
4.747
4.797
19.3
17.7
16.1
1195.8
1194.7
1193.5
4.810
4.860
4.910
34.3
32.7
31.0
1204.0
1202.8
1201.6
4.934
4.987
5.040
321
320
319
90.9
89.6
88.3
9914
9905
9895
1176.6
1175.6
1174.4
4.799
4.860
4.922
0.3
1184.4
4.845
14.4
12.9
11.3
1192.3
1191.2
1190.1
4.965
5.018
5.073
29.3
27.7
26.0
1200.4
1199.2
1198.0
5.093
5.146
5.200
9992
9982
1183.3
1182.1
4.903
4.965
318
317
316
87.1
85.9
84.6
9885
9875
9865
1173.3
1172.1
1170.9
4.985
5.048
5.112
9972
9962
9952
1181.0
1179.8
1178.6
5.029
5.092
5.157
9.7
8.1
6.5
1188.9
1187.7
1186.5
5.128
5.182
5.239
24.4
22.7
21.0
1196.9
1195.7
1194.5
5.257
5.314
5.370
315
314
313
312
311
310
83.4
82.3
81.1
79.9
78.8
77.6
9856
9846
9836
9827
9817
9808
1169.8
1168.7
1167.6
1166.4
1165.3
1164.1
5.178
5.244
5.311
5.378
5.445
5.514
9942
9932
9922
9913
9903
9893
1177.5
1176.4
1175.3
1174.1
1173.0
1171.8
5.224
5.290
5.357
5.424
5.492
5.562
4.9
3.3
1.6
1185.3
1184.2
1183.0
5.296
5.351
5.410
19.3
17.6
16.0
14.3
12.6
11.0
1193.4
1192.2
1191.0
1189.8
1188.6
1187.4
5.429
5.487
5.545
5.605
5.665
5.725
9999
9989
9978
1181.8
1180.6
1179.4
5.471
5.540
5.610
309
308
307
76.5
75.4
74.3
9798
9789
9779
1163.0
1161.8
1160.6
5.584
5.656
5.729
9883
9874
9864
1170.6
1169.5
1168.3
5.632
5.705
5.779
9968
9959
9948
1178.3
1177.1
1175.9
5.681
5.754
5.829
9.3
7.6
5.8
1186.2
1184.9
1183.6
5.788
5.850
5.915
306
305
304
303
302
301
73.2
72.2
71.1
70.0
69.0
68.0
9770
9760
9750
9741
9731
9722
1159.5
1158.3
1157.1
1156.0
1154.9
1153.7
5.804
5.879
5.956
6.034
6.113
6.194
9854
* 9844
9834
9825
9815
9306
1167.2
1165.9
1164.8
1163.7
1162.5
1161.3
5.855
5.930
6.008
6.086
6.166
6.247
9939
9929
9918
9909
9899
9889
1174.8
1173.6
1172.4
1171.3
1170.1
1168.9
5.905
5.981
6.059
6.139
6.218
6.300
4.0
2.2
0.4
1182.4
1181.2
1180.0
5.980
6.047
6.110
9993
9983
9973
1178.9
1177.7
1176.5
6.191
6.271
6.353
300
299
298
67.0
66.0
65.0
9712
9703
9693
1152.5
1151.4
1150.2
6.276
6.359
6.443
9795
9786
9776
1160.1
1159.0
1157.8
6.330
6.414
6.498
9879
9870
9859
1167.7
1166.6
1165.4
6.384
6.469
6.554
9963
9953
9943
1175.3
1174.1
1172.9
6.438
6.523
6.609
297
296
295
64.0
63.1
62.1
9684
9674
9665
1149.0
1147.8
1146.7
6.530
6.617
6.706
9767
9757
9748
1156.6
1155.4
1154.3
6.585
6.673
6.762
9850
9840
9830
1164.2
1162.9
1161.8
6.641
6.729
6.819
9933
9923
9913
1171.7
1170.5
1169.3
6.697
6.786
6.877
294
293
292
61.2
60.2
59.3
9655
9646
9637
1145.5
1144.4
1143.2
6.795
6.887
6.980
9737
9728
9719
1153.1
1151.9
1150.7
6.852
6.945
7.038
9820
9811
9801
1160.6
1159.4
1158.2
6.910
7.004
7.098
9902
9893
9883
116*8.1
1166.9
1165.7
5.968
7.063
7.157
291
290
289
58.4
57.5
56.7
9628
9618
9609
1142.0
1140.9
1139.7
7.075
7.169
7.268
9710
9700
9690
1149.6
1148.4
1147.2
7.134
7.229
7.329
9792
9782
9772
1157.1
1155.9
1154.7
7.194
7.290
7.390
9874
9863
9854
1164.5
1163.3
1162.1
7.254
7.351
7.452
288
287
286
55.8
54.9
54.1
9599
9590
9581
1138.5
1137.3
1136.2
7.367
7.469
7.572
9680
9671
9662
1146.0
1144.8
1143.6
7.430
7.533
7.637
9762
9752
9743
1153.5
1152.3
1151.1
7.491
7.595
7.700
9843
9834
9824
1160.9
1159.7
1158.5
7.554
7.658
7.764
285
284
283
53.2
52.4
51.6
9571
9562
9553
1135.0
1133.8
1132.6
7.678
7.784
7.892
9652
9642
9633
1142.4
1141.2
1140.0
7.743
7.850
7.959
9733
9723
9714
1149.9
1148.6
1147.4
7.807
7.915
8.024
9814
9804
9794
1157.3
1156.1
1154.9
7.872
7.980
8.091
282
281
280
50.8
50.0
49.19
9543
9534
9525
1131.4
1130.3
1129.1
8.003
8.116
8.230
9624
9614
9605
1138.8
1137.6
1136.5
8.071
8.184
8.299
9704
9695
9685
1146.2
1145.1
1143.9
8.137
8.251
8.368
9784
9775
9765
1153.7
1152.5
1151.3
8.204
8.319
8.436
279
278
277
48.41
47.64
46.88
9515
9506
9497
1127.9
1126.6
1125.4
8.344
8.461
8.580
9595
9586
9576
1135.2
1134.0
1132.8
8.414
8.532
8.651
9675
9665
9656
1142.6
1141.4
1140.2
8.484
8.603
8.723
9755
9745
9736
1150.0
1148.7
1147.5
8.553
8.673
8.794
TEMPERATURE-ENTROPY TABLE.
97
j
1
1.64
1.65
1.66
1.67
ttT ^
3
i!
<|
Is
!
g
Jj
I
-n j2
<5 .3
s l
J*
3$
B
H
E
PH
I
*j C
K
I 1
1
K
cc
<
- a
I 1
1
I 1
P
324
94.8
49.4
1212.0
5.048
66.0
1220.9
5.160
82.6
1229.5
5.273
99.9
1238.3
5.400
323
93.5
47.8
1210.8
5.100
64.2
1219.6
5.216
80.8
1228.2
5.330
98.0
1237. 015.459
322
92.2
46.0
1209.6
5.155
62.4
1218.3
5.270
78.9
1226.9
5.389
96.1
1235.7
5.518
321
90.9
44.3
1208.4
5.210
60.6
1217.1
5.327
77.0
1225.6
5.446
94.2
1234.4
5.575
320
89.6
42.6
1207.2
5.265
58.8
1215.9
5.384
75.1
1224.3
5.506
92.4
1233.1
5.635
319
88.3
40.9
1206.0
5.322
57.0
1214.6
5.440
73.3
1223.0
5.565
90.5
1231.8
5.697
318
87.1
39.1
1204.8
5.380
55.1
1213.3
5.500
71.4
1221.7
5.625
88.7
1230.5
5.759
317
85.9
37.5
1203.6
5.435
53.3
1212.0
5.560
69.6
1220.4
5.685
86.8
1229.2
5.820
316
84.6
35.7
1202.4
5.495
51.5
1210.8
5.623
67.8
1219.1
5.750
84.9
1227.9
5.885
315
83.4
34.0
1201.2
5.554
49.8
1209.6
5.685
66.0
1217.8
5.813
83.0
1226.6
5.949
314 82.3
32.3
1200.0
5.614
48.0
1208.3
5.745
64.1
1216.55.875
81.1
1225.3
6.02
313
81.1
30.5
1198.8
5.673
46.2
1207.1
5.810
62.3
1215.2
5.940
79.2
1224.0
6.09
312
79.9
28.8
1197.6
5.734
44.4
1205.9
5.873
60.4
1214.0
6.00
77.3
1222.7
6.16
311
78.8
27.0
1196.4
5.798
42.7
1204.7
5.937
58.6
1212.8
6.07
75.4
1221.4
6.23
310
77.6
25.4
1195.2
5.863
40.9
1203.5
6.00
56.8
1211.6
6.14
73.4
1220.1
6.30
309
76.5
23.7
1193.9
5.928
39.1
1202.2
6.07
55.0
1210.3
6.20
71.5
1218.7
6.37
308 75.4
21.9
1192.75.990
37.3
1200.9
6.14
53.1
1209.0
6.27
69.6
1217.4
6.44
307
74.3
20.1
1191.5
6.06
35.5
1199.7
6.21
51.3
1207.7
6.34
67.7
1216.1
6.51
306
73.2
18.5
1190.3
6.12
33.8
1198.5
6.27
49.4
1206.5
6.41
65.8
1214.8
6.58
305
72.2
16.8
1189.1 6.19
32.0
1197.3
6.34
47.5
1205. 2)6. 48
63.9
1213.5
6.65
304
71.1
15.0
1187.9
6.26
30.1
1196.0
6.41
45.7
1203.9
6.55
62.0
1212.2
6.73
303
70.0
13.3
1186.7
6.33
28.3
1194.7
6.49
43.9
1202.6
6.62
60.1
1210.9
6.80
302 69.0
11.6
1185.56.40
26.5
1193.4
6.56
42.0
1201.3
6.70
58.2
1209.6
6.88
301
68.0
9.9
1184.3
6.48
24.8
1192.2
6.64
40.1
1200.0
6.78
56.3
1208.3
6.96
300
67.0
8.1
1183.1
6.56
23.0
1191.0
6.71
38.3
1198.7
6.86
54.4
1207.0
7.04
299 66.0
6.4
1181.96.64
21.2
1189.8
6.79
36.4
1197.4
6.94
52.5
1205.7
7.12
298
65.0
4.7
1180.7
6.71
19.4
1188.5
6.87
34.5
1196.2
7.01
50.5
1204.4
7.20
297
64.0
2.9
1179.4
6.78
17.6
1187.2
6.95
32.6
1194.9
7.09
48.6
1203.1
7.28
296
63.1
1.2
1178.1 6.86
15.8 1185.9
7.02
30.8
1193.6
7.17
46.7
1201.8
7.37
295
62.1
9996
1176.8
6.934
14.0
1184.6
7.10
29.0
1192.3
7.25
44.8
1200.5
7.45
294
61.2
9985
1175.6
7.026
12.2
1183.4
7.18
27.1
1191.0
7.34
42.9
1199.2
7.53
293
60.2
9975
1174.47.121
10.4
1182.2
7.27
25.3
1189.7
7.43
41.0
1197.9
7.62
292
59.3
9965
1173.2
7.217
8.6
1181.0
7.35
23.4
1188.4
7.51
39.0
1196.6
7.70
291
58.4
9956
1172.0
7.314
6.8
1179.7
7.44
21.5
1187.1
7.60
37.0
1195.3
7.80
290
57.5
9945
1170.8
7.412
5.0
1178.5
7.52
19.7
1185.9
7.69
35.0
1194.0
7.89
289
56.7
9935
1169.5
7.514
3.2
1177.2
7.61
17.9
1184.7
7.78
33.1
1192.7
7.99
288
55.8
9925
1168.3
7.616
1.3
1176.0
7.70
16.0
1183.5
7.88
31.2
1191.4
8.08
287
54.9
9915
1167.1
7.722
9996
1174.6
7.785
14.1
1182.2
7.97
29.3
1190.1
8.17
286
54.1
9905
1166.0
7.828
9986
1173.4
7.892
12.3
1180.9
8.06
27.4
1188.8
8.27
285
53.2
9895
1164.7
7.937
9976
1172.1
8.002
10.4
1179.7
8.15
25.5
1187.5
8.36
284 52.4
9885
1163. 418.046
9965
1170.88.112
8.5
1178.5
8.25
23.6
1186.2
8.45
283
51.6
9875
1162.2
8.158
9955
1169.6
8.224
6.7
1177.3
8.35
21.7
1184.9
8.55
282
50.8
9865
1161.1
8.272
9945
1168.5
8.339
4.9
1176.0
8.45
19.8
1183.6
8.65
281
50.0
9855
1159.9
8.388
9935
1167.38.456
3.0
1174.7
8.55
17.9
1182.3
8.76
280
49.19
9845
1158.7
8.505
9925
1166.1 8.575
1.1
1173.48.65
16.0
1181.0
8.86
279
48.41
9835
1157.4
8.623
9915
1164.88.693
9994
1172.2
8.763
14.0
1179.7
8.97
278 47.64
9825
1156.1
8.744
9905
1163.58.815
9984
1170.9
8.886
12.1
1178.4
9.07
277, 46.88
9815
1154.9
8.866
9895
1162.38.938
9974
1169.7
9.010
10.1
1177.1
9.18
98
TEMPERATURE-ENTROPY TABLE.
to to to 1 Temperature,
^ 1 Degrees Fahr.
Pressure, Pounds!
per Square
Inch.
1.60
1.61
1.62
1.63
>,
<
I.J
|I
d
il
P
02
>,
1
0"
1*
|l
-1
5.
\>
02
>>
1
3
&
l|
I'J
,1
'o
l>
02
>,
4*
"rt
J3
a
c
6 %
13
o a
= 3.
'5 o
r
46.13
45.39
44.67
9488
9479
9470
1124.3
1123.1
1121.9
8.701
8.825
8.953
9567
9558
9549
1131.7
1130.5
1129.2
8.773
8.899
9.027
9647
9637
9628
1139.0
1137.8
1136.5
8.846
8.972
9.102
9726
9716
9707
1146.4
1145.2
1143.9
8.918
9.045
9.176
273
272
271
43.95
43.24
42.54
9461
9451
9442
1120.7
1119.5
1118.3
9.082
9.215
9.350
9539
9530
9521
1128.0
1126.8
1125.6
9.158
9.292
9.427
9618
9609
9599
1135.3
1134.1
1132.9
9.234
9.369
9.505
9697
9687
9678
1142.7
1141.5
1140.2
9.308
9.445
9.583
270
269
268
41.84
41.16
40.49
9433
9424
9414
1117.1
1115.9
1114.7
9.481
9.623
9.763
9511
9502
9492
1124.3
1123.2
1122.0
9.560
9.703
9.844
9590
9580
9570
1131.6
1130.4
1129.2
9.639
9.782
9.925
9668
9658
9648
1138.9
1137.7
1136.5
9.717
9.862
10.00
267
266
265
39.83
39.17
38.53
9406
9395
9387
1113.5
1112.2
1111.0
9.905
10.05
10.20
9483
9473
9465
1120.8
1119.5
1118.3
9.987
10.14
10.29
9561
9551
9542
1128.0
1126.7
1125.5
10.07
10.22
10.37
9639
9629
9620
1135.3
1134.0
1132.8
10.15
10.30
10.46
264
263
262
37.89
37.26
36.64
9378
9369
9360
1109.8
1108.6
1107.4
10.35
10.50
10.66
9456
9446
9437
1117.0
1115.8
1114.6
10.44
10.59
10.75
9533
9523
9514
1124.3
1123.1
1121.8
10.52
10.68
10.84
9610
9601
9591
1131.5
1130.3
1129.1
10.61
10.76
10.92
261
260
259
36.02
35.42
34.83
9351
9341
9332
1106.2
1105.0
1103.8
10.82
10.98
11.14
9428
9418
9409
1113.4
1112.2
1110.9
10.91
11.07
11.23
9504
9495
9485
1120.6
1119.4
1118-.1
11.00
11.16
11.33
9581
9572
9562
1127.9
1126.6
1125.3
11.09
11.25
11.42
258
257
256
34.24
33.66
33.09
9323
9315
9305
1102.5
1101.3
1100.1
11.31
11.48
11.66
9399
9391
9381
1109.6
1108.5
1107.3
11.40
11.58
11.75
9476
9467
9458
1116.8
1115.6
1114.4
11.49
11.67
11.85
9552
9543
9534
1124.0
1122.8
1121.6
11.59
11.77
11.95
255
254
253
32.53
31.97
31.42
9296
9287
9278
1098.8
1097.6
1096.4
11.83
12.02
12.21
9372
9363
9353
1106.0
1104.7
1103.5
11.93
12.12
12.31
9448
9438
9429
1113.1
1111.8
1110.6
12.03
12.21
12.41
9524
9514
9505
1120.3
1119.0
1117.8
12.12
12.31
12.51
252
251
250
30.88
30.35
29.82
9269
9260
9251
1095.2
1094.0
1092.7
12.39
12.58
12.78
9345
9335
9326
1102.3
1101.1
1099.8
12.49
12.69
12.89
9420
9410
9401
1109.4
1108.2
1106.9
12.60
12.79
12.99
9495
9486
9476
1116.5
1115.3
1114.0
12.70
12.89
13.10
249
248
247
29.30
28.79
28.29
9242
9233
9225
1091.5
1090.2
1089.0
12.99
13.18
13.39
9317
9308
9299
1098.6
1097.3
1096.1
13.09
13.29
13.50
9392
9383
9374
1105.6
1104.3
1103.1
13.20
13.40
13.61
9467
9457
9448
1112.7
1111.4
1110.2
13.30
13.51
13.72
246
245
244
27.80
27.31
26.83
9215
9206
9198
1087.8
1086.6
1085.3
13.61
13.82
14.04
9290
9280
9272
1094.8
1093.6
1092.4
13.72
13.93
14.15
9364
9355
9346
1101.9
1100.7
1099.4
13.83
14.04
14.26
9439
9429
9420
1108.9
1107.7
1106.4
13.94
14.15
14.38
243
242
241
26.35
25.88
25.42
9188
9180
9171
1084.1
1082.9
1081.6
14.25
14.48
14.71
9262
9254
9244
1091.2
1089.9
1088.6
14.37
14.59
14.83
9336
9328
9318
1098.2
1096.9
1095.6
14.48
14.71
14.95
9410
9401
9392
1105.2
1103.9
1102.6
14.60
14.83
15.06
240
239
238
24.97
24.52
24.08
9162
9153
9144
1080.3
1079.1
1077.8
14.94
15.18
15.43
9236
9226
9217
1087.3
1086.1
1084.8
15.06
15.31
15.55
9309
9300
9291
1094.3
1093.1
1091.8
15.18
15.43
15.67
9383
9373
9364
1101.3
1100.1
1098.8
15.30
15.55
15.80
237
236
235
23.64
23.21
22.79
9135
9127
9117
1076.6
1075.4
1074.1
15.68
15.93
16.20
9208
9199
9190
1083.6
1082.3
1081.0
15.80
16.06
16.33
9281
9272
9263
1090.6
1089.3
1088.0
15.93
16.19
16.46
9354
9345
9335
1097.5
1096.2
1094.9
16.05
16.32
16.59
234
233
232
22.38
21.97
21.57
9109
9100
9091
1072.8
1071.6
1070.3
16.47
16.74
17.01
9181
9173
9163
1079.7
1078.5
1077.2
16.60
16.87
17.14
9254
9245
9235
1086.6
1085.4
1084.1
16.73
17.00
17.28
9326
9317
9308
1093.6
1092.3
1091.0
16.86
17.13
17.41
231
230
229
21.17
20.78
20.40
9082
9074
9064
1069.1
1067.8
1066.5
17.29
17.58
17.87
9154
9146
9136
1076.0
1074.7
1073.4
17.43
17.72
18.02
9226
9218
9208
1082.9
1081.6
1080.3
17.57
17.85
18.16
9299
9290
9280
1089.8
1088.5
1087.2
17.70
17.99
18.30
TEMPERATURE-ENTROPY TABLE.
99
Temperature,
Degrees Fahr. I
T3
C
o
I't
jy
1.64 1.65
1.66
1.67
>>
Is
I 1
g
i|
5 o
r
J<3
IJ
1
ll
1*
DO
>>
9
!<2
jl
d
&\
V-
cc
a
6 2
|l
*j
l>
cc
276
275
274
46.13
45.39
44.67
9805
9796
9786
1153.7
1152.5
1151.2
8.991
9.119
9.251
9885
9875
9865
1161.1
1159.8
1158.5
9.063
9.193
9.325
9964
9954
9944
1168.5
1167.2
1165.9
9.136
9.266
9.400
8.2
6.3
4.3
1175.9
1174.6
1173.3
9.29
9.40
9.51
273
272
271
43.95
43.24
42.54
9776
9766
9756
1150.0
1148.8
1147.5
9.384
9.521
9.660
9855
9845
9835
1157.3
1156.1
1154.8
9.460
9.598
9.737
9934
9924
9913
1164.6
1163.4
1162.1
9.536
9.675
9.815
2.4
0.6
1172.0
1170.7
9.63
9.76
9992
1169.4
9.89
270
269
268
41.84
41.16
40.49
9746
9737
9726
1146.2
1145.0
1143.8
9.795
9.941
10.09
9825
9815
9804
1153.5
1152.3
1151.1
9.874
10.02
10.17
9903
9893
9882
1160.89.953
1159.6 10.10
1158.3 10.25
9982
9971
9960
1168.1
1166.9
1165.6
10.03
10.18
10.33
267
266
265
39.83
39.17
38.53
9717
9706
9697
1142.5
1141.2
1140.0
10.23
10.39
10.54
9795
9784
9775
1149.8
1148.5
1147.3
10.31
10.47
10.63
9873
9861
9852
1157.0
1155.7
1154.5
10.40
10.55
10.71
9950
9937
9930
1164.3
1163.0
1161.8
10.48
10.64
10.79
264
263
262
37.89
37.26
36.64
9688
9678
9668
1138.7
1137.5
1136.3
10.70
10.85
11.01
9765
9755
9745
1146.0
1144.8
1143.5
10.78
10.94
11.10
9842
9832
9822
1153.2
1152.0
1150.7
10.87
11.02
11.19
9920
9910
9899
1160.5
1159.2
1157.9
10.95
11.11
11.28
261
260
259
36.02
35.42
34.83
9658
9648
9639
1135.1
1133.8
1132.5
11.17
11.34
11.51
9735
9725
9715
1142.3
1141.0
1139.7
11.26
11.43
11.60
9812
9802
9792
1149.5
1148.2
1146.9
11.35
11.52
11.69
9889
9878
9868
1156.7
1155.4
1154.1
11.44
11.61
11.78
258
257
256
34.24
33.66
33.09
9629
9620
9610
1131.2
1130.0
1128.7
11.68
11.86
12.04
9705
9696
9686
1138.3
1137.1
1135.9
11.77
11.95
12.14
9781
9772
9762
1145.5
1144.3
1143.0
11.86
12.05
12.23
9858
9848
9838
1152.7
1151.5
1150.2
11.96
12.14
12.33
255
254
253
32.53
31.97
31.42
9600
9590
9580
1127.4
11 26/1
1124.9
12.22
12.. 41
12.61
9676
9666
9656
1134.6
1133.2
1132.0
12.32
12.51
12.71
9752
9741
9731
1141.7
1140.4
1139.2
12.41
12.61
12.81
9828
9817
9807
1148.9
1147.5
1146.3
12.51
12.70
12.91
252
251
250
30.88
30.35
29.82
9571
9561
9551
1123.6
1122.4
1121.1
12.80
12.99
13.20
9646
9636
9626
1130.7
1129.5
1128.2
12.90
13.10
13.30
9722
9712
9701
1137.9
1136.6
1135.3
13.00
13.20
13.41
9797
9787
9776
1145.0
1143.7
1142.4
13.10
13.30
13.51
249
248
247
29.30
28.79
28.29
9542
9532
9523
1119.8
1118.5
1117.3
13.41
13.61
13.83
9617
9607
9598
1126.9
1125.6
1124.3
13.51
13.72
13.94
9692
9682
9672
1134.0
1132.6
1131.4
13.62
13.83
14.04
9767
9757
9747
1141.1
1139.7
1138.4
13.72
13.93
14.15
246
245
244
27.80
27.31
26.83
9513
9503
9494
1116.0
1114.8
1113.5
14.05
14.26
14.49
9588
9578
9569
1123.0
1121.8
1120.5
14.16
14.38
14.60
9662
9652
9643
1130.1
1128.8
1127.5
14.27
14.49
14.71
9737
9726
9717
1137.1
1135.9
1134.6
14.38
14.60
14.83
243
242
241
26.35
25.88
25.42
9484
9475
9465
1112.2
1110.9
1109.6
14.71
14.94
15.18
9558
9549
9539
1119.2
1117.9
1116.6
14.83
15.06
15.30
9632
9623
9613
1126,3
1125.0
1123.7
14.94
15.18
15.42
9706
9697
9686
1133.3
1132.0
1130.7
15.05
15.29
15.54
240
239
238
24.97
24.52
24.08
9456
9446
9437
1108.3
1107.0
1105.7
15.42
15.67
15.92
9530
9520
9510
1115.3
1114.0
1112.7
15.54
15.79
16.04
9603
9593
9584
1122.3
1121.0
1119.7
15.66
15.91
16.17
9677
9666
9657
1129.3
1128.0
1126.7
15.78
16.04
16.29
237
236
235
23.64
23.21
22.79
9427
9418
9408
1104.5
1103.2
1101.9
16.18
16.44
16.72
9500
9491
9481
1111.4
1110.1
1108.8
16.30
16.57
16.85
9573
9564
9554
1118.4
1117.1
1115.8
16.43
16.70
16.98
9646
9637
9626
1125.4
1124.0
1122.7
16.55
16.83
17.11
234
233
332
22.38
21.97
21.57
9399
9390
9380
1100.5
1099.2
1097.9
16.99
17.27
17.55
9472
9462
9452
1107.4
1106.1
1104.8
17.12
17.40
17.68
9544
9535
9524
1114.4
1113.1
1111.8
17.26
17.53
17.82
9617
9607
9597
1121.3
1120.0
1118.7
17.39
17.67
17.96
231
230
229
21.17
20.78
20.40
9371
9362
9351
1096.7
1095.4
1094.1
17.84
18.13
18.44
9443
9434
9423
1103.6
1102.3
1100.9
17.98
18.27
18.58
9515
9505
9495
1110.5
1109.2
1107.8
18.12
18.41
18.72
9587
9577
9567
1117.4
1116.1
1114.7
18.25
18.55
18.87
100
TEMPERATURE-ENTROPY TABLE.
ll
II
228
227
226
Pressure, Pounds]
per Square
Inch.
1.60
1.61
1.62
1.63
>>
I
||
ll
H
4
ll
3 o
r
>
"3
3
a
63
+3 a
11
*j
F
OJ
>>
5
3
0"
l|
|l
!
'5
1
1
l|
ll
0>
ll
ll
02
20.02
19.64
19.28
9055
9047
9039
1065.2
1064.0
1062.7
18.17
18.47
18.78
9127
9118
9110
1072.1
1070.9
1069.6
18.32
18.62
18.93
9198
9190
9182
1079.0
1077.7
1076.4
18.46
18.77
19.08
9270
9261
9253
1085.8
1084.6
1083.3
18.60
18.91
19.23
225
224
223
18.91
18.56
18.21
9029
9020
9012
1061.5
1060.2
1059.0
19.11
19.43
19.76
9100
9091
9083
1068.3
1067.0
1065.8
19.26
19.58
19.92
9171
9162
9154
1075.1
1073.8
1072.6
19.41
19.74
20.07
9243
9234
9224
1082.0
1080.7
1079.4
19.56
19.89
20.23
222
221
220
17.86
17.52
17.19
9003
8995
8986
1057.7
1056.5
1055:2
20.10
20.44
20.79
9074
9065
9056
1064.5
1063.3
1062.0
20.26
20.60
20.96
9145
9136
9127
1071.3
1070.1
1068.8
20.42
20.77
21.12
9215
9206
9197
1078.1
1076.9
1075.6
20.58
20.93
21.28
219
218
217
16.86
16.54
16.22
8976
8968
8959
1053.9
1052.6
1051.3
21.15
21.51
21.89
9047
9038
9029
10G0.7
1059.:
1058.0
21.31
21.68
22.06
9117
9108
9099
1067.4
1066.0
1064.8
21.48
21.85
22.23
9107
9178
9169
1074.2
1072.8
1071.5
21.65
22.02
22.40
216
215
214
15.90
15.60
15.29
8950
8942
8933
1050.0
1048.7
1047.4
22.27
22.66
23.06
9020
9011
9002
1056.7
1055.4
1054.1
22.44
22.83
23.24
9090
9081
9072
1003.5
1062.2
1060.9
CC.62
23.01
23.41
9160
9151
9141
1070.2
1068.9
1067.6
22.79
23.19
23.59
213
212
211
14.99
14.70
14.41
8924
8915
8907
1046.2
1044.9
1043.6
23.46
23.88
24.31
8994
8985
8976
1052.9
1051.6
1050.3
23.64
24.06
24.50
9063
9054
9045
1059.6
1058.3
1057.0
23 G
24^25
24.68
9132
9123
9115
1066.3
1065.0
1063.7
24.01
24.43
24.87
210
209
208
14.13
13.85
13.57
8899
8890
8882
1042.3
1041.0
1039.7
24.74
25.18
25.63
8968
8959
8950
1049.0
1047.7
1046.4
24.93
25.37
25.83
9037
9028
9019
1055.7
1054.3
1053.0
25.12
25.57
26.03
9106
9097
9088
1062.4
1061.0
1059.7
25.31
25.76
26.23
207
206
205
13.30
13.03
12.77
8873
8864
8855
1038.4
1037.1
1035.8
26.09
26.57
27.06
8941
8932
8923
1045.0
1043.7
1042.4
26.30
26.78
27.27
9010
9001
8992
1051.7
1050.4
1049.1
26.50
26.98
C7.48
9078
9069
9060
1058.4
1057.1
1055.7
26.70
27.19
27.69
204
203
202
12.51
12.26
12.01
8846
8837
8830
1034.5
1033.2
1031.9
27.56
28.06
28.58
8914
8905
8897
1041.1
1039.8
1038.6
27.77
28.27
28.80
8983
8973
8965
1047.8
1046.4
1045.2
27.98
28.49
29.02
9051
9041
9033
1054.4
1053.1
1051.8
28.19
28.71
29.24
201
200
198
11.77
11.53
11.29
8821
8812
8803
1030.6
1029.3
1028.0
29.10
29.63
30.17
8888
8879
8871
1037.2
1035.9
1034.6
29.32
29.85
30.40
8956
8947
8938
1043.8
1042.5
1041.2
29.55
30.08
30.63
9024
9014
9005
1050.4
1049.1
1047.7
29.77
30.31
30.86
198
197
196
11.06
10.83
10.61
8795
8786
8777
1026.7
1025.3
1024.0
30.72
31.29
31.87
8862
8853
8844
1033.3
1031.9
1030.5
30.96
31.53
32.11
8929
8920
8911
1039.9
1038.4
1037.1
31.19
31.76
32.36
8997
8987
8978
1046.5
1045.0
1043.6
31.43
32.00
32.60
195
194
193
10.39
10.17
9.96
8769
8760
8752
1022.7
1021.4
1020.1
32.47
33.09
33.72
8836
8827
8818
1029.3
1027.9
1026.6
32.72
33.34
33.98
8902
8893
8885
1035.8
1034.5
1033.2
32.97
33.59
34.23
8969
8960
8951
1042.4
1041.0
1039.7
33.21
33.84
34.49
192
191
190
9.75
9.54
9.34
8743
8734
8725
1018.8
1017.4
1016.2
34.37
35.03
35.70
8809
8800
8791
1025.3
1023.9
1022.6
34.63
35.30
35.97
8875
8866
8857
1031.8
1030.4
1029.1
34.89
35.56
36.24
8942
8932
8923
1038.3
1037.0
1035.6
35.15
35.83
36.51
189
188
187
9.14
8.95
8.76
8717
8708
8699
1014.9
1013.5
1012.2
36.39
37.09
37.80
8783
8774
8765
1021.4
1020.0
1018.7
36.67
37.37
38.08
8849
8839
8830
1027.8
1026.5
1025.2
36.94
37.65
38.37
8915
8905
8896
1034.3
1032.9
1031.6
37.22
37.93
38.65
186
185
184
8.57
8.38
8.20
8690
8682
8673
1010.9
1009.6
1008.2
38.52
39.27
40.04
8756
8747
8738
1017.3
1016.0
1014.6
38.81
39.56
40.34
8821
8812
8803
1023.8
1022.5
1021.1
39.10
39.86
40.64
8887
8878
8868
1030.2
1028.9
1027.5
39.39
40.15
40.94
183
182
181
8.02
7.85
7.68
8664
8656
8648
1006.9
1005.4
1004.2
40.83
41.64
42.49
8729
8721
8712
1013.3
1012.0
1010.6
41.13
41.96
42.80
8795
8786
8777
1019.8
1018.4
1017.0
41.44
42.27
43.12
8860
8851
8842
1026.2
1024.8
1023.4
41.75
42.58
43.44
TEMPERATURE-ENTROPY TABLE.
101
Temporal uro,
Degrees Fahr. 1
*f
i^
(&H
c
1.64 1.65 1.66
1.67
,
8
6 3
jJ
-i
<n 2.
\>
$
5
Jj
11
H
J
!?
>>
1
l|
|l
!
*5 ^
>
c
3s
I 1
ll
V
228
227
226
20.02
19.64
19.28
9342
9333
9324
1092.7
1091.4
1090.1
18.75
19.06
19.38
9413
9404
9396
1099.6
1098.3
1097.0
18.89
19.20
19.52
9485
9476
9467
1106.5
1105.2
1103.9
19.04
19.35
19.67
9557
9547
9539
1113.3
1112.0
1110.7
19.18
19.50
19.82
225
224
223
18.91
18.56
18.21
9314
9305
9295
1088.8
1087.5
1086.2
19.71
20.04
20.38
9385
9376
9366
1095.7
1094.3
1093.1
19.86
20.20
20.54
9456
9447
9437
1102.6
1101.2
1099.9
20.01
20.35
20.70
9527
9518
9508
1109.4
1108.0
1106.7
20.16
20.50
20.85
222
221
220
17.86
17.52
17.19
9286
9277
9268
1084.9
1083.6
1082.3
20.74
21.09
21.45
9357
9347
9338
1091.8
1090.5
1089.1
20.89
21.25
21.61
9428
9418
9408
1098.6
1097.3
1095.9
21.05
21.41
21.77
9498
9489
9479
1105.4
1104.1
1102.7
21.21
21.57
21.93
219
218
217
16.86
16.54
16.22
9258
9248
9239
1081.0
1079.6
1078.3
21.81
22.19
22.57
9328
9318
9309
1087.8
1086.4
1085.1
21.98
22.35
22.74
9398
9388
9379
1094.522.14
1093.1 22.52
1091.822.91
9468
9459
9449
1101.3
1099.9
1098.6
22.31
22.69
23.08
216
215
214
15.90
15.60
15.29
9230
9220
9211
1077.0
1075.7
1074.4
22.96
23.36
23.77
9300
9290
9281
1083.7
1082.4
1081.1
23.14
23.54
23.95
9369
9360
9350
1090.5
1089.2
1087.8
23.31
23.72
24.13
9439
9430
9420
1097.2
1095.9
1094.6
23.48
23.89
24.31
213
212
211
14.99
14.70
14.41
9202
9192
9184
1073.1
1071.7
1070.4
24.19
24.62
25.06
9271
9262
9253
1079.8
1078.4
1077.1
24.37
24.80
25.25
9341
9331
9322
1086.5
1085.1
1083.8
24.56
24.99
25.44
9410
9400
9391
1093.324.74
1091.9J25.17
1090.625.63
210
209
208
14.13
13.85
13.57
9174
9166
9156
1069.1
1067.7
1066.4
25.51
25.96
26.42
9243
9234
9225
1075.8
1074.4
1073.1
25.70
26.15
26.62
9312
9303
9294
1082.5
1081.1
1079.7
25.89
26.35
26.82
9381
9372
9362
1089.2
1087.8
1086.4
26.08
26.54
27.02
207
206
205
13.30
13.03
12.77
9147
9137
9128
1065.0
1063.7
1062.4
26.90
27.39
27.90
9215
9206
9196
1071.7
1070.4
1069.0
27.10
27.60
28.10
9284
9274
9265
1078.4
1077.0
1075.7
27.30
27.80
28.31
9352
9342
9333
1085.0
1083.7
1082.3
27.51
28.01
28.52
204
203
202
12.51
12.26
12.01
9119
9109
9101
1061.0
1059.7
1058.4
28.40
28.92
29.46
9187
9177
9168
1067.7
1066.3
1065.0
28.62
29.14
29.68
9255
9245
9236
1074.3
1072.9
1071.6
28.83
29.35
29.90
9323
9313
9304
1080.9
1079.6
1078.2
29.04
29.57
30.12
201
200
199
11.77
11.53
11.29
9091
9082
9073
1057.0
1055.7
1054.3
29.99
30.53
31.09
9159
9149
9140
1063.6
1062.3
1060.9
30.21
30.76
31.32
9227
9217
9207
1070.3
1068.9
1067.5
30.44
30.99
31.55
9294
9284
9275
1076.9
1075.5
1074.1
30.66
31.21
31.78
198
197
196
11.06
10.83
10.61
9064
9054
9045
1053.0
1051.6
1050.2
31.66
32.24
32.84
9131
9121
9112
1059.6
1058.1
1056.8
31.89
32.48
33.08
9198
9188
9179
1066.2
1064.7
1063.3
32.13
32.72
33.33
9265
9255
9245
1072.8
1071.3
1069.9
32.36
32.96
33.57
195
194
193
10.39
10.17
9.96
9036
9026
9018
1048.933.46
1047.5 34.09
1046.2j34.74
9103
9093
9084
1055.4
1054.1
1052.7
33.71
34.34
35.00
9170
9160
9151
1062.0
1060.6
1059.3
33.95
34.60
35.26
9236
9226
9217
1068.5
1067.1
1065.8
34.20
34.85
35.51
192 9.75
1911 9.54
190 9.34
9008
8998
8989
1044.8
1043.5
1042.1
35.41
36.09
36.78
9074
9065
9055
1051.4
1050.0
1048.6
35.67
36.36
37.05
9141
9131
9121
1057.9
1056.5
1055.1
35.93
36.62
37.32
9207
9197
9188
1064.4
1063.0
1061.6
36.19
36.89
37.60
189 9.14
188 8.95
187 8.76
8980
8971
8962
1040.8
1039.4
1038.1
37.49
38.21
38.94
9046
9037
9027
1047.3
1045.9
1044.6
37.77
38.49
39.22
9112
9102
9093
1053.8
1052.4
1051.0
38.04 9178
38.77i 9168
39.51 9159
1060.3
1058.8
1057.5
38.32
39.05
39.79
186
185
184
8.57
8.38
8.20
8954
8943
8933
1036.7
1035.4
1034.0
39.68
40.45
41.25
9018
9008
8999
1043.1
1041.8
1040.4
39.97
40.74
41.55
9083
9074
9064
1049.6
1048.2
1046.8
40.27
41.04
41.85
9149
9139
9129
1056.1
11054.7
1053.2
40.56
41.33
42.15
183
182
181
8.02
7.85
7.68
8925
8916
8907
1032.6
1031.3
1029.8
42.05
42.89
43.76
8990
8981
8972
1039.0
1037.7
1036.2
42.36
43.21
44.08
9055
9046
9036
1045.5
1044.1
1042.6
42.67
43.52
44.40
9120
9111
9101
1051.9
1050.5
1049.0
42.97
43.83
44.71
IO2
TEMPERATURE-ENTROPY TABLE.
h
1
1.60
1.61
1.62
1.63
*3
o
3
||
oTo 1
^CQ -H
6
!*
z i
1 j
3
g
Ijs
v 1
l|
to
ii
?
IHs
1
I 1
02
1
ll
w
02
1
I 1
02*
"d
G
W ^
J|
02
180
7.51
8639
1002.8
43.37
8703
1009.2
43.69
8768
1015.6
44.01
8833
1022.0
44.34
179
7.35
8630
1001.5
44.19
8695
1007.9
44.52
8759
1014.3
44.85
8824
1020.7
45.18
178
7.19
8622
1000.2
45.09
8686
1006.6
45.43
8750
1012.9
45.76
8815
1019.3
46.10
177
7.03
8613
998.9
45.99
8678
1005.2
46.34
8742
1011.6
46.68
8806
1018.0
47.02
176
6.87
8604
997.5
46.89
8668
1003.8
47.24
8732
1010.2
47.59
8796
1016.5
47.94
175
6.71
8596
996.1
47.88
8660
1002.5
48.23
8724
1008.8
48.59
8788
1015.2
48.95
174
6.56
8587
994.8
48.86
8651
1001.2
49.22
8715
1007.5
49.59
8779
1013.8
49.95
173
6.42
8579
993.5
49.84
8643
999.8
50.2
8706
1006.1
50.6
8770
1012.5
51.0
172
6.27
8570
992.1
50.8
8634
998.5
51.2
8697
1004.8
51.6
8761
1011.1
52.0
171
6.13
8561
990.7
51.9
8624
997.0
52.3
8688
1003.4
52.6
8751
1009.7
53.0
170
5.99
8552
989.4
53.0
8616
995.7
53.4
8679
1002.0
53.8
8742
1008.3
54.2
169
5.85
8544
988.1
54.2
8607
994.3
54.6
8670
1000.6
55.0
8733
1006.9
55.4
168
5.72
8536
986.7
55.3
8599
993.0
55.7
8662
999.3
56.1
8725
1005.5
56.5
167
5.59
8527
985.3
56.4
8589
991.6
56.9
8652
997.9
57.3
8715
1004.1
57.7
166
5.46
8518
984.0
57.7
8581
990.2
58.1
8644
996.5
58.5
8706
1002.8
58.9
165
5.33
8510
982.6
58.8
8572
988.9
59.2
8635
995.1
59.7
8697
1001.4
60.1
164
5.21
8501
981.3
60.0
8563
987.5
60.5
8626
993.7
60.9
8688
1000.0
61.3
163
5.09
8492
979.9
61.2
8555
986.1
61.7
8617
992.4
62.1
8679
998.6
62.6
162
4.969
8484
978.5
62.5
8546
984.7
63.0
8608
991.0
63.4
8670
997.2
63.9
161
4.852
8475
977.2
63.9
8537
983.4
64.4
8599
989.6
64.8
8661
995.8
65.3
160
4.738
8467
975.8
65.4
8529
982.0
65.8
8590
988.2
66.3
8652
994.4
66.8
159
4.626
8458
974.5
66.7
8520
980.7
67.2
8582
986.8
67.7
8643
993.0
68.2
158
4.517
8449
973.1
68.2
8511
979.3
68.7
8573
985.4
69.2
8634
991.6
69.7
157
4.409
8441
971.8
69.7
8503
977.9
70.2
8564
984.1
70.7
8626
990.3
71.2
156
4.303
8432
970.4
71.3
8494
976.5
71.8
8555
982.7
72.3
8616
988.8
72.8
155
4.200
8424
969.0
72.8
8485
975.1
73.3
8546
981.3
73.8
8607
987.4
74.4
154
4.099
8415
967.6
74.4
8476
973.7
74.9
8537
979.9
75.5
8598
986.0
76.0
153
4.000
8406
966.2
76.0
8467
972.4
76.5
8528
978.5
77.1
8589
984.6
77.6
152
3.903
8397
964.8
77.7
8458
971.0
78.2
8519
977.1
78.8
8580
983.2
79.4
151
3.808
8388
963.4
79.4
8449
969.5
80.0
8510
975.7
80.6
8570
981.8
81.2
150
3.715
8380
962.1
81.2
8441
968.2
81.8
8501
974.3
82.4
8562
980.4
83.0
149
3.624
8371
960.7
83.0
8432
966.8
83.6
8492
972.9
84.2
8552
978.9
84.8
148
3.535
8363
959.3
85.0
8423
965.4
85.6
8483
971.5
86.2
8544
977.6
86.8
147
3.447
8354
957.9
86.9
8414
964.0
87.5
8474
970.0
88.1
8534
976.1
88.8
146
3.361
8345
956.6
88.9
8405
962.6
89.5
8465
968.7
90.2
8525
974.7
90.8
145
3.278
8336
955.1
90.9
8396
961.2
91.5
8456
967.2
92.2
8516
973.3
92.8
144
3.196
8328
953.8
92.9
8388
959.8
93.6
8447
965.8
94.3
8507
971.9
94.9
143
3.116
8319
952.3
95.1
8378
958.4
95.8
8438
964.4
96.4
8498
970.4
97.1
142
3.037
8311
951.0
97.3
8370
957.0
98.0
8429
963.0
98.7
8489
969.0
99.4
141
2.960
8302
949.6
99.5
8361
955.6
100.3
8421
961.6
101.0
8480
967.6
101.7
140
2.885
8293
948.1
101.8
8352
954.1
102.6
8411
960.1
103.3
8470
966.1
104.0
139
2.812
8285
946.8
104.3
8344
952.7
105.0
8403
958.7
105.8
8462
964.7
106.5
138
2.740
8276
945.4
106.7
8335
951.3
107.4
8394
957.3
108.2
8453
963.3
109.0
137
2.669
8267
943.9
109.2
8326
949.9
110.0
8384
955.8
110.8
8443
961.8
111.5
136
2.600
8258
942.5
111.8
8317
948.5
112.6
8376
954.4
113.4
8434
960.4
114.2
135
2.533
8250
941.1
114.5
8309
947.1
115.3
8367
953.0
116.1
8426
959.0
116.9
134
2.467
8241
939.7
117.2
8299
945.6
118.0
8358
951.5
118.8
8416
957.5
119.7
133
2.403
8232
938.3
120.0
8291
944.2
120.9
8349
950.1
121.7
8407
956.0
122.6
TEMPERATURE-ENTROPY TABLE.
103
jj
1.64
1.65
1.66
1.67
t*
3 a,
CM
3
fia
.3
>>
Ja
of
*
Is
j
|j
||
>>
J|
J
a
K&s
3
V %
>
1
il
'1^
13
3
11
'1^
3
1 -2
'1^
EH
PL,
&
K
02
a
B
tn
a
B
9
B
GO
180
7.51
8897
1028.4
44.66
8962
1034.8
44.99
9026
1041.2
45.31
9091
1047.6
45.64
179
7.35
8888
1027.0
45.51
8953
1033.4
45.84
9017
1039.8
46.17
9082
1046.2
46.50
178
7.19
8879
1025.7
46.44
8944
1032.1
46.77
9008
1038.4
47.11
9072
1044.8
47.45
177
7.03
8870
1024.3
47.37
8934
1030.7
47.71
8999
1037.1
48.05
9063
1043.4
48.39
176
6.87
8860
1022.9
48.29
8925
1029.3
48.64
8989
1035.6
48.99
9053
1042.0
49.34
175
6.71
8852
1021.5
49.30
8916
1027.9
49.66
8979
1034.2
50.0
9043
1040.6
50.4
174
6.56
8843
1020.2
50.3
8906
1026.5
50.7
8970
1032.8
51.0
9034
1039.2
51.4
173
6.42
8833
1018.8
51.3
8897
1025.1
51.7
8961
1031.4
52.1
9024
1037.8
52.4
172
6.27
8824
1017.4
52.3
8888
1023.7
52.7
8951
1030.0
53.1
9015
1036.4
53.5
171
6.13
8815
1016.0
53.4
8878
1022.3
53.8
8941
1028.6
54.2
9005
1034.9
54.6
170
5.99
8805
1014.6
54.6
8869
1020.9
55.0
8932
1027.2
55.4
8995
1033.5
55.8
169
5.85
8796
1013.2
55.8
8859
1019.5
56.2
8922
1025.8
56.6
8986
1032.0
57.0
168
5.72
8788
1011.8
56.9
8851
1018.1
57.4
8914
1024.457.8
8977
1030.6
58.2
167
5.59
8778
1010.4
58.1
8841
1016.7
58.5
8904
1022.9
58.9
8966
1029.2
59.4
166
5.46
8769
1009.0
59.4
8832
1015.3
59.8
8894
1021.6
60.2
8957
1027.8
60.6
165
5.33
8760
1007.6
60.5
8822
1013.9
61.0
8885
1020.1
61.4
8948
1026.3
61.8
164
5.21
8751
1006.2
61.8
8813
1012.4
62.2
8876
1018.7
62.7
8938
1024.9
63.1
163
5.09
8742
1004.8
63.0
8804
1011.0
63.5
8866
1017.3
63.9
8928
1023.5
64.4
162
4.969
8732
1003.4
64.4
8794
1009.6
64.8
8856
1015.8
65.3
8919
1022.0
65.7
161
4.852
8723
1002.0
65.8
8785
1008.2
66.2
8847
1014.5
66.7
8909
1020.7167.2
160
4.738
8714
1000.6
67.3
8776
1006.8
67.8
8838
1013.0
68.2
8900
1019.2
68.7
159
4.626
8705
999.2
68.7
8767
1005.4
69.2
8829
1011.6
69.7
8890
1017.8
70.1
158
4.517
8696
997.8
70.2
8757
1004.0
70.7
8819
1010.1
71.2
8881
1016.3
71.7
157
4.409
8687
996.4
71.8
8748
1002.6
72.3
8810
1008.8
72.8
8871
1014.9
73.3
156 1 4.303
8678
995.0
73.3
8739
1001.1
73.8
8800
1007.3
74.4
8862
1013.5
74.9
155 4.200
8668
993.6
74.9
8729
999.7175.4
8791
1005.9
76.0
8852
1012.0
76.5
154J 4.099
8659
992.1
76.5
8720
998.3
77.1
8781
1004.4
77.6
8842
1010.5
78.2
153 4.000
8650
990.7
78.2
8711
996.9
78.7
8772
1003.0
79.3
8833
1009.1
79.8
152
3.903
8640
989.3
79.9
8701
995.4
80.5
8762
1001.5
81.0
8823
1007.7
81.6
151
3.808
8631
987.9
81.7
8692
994.0
82.3
8752
1000.1
82.9
8813
1006.2
83.5
150
3.715
8622
986.5
83.5
8683
992.6
84.1
8743
998.7
84.7
8804
1004.8
85.3
149
3.624
8613
985.0
85.4
8673
991.1
86.0
8733
997.2
86.6
8794
1003.3
87.2
148
3.535
8604
983.6
87.4
8664
989.7
88.0
8724
995.8
88.6
8785
1001.9
89.3
147
3.447
8594
982.2
89.4
8654
988.2
90.0
8715
994.3
90.6
8775
1000.4
91.3
146
3.361
8585
980.8
91.4
8645
986.892.1
8705
992.9
92.7
8765
998.9
93.3
145
3.278
8576
979.3
93.5
8636
985.4
94.1
8695
991.4
94.8
8755
997.4
95.4
144
3.196
8567
977.9
95.6
8626
983.9
96.3
8686
990.0
96.9
8746
996.0
97.6
143
3.116
8557
976.4
97.8
8617
982.5
98.5
8676
988.5
99.2
8736
994.5
99.9
142
3.037
8548
975.0
100.1
8608
981.0
100.8
8667
987.0
101.5
8727
993.1
102.2
141
2.960
8539
973.6
102.4
8598
979.6
103.1
8658
985.6
103.8
8717
991.6
104.5
140 1 2.885
8530
972.1
104.7
8589
978.1
105.5
8648
984.1
106.2
8707
990.1
106.9
139
2.812
8521
970.7
107.3
8580
976.7
108.0
8639
982.7
108.7
8698
988.6
109.5
138
2.740
8512
969.3
109.7
8571
975.2
110.5
8630
981.2
111.2
8689
987.2
112.0
137
2.669
8502
967.8
112.3
8561
973.7 113.1
8620
979.7
113.9
8678
985.7
114.6
136
2.600
8493
966.3
115.0
8552
972.3
115.8
8610
978.3
116.6
8669
984.2
117.4
136
2.533
8484
964.9
117.8
8543
970.9
118.6
8601
976.8
119.4
8660
982.7
120.2
134 2.467
8474
963.4 120.5
8533
969.3
121.3
8591
975.3
122.2
8649
981.2
123.0
133 2.403
8465
962.0 123.4
8524
967.9
124.3
8582
973.8
125.1
8640
979.7
126.0
104
TEMPERATURE-ENTROPY TABLE.
.1
1
1.60
1.61
1.62
1.63
3^ H
n<!
,
O
,
CJ
,
,
,
|l
!&
g
1 JS
jj
>,
J <2
>,
rS ri
|
g
r^
a
SQ
lS*S
$
o> >
$Z
%>
3
2
3
1 "
H
&
B
OQ
<y
B
OQ
&
B
O"
w "*
DO
132
2.341
8224
936.9
122.9
8282
942.8
123.8
8340
948.7
124.7
8398
954.6
125.6
131
2.280
8215
935.4
125.9
8273
941.3
126.7
8331
947.3
127.6
8389
953.2
128.5
130
2.220
8207
934.0
128.9
8265
939.9
129.8
8323
945.8
130.7
8380
951.7
131.7
129
2.161
8198
932.6
132.1
8256
938.5
133.0
8314
944.4
133.9
8371
950.3
134.9
128
2.103
8189
931.2
135.3
8247
937.1
136.2
8305
942.9
137.2
~8362
948.8
138.1
127
2.047
8181
929.8
138.6
8238
935.7
139.6
8296
941.5
140.5
8353
947.4
141.5
126
.992
8172
928.3
142.0
8229
934.2
143.0
8287
940.0
144.0
8344
945.9
145.0
125
.938
8163
926.9
145.5
8220
932.8
146.6
8278
938.6
147.6
8335
944.5
148.6
124
.886
8154
925.5
149.1
8211
931.3
150.2
8268
937.1
151.2
8326
943.0
152.3
123
.835
8145
924.1
152.9
8202
929.9
154.0
8259
935.7
155.0
8316
941.6
156.1
122
.785
8137
922.6
156.8
8194
928.4
157.9
8250
934.2
159.0
8307
940.1
160.1
121
.737
8129
921.2
160.8
8185
927.0
161.9
8242
932.8
163.0
8299
938.6
164.1
120
.689
8120
919.8
164.8
8176
925.6
166.0
8233
931.3
167.1
8289
937.1
168.3
119
.642
8111
918.4
169.0
8167
924.2
170.2
8224
929.9
171.4
8280
935.7
172.6
118
.597
8102
916.9
173.4
8159
922.7
174.6
8215
928.5
175.8
8271
934.2
177.0
117
.552
8093
915.5
177.9
8149
921.2
179.1
8206
927.0
180.4
8262
932.7
181.6
116
.509
8084
914.0
182.5
8140
919.7
183.7
8196
925.5
185.0
8253
931.2
186.3
115
.467
8076
912.6
187.2
8132
918.3
188.5
8188
924.1
189.8
8244
929.8
191.1
114
.426
8067
911.1
192.0
8122
916.8
193.3
8178
922.6
194.6
8234
928.3
196.0
113
.386
8058
909.7
196.9
8113
915.4
198.3
8169
921.1
199.6
8225
926.9
201.0
112
.347
8049
908.2
202.1
8104
913.9
203.5
8160
919.6
204.9
8216
925.4
206.3
111
.308
8040
906.8
207.4
8095
912.5
208.9
8151
918.2
210.3
8206
923.9
211.7
110
.271
8031
905.3
213.0
8087
911.0
214.5
8142
916.7
215.9
8197
922.4
217.4
109
.235
8022
903.9
218.7
8077
909.6
220.2
8132
915.2
221.7
8188
920.9
223.2
108
.200
8014
902.4
224.5
8069
908.1
226.1
8124
913.7
227.6
8179
919.4
229.2
107
.165
8004
901.0
230.7
8059
906.6
232.3
8114
912.3
233.9
8169
917.9
235.4
106
.131
7996
899.5
237.0
8051
905.1
238.6
8105
910.8
240.2
8160
916.4
241.9
105
1.098
7987
898.0
243.4
8042
903.6
245.1
8096
909.3
246.8
8151
914.9
248.4
104
1.066
7978
896.5
250.1
8032
902.1
251.8
8087
907.8
253.5
8142
913.4
255.2
103
1.035
7969
895.1
256.9
8024
900.7
258.7
8078
906.3
260.4
8133
911.9
262.2
102
1.005
7961
893.6
264.0
8015
899.2
265.8
8069
904.8
267.6
8123
910.4
269.4
101
0.975
7952
892.1
271.2
8006
897.7
273.1
8060
903.3
274.9
8115
908.9
276.8
100
0.946
7943
890.6
278.6
7997
896.2
280.5
8051
901.8
282.4
8105
907.4
284.3
99
0.918
7934
889.2
286.4
7988
894.8
288.3
8042
900.3
290.2
8096
905.9
292.2
98
0.891
7925
887.7
294.3
7979
893.3
296.3
8033
898.8
298.3
8087
904.4
300.3
97
0.864
7917
886.3
302.5
7970
891.9
304.5
8024
897.4
306.6
8077
903.0
308.6
96
0.838
7908
884.9
311.0
7961
890.4
313.1
8015
896.0
315.2
8068
901.5
317.3
95
0.813
7899
883.4
319.8
7952
888.9
321.9
8006
894.5
324.1
8059
900.0
326.2
94
0.788
7890
881.9
328.8
7943
887.4
331.0
7997
893.0
333.2
8050
898.5
335.4
93
0.764
7882
880.4
338.2
7935
885.9
340.5
7988
891.5
342.8
8041
897.0
345.0
92
0.741
7872
878.9
348.0
7925
884.4
350.3
7978
889.9
352.6
8031
895.5
355.0
91
0.718
7864
877.4
358.1
7917
882.9
360.5
7969
888.4
362.9
8022
894.0
365.3
90
0.696
7855
875.9
368.5
7908
881.4
371.0
7960
886.9
373.5
8013
892.4
376.0
89
0.675
7846
874.4
379.3
7899
879.9
381.8
7951
885.4
384.4
8004
890.9
386.9
88
0.654
7837
872.9
390.3
7890
-878.4
392.9
7942
883.9
395.5
7995
889.3
398.1
87
0.633
7829
871.4
401.6
7881
876.9
404.3
7933
882.4
407.0
7986
887.8
409.7
86
0.613
7820
869.9
412.9
7872
875.4
415.6
7924
880.9
418.4
7976
886.3
421.2
85
0.594
7811
868.4
424.9
7863
873.9
427.7
7915
879.3
430.6
7967
884.8
433.4
TEMPERATURE-ENTROPY TABLE.
105
H
o
a
1.64
1.65
1.66
1.67
rfj
o
En
fs
I'fc
<
6 3
ll
.
1
!
g
JS
J
Jj
J
SQ
fa
|
11
1
*s C
'i J-
1
11
'!
1 -S
'S j>
H
<
B
OJ
s
& **
05
N
cc
a
&
132
2.341
8456
960.5
126.4
8515
966.4
127.3
8573
972.3
128.2
8631
978.3
129.0
131 2.280
8447
959.1
129.4
8505
965.0
130.3
8563
970.9
131.2
8621
976.8
132.1
130
2.220
8438
957.6
132.6
8496
963.5
133.5
8554
969.4
134.4
8612
975.3
135.3
129
2.161
8429
956.2
135.8
8487
962.0
136.7
8544
967.9
137.7
8602
973.8
138.6
128
2.103
8420
954.7
139.1
8478
960.6
140.0
8535
966.4
141.0
8593
972.3
142.0
127
2.047
8411
953.3
142.5
8468
959.1
143.4
8526
965.0
144.4
8583
970.8
145.4
126
.992
8401
951.8
146.0
8459
957.6
147.0
8516
963.5
148.0
8573
969.3
149.0
125 .938
8392
950.4
149.6
8449
956.2
150.6
8506
962.1
151.7
8564
967.7
152.7
124
.886
8383
948.8
153.3
8440
954.6
154.4
8497
960.5
155.4
8554
966.3
156.4
123
.835
8373
947.4
157.2
8430
953.2
158.2
8487
959.1
159.3
8544
964.9
160.4
122
.785
8364
945.9
161.2
8421
951.7
162.3
8478
957.5
163.4
8535
963.3
164.5
121
.737
8355
944.4
165.3
8412
950.2
166.4
8469
956.0
167.5
8525
961.8
168.6
120
.689
8346
942.9
169.4
8403
948.7
170.6
8459
954.5
171.7
8516
960.3
172.9
119 .642
8336
941.5
173.7
8393
947.3
174.9
8449
953.0
176.1
8506
958.8
177.3
118
.597
8328
940.0
178.2
8384
945.8
179.4
8440
951.5
180.6
8496
957.3
181.8
117
.552
8318
938.5
182.8
8374
944.3
184.1
8430
950.0
185.3
8487
955.8
186.5
116
.509
8309
937.0
187.5
8365
942.8
188.8
8421
948.5
190.1
8477
954.2
191.3
115
.467
8300
935.5
192.4
8355
941.3
193.7
8411
947.0
195.0
8467
952.8
196.3
114
.426
8290
934.0
197.3
8346
939.8
198.6
8401
945.5
200.0
8457
951.3
201.3
113
.386
8280
932.6
202.4
8336
938.3
203.7
8392
944.0
205.1
8447
949.8
206.4
112
.347
8271
931.1
207.7
8327
936.8
209.1
8382
942.5
210.5
8438
948.2
211.9
111
.308
8261
929.6
213.1
8317
935.3
214.6
8372
941.0
216.0
8428
946.7
217.4
110
.271
8253
928.1
218.9
8308
933.8
220.3
8363
939.5
221.8
8418
945.2
223.3
109
.235
8243
926.6
224.7
8298
932.3
226.2
8353
938.0
227.7
8408
943.7
229.2
108
.200
8234
925.1
230.7
8289
930.8
232.3
8344
936.4
233.8
8399
942.1
235.3
107
.165
8224
923.6
237.0
8279
929.3
238.6
8334
934.9
240.2
8389
940.6
241.8
106
.131
8215
922.1
243.5
8270
927.7
245.1
8324
933.4
246.7
8379
939.0
248.4
105
.098
8206
920.6
250.1
8260
926.2
251.8
8315
931.9
253.4
8370
937.5
255.1
104
.066
8196
919.1
256.9
8251
924.7
258.7
8305
930.3
260.4
8360
936.0262.1
103
.035
8187
917.6
263.9
8241
923.2
265.7
8296
928.8
267.5
8350
934.5
269.2
102
1.005
8178
916.1
271.2
8232
921.7
273.0
8286
927.3
274.8
8341
932.9
276.6
101
0.975
8169
914.5
278.6
8223
920.2
280.5
8277
925.8
282.3
8331
931.4
284.2
100
0.946
8159
913.0
286.2
8213
918.6
288.1
8267
924.2
290.0
8321
929.8
291.9
99
0.918
8150
911.5
294.1
8205
917.1
296.1
8257
922.7
298.0
8311
928.3
300.0
98
0.891
8140
910.0
302.3
8194
915.6
304.2
8248
921.2
306.2
8302
926.7
308.2
97
0.864
8131
908.5
310.7
8185
914.1
312.7
8238
919.7
314.8
8292
925.2
316.8
96
0.838
8122
907.1
319.4
8175
912.6
321.5
8229
918.2
323.6
8282
923.7
325.7
95
0.813
8113
905.5
328.4
8166
911.1
330.6
8219
916.7
332.7
8273
922.2
334.9
94
0.788
8103
904.0
337.7
8157
909.6
339.9
8210
915.1
342.1
8263
920.6
344.3
93
0.764
8094
902.5
347.3
8147
908.1
349.6
8200
913.6
351.9
8254
919.1
354.2
92
0.741 8085
901.0
357.3
8138
906.5
359.7
8191
912.0
362.0
8244
917.5
364.4
91
0.718
8075
899.4
367.7
8128
905.0
370.2
8181
910.5
372.6
8234
916.0
375.0
90
0.696
8066
897.9
378.5
8119
903.4
380.9
8171
908.9
383.4
8224
914.4
385.9
89
0.675
8057
896.4389.5
8109
901.9
392.0
8162
907.4
394.5
8215
912.9
397.1
88
0.654
8047
894.8
400.7
8100
900.3
403.4
8152
905.8
406.0
8205
911.2
408.6
87
0.633
8038
893.3
412.4
8091
898.8
415.0
8143
904.3
417.7
8195
909.7420.4
86
0.613 : 8029
891.8
423.9
8081
897.2
426.7
8133
902.7
429.4
8186
908.1 1432. 2
85
0.5941 8019
890.2
436.2 8072
895.7
439.1
8124
901.1
441.9
8176
906.5J444.8
io6
TEMPERATURE-ENTROPY TABLE.
ll
i
H
a
If
aJ a*
ill
1.68
1.69
1.70
1.71
1
la
+ c
r
Specific
Volume.
I
Heat Con-
tents.
Specific
Volume.
>
1
a
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
420
419
418
417
416
415
414
413
412
411
410
409
408
407
406
405
404
403
402
401
400
399
398
397
396
395
394
393
392
391
390
389
388
387
386
385
384
383
382
381
380
379
378
377
376
375
374
373
308.5
305.1
301.8
298.5
295.2
292.0
288.9
285.7
282.5
279.4
276.3
273.3
270.3
267.3
264.3
261.3
258.4
255.5
252.6
249.7
246.9
244.1
241.4
238.6
235.9
233.2
230.5
227.9
225.2
222.6
220.1
217.5
215.0
212.5
210.0
207.5
205.1
202.6
200.3
197.9
195.5
193.2
190.9
188.6
186.3
184.1
181.9
179.7
...
...
300.9
298.7
296.6
294.5
292.4
290.4
288.3
286.2
284.1
282.0
280.0
277.9
275.9
273.8
271.7
269.6
267.6
265.5
263.5
261.4
259.4
257.3
255.3
253.3
251.2
249.2
247.1
245.0
243.0
241.0
238.9
236.9
234.8
232.7
230.6
228.5
226.5
224.4
222.4
220.3
218.2
216.2
1368.3
1366.8
1365.4
1364.0
1362.6
1361.3
1359.9
1358.6
1357.3
1355.9
1354.6
1353.3
1351.9
1350.5
1349.1
1347.8
1346.4
1345.0
1343.7
1342.4
1341.0
1339.7
1338.3
1337.0
1335.7
1334.3
1333.0
1331.7
1330.4
1329.0
1327.7
1326.4
1325.0
1323.6
1322.3
1320.9
1319.5
1318.1
1316.8
1315.5
1314.1
1312.8
2.410
2.430
2.450
2.470
2.490
2.510
2.530
2.551
2.572
2.593
2.614
2.636
2.658
2.680
2.703
2.725
2.748
2.770
2.794
2.820
2.843
2.868
2.892
2.917
2.941
2.967
2.993
3.019
3.045
3.071
3.099
3.126
3.153
3.181
3.210
3.237
3.267
3.297
3.325
3.354
3.384
3.415
abi'.o
298.9
296.7
294.5
292.3
290.2
288.1
286.0
283.9
281.9
279.8
277.7
275.5
273.3
271.1
269.0
266.9
264.8
262.6
260.4
258.3
256.1
254.0
251.9
249.8
247.7
245.6
243.5
241.4
239.3
237.1
1364'. 9
1363.
1362.
1360.
1359.
1357.
1356.
1355.
1353.
1352.
1351.
1349.8
1348.3
1346.9
1345.5
1344.0
1342.6
1341.2
1339.8
1338.4
1337.0
1335.7
1334.3
1332.9
1331.6
1330.2
1328.9
1327.5
1326.1
1324.7
1323.3
21697
2.720
2.742
2.765
2.788
2.811
2.835
2.859
2.884
2.909
2.933
2.958
2.983
3.009
3.036
3.061
3.089
3.116
3.144
3.171
3.200
3.229
3.258
3.287
3.316
3.346
3.376
3.408
3.438
3.469
3.501
...
299'. 9
297.6
295.4
293.2
291.1
289.0
287.0
284.9
282.7
280.5
278.3
276.1
273.9
271.8
269.6
267.4
265.2
263.0
261.0
258.9
1361.0
1359.6
1358.2
1356.8
1355.4
1354.0
1352.6
1351.2
1349.7
1348.2
1346.7
1345.3
1343.8
1342.4
1340.9
1339.5
1338.1
1336.8
1335.4
1334.1
3i 030
3.056
3.083
3.109
3.136
3.164
3.191
3.219
3.246
3.275
3.304
3.333
3.362
3.392
3.421
3.452
3.482
3.513
3.545
3.578
300 . 9
298.6
296.3
294.1
292.0
289.8
287.7
285.5
283.3
281.1
1358.4
1356.9
1355.4
1354.0
1352.7
1351.2
1349.8
1348.3
1346.8
1345.3
3.386
3.415
3.445
3.476
3.506
3.537
3.568
3.599
3.631
3.663
TEMPERATURE-ENTROPY TABLE
lO/
J
i
2
1.72
1.73
1.74
1.75
Temperatur
Degrees I
*&*
{si
X
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
420
308 5
419
305 1
418
301 8
417
298 5
416
295 2
415
292
414
288.9
413
285.7
412
282.5
411
279 4
410
276 3
409
273 3
408
270 3
407
267 3
406
264 3
405
261 3
404
258 4
403
255 5
402
252 6
401
249 7
400
246 9
399
244 1
398
241 4
397
238 6
396
235.9
395
233 2
394
230 5
393
227.9
392
225 2
391
222 6
390
220 1
389
217 5
388
215
,
387
212.5
386
210
385
207 5
384
205.1
383
202.6
382
200.3
381
197 9
380
195 5
379
193 2
378
190 9
377
188.6
376
186.3
375
184.1
374
181.9
373
179.7
io8
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr. |
1
ll
p!
m
1.68
1.69
1.70
1.71
i
$
Jj
|l
ll
&
1
O"
ll
|
en .2
co
3
a
l|
"S
o> **
B
3
OC
Is
3
a
l|
& *
SJ
ll
CQ
372
371
370
177.5
175.3
173.2
214.1
212.1
210.0
1311.5
1310.2
1308.8
3.446
3.478
3.509
235.0
232.9
230.8
1321.9
1320.6
1319.2
3.533
3.565
3.599
256.7
254.5
252.3
1332.7
1331.2
1329.8
3.608
3.642
3.676
279.0
276.8
274.5
1344.0
1342.5
1341.0
3.698
3.730
3.765
369
368
367
171.1
169.0
166.9
208.0
206.0
204.0
1307.5
1306.2
1304.9
3.540
3.573
3.605
228.8
226.7
224.6
1317.8
1316.5
1315.1
3.631
3.666
3.700
250.1
248.0
245.9
1328.4
1327.0
1325.6
3.709
3.743
3.779
272.2
270.0
267.8
1339.5
1338.0
1336.5
3.799
3.834
3.870
366
365
364
164.8
162.8
160.8
202.0
200.0
198.0
1303.5
1302.2
1300.9
3.640
3.674
3.708
222.5
220.4
218.3
1313.7
1312.4
1311.1
3.734
3.768
3.804
243.7
241.5
239.4
1324.2
1322.8
1321.4
3.814
3.849
3.885
265.6
263.4
261.1
1335.1
1333.7
1332.2
3.505
3.940
3.979
363
362
361
158.8
156.8
154.8
195.9
193.9
191.9
1299.5
1298.2
1296.9
3.744
3.780
3.815
216.2
214.1
212.0
1309.8
1308.4
1307.1
3.840
3.875
3.912
237.2
235.0
232.9
1320.0
1318.6
1317.2
3.921
3.959
3.997
258.9
256.7
254.5
1330.8
1329.4
1328.0
4.015
4.053
4.092
360
359
358
357
356
355
152.9
151.0
149.1
147.2
145.3
143.5
189.9
187.9
185.8
183.8
181.7
179.7
1295.5
1294.2
1292.9
1291.6
1290.3
1288.9
3.853
3.890
3.927
3.965
4.004
4.043
210.1
208.1
206.0
204.0
201.9
199.8
1305.7
1304.3
1302.9
1301.5
1300.1
1298.8
3.948
3.986
4.023
4.061
4.100
4.140
230.8
228.7
226.6
224.4
222.3
220.1
1315.8
1314.4
1313.0
1311.6
1310.3
1308.9
4.035
4.074
4.113
4.152
4.193
4.232
252.3
250.1
247.9
245.7
243.5
241.3
1326.6
1325.1
1323.7
1322.3
1320.8
1319.4
4.131
4.170
4.210
4.250
4.292
4.334
354
353
352
141.6
139.8
138.0
177.7
175.7
173.7
1287.6
1286.3
1284.9
4.082
4.122
4.162
197.7
195.6
193.5
1297.4
1296.0
1294.6
4.180
4.220
4.260
218.0
216.0
213.9
1307.5
1306.1
1304.8
4.275
4.315
4.358
239.1
236.9
234.7
1318.0
1316.7
1315.4
4.376
4.418
4.460
351
350
349
136.3
134.5
132.8
171.6
169.6
167.6
1283.5
1282.1
1280.7
4.204
4.246
4.288
191.4
189.3
187.2
1293.2
1291.8
1290 5
4.303
4.346
4.388
211.9
209.8
207.7
1303.4
1302.1
1300.7
4.400
4.442
4.486
232.4
230.2
228.1
1314.1
1312.6
1311.1
4.502
4.546
4.591
348
347
346
131.1
129.4
127.7
165.5
163.5
161.4
1279.3
1277.9
1276.6
4.330
4.373
4.416
185.1
183.1
181.0
1289.2
1287.8
1286.5
4.430
4.474
4.519
205.5
203.4
201.2
1299.3
1297.9
1296.5
4.530
4.575
4.620
226.0
223.9
221.7
1309.6
1308.1
1306.6
4.638
4.684
4.730
345
344
343
126.0
124.4
122.7
159.4
157.4
155.4
1275.3
1274.0
1272.7
4.459
4.504
4.549
179.0
177.0
175.0
1285.1
1283.8
1282.5
4.562
4.609
4.656
199.1
197.0
194.9
1295.1
1293.6
1292.2
4.668
4.713
4.760
219.5
217.3
215.1
1305.1
1303.7
1302.3
4.779
4.825
4.873
342
341
340
121.1
119.5
117.9
153.4
151.3
149.3
1271.3
1270.0
1268.6
4.594
4.640
4.688
172.9
170.9
168.8
1281.1
1279.7
1278.3
4.701
4.750
4.800
192.8
190.6
188.5
1290.8
1289.4
1288.0
4.810
4.857
4.907
213.0
210.9
208.8
1300.9
1299.5
1298.1
4.920
4.970
5.020
339
338
337
116.3
114.8
113.3
147.3
145.3
143.3
1267.2
1265.9
1264.5
4.734
4.782
4.830
166.7
164.6
162.5
1277.0
1275.6
1274.2
4.848
4.896
4.946
186.4
184.2
182.0
1286.6
1285.2
1283.8
4.957
5.008
5.059
206.7
204.5
202.3
1296.6
1295.2
1293.8
5.071
5.123
5.177
336
335
334
111.7
110.3
108.8
141.3
139.3
137.3
1263.2
1261.8
1260.5
4.880
4.930
4.980
160.4
158.4
156.3
1272.8
1271.4
1270.0
4.998
5.048
5.099
179.9
177.9
175.7
1282.4
1281.0
1279.6
5.110
5.165
5.220
200.1
197.9
195.7
1292.3
1290.9
1289.5
5.230
5.285
5.340
333
332
331
107.3
105.8
104.4
135.3
133.3
131.3
1259.2
1257.9
1256.6
5.030
5.083
5.137
154.3
152.2
150.2
1268.6
1267.2
1265.9
5.150
5.203
5.257
173.5
171.4
169.3
1278.2
1276.8
1275.4
5.274
5.330
5.385
193.5
191.3
189.1
1288.1
1286.7
1285.2
5.395
5.450
5.510
330
329
328
103.0
101.6
100.2
129.3
127.3
125.3
1255.2
1253.8
1252.5
5.190
5.245
5.300
148.1
146.0
144.0
1264.5
1263.2
1261.9
5.310
5.366
5.421
167.2
165.0
162.9
1274.0
1272.5
1271.1
5.444
5.500
5.560
187.0
184.9
182.7
1283.8
1282.4
1280.9
5.567
5.625
5.684
327
326
325
98.8
97.5
96.1
123.3
121.3
119.3
1251.2
1249.8
1248.4
5.358
5.413
5.470
142.0
139.9
137.9
1260.5
1259.1
1257.8
5.479
5.537
5.595
160.8
158.7
156.5
1269.7
1268.3
1266.9
5.617
5.676
5.735
180.5
178.3
176.1
1279.5
1278.0
1276.6
5.743
5.805
5.865
TEMPERATURE-ENTROPY TABLE.
109
Temperature,
Degrees Fahr.
o
2
OH OS
fig
S fa
8^5
1.72
1.73
1.74
1.75
Quality.
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
1
Heat Con-
tents.
Specific
Volume.
372
371
370
369
368
367
366
365
364
363
362
361
360
359
358
357
356
355
354
353
352
351
350
349
348
347
346
345
344
343
342
341
340
339
338
337
336
335
334
333
332
331
330
329
328
327
326
325
177.5
175.3
173.2
171.1
169.0
166.9
164.8
162.8
160.8
158.8
156.8
154.8
152.9
151.0
149.1
147.2
145.3
143.5
141.6
139.8
138.0
136.3
134.5
132.8
131.1
129.4
127.7
126.0
124.4
122.7
121.1
119.5
117.9
116.3
114.8
113.3
111.7
110.3
108.8
107.3
105.8
104.4
103.0
101.6
100.2
98.8
97.5
96.1
300.3
298.0
295.7
293.6
291.4
289.2
287.0
284.9
282.7
280.5
278.3
276.0
273.7
271.4
269.2
267.0
264.7
262.4
260.1
258.0
255.8
253.5
251.3
249.0
246.7
244.4
242.2
240.0
237.7
235.4
233.1
230.9
228.7
226.4
224.1
221.9
219.7
217.6
215.4
213.1
211.1
208.9
206.6
204.3
202.1
199.9
197.6
195.4
1354.6
1353.1
1351.6
1350.1
1348.6
1347.2
1345.8
1344.4
1343.0
1341.6
1340.2
1338.7
1337.3
1335.8
1334.3
1332.8
1331.4
1330.0
1328.5
1327.0
1325.6
1324.1
1322.6
1321.1
1319.7
1318.2
1316.7
1315.2
1313.8
1312.3
1310.8
1309.3
1307.8
1306.3
1304.8
1303.3
1301.9
1300.5
1299.1
1297.6
1296.2
1294.8
1293.4
1292.0
1290.5
1289.0
1287.5
1286.0
3.783
3.817
3.850
3.886
3.922
3.959
3.995
4.031
4.070
4.107
4.145
4.185
4.225
4.265
4.305
4.348
4.390
4.430
4.474
4.519
4.562
4.608
4.653
4.699
4.744
4.790
4.838
4.888
4.935
4.983
5.031
5.082
5.135
5.186
5.239
5.293
5.345
5.400
5.455
5.510
5.567
5.626
5.683
5.740
5.800
5.863
5.925
5.987
300.3
298.0
295.6
293.3
291.0
288.7
286.4
284.1
281.8
279.5
277.2
274.9
272.6
270.4
268.1
265.9
263.7
261.4
259.1
256.9
254.6
252.3
250.1
247.8
245.5
243.3
241.0
238.8
236.5
234.2
231.9
229.6
227.3
225.0
222.7
220.4
218.1
215.8
1351.3
1349.7
1348.1
1346.5
1345.0
1343.5
1342.0
1340.5
1339.0
1337.5
1336.0
1334.5
1333.0
1331.5
1330.1
1328.7
1327.2
1325.8
1324.3
1322.9
1321.4
1320.0
1318.5
1317.0
1315.5
1314.0
1312.6
1311.1
1309.6
1308.1
1306.6
1305.1
1303.6
1302.1
1300.5
1299.0
1297.5
1296.0
4.240
4.283
4.324
4.365
4.407
4.450
4.490
4.534
4.579
4.623
4.667
4.713
4.760
4.805
4.852
4.900
4.948
4.996
5.046
5.098
5.150
5.203
5.255
5.308
5.363
5.419
5.474
5.529
5.588
5.643
5.700
5.760
5.820
5.880
5.940
6.000
6.063
6.128
1343*. 9
1342.4
1340.9
1339.4
1337.8
1336.3
1334.7
1333.1
1331.6
1330.0
1328.4
1326.9
1325.3
1323.8
1322.3
1320.8
1319.3
1317.8
1316.3
5.323
5.381
5.430
5.486
5.540
5.598
5.654
5.710
5.768
5.829
5.889
5.949
6.009
6.071
6.139
6.205
6.270
6.337
6.403
299'. 6
297.2
294.9
292.6
290.3
288.0
285.6
283.3
281.0
278.6
276.2
273.8
271.5
269.2
266.8
264.4
262.1
259.8
257.4
255.1
252.8
250.5
248.2
245.8
243.4
241.1
238.7
236.4
134Y.O
1345.5
1344.0
1342.5
1341.0
1339.5
1338.0
1336.5
1335.0
1333.5
1332.0
1330.5
1329.0
1327.5
1325.9
1324.4
1322.9
1321.4
1319.9
1318.3
1316.8
1315.3
1313.8
1312.3
1310.8
1309.3
1307.8
1306.3
4i 777
4.823
4.870
4.918
4.966
5.014
5.063
5.113
5.165
5.215
5.269
5.320
5.376
5.430
5.485
5.540
5.596
5.652
5.710
5.767
5.825
5.884
5.945
6.006
6.068
6.130
6.192
6.255
299'. 7
297.4
295.0
292.6
290.2
287.9
285.5
283.1
280.7
278.3
275.9
273.5
271.1
268.7
266.3
263.9
261.6
259.2
256.8
no
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
'O
a
O tw
ft
1.68
1.69
1.70
1.71
<
a
6|
w "*
ll
GO
"3
3
a
a
21
GO
ks
<
-P B
"*
*J
'5 o
GO
"3
I is
+3 a
sS "*
w 5
&
GO
324
323
322
94.8
93.5
92.2
117.3
115.3
113.3
1247.0
1245.6
1244.3
5.528
5.588
5.646
135.9
133.8
131.8
1256.4
1255.0
1253.7
5.653
5.713
5.777
154.4
152.2
150.0
1265.5
1264.0
1262.6
5.795
5.857
5.919
174.0
171.9
169.7
1275.2
1273.8
1272.4
5.928
5.988
6.05
321
320
319
90.9
89.6
88.3
111.3
109.4
107.4
1242.9
1241.6
1240.2
5.705
5.768
5.832
129.7
127.7
125.7
1252.3
1250.9
1249.5
5.839
5.905
5.969
148.0
145.9
143.7
1261.2
1259.8
1258.4
5.980
6.05
6.11
167.5
165.3
163.1
1271.0
1269.6
1268.1
6.11
6.18
6.25
318
317
316
87.1
85.9
84.6
105.4
103.4
101.4
1238.9
1237.4
1236.1
5.898
5.960
6.03
123.7
121.7
119.7
1248.2
1246.8
1245.5
6.03
6.10
6.17
141.7
139.6
137.5
1257.1
1255.7
1254.3
6.18
6.25
6.32
161.0
158.8
156.6
1266.7
1265.3
1263.8
6.32
6.40
6.46
315
314
313
83.4
82.3
81.1
99.5
97.5
95.5
1234.8
1233.5
1232.1
6.10
6.17
6.23
117.7
115.6
113.6
1244.1
1242.7
1241.3
6.24
6.30
6.37
135.4
133.3
131.2
1252.9
1251.6
1250.2
6.39
6.46
6.53
154.4
152.2
150.0
1262.3
1260.9
1259.4
6.54
6.60
6.67
312
311
310
79.9
78.8
77.6
93.5
91.6
89.7
1230.8
1229.5
1228.2
6.30
6.37
6.44
111.6
109.6
107.5
1240.0
1238.6
1237.2
6.44
6.51
6.58
129.1
127.0
125.0
1248.8
1247.4
1246.0
6.60
6.67
6.75
147.9
145.7
143.5
1258.0
1256.5
1255.0
6.75
6.83
6.90
309
308
307
76.5
75.4
74.3
87.7
85.7
83.8
1226.9
1225.6
1224.2
6.51
6.58
6.65
105.5
103.5
101.5
1235.9
1234.5
1233.2
6.65
6.73
6.80
122.9
120.9
118.9
1244.6
1243.2
1241.8
6.81
6.89
6.97
141.3
139.1
137.0
1253.6
1252.2
1250.8
6.97
7.05
7.13
306
305
304
73.2
72.2
71.1
81.9
79.9
78.0
1222.9
1221.6
1220.3
6.73
6.80
6.88
99.5
97.5
95.4
1231.9
1230.5
1229.1
6.88
6.96
7.04
116.8
114.7
112.6
1240.4
1239.0
1237.6
7.04
7.12
7.20
134.9
132.7
130.5
1249.4
1248.0
1246.6
7.21
7.29
7.37
303
302
301
70.0
69.0
68.0
76.0
74.0
72.1
1218.9
1217.6
1216.2
6.96
7.03
7.11
93.4
91.4
89.4
1227.7
1226.3
1225.0
7.11
7.20
7.28
110.5
108.4
106.3
1236.2
1234.8
1233.4
7.28
7.37
7.45
128.4
126.3
124.1
1245.1
1243.8
1242.3
7.45
7.54
7.63
300
299
298
67.0
66.0
65.0
70.2
68.3
66.3
1214.9
1213.6
1212.3
7.20
7.28
7.36
87.3
85.3
83.3
1223.6
1222.2
1220.8
7.36
7.45
7.54
104.2
102.1
100.0
1232.0
1230.7
1229.4
7.54
7.62
7.70
122.0
119.9
117.7
1240.9
1239.4
1238.0
7.71
7.80
7.89
297
296
295
64.0
63.1
62.1
64.4
62.4
60.5
1211.0
1209.7
1208.4
7.44
7.53
7.61
81.2
79.2
77.2
1219.4
1218.0
1216.6
7.62
7.70
7.80
98.0
96.0
94.0
1228.0
1226.6
1225.2
7.80
7.89
7.99
115.5
113.4
111.3
1236.6
1235.2
1233.8
7.98
8.07
8.17
294
293
292
61.2
60.2
59.3
58.6
56.7
54.7
1207.1
1205.8
1204.5
7.70
7.79
7.88
75.2
73.1
71.1
1215.3
1213.9
1212.6
7.89
7.99
8.08
91.9
89.9
87.8
1223.9
1222.5
1221.1
8.07
8.16
8.26
109.1
107.0
104.9
1232.4
1231.0
1229.5
8.26
8.35
8.45
291
290
289
58.4
57.5
56.7
52.7
50.8
48.9
1203.1
1201.8
1200.5
7.98
8.08
8.17
69.0
67.0
65.0
1211.3
1209.9
1208.6
8.17
8.27
8.37
85.7
83.6
81.5
1219.7
1218.3
1216.9
8.36
8.46
8.55
102.7
100.6
98.4
1228.0
1226.6
1225.1
8.55
8.65
8.75
288
287
286
55.8
54.9
54.1
46.9
44.9
43.0
1199.1
1197.8
1196.5
8.26
8.35
8.45
63.0
61.0
58.9
1207.3
1206.0
1204.6
8.46
8.56
8.66
79.4
77.4
75.3
1215.5
1214.1
1212.7
8.65
8.75
8.86
96.3
94.1
92.0
1223.6
1222.2
1220.8
8.85
8.96
9.07
285
284
283
53.2
52.4
51.6
41.0
39.0
37.0
1195.2
1193.8
1192.5
8.55
8.65
8.75
56.9
54.9
52.9
1203.2
1201.9
1200.5
8.76
8.87
8.98
73.2
71.1
69.1
1211.3
1209.9
1208.5
8.96
9.07
9.18
89.9
87.8
85.7
1219.4
1218.0
1216.5
9.18
9.28
9.40
282
281
280
50.8
50.0
49.19
35.0
33.1
31.1
1191.2
1189.9
1188.6
8.85
8.96
9.06
50.9
48.8
46.8
1199.2
1197.8
1196.4
9.08
9.20
9.30
67.0
65.0
62.9
1207.1
1205.7
1204.4
9.29
9.40
9.51
83.5
81.4
79.3
1215.1
1213.7
1212.3
9.50
9.62
9.74
279
278
277
48.41
47 . 64
46.88
29.2
27.3
25.3
1187.3
1186.0
1184.6
9.17
9.28
9.40
44.7
42.7
40.7
1195.09.41
1193.79.52
1192.39.63
60.9
58.8
56.8
1203.0
1201.7
1200.3
9.62
9.74
9.86
77.2
75.0
73.0
1211.0
1209.6
1208.2
9.85
9.97
10.10
TEMPERATURE-ENTROPY TABLE.
Ill
Temperature,
l)-n-i-.s Kalir.
1
" O 1
3 M .d
l u
1.72
1.73
1.74
1.75
1
la
I 1
1 !
1
d 3
JJ
OQ
1
11
H
o I
n .2
j
Si
- O
&
fj
324
323
322
94.8
93.5
92.2
193.2
191.0
188.8
1284.5
1283.0
1281.6
6.06
6.12
6.18
213.5
211.2
208.9
1294.5
1293.0
1291.5
6.20
6.26
6.33
234.0
231.6
229.3
1304.7
1303.1
1301.5
6.33
6.40
6.47
254.4
252.1
249.7
1314.7
1313.2
1311.6
6.47
6.54
6.60
321
320
319
90.9
89.6
88.3
186.5
184.3
182.0
1280.1
1278.7
1277.3
6.25
6.32
6.38
206.6
204.3
202.0
1290.0
1288.5
1287.0
6.40
6.47
6.54
226.9
224.5
222.2
1299.9
1298.4
1296.8
6.55
6.61
6.69
247.4
245.0
242.6
1310.1
1308.5
1306.9
6.67
6.75
6.82
318
317
316
87.1
85.9
84.6
179.9
177.6
175.4
1275.9
1274.5
1273.0
6.45
6.53
6.60
199.7
197.4
195.1
1285.5
1284.0
1282.5
6.60
6.67
6.74
219.9
217.5
215.1
1295.3
1293.8
1292.3
6.76
6.83
6.90
240.3
238.0
235.6
1305.4
1303.9
1302.4
6.89
6.97
7.04
315
314
313
83.4
82.3
81.1
173.1
171.0
168.8
1271.6
1270.1
1268.6
6.67
6.74
6.81
192.81281.0
190.5 1279.5
188.21278.0
6.81
6.89
6.98
212.8
210.4
208.0
1290.7
1289.2
1287.6
6.98
7.05
7.13
233.3
230.9
228.5
1300.8
1299.3
1297.8
7.12
7.20
7.28
312
311
310
79.9
78.8
77.6
166.6
164.3
162.1
1267.1
1265.7
1264.2
6.89
6.97
7.04
185.9
183.6
181.3
1276.5
1275.0
1273.5
7.05
7.13
7.20
205.6
203.2
200.8
1286.1
1284.5
1283.0
7.21
7.29
7.37
226.1
223.7
221.4
1296.3
1294.8
1293.3
7.36
7.44
7.53
309
308
307
76.5
75.4
74.3
159.9
157.6
155.3
1262.7
1261.2
1259.8
7.12
7.20
7.28
179.0
176.7
174.4
1272.0
1270.5
1269.0
7.28
7.36
7.44
198.5
196.1
193.7
1281.5
1280.0
1278.4
7.45
7.54
7.62
219.0
216.7
214.3
1291.8
1290.3
1288.8
7.61
7.69
7.78
306
305
304
73.2
72.2
71.1
153.1
150.9
148.6
1258.3
1256.8
1255.3
7.36
7.44
7.52
172.1
169.8
167.6
1267.5
1266.0
1264.5
7.52
7-61
7.70
191.4
189.1
186.7
1276.9
1275.4
1273.9
7.70
7.79
7.88
211.9
209.5
207.1
1287.2
1285.6
1284.0
7.87
7.96
8.05
303
302
301
70.0
69.0
68.0
146.5
144.2
142.0
1253.9
1252.4
1251.0
7.61
7.70
7.79
165.3
163.0
160.7
1262.9
1261.4
1259.9
7.79
7.88
7.97
184.4
182.1
179.8
1272.3
1270.8
1269.3
7.97
8.06
8.15
204.7
202.3
199.9
1282.4
1280.8
1279.2
8.15
8.24
8.34
300
299
298
67.0
66.0
65.0
139.8
137.7
135.4
1249.5
1248.1
1246.6
7.88
7-97
8-06
158.4
156.1
153.8
1258.4
1256.9
1255.4
8.06
8.15
8.25
177.4
175.1
172.8
1267.8
1266.2
1264.7
8.24
8-34
8.43
197.5
195.1
192.7
1277.6
1276.0
1274.5
8.43
8.52
8.61
297
296
295
64.0
63.1
62.1
133.2
131.0
128.9
1245.1
1243.6
1242.2
8.15
8.24
8.34
151. "6
149.3
147.0
1253.9
1252.4
1250.9
8.34
8.44
8.53
170.5
168.2
165.9
1263.2
1261.7
1260.1
8.53
8.63
8.73
190.3
187.9
185.5
1272.9
1271.4
1269.9
8.71
8.81
8.91
294
293
292
61.2
60.2
59.3
126.7
124.5
122.2
1240.7
1239.2
1237.7
8.43
8-53
8.63
144.7
142.5
140.3
1249.4
1247.9
1246.5
8.63
8.73
8.83
163.6
161.3
158.9
1258.6
1257.1
1255.6
8.83
8.93
9.03
183.1
180.8
178.4
1268.4
1266.9
1265.3
9.02
9.12
9.23
291
290
289
58.4
57.5
56.7
120.0
118.0
115.8
1236.2
1234.8
1233.4
8.73
8.84
8.94
138.0
135.7
133.5
1245.0
1243.5
1242.1
8.93
9.04
9.15
156.6
154.3
152.0
1254.0
1252.5
1251.0
9.14
9.24
9.35
176.0
173.6
171.3
1263.8
1262.2
1260.7
9.34
9.46
9.57
288
287
286
55.8
54.9
54.1
113.6
111.4
109.2
1232.0
1230.6
1229.2
9.04
9.15
9.26
131.2
129.0
126.8
1240.7
1239.3
1237.9
9.25
9.36
9.47
149.6
147.3
145.0
1249.5
1248.0
1246.5
9.46
9.57
9.68
168.9
166.6
164.2
1259.1
1257.6
1256.1
9.67
9.79
9.90
lit
283
53.2
52.4
51.6
107.0
104.8
102.7
1227.7
1226.3
1224.8
9.37
9.49
9.60
124.6
122.3
120.0
1236.4
1235.0
1233.5
9.58
9.70
9.82
142.7
140.4
138.1
1245.0
1243.5
1242.0
9.80
9.92
10.04
161.8
159.4
157.0
1254.5
1253.0
1251.4
10.03
10.15
10.27
282
281
280
50.8
50.0
49.19
100.5
98.3
96.1
1223.4
1222.0
1220.6
9.71
9.83
9.95
117.8
115.6
113.4
1232.0
1230.5
1229.0
9.94
10.06
10.18
135.8
133.5
131.2
1240.5
1239.1
1237.7
10.16
10.29
10.41
154.6
152.3
149.9
1249.8
1248.2
1246.7
10.39
10.51
10.64
279
278
277
48.41
47.64
46.88
94.01219.2
91. 811217. 8
89.6!1216.4
10.07
10.19
10.31
111.1
108.9
106.7
1227.510.30
1226.1H0.43
1224.610.56
128.9'l236.3
126.7 1234.8
124.4 1233.3
10.53
10.67
10.80
147.5
145.1
142.8
1245.1
1243.6
1242.1
10.77
10.90
11.04
112
TEMPERATURE-ENTROPY TABLE.
to to to 1 Temperature,
332 1 Degrees Fahr. |
"O
c
o
jfl
1.68
1.69
1.70
1.71
I'
J*
OJ
IJ
8 45
|J
&
J
Ijs
V
o 1
s -
3 o
oc
K *
CQ
& ^
I 1
5
II
02
a
w **
46.13
45.39
44.67
23.3
21.3
19.3
1183.4
1182.1
1180.8
9.51
9.62
9.73
38.6
36.6
34.5
1191.0
1189.6
1188.3
9.75
9.87
10.00
54.7
52.6
50.5
1199.0
1197.6
1196.2
9.98
10.10
10.22
70.9
68.8
66.7
1206.8
1205.4
1204.0
10.22
10.34
10.47
273
272
271
43.95
43.24
42.54
17.4
15.4
13.4
1179.6
1178.3
1177.0
9.85
9.97
10.10
32.5
30.5
28.4
1187.0
1185.7
1184.3
10.11
10.23
10.36
48.4
46.3
44.2
1194.8
1193.4
1192.0
10.34
10.47
10.60
64.5
62.4
60.3
1202.6
1201.2
1199.8
10.60
10.73
10.86
270
269
268
41.84
41.16
40.49
11.5
9.5
7.5
1175.7
1174.4
1173.1
10.23
10.35
10.48
26.4
24.3
22.3
1183.0
1181.7
1180.3
10.49
10.61
10.75
42.1
40.0
38.0
1190.6
1189.2
1187.9
10.74
10.88
11.01
58.2
56.1
54.0
1198.4
1197.0
1195.7
10.99
11.13
11.27
267
266
265
264
263
262
39.83
39.17
38.53
37.89
37.26
36.64
5.6
3.6
1.6
1171.8
1170.5
1169.2
10.61
10.75
10.89
20.3
18.3
16.2
14.2
12.1
10.1
1178.9
1177.5
1176.1
1174.8
1173.5
1172.2
10.89
11.02
11.16
11.30
11.44
11.58
36.0
33.9
31.9
29.8
27.7
25.7
1186.5
1185.2
1183.8
1182.5
1181.1
1179.8
11.14
11.29
11.42
11.57
11.70
11.86
51.9
49.8
47.7
45.5
43.4
41.3
1194.3
1192.9
1191.6
1190.2
1188.8
1187.5
11.41
11.55
11.70
11.85
12.00
12.15
9997
9987
9976
1167.8
1166.5
1165.1
11.04
11.20
11.36
261
260
259
36.02
35.42
34.83
9966
9955
9945
1163.9
1162.6
1161.3
11.53
11.70
11.87
8.0
6.0
4.0
1170.9
1169.6
1168.3
11.71
11.87
12.02
23.6
21.6
19.5
1178.4
1177.1
1175.8
12.01
12.16
12.31
39.3
37.2
35.1
1186.1
1184.8
1183.5
12.30
12.46
12.62
258
257
256
34.24
33.66
33.09
9934
9925
9914
1159.9
1158.6
1157.3
12.05
12.24
12.42
2.0
0.0
1166.9
1165.6
12.18
12.33
17.4
15.3
13.2
1174.4
1173.0
1171.7
12.48
12.63
12.80
33.0
30.9
28.8
1182.1
1180.7
1179.4
12.79
12.95
13.11
9990
1164.4
12.52
255
254
253
32.53
31.97
31.42
9903
9893
9882
1156.0
1154.6
1153.4
12.61
12.80
13.01
9979
9969
9958
1163.1
1161.7
1160.4
12.70
12.90
13.10
11.0
8.9
6.8
1170.3
1168.9
1167.5
12.96
13.13
13.30
26.7
24.5
22.4
1178.0
1176.6
1175.2
13.29
13.46
13.63
252
251
250
249
248
247
30.88
30.35
29.82
29.30
28.79
28.29
9873
9862
9852
9842
9831
9822
1152.1
1150.8
1149.5
1148.2
1146.8
1145.5
13.20
13.40
13.61
13.83
14.04
14.26
9948
9937
9927
9917
9906
9896
1159.1
1157.8
1156.5
1155.2
1153.9
1152.6
13.30
13.50
13.72
13.93
14.15
14.37
4.7
2.6
0.6
1166.1
1164.8
1163.5
13.47
13.65
13.83
20.3
18.1
16.0
13.9
11.7
9.6
1173.9
1172.6
1171.2
1169.9
1168.5
1167.2
13.81
14.00
14.17
14.36
14.54
14.73
9992
9981
9971
1162.3
1161.0
1159.7
14.04
14.25
14.48
246
245
244
27.80
27.31
26.83
9811
9801
9791
1144.2
1142.9
1141.6
14.49
14.71
14.94
9885
9875
9865
1151.3
1150.0
1148.6
14.60
14.82
15.05
9960
9949
9939
1158.4
1157.1
1155.7
14.71
14.93
15.17
7.5
5.3
3.1
1165.8'l4.92
1164.4,15.11
1163.0 15.31
243
242
241
26.35
25.88
25.42
9780
9771
9760
1140.3
1139.0
1137.7
15.17
15.41
15.66
9854
9844
9834
1147.3
1146.0
1144.7
15.28
15.52
15.77
9928
9918
9907
1154.4
1153.0
1151.7
15.40
15.64
15.89
0.8
1161.5
15.52
9992
9981
1160.0
1158.7
15.76
16.01
240
239
238
24.97
24.52
24.08
9750
9740
9730
1136.3
1135.0
1133.6
15.90
16.16
16.39
9824
9813
9803
1143.3
1142.0
1140.6
16.02
16.28
16.54
9897
9887
9876
1150.3
1149.0
1147.6
16.14
16.40
16.66
9971
9960
9950
1157.3
1156.0
1154.6
16.26
16.52
16.78
237
236
235
23.64
23.21
22.79
9719
9710
9699
1132.3
1131.0
1129.7
16.68
16.95
17 .24
9793
9783
9772
1139.3
1138.0
1136.6
16.80
17.08
17.36
9866
9856
9845
1146.3
1144.9
1143.5
16.93
17.21
17.49
9939
9928
9917
1153.3
1151.9
1150.5
17.05
17.33
17.62
234
233
232
22.38
21.97
21.57
9689
9680
9669
1128.3
1127.0
1125.6
17.52
17.80
18.09
9762
9752
9741
1135.2
1133.9
1132.5
17.65
17.93
18.23
9834
9824
9814
1142.1
1140.8
1139.4
17.78
18.07
18.36
9907
9897
9886
1149.1
1147.7
1146.3
17.91
18.20
18.50
231
230
229
21.17
20.78
20.40
9659
9649
9639
1124.3
1123.0
1121.6
18.39
18.69
19.01
9731
9721
9711
1131.2
1129.9
1128.5
18.53
18.83
19.15
9803
9793
9782
1138.1
1136.8
1135.4
18.67
18.97
19.29
9876
9865
9854
1145.0
1143.7
1142.3
18.80
19.11
19.43
TEMPERATURE-ENTROPY TABLE.
u
g
C
1.72 1.73
1.74
1.75
2g
|
j
,
d
,
.
,
2|
|S
1
|*d
m u U
I&s
1
6 3
*s C
F
1
jl
|j
3
6 3
H
||
I
3
8s
11
iJ
H
a
00
&
' T -
5
n
02
a
n
02
276
46.13
87.5
1215.0
10.44
104.4
1223.2
10.69
122.1
1231.8
10.93
140.4
1240.6
11.16
275
45.39
85.3
1213.5
10.57
102.1
1221.8
10.81
119.8
1230.4
11.06
138.0
1239.0 11.30
274
44.67
83.1
1212.1
10.70
99.9
1220.3
10.96
117.5
1228.9
11.20
135.7
1237.5
11.44
273
43.95
81.0
1210.7
10.83
97.7
1218.8
11.09
115.2
1227.4
11.33
133.3
1236.0
11.59
272
43.24
78.8
1209.3
10.97
95.5
1217.3
11.22
113.0
1225.9
11.48
131.0
1234. 5111.72
271
42.54
76.6
1207.8
11.10
93.3
1215.8
11.37
110.7
1224.4
11.61
128.6
1233.0
11.88
270
41.84
74.5
1206.4
11.24
91.0
1214.4
11.50
108.4
1222.9
11.77
126.2
1231.5
12.03
269
41.16
72.3
1204.9
11.38
88.8
1213.0
11.65
106.1
1221.4
11.90
123.9
1230.0
12.18
268
40.49
70.1
1203.5
11.52
86.6
1211.5
11.80
103.8
1220.0
12.05
121.5
1228.4
12.33
267
39.83
68.0
1202.1
11.67
84.3
1210.1
11.95
101.6
1218.5
12.21
119.1
1226.9
12.49
266
39.17
65.8
1200.7
11.81
82.1
1208.6 12.10
99.3
1217. 1112.37
116.8
1225.4
12.64
265
38.53
63.6
1199.3
11.96
79.9
1207.2
12.26
97.0
1215.6
12.53
114.5
1223.9
12.80
264
37.89
61.5
1197.9
12.11
77.7
1205.8
12.41
94.8
1214.2
12.70
112.1
1222.4
12.97
263
37.26
59.4
1196.5
12.27
75.5
1204.3
12.56
92.5
1212.7
12.85
109.8
1220.9
13.14
262
36.64
57.2
1195.1
12.42
73.2
1202.9
12.73
90.2
1211.3
13.01
107.5
1219.4
13.30
261
36.02
55.0
1193.7
12.59
71.0
1201.5
12.90
88.0
1209.8
13.20
105.1
1217.9
13.48
260
35.42
52.8 -1192.3
12.75
68.8
1200.1
13.07
85.5
1208.3
13.36
102.7
1216.5
13.65
259
34.83
50.6
1190.9
12.90
66.6
1198.7
13.24
83.3
1206.8
13.54
100.4
1215.0
13.82
258
34.24
48.4
1189.5
13.08
64.4
1197.3
13.40
81.0
1205.3
13.70
98.1
1213.5
14.00
257
33.66
46.2
1188.1
13.25
62.1
1195.9
13.58
78.7
1203.8
13.89
95.8
1212.0
14.19
256
33.09
44.0
1186.7
13.41
59.9
1194.4
13.76
76.4
1202.4
14.08
93.4
1210.5
14.39
255
32.53
41.9
1185.3
13.59
57.7
1193.0
13.94
74.1
1200.9
14.25
91.1
1209.0
14.57
254
31.97
39.7 1183.9
13.78
55.5
1191.5
14.12
71.8
1199.4
14.44
88.7
1207.5
14.76
253
31.42
37.5
1182.5
13.95
53.3
1190.1
14.31
69.5
1197.9
14.63
86.3
1206.0
14.96
252
30.88
35.3
1181.1
14.14
51.1
1188.7
14.50
67.2
1196.5
14.82
84.0
1204.5
15.15
251
30.35
33.1 1179.7
14.33
49.0
1187.2
14.70
64.9
1195.0
15.02
81.6
1203.0
15.35
250
29.82
31.0
1178.3
14.51
46.7
1185.8
14.90
62.6
1193.5
15.22
79.3
1201.5
15.56
249
29.30
28.8
1177.0
14.70
44.5
1184.4
15.09
60.3
1192.0
15.42
77.0
1200.0
15.77
248
28.79
26.6
1175.6
14.90
42.3
1183.0
15.29
58.0
1190.6
15.63
74.6
1198.5
15.99
247
28.29
24.4
1174.2
15.09
40.1
1181.6
15.49
55.7
1189.1
15.83
72.2
1197.0
16.20
246
27.80
22.2
1172.8
15.29
37.9
1180.1
15.70
53.4
1187.6
16.04
69.9
1195.5
16.40
245
27.31
20.0 i!171.4
15.49
35.7
1178.7
15.90
51.1
1186.1
16.26
67.5
1194.0
16.62
244
26.83
17.8
1170.0
15.70
33.411177.2
16.11
48.8
1184.7
16.48
65.1
1192.5
16.85
243
26.35
15.7
1168.6
15.90
31.1
1175.7
16.32
46.4
1183.2
16.70
62.7
1191.0
17.08
242
25.88
13.5
1167.2 16.12
28.8
1174.3
16.55
44.1
1181.7
16.93
60.4
1189.5
17.30
241
25.42
11.3
1165.8
16.33
26.5
1172.8
16.78
41.8
1180.2
17.15
58.0
1188.0
17.54
240
24.97
9.1
1164.4
16.56
24.2
1171.4
17.00
39.5
1178.8
17.38
55.6
1186.5
17.78
239
24.52
6.9
1163.0 16.79
21. 911170. OU7. 23
37.2
1177.4
17.61
53.3
1185.0
18.02
238
24.08
4.7
1161.6
17.00
19.7
1168.6
17.45
35.0
1176.0
17.85
51.0
1183.5
18.28
237
23.64
2.5
1160.2
17.23
17.5
1167.2
17.69
32.8
1174.6
18.10
48.6
1182.0
18.52
236
23.21
0.1
1158.9
17.46
15.2
1165.8
17.94
30.5
1173.1
18.34
46.2
1180.5
18.78
235
22.79
9990
1157.4
17.75
12.9
1164.4
18.17
28.3
1171.6
18.59
43.8
1179.0
19.04
234
22.38
9980
1156.0
18.04
10.7
1163.0
18.42
26.0
1170.2
18.84
41.5
1177.5
19.30
233
21.97
9969
1154.6 18.33
8.5 1161.6118. 67
23.7
1168.7
19.10
39.1
1176.0
19.57
232
21.57
9958
1153.2
18.63
6.3
1160.2
18.93
21.4
1167.3
19.39
36.8
1174.6
19.84
231
21.17
9948
1151.9
18.94
4.1
1158.8
19.19
19.1
1165.8
19.64
34.5
1173.2
20.11
230
20.78
9937
1150.6
19.25
1.8 1157.4 19.45
16.9
1164.4 19.92
32.2
1171.7
20.40
229
20.40 9926
1149.2
19.57
9998 1156.0 19.711 14.7 1163.0 20.20
30.0
1170.3
20.69
1 1
1
114
TEMPERATURE-ENTROPY TABLE.
to to to 1 Temperature,
Cj^oo 1 Degrees Fahr. |
a
fcj
<*
8 fa o
e*3
W M*-
PH
1.68
1.69
1.70
1.71
$4
*]
>>
$4
,B i
>
a
Zz
||
>,
Ij
B
J
5 o
02
|l
*>
<n
c
3
a
2^
l>
&
<
g^
l>
OQ
g
W
20.02
19.64
19.28
9628
9619
9609
1120.2
1118.9
1117.6
19.32
19.64
19.97
9700
9690
9680
1127.1
1125.8
1124.4
19.47
19.79
20.12
9772
9762
9752
1134.0
1132.7
1131.3
19.61
19.93
20.27
9843
9833
9823
1140.8
1139.5
1138.1
19.76
20.08
20.41
225
224
223
18.91
18.56
18.21
9599
9589
9579
1116.3
1114.9
1113.6
20.31
20.65
21.01
9670
9660
9650
1123.1
1121.7
1120.4
20.46
20.81
21.16
9741
9731
9721
1129.9
1128.5
1127.2
20.61
20.96
21.32
9812
9802
9792
1136.8
1135.4
1134.0
20.76
21.11
21.47
222
221
220
17.86
17.52
17.19
9569
9559
9549
1112.2
1110.9
1109.5
21.37
21.73
22.10
9640
9630
9620
1119.0
1117.7
1116.3
21.53
21.89
22.26
9711
9700
9690
1125.8
1124.5
1123.1
21.68
22.05
22.42
9781
9771
9761
1132.6
1131.3
1129.9
21.84
22.21
22.59
219
218
217
16.86
16.54
16.22
9539
9529
9519
1108.1
1106.7
1105.4
22.47
22.86
23.25
9609
9599
9589
1114.9
1113.5
1112.1
22.64
23.03
23.43
9679
9669
9659
1121.7
1120.3
1118.9
22.80
23.20
23.60
9750
9739
9729
1128.5
1127.0
1125.6
22.97
23.36
23.77
216
215
214
15.90
15.60
15.29
9509
9499
9489
1104.0
1102.7
1101.3
23.66
24.07
24.49
9579
9569
9559
1110.7
1109.4
1108.0
23.83
24.25
24.67
9649
9639
9628
1117.5
1116.2
1114.8
24.01
24.42
24.85
9719
9708
9698
1124.3
1122.9
1121.5
24.18
24.60
25.03
213
212
211
14.99
14.70
14.41
9479
9469
9460
1100.0
1098.6
1097.3
24.92
25.36
25.82
9549
9539
9529
1106.7
1105.3
1103.9
25.10
25.54
26.01
9618
9608
9598
1113.4
1112.0
1110.6
25.29
25.73
26.19
9688
9677
9667
1120.1
1118.7
1117.3
25.47
25.92
26.38
210
209
208
14.1?
13. 8
13.57
9450
9441
9431
1095.9
1094.4
1093.1
26.27
26.74
27.22
9519
9510
9500
1102.5
1101.1
1099.8
26.46
26.93
27.42
9588
9579
9568
1109.2
1107.8
1106.4
26.66
27.13
27.61
9657
9647
9637
1115.9
1114.5
1113.1
26.85
27.32
27.81
207
206
205
13. 3C
13.03
12.77
9421
9411
9401
1091.7
1090.3
1088.9
27.71
28.21
28.73
9489
9479
9469
1098.4
1097.0
1095.6
27.91
28.42
28.93
9558
9548
9537
1105.0
1103.6
1102.2
28.11
28.62
29.15
9626
9616
9606
1111.7
1110.3
1108.9
28.31
28.83
29.35
204
203
202
12.51
12.26
12.01
9391
9381
9372
1087.6
1086.2
1084.9
29.25
29.78
30.34
9459
9449
9440
1094.2
1092.8
1091.5
29.46
30.00
30.56
9527
9517
9507
1100.8
1099.4
1098.1
29.68
30.22
30.78
9595
9585
9575
1107.5
1106.1
1104.7
29.89
30.43
30.99
201
200
199
11.77
11.53
11.29
9362
9352
9342
1083.5
1082.1
1080.7
30.88
31.44
32.02
9429
9419
9409
1090.1
1088.7
1087.3
31.11
31.67
32.25
9497
9487
9477
1096.7
1095.3
1093.8
31.33
31 . 89
32.48
9565
9554
9544
1103.3
1101.9
1100.4
31.55
32.12
32.71
198
197
196
11.06
10.83
10.61
9333
9323
9312
1079.3
1077.8
1076.4
32.60
33.20
33.81
9400
9390
9379
1085.9
1084.4
1083.0
32.83
33.44
34.06
9467
9457
9446
1092.5
1091.0
1089.5
33.07
33.67
34.30
9534
9524
9513
1099.1
1097.5
1096.1
33.30
33.91
34.54
195
194
193
10.39
10.17
9.96
9303
9293
9284
1075.1
1073.7
1072.3
34.45
35.10
35.77
9370
9360
9350
1081.6
1080.2
1078.8
34.70
35.35
36.03
9437
9426
9416
1088.2
1086.7
1085.4
34.94
35.60
36.28
9503
9493
9483
1094.7
1093.3
1091.9
35.19
35.85
36.54
192
191
190
9.75
9.54
9.34
9273
9263
9254
1070.9
1069.5
1068.1
36.45
37.15
37.87
9340
9329
9320
1077.4
1076.0
1074.6
36.71
37.42
38.14
9406
9395
9386
1083.9
1082.5
1081.1
36.97
37.68
38.41
9472
9462
9452
1090.4
1089.0
1087.6
37.24
37.95
38.68
189
188
187
9.14
8.95
8.76
9244
9234
9224
1066.8
1065.3
1063.9
38.59
39.33
40.08
9310
9300
9290
1073.2
1071.8
1070.4
38.87
39.61
40.36
9376
9365
9355
1079.7
1078.3
1076.9
39.14
39.89
40.65
9442
9431
9421
1086.2
1084.7
1083.3
39.42
40.17
40.93
186
185
184
8.57
8.38
8.20
9214
9204
9194
1062.5
1061.1
1059.7
40.85
41.63
42.45
9280
9270
9259
1069.0
1067.6
1066.1
41.14
41.93
42.75
9345
9335
9325
1075.4
1074.0
1072.6
41.43
42.22
43.05
9410
9400
9390
1081.9
1080.5
1079.0
41.72
42.52
43.35
183
182
181
8.02
7.85
7.68
9185
9175
9166
1058.3
1056.9
1055.4
43.28
44.14
45.03
9250
9240
9231
1064.7
1063.3
1061.8
43.59
44.45
45.35
9315
9305
9295
1071.2
1069.8
1068.2
43.89
44.77
45.67
9380
9370
9360
1077.6
1076.2
1074.7
44.20
45.08
45.99
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
r
&
1.72
1.73
1.74
1.75
1
P
IJ
1
ll
r
0)
o S
^1 "3
03
5
a
63
*j a
m
|J
OQ
<
a
3s
I!
H
||
228
227
226
20.02
19.64
19.28
9915
9905
9894
1147.7
1146.4
1145.0
19.90
20.23
20.56
9987
9977
9966
1154.6
1153.2
1151.8
20.04
20.37
20.71
12.4
10.1
7.9
1161.5
1160.0
1158.6
20.48
20.77
21.06
27.7
25.4
23.0
1168.8
1167.4
1166.0
21.00
21.29
21.59
225
224
223
222
221
220
18.91
18.56
18.21
17.86
17.52
17.19
9883
9873
9863
9852
9842
9831
1143.6
1142.2
1140.9
1139.5
1138.1
1136.7
20.91
21.27
21.63
22.00
22.37
22.75
9955
9944
9933
9923
9912
9902
1150.4
1149.0
1147.7
1146.3
1144.9
1143.5
21.06
21.42
21.78
22.16
22.53
22.91
5.6
3.4
1.1
1157.2
1155.8
1154.4
21.37
21.68
22.00
20.7
18.3
16.0
13.7
11.3
9.0
1164.5
1163.0
1161.6
1160.1
1158.6
1157.2
21.89
22.19
22.51
22.83
23.17
23.50
9994
9983
.9972
1153.0
1151.6
1150.2
22.32
22.69
23.08
219
218
217
216
215
214
16.86
16.54
16.22
15.90
15.60
15.29
9820
9809
9799
9788
9778
9767
1135.3
1133.8
1132.4
1131.0
1129.6
1128.2
23.14
23.53
23.94
24.35
24.78
25.21
9890
9879
9869
9858
9848
9837
1142.1
1140.6
1139.2
1137.8
1136.4
1135.0
23.30
23.70
24.11
24.53
24.95
25.39
9960
9950
9939
9928
9917
9906
1148.8
1147.3
1145.9
1144.5
1143.1
1141.7
23.47
23.87
24.28
24.70
25.13
25.57
6.6
4.2
1.9
1155.7
1154.2
1152.8
23.83
24.16
24.50
9998
9987
9976
1151.3
1149.8
1148.4
24.87
25.31
25.75
213
212
211
14.99
14.70
14.41
9757
9746
9737
1126.8
1125.4
1124.0
25.65
26.10
26.57
9826
9816
9806
1133.6
1132.2
1130.8
25.83
26.29
26.76
9896
9885
9875
1140.326.02
1138.926.47
1137.526.95
9965
9955
9944
1147.0
1145.6
1144.2
26.20
26.66
27.14
210
209
208
14.13
13.85
13.57
9726
9716
9705
1122.6
1121.2
1119.8
27.04
27.52
28.01
9795
9785
9774
1129.3
1127.9
1126.5
27.23
27.71
28.21
9864
9854
9843
1136.027.42
1134.6127.91
1133.128.41
9933
9923
9911
1142.7
1141.2
1139.8
27.61
28.10
28.60
207
206
205
13.30
13.03
12.77
9695
9684
9674
1118.4
1116.9
1115.5
28.51
29.03
29.56
9763
9753
9742
1125.0
1123.6
1122.2
28.71
29.24
29.77
9832
9821
9810
1131.7
1130.3
1128.8
28.92
29.44
29.98
9900
9889
9878
1138.4
1136.9
1135.5
29.12
29.65
30.19
204
203
202
12.51
12.26
12.01
9663
9653
9643
1114.1
1112.7
1111.3
30.10
30.65
31.21
9731
9720
9711
1120.7
1119.3
1117.9
30.31
30.86
31.43
9799
9788
9778
1127.4
1125.9
1124.5
30.52
31.08
31.65
9867
9856
9846
1134.0
1132.6
1131.2
30.74
31.29
31.87
201
200
199
11.77
11.53
11.29
9632
9622
9611
1109.9
1108.4
1107.0
31.78
32.35
32.94
9700
9689
9679
1116.5
1115.0
1113.6
32.00
32.58
33.17
9768
9757
9746
1123.1
1121.6
1120.2
32.22
32.80
33.40
9835
9824
9813
1129.7
1128.2
1126.8
32.45
33.03
33.63
198
197
196
11.06
10.83
10.61
9601
9591
9580
1105.6
1104.1
1102.6
33.54
34.15
34.78
9669
9658
9647
1112.2
1110.7
1109.2
33.77
34.39
35.03
9736
9725
9714
1118.8
1117.2
1115.8
34.01
34.63
35.27
9803'
9792
9781
1125.4
1123.8
1122.3
34.24
34.87
35.51
195
194
193
10.39
10.17
9.96
9570
9559
9549
1101.335.44
1099.836.11
1098.436.79
9637
9626
9616
1107.8
1106.3
1104.9
35.69
36.36
37.05
9704
9693
9682
1114.335.93
1112. 9136.61
1111.5:37.31
9770
9759
9749
1120.9
1119.4
1118.0
36.18
36.86
37.56
192
191
190
9.75
9.54
9.34
9539
9528
9518
1097.0
1095.5
1094.1
37.50
38.22
38.95
9605
9594
9584
1103.5
1102.0
1100.6
37.76
38.48
39.22
9671
9660
9650
1110.0
1108.5
1107.1
38.02
38.75
39.49
9738
9726
9716
1116.5
1115.0
1113.6
38.28
39.01
39.76
189
188
187
9.14
8.95
8.76
9508
9497
9487
1092.7
1091.2
1089.8
39.69
40.45
41.22
9574
9563
9552
1099.2
1097.7
1096.3
39.97
40.73
41.50
9639
9628
9618
1105.7
1104.2
1102.7
40.24
41.01
41.79
9705
9694
9683
1112.1
1110.6
1109.2
40.52
41.29
42.07
186
185
184
8.57
8.38
8.20
9476
9466
9455
1088.342.01
1086.942.81
1085.443.65
9541
9531
9520
1094.8
1093.4
1091.9
42.30
43.11
43.95
9607
9596
9585
1101.2
1099.8
1098.3
42.59
43.40
44.26
9672
9662
9650
1107.7
1106.3
1104.7
42.88
43.70
44.56
183
182
181
8.02
7.85
7.68
9445
9435
9425
1084.0
1082.6
1081.1
44.50
45.39
46.30
9510
9499
9490
1090.4
1089.0
1087.5
44.81
45.70
46.62
9575
9565
9555
1096.945.12
1095.448.02
1093.946.94
9640
9630
9619
1103.3
1101.8
1100.3
45.42
46.33
47.26
n6
TEMPERATURE-ENTROPY TABLE.
MMM 1 Temperature,
3 | Degrees Fahr. |
8
c
.3
0) O 1
1.68
1.69
1.70
1.71
<
1*
ll
02
13
3
11
W
OQ
15
3
a
1
W
^
&>
OQ
15
3
a
11
o 1
!^
DO
7.51
7.35
7.19
9156
9146
9137
1054.0
1052.6
1051.2
45.96
46.83
47.78
9220
9211
9201
1060.4
1059.0
1057.6
46.29
47.16
48.12
9285
9275
9265
1066.8
1065.4
1063.9
46.61
47.49
48.46
9350
9340
9330
1073.2
1071.7
1070.3
46.93
47.82
48.79
177
176
175
7.03
6.87
6.71
9127
9117
9107
1049.8
1048.3
1046.9
48.74
49.69
50.7
9191
9181
9171
1056.1
1054.7
1053.3
49.08
50.10
51.1
9255
9245
9235
1062.5
1061.0
1059.6
49.42
50.4
51.4
9320
9309
9299
1068.9
1067.4
1065.9
49.77
50.7
51.8
174
173
172
6.56
6.42
6.27
9098
9088
9078
1045.5
1044.1
1042.7
51.8
52.8
53.8
9161
9152
9142
1051.8
1050.4
1049.0
52.1
53.2
54.2
9225
9215
9205
1058.2
1056.7
1055.3
52.5
53.5
54.6
9289
9279
9269
1064.5
1063.1
1061.6
52.9
53.9
55.0
171
170
169
6.13
5.99
5.85
9068
9058
9049
1041.2
1039.8
1038.3
55.0
56.2
57.4
9131
9122
9112
1047.5
1046.1
1044.6
55.3
56.6
57.8
9195
9185
9175
1053.8
1052.3
1050.9
55.7
56.9
58.2
9258
9248
9238
1060.1
1058.6
1057.2
56.1
57.3
58.6
168
167
166
5.72
5.59
5.46
9040
9029
9020
1036.9
1035.5
1034.0
58.6
59.8
61.1
9103
9092
9082
1043.2
1041.7
1040.3
59.0
60.2
61.5
9165
9155
9145
1049.5
1048.0
1046.5
59.4
60.6
61.9
9228
9218
9208
1055.7
1054.3
1052.8
59.8
61.0
62.3
165
164
163
5.33
5.21
5.09
9010
9000
8991
1032.6
1031.1
1029.7
62.3
63.5
64.8
9073
9063
9053
1038.8
1037.4
1035.9
62.7
64.0
65.3
9135
9125
9115
1045.1
1043.6
1042.2
63.1
64.4
65.7
9198
9188
9177
1051.3
1049.9
1048.4
63.6
64.9
66.2
162
161
160
4.969
4.852
4.738
8981
8971
8962
1028.3
1026.9
1025.4
66.2
67.6
69.2
9043
9033
9023
1034.5
1033.1
1031.6
66.6
68.1
69.7
9105
9095
9085
1040.7
1039.3
1037.8
67.1
68.6
70.1
9167
9157
9147
1046.9
1045.5
1044.0
67.6
69.0
70.6
159
158
157
4.626
4.517
4.409
8952
8942
8933
1023.9
1022.5
1021.1
70.6
72.2
73.8
9014
9004
8994
1030.1
1028.6
1027.2
71.1
72.7
74.3
9075
9065
9056
1036.3
1034.8
1033.4
71.6
73.2
74.8
9137
9127
9117
1042.5
1041.0
1039.6
72.1
73.7
75.3
156
155
154
4.303
4.200
4.099
8923
8913
8903
1019.6
1018.1
1016.7
75.4
77.0
78.7
8984
8974
8964
1025.8
1024.3
1022.8
75.9
77.5
79.2
9046
9035
9025
1031.9
1030.4
1028.9
76.4
78.1
79.8
9107
9097
9086
1038.1
1036.6
1035.1
77.0
78.6
80.3
153
152
151
4.000
3.903
3.808
8894
8883
8873
1015.2
1013.8
1012.3
80.4
82.2
84.0
8955
8944
8934
1021.480.9
1019.9 82.7
1018.484.6
9015
9005
8995
1027.5
1026.0
1024.5
81.5
83.3
85.2
9076
9066
9055
1033.6
1032.1
1030.6
82.0
83.9
85.8
150
149
148
3.715
3.624
3.535
8864
8854
8845
1010.8
1009.4
1007.9
85.9
87.8
89.9
8925
8915
8905
1017.0
1015.4
1014.0
86.5
88.4
90.5
8985
8975
8965
1023.0
1021.5
1020.1
87.1
89.0
91.1
9046
9035
9026
1029.1
1027.6
1026.2
87.7
89.6
91.7
147
146
145
3.447
3.361
3.278
8835
8825
8815
1006.4
1005.0
1003.5
91.9
94.0
96.1
8895
8885
8875
1012.5
1011.0
1009.5
92.5 '
94.6
96.7
8955
8945
8935
1018.6
1017.1
1015.6
93.1
95.3
97.4
9015
9005
8995
1024.6
1023.2
1021.6
93.8
95.9
98.0
144
143
142
3.196
3.116
3.037
8805
8795
8786
1002.0
1000.5
999.1
98.3
100.5
102.9
8865
8855
8845
1008.1
1006.6
1005.1
98.9
101.2
103.6
8925
8915
8905
1014.1
1012.6
1011.1
99.6
101.9
104.3
8985
8974
8964
1020.1
1018.6
1017.1
100.3
102.6
105.0
141
140
139
2.960
2.885
2.812
8776
8766
8757
997.6
996.1
994.6
105.2
107.7
110.2
8836
8826
8816
1003.6
1002.1
1000.6
105.9
108.4
111.0
8895
8885
8875
1009.6
1008.1
1006.6
106.7
109.1
111.7
8954
8944
8934
1015.6
1014.1
1012.6
107.4
109.8
112.5
138
137
136
2.740
2.669
2.600
8747
8737
8728
993.2
991.6
990.2
112.8
115.4
118.2
8806
8796
8786
999.1
997.6
996.1
113.5
116.2
119.0
8865
8855
8845
1005.1
1003.6
1002.1
114.3
117.0
119.8
8924
8913
8904
1011.1
1009.5
1008.0
115.0
117.7
120.6
135
134
133
2.533
2.467
2.403
8718
8708
8698
988.7
987.1
985.7
121.0
123.8
126.8
8777
8766
8757
994.6
993.1
991.6
121.8
124.7
127.7
8835
8825
8815
1000.6
999.0
997.5
122.6
125.5
128.6
8894
8883
8873
1006.5
1005.0
1003.4
123.4
126.3
129.4
TEMPERATURE-ENTROPY TABLE.
II/
j3
-c
c
1.72
1.73
1.74
1.75
s
3 a
$
_
11
&
**
g
I-S
,1
>,
la
<g i
<2
2
c
o |
& a)
1
its
"3
3
1 *
l>
1
1 s
1^
1
IJ
l>
1
+a O
3*
II
H
9
K
OQ
<y
K
02
a
M
02
<y
H
02 ^
180
7.51
9414
1079.6
47.26
9479
1086.0
47.58
9543
1092.4
47.91
9608
1098.7
48.23
179
7.35
9404
1078.1
48.15
9469
1084.5
48.48
9533
1090.9
48.81
9598
1097.3
49.14
178
7.19
9394
1076.7
49.13
9458
1083.1
49.47
9523
1089.4
49.80
9587
1095.8
50.1
177
7.03
9384
1075.2
50.1
9448
1081.6
50.5
9512
1088.0
50.8
9576
1094.3
51.1
176
6.87
9373
1073.7
51.1
9437
1080.1
51.4
9501
1086.4
51.8
9565
1092.8
52.1
175
6.71
9363
1072.3
52.2
9427
1078.6
52.5
9491
1085.0
52.9
9555
1091.3
53.2
174
6.56
9353
1070.8
53.2
9417
1077.2
53.6
9480
1083.5
53.9
9544
1089.8
54.3
173
6.42
9343
1069.4
54.3
9406
1075.7
54.7
9470
1082.0
55.0
9534
1088.4
55.4
172
6.27
9332
1067.9
55.3
9396
1074.2
55.7
9459
1080.6
56.1
9523
1086.9
56.5
171
6.13
9322
1C36.4
56.5
9385
1072.7
56.9
9448
1079.0
57.3
9512
1085.3
57.6
170
5.99
9311
1064.9
57.7
9375
1071.2
58.1
9438
1077.5
58.5
9501
1083.8
58.9
169
5.85
9301
1063.5
59.0
9364
1069.8
59.4
9427
1076.0
59.8
9490
1082.3
60.2
168
5.72
9291
1062.0
60.2
9354
1068.3
60.6
9417
1074.6
61.0
9480
1080.8
61.4
167
5.59
9280
1060.5
61.4
9343
1066.8
61.9
9406
1073.1
62.3
9469
1079.3
62.7
166
5.46
9270
1059.1
62.8
9333
1065.3
63.2
9396
1071.6
63.6
9458
1077.8
64.0
165
5.33
9260
1057.6
64.0
9323
1063.8
64.4
9385
1070.1
64.9
9448
1076.3
65.3
164
5.21
9250
1056.1
65.3
9312
1062.3
65.7
9375
1068.6
66.2
9437
1074.8
66.6
163
5.09
9240
1054.6
66.6
9302
1060.8
67.1
9364
1067.1
67.5
9427
1073.3
68.0
162
4.969
9229
1053.1
68.0
9291
1059.3
68.5
9354
1065.5
68.9
9416
1071.8
69.4
161
4.852
9219
1051.7
69.5
9281
1057.9
70.0
9343
1064.1
70.4
9405
1070.3
70.9
160
4.738
9209
1050.2
71.1
9271
1056.4
71.6
9333
1062.6
72.0
9395
1068.8
72.5
159
4.626
9199
1048.7
72.6
9261
1054.9
73.1
9322
1061.1
73.6
9384
1067.2
74.0
158
4.517
9189
1047.2
74.2
9250
1053.4
74.6
9312
1059.5
75.1
9373
1065.7
75.6
157
4.409
9179
1045.7
75.8
9240
1051.9
76.3
9302
1058.1
76.8
9363
1064.2
77.3
156
4.303
9168
1044.2
77.5
9230
1050.4
78.0
9291
1056.5
78.5
9352
1062.7
79.0
155
4.200
9158
1042.7
79.1
9219
1048.9
79.7
9280
1055.0
80.2
9341
1061.2
80.7
154
4.099
9147
1041.2
80.9
9208
1047.3
81.4
9269
1053.5
81.9
9330
1059.6
82.5
153
4.000
9137
1039.7
82.6
9198
1045.9
83.2
9259
1052.0
83.7
9320
1058.1
84.3
152
3.903
9127
1038.2
84.4
9187
1044.3
85.0
9248
1050.5
85.5
9309
1056.6
86.1
151
3.808
9116
1036.7
86.3
9177
1042.8
86.9
9237
1048.9
87.5
9298
1055.0
88.1
150
3.715
9106
1035.2
88.2
9167
1041.3
88.8
9227
1047.4
89.4
9288
1053.5
90.0
149
3.624
9096
1033.7
90.2
9156
1039.8
90.8
9216
1045.9
91.4
9277
1052.0
92.0
148
3.535
9086
1032.2
92.3
9146
1038.3
92.9
9206
1044.4
93.5
9267
1050.5
94.1
147
3.447
9075
1030.7
94.4
9135
1036.8
95.0
9195
1042.8
95.6
9256
1048.9
96.3
146
3.361
9065
1029.2
96.5
9125
1035.3
97.2
9185
1041.3
97.8
9245
1047.4
98.5
145
3.278
9054
1027.7
98.7
9114
1033.7
99.3
9174
1039.8
100.0
9234
1045.8
100.6
144
3.196
9044
1026.2
100.9
9104
1032.2
101.6
9164
1038.3
102.3
9223
1044.3
102.9
143
3.116
9034
1024.6
103.3
9093
1030.7
103.9
9153
1036.7
104.6
9212
1042.7
105.3
142
3.037
9024
1023.1
105.7
9083
1029.2
106.4
9143
1035.2
107.1
9202
1041.2
107.8
141
2.960
9014
1021.6
108.1
9073
1027.6
108.8
9132
1033.6
109.5
9192
1039.7
110.2
140
2.885
9003
1020.1
110.6
9062
1026.1
111.3
9121
1032.1
112.0
9181
1038.1
112.7
139
2.812
8993
1018.6
113.2
9052
1024.6
114.0
9111
1030.5
114.7
9170
1036.5
115.5
138
2.740
8983
1017.1
115.8
9042
1023.0
116.6
9101
1029.0
117.3
9160
1035.0
118.1
137
2.669
8972
1015.5
118.5
9031
1021.5
119.3
9090
1027.4
120.1
9149
1033.4
120.9
136
2.600
8962
1014.0
121.3
9021
1019.9
122.1
9080
1025.9
122.9
9138
1031.8
123.7
135
2.533
8952
1012.5
124.3
9011
1018.4
125.1
9069
1024.4
125.9
9128
1030.3
126.7
134
2.467
8941
1010.9
127.1
9000 11016.8
128.0
9058
1022.8
128.8
9117
1028.7
129.6
133
2.403
8931
1009.4
130.2
8990
1015.3
131.1
9048
1021.2
131.9
9106
1027.1
132.8
118
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr. I
1
*|
oTo*
P
1.68
1.69
1.70
1.71
>
"3
s
0"
||
ll
4
si
l>
GO
>>
1
l|
I 1
. 6
|l
'o
&**
02
_>>
1
I*
I 1
OJ
I
en 2.
'
&*
OQ
>>
1
J'J
I 1
S3
|1
'5
132
131
130
2.341
2.280
2.220
8689
8679
8670
984.2
982.7
981.2
129.9
133.0
136.2
8747
8737
8728
990.1
988.6
987.1
130.8
133.9
137.1
8805
8795
8786
996.0
994.5
993.0
131.6
134.7
138.0
8863
8853
8843
1001.9
1000.4
998.9
132.5
135.6
138.9
129
128
127
2.161
2.103
2.047
8660
8650
8641
979.7
978.2
976.7
139.5
142.9
146.4
8718
8708
8698
985.6
984.1
982.6
140.
143.
147.
8775
8766
8756
991.5
989.9
988.4
141.4
144.8
148.3
8833
8823
8813
997.3
995.8
994.3
142.3
145.8
149.3
126
125
124
1.992
1.938
1.886
8631
8621
8611
975.2
973.7
972.2
150.0
153.7
157.5
8688
8678
8668
981.0
979.5
978.0
151.
154.
158.
8745
8735
8725
986.9
985.4
983.8
152.0
155.8
159.6
8803
8793
8782
992.7
991.2
989.7
153.0
156.8
160.6
123
122
121
1.835
1.785
1.737
8601
8591
8582
970.7
969.1
967.6
161.4
165.6
169.8
8658
8648
8639
976.5
974.9
973.4
162.
166.
170.
8715
8705
8695
982.3
980.7
979.2
163.6
167.7
172.0
8772
8762
8752
988.2
986.6
985.1
164.6
168.8
173.1
120
119
118
1.689
1.642
1.597
8572
8562
8553
966.1
964.6
963.1
174.0
178.4
183.0
8629
8619
8609
971.9
970.4
968.9
175.
179.
184.
8685
8675
8665
977.7
976.2
974.7
176.3
180.8
185.4
8742
8732
8722
983.5
982.0
980.4
177.5
182.0
186.6
117
116
115
1.552
1.509
1.467
8543
8533
8523
961.6
960.0
958.5
187.8
192.6
197.6
8599
8589
8579
967.4
965.8
964.3
189.0
193.8
198.9
8655
8645
8635
973.1
971.5
970.0
190.2
195.1
200.2
8711
8701
8691
978.9
977.3
975.8
191.5
196.4
201.5
114
113
112
1.426
1.386
1.347
8513
8503
8493
957.0
955.5
953.9
202.6
207.8
213.3
8569
8559
8549
962.7
961.2
959.7
203.9
209.
214.
8625
8614
8604
968.5
967.0
965.4
205.3
210.5
216.1
8680
8670
8660
974.2
972.7
971.1
206.6
211.9
217.4
111
110
109
1.308
1.271
1.235
8483
8474
8463
952.4
950.9
949.4
218.9
224.7
230.7
8539
8529
8518
958.2
956.6
955.1
220.
226.
232.
8594
8584
8574
963.9
962.2
960.7
221.7
227.7
233.7
8649
8640
8629
969.6
968.0
966.4
223.2
229.1
235.2
108
107
106
1.200
1.165
1.131
8454
8444
8434
947.8
946.3
944.7
236.9
243.3
250.0
8509
8499
8489
953.5
952.0
950.4
238.
244.
251.6
8564
8554
8544
959.1
957.6
956.0
240.0
246.5
253.2
8619
8608
8598
964.8
963.3
961.7
241.5
248.1
254.9
105
104
103
1.098
1.066
1.035
8424
8414
8405
943.2
941.6
940.1
256.8
263.8
271.0
8479
8469
8459
948.8
947.2
945.7
258.4
265.5
272.7
8534
8523
8513
954.5
952.9
951.4
260.1
267.2
274.5
8588
8578
8568
960.1
958.5
957.0
261.8
268.9
276.2
102
101
100
1.005
0.975
0.946
8395
8385
8375
938.5
937.0
935.4
278.4
286.0
293.8
8449
8439
8429
944.1
942.6
941.0
280.2
287.9
295.7
8503
8494
8483
949.8
948.2
946.6
282.0
289.7
297.6
8558
8548
8537
955.4
953.8
952.2
283.8
291.6
299.5
99
98
97
0.918
0.891
0.864
8365 "
8356
8346
933.9
932.3
930.8
301.9
310.2
318.9
8419
8409
8399
939.5
937.9
936.4
303.8
312.2
320.9
8473
8463
8453
945.0
943.4
941.9
305.8
314.2
323.0
8527
8517
8507
950.6
949.0
947.5
307.7
316.2
325.0
96
95
94
0.838
0.813
0.788
8336
8326
8316
929.3
927.8
926.2
327.9
337.0
346.5
8389
8380
8370
934.8
933.3
931.7
330.0
339.2
348.8
8443
8433
8423
940.4
938.8
937.2
332.1
341.4
351.0
8497
8486
8476
946.0
944.4
942.8
334.2
343.5
353.2
93
92
91
0.764
0.741
0.718
8307
8297
8287
924.6
923.0
921.5
356.4
366.6
377.4
8360
8350
8340
930.1
928.5
927.0
358.7
369.1
379.8
8413
8403
8393
935.7
934.1
932.5
361.0
371.4
382.2
8466
8456
8446
941.3
939.6
938.0
363.3
373.7
384.6
90
89
88
0.696
0.675
0.654
8277
8267
8257
919.9
918.3
916.7
388.4
399.6
411.2
8330
8320
8310
925.4
923.8
922.2
390.8
402.2
413.8
8383
8373
8362
930.9
929.3
927.7
393.3
404.7
416.4
8435
8425
8415
936.4
934.8
933.1
395.8
407.3
419.1
87
86
85
0.633
0.613
0.594
8248
8238
8228
915.2
913.6
912.0
423.1
435.0
447.6
8300
8290
8280
920.6
919.0
917.4
425.8
437.7
450.4
8353
8342
8332
926.1
924.5
922.9
428.5
440.5
453.3
8405
8395
8384
931.6
930.0
928.3
431.2
443.2
456.1
TEMPERATURE-ENTROPY TABLE.
u
o
c
1.72
1.73
1.74
1.75
el
o 2
2 =o
II
fff.
6 a
<si
.
la
||
g
la
ll
g
la
! J
ft S 1
H
I
I 1
1
*> o
& **
QQ
1
I 1
I
132
2.341
8921
1007.8
133.4
8980
1013.7
134.2
9038
1019.6
135.1
9096
1025.6
136.0
131
2.280
8911
1006.3 136.5
8969
1012.2
137.4
9027
1018.1
138.3
9085
1024.0
139.2
130
2.220
8901
1004.8
139.8
8959
1010.7
140.7
9017
1016.6
141.7
9075
1022.5
142.6
129
2.161
8891
1003.2
143.2
8949
1009.1
144.2
9006
1015.0
145.1
9064
1020.9
146.0
128
2.103
8881
1001.7
146.7
8938
1007.6
147.7
8996
1013.4
148.6
9054
1019.3
149.6
127
2.047
8870
1000.2
150.3
8928
1006.1
151.2
8985
1011.9
152.2
9043
1017.8
153.2
126
.992
8860
998.6
154.0
8917
1004.5
155.0
8975
1010.3
156.0
9032
1016.2
157.0
125
.938
8850
997.11157.8
8907
1003.0
158.8
8964
1008.8
159.8
9021
1014.7
160.9
124
.886
8839
995.5
161.7
8896
1001.3
162.7
8953
1007.2
163.8
9011
1013.0
164.8
123
.835
8829
994.0
165.7
8886
999.8
166.8
8943
1005.6
167.9
9000
1011.4
168.9
122
.785
8819
992.4169.9
8876
998.2
171.0
8932
1004.0
172.1
8989
1009.8
173.2
121
.737
8809
990.9
174.2
8866
996.7
175.4
8922
1002.5
176.5
8979
1008.3
177.6
120
.689
8799
989.3
178.6
8855
995.1
179.8
8912
1000.9
180.9
8968
1006.7
182.1
119
.642
8788
987.8
183.1
8844
993.6
184.3
8901
999.4
185.5
8957
1005.1
186.7
118
.597
8778
986.2
187.8
8834
992.0
189.0
8891
997.8
190.2
8947
1003.5
191.4
117
.552
8767
984.6
192.7
8824
990.4
193.9
8880
996.2
195.2
8936
1001.9
196.4
116
.509
8757
983.0
197.6
8813
988.8
198.9
8869
994.5
200.2
8925
1000.3
201.4
115
.467
8747
981.5
202.8
8803
987.3
204.0
8859
993.0
205.3
8915
998.7
206.6
114
.426
8736
979.9
207.9
8792
985.7
209.2
8848
991.4
210.6
8904
997.1
211.9
113
.386
8726
978.41213.3
8781
984.1
214.6
8837
989.8
216.0
8893
995.5
217.3
112
.347
8715
976.8
218.8
8771
982.5
220.2
8826
988.2
221.6
8882
993.9
223.0
111
.308
8705
975.3
224.6
8760
980.9
226.0
8816
986.6
227.4
8871
992.3
228.9
110
.271
8695
973.7
230.6
8750
979.3
232.1
8805
985.0
233.5
8861
990.7
235.0
109
.235
8684
972.1
236.7
8739
977.8
238.2
8794
983.4
239.7
8849
989.1
241.2
108
.200
8674
970.5
243.0
8729
976.2
244.6
8784
981.8
246.1
8839
987.5
247.7
107
.165
8663
968.9
249.7
8718
974.6
251.3
8773
980.2
252.8
8828
985.9
254.4
106
.131
8653
967.3
256.5
8708
973.0
258.1
8763
978.6
259.7
8817
984.3
261.3
105
.098
8643
965.7
263.4
8698
971.4
265.1
8752
977.0
266.8
8807
982.7
268.4
104
.066
8632
964.1
270.6
8687
969.8
272.3
8741
975.4
274.0
8796
981.0
275.7
103
.035
8622
962.6
278.0
8677
968.2
279.7
8731
973.8
281.5
8785
979.4
283.2
102
1.005
8612
961.0
285.6
8666
966.6
287.4
8720
972.2
289.2
8775
977.8
291.0
101
0.975
8602
959.4
293.4
8656
965.0
295.3
8710
970.6
297.1
8764
976.2
298.9
100
0.946
8591
957.8
301.4
8645
963.4
303.3
8699
969.0
305.2
8753
974.6
307.1
99
0.918
8581
956.2
309.7
8635
961.8
311.6
8689
967.4
313.6
8743
973.0
315.5
98 0.891
8571
954.6318.2
8624
960.2
320.2
8678
965.8
322.2
8732
971.3
324.2
97
0.864
8560
953.1
327.1
8614
958.5
329.1
8668
964.2
331.2
8721
969.8
333.2
96
0.838
8550
951.5
336.3
8604
957.0
338.4
8657
962.6
340.5
8711
968.2
342.6
95
0.813
8540
949.91345.7
8593
955.4
347.9
8647
961.0
350.0
8700
966.6
352.2
94
0.788
8529
948.3
355.4
8583
953.8
357.6
8636
959.4
359.9
8689
964.9
362.1
93
0.764
8519
946.7
365.6
8572
952.2
367.8
8626
957.8
370.1
8679
963.3
372.4
92 0.741 8509
945.1 376.1
8562
950.6
378.4
8615
956.1
380.8
8668
961.6
383.1
91
0.718
8498
943.5
387.0
8551
949.0
389.4
8604
954.5
391.8
8657
960.0
394.2
90
0.696
8488
941.9
398.3
8541
947.4
400.7
8594
952.9
403.2
8646
958.3
405.7
89
0.675
8478
940.3409.8
8531
945.8
412.4
8583
951.3414.9
8636
956.7
417.5
88
0.654
8467
938.6
421.7
8520
944.1
424.3
8572
949.6
426.9
8625
955.0
429.5
87
0.633
8457
937.0
433.9
8510
942.5
436.6
8562
948.0
439.2
8615
953.4
441.9
86
0.613 8447
935.4446.0
8499
940.9
448.8
9552
946.3
451.5
8604
951.8454.3
85
0.594 8437
933.8458.9
8489
939.2
461.8
8541
944.7464.6
8593
950.1467.5
120
TEMPERATURE-ENTROPY TABLE.
"S
1
1.76
1.77
1.78
1.79
v M
PH d
Ijs
<J
<r 3
Jj
ij
g
a
642
a>
I ]
g
J*
ii
H
1
23
02
5
23
W
GQ
1
23
OQ
1
23
'" :>
324
94 8
276
1325 4
6 60
297 5
1336 1
6 77
323
93 5
273 4
1323 7
6 67
295
1334 4
6 84
322
92 2
271
1322 1
6 75
292 5
1332 7
6 92
321
90 9
268 4
1320 4
6 82
289 9
1331 1
6 99
320
89 6
266
1318 8
6 90
287 4
1329 5
7 06
319
88 3
263.5
1317.1
6.97
284.9
1327.8
7.14
318
317
316
87.1
85.9
84.6
260.9
258.4
255.9
1315.5
1313.9
1312.2
7.04
7.11
7.19
282.3
279.8
277.3
1326.2
1324.5
1322.9
7.21
7.29
7.37
300.8
298.3
i335'.o
1333.3
7^52
315
314
313
83.4
82.3
81.1
253.4
250.9
248.4
1310.6
1309.0
1307.4
7.28
7.35
7.44
274.7
272.1
269.6
1321.2
1319.5
1317.8
7.45
7.53
7.62
295.7
293.1
290.5
1331.6
1329.9
1328.3
7.60
7.69
7.77
...
312
311
310
79.9
78.8
77.6
245.9
243.4
241.0
1305.8
1304.2
1302.6
7.52
7.60
7.68
267.1
264.5
262.0
1316.2
1314.6
1313.0
7.70
7.79
7.88
288.0
285.5
283.0
1326.6
1324.9
1323.3
7.86
7.95
8.03
...
309
308
307
76.5
75.4
74.3
238.5
236.0
233.6
1301.0
1299.4
1297.8
7.77
7.86
7.95
259.5
257.0
254.4
1311.4
1309.7
1308.1
7.97
8.05
8.14
280.5
278.0
275.5
1321.7
1320.0
1318.3
8.12
8.21
8.30
299'. 1
296.5
1330.3
1328.6
8.40
8.50
306
305
304
73.2
72.2
71.1
231.2
228.8
226.4
1296.3
1294.7
1293.1
8.04
8.13
8.22
251.9
249.3
246.9
1306.4
1304.8
1303.2
8.23
8.33
8.42
273.0
270.5
267.9
1316.7
1315.0
1313.4
8.40
8.49
8.59
294.0
291.4
288.8
1326.9
1325.3
1323.6
8.59
8.69
8.79
303
302
301
70.0
69.0
68.0
224.0
221.7
219.2
1291.5
1289.9
1288.4
8.31
8.40
8.50
244.4
241.9
239.4
1301.6
1300.0
1298.3
8.51
8.60
8.70
265.3
262.8
260.1
1311.7
1310.0
1308.3
8.69
8.79
8.89
286.2
283.5
281.0
1321. g
1320.2
1318.5
8.89
8.99
9.09
300
299
298
67.0
66.0
65.0
216.7
214.2
211.8
1286.8
1285.2
1283.6
8.60
8.70
8.80
236.9
234.4
231.9
1296.7
1295.1
1293.5
8.80
8.91
9.01
257.6
255.0
252.5
1306.6
1304.9
1303.3
8.99
9.09
9.20
278.4
275.9
273.2
1316.8
1315.1
1313.4
9.19
9.29
9.40
297
296
295
64.0
63.1
62.1
209.3
206.8
204.4
1282.0
1280.4
1278.8
8.90
9.00
9.10
229.4
227.0
224.6
1291.9
1290.3
1288.7
9.11
9.22
9.33
250.0
247.4
244.9
1301.7
1300.1
1298.4
9.30
9.41
9.51
270.5
268.0
265.4
1311.7
1310.1
1308.5
9.50
9.61
9.72
294
293
292
61.2
60.2
59.3
202.0
199.5
197.1
1277.2
1275.6
1274.0
9.21
9.33
9.44
222.1
219.6
217.2
1287.1
1285.5
1283.9
9.44
9.55
9.66
242.3
239.8
237.3
1296.8
1295.2
1293.6
9.62
9.73
9.85
262.9
260.3
257.7
1306.8
1305.2
1303.5
9.83
9.95
10.06
291
290
289
58.4
57.5
56.7
194.7
192.3
189.8
1272.5
1271.0
1269.4
9.55
9.66
9.78
214.7
212.1
209.6
1282.3
1280.6
1279.0
9.77
9.88
10.00
234.7
232.1
229.6
1291.8
1290.2
1288.5
9.97
10.09
10.20
255.1
252.6
250.0
1301.9
1300.2
1298.5
10.18
10.30
10.42
288
287
286
55.8
54.9
54.1
187.4
185.0
182.6
1267.9
1266.4
1264.8
9.89
10.01
10.13
207.0
204.4
201.9
1277.4
1275.8
1274.2
10.12
10.24
10.36
227.0
224.5
222.0
1286.9
1285.2
1283.6
10.32
10.45
10.58
247.3
244.7
242.1
1296.9
1295.2
1293.5
10.56
10.68
10.80
285
284
283
53.2
52.4
51.6
180.2
177.8
175.4
1263.3
1261.7
1260.1
10.25
10.37
10.50
199.4
196.9
194.4
1272.6
1271.0
1269.4
10.48
10.61
10.74
219.4
216.9
214.4
1282.0
1280.4
1278.8
10.70
10.83
10.97
239.5
236.9
234.3
1291.8
1290.2
1288.5
10.94
11.06
11.20
282
281
280
50.8
50.0
49.19
173.0
170.6
168.2
1258.5
1257.0
1255.4
10.62
10.75
10.88
191.9
189.5
187.0
1267.8
1266.2
1264.6
10.87
1 .00
1 .14
211.9
209.4
206.8
1277.2
1275.6
1274.0
11.10
11.23
11.36
231.7
229.1
226.5
1286.8
1285.2
1283.5
11.34
11.47
11.62
279
278
277
48.41
47.64
46.88
165.8
163.4
161.0
1253.9
1252.4
1250.9
11.02
11.15
11.29
184.6
182.2
179.7
1263.1
1261.6
1260.0
1 .28
1 .42
1 .56
204.4
202.0
199.5
1272.4
1270.9
1269.3
11.50
11.65
11.80
224.0
221.4
218.8
1281.8
1280.2
1278.6
11.76
11.90
12.05
TEMPERATURE-ENTROPY TABLE.
121
J
1
le
1.80
1.81
1.82
1.83
ITemperatur
Degrees ]
!!
<**
iu
Quality.
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
Quality.
Heat Con-
tents.
Specific
Volume.
324
94.8
323
93.5
39!?,
92.2
321
90.9
I
320
89.6
319
88.3
318
87.1
317
85.9
316
84.6
315
83 4
314
82 3
313
81.1
312
79.9
311
78.8
310
77.6
309
76.5
308
75.4
307
74.3
306
73 2
305
72 2
304
71.1
303
'70.0
30?,
69.0
301
68.0
300
67.0
299.0
1326.7
9.37
299
66.0
296.3
1325.0
9.48
298
65.0
293.7
1323.3
9.60
297
64
291.0
1321.6
9 70
296
63 1
288.4
1319 9
9 81
295
294
62.1
61.2
285.8
283.1
1318.2
1316.4
9.92
10.03
293
60.2
280.5
1314.7
10.15
301.5
1325 2
10 36
292
59.3
277.8
1313.0
10.27
298.7
1323 4
10 48
291
58.4
275.1
1311.4
10.39
296
1321 7
10 60
290
57.5
272.4
1309.7
10.52
293.3
1320.0
10.73
2R9
56.7
269.8
1308.0
10 65
290 6
1318 3
10 86
288
55.8
267.2
1306.4
10.77
288.0
1316.6
10.99
287
54.9
264.5
1304.7
10.90
285.3
1314.8
11.11
286
54.1
261.9
1303.0
11.03
282.5
1313.1
11.25
285
284
283
282
281
280
279
278
277
53.2
52.4
51.6
50.8
50.0
49.19
48.41
47.64
46.88
259.3
256.7
254.0
251.4
248.7
246.0
243.3
240.7
238.1
1301.4
1299.7
1298.0
1296.4
1294.7
1293.0
1291.4
1289.7
1288.0
11.16
11.29
11.43
11.57
11.72
11.86
12.00
12.15
12.30
279.8
277.1
274.4
271.7
269.0
266.3
263.6
261.0
258.3
1311.4
1309.7
1308.0
1306.3
1304.6
1302.9
1301.2
1299.5
1297.8
11.39
11.53
11.67
11.81
11.96
12.10
12.25
12.40
12.56
301.0
298.3
295.5
292.8
290.0
287.2
284.5
281.7
279.0
1321.9
1320.1
1318.3
1316.5
1314.8
1313.0
1311.2
1309.5
1307.7
11.64
11.78
11.93
12.07
12.22
12.37
12.53
12.69
12.84
30l'.5
298.8
13Y9.0
1317.3
12.95
13.10
122
TEMPERATURE-ENTROPY TABLE.
b
a
o
1.76
1.77
1.78
1.79
<!>
03 JJ)
5i
c
c5
<!
>,
da
si
6a
a!
s -
g
da
d
ll
F
jy
1
|3
1*
a
*
GO
a
^
CO*
03
<
23
CO
276
275
274
46.13
45.39
44.67
158.6
156.2
153.8
1249.3
1247.8
1246.3
11.43
11.57
11.72
177.3
174.8
172.3
1258.4
1256.8
1255.2
11.70
11.84
11.99
197.0
194.4
191.9
1267.7
1266.0
1264.4
11.94
12.09
12.24
216.2
213.6
211.0
1277.0
1275.3
1273.6
12.20
12.35
12.50
273
272
271
43.95
43.24
42.54
151.4
149.0
146.6
1244.7
1243.2
1241.7
11.86
12.01
12.16
169.9
167.4
165.0
1253.6
1252.0
1250.4
12.13
12.29
12.44
189.4
186.9
184.3
1262.8
1261.2
1259.6
12.39
12.54
12.70
208.4
205.8
203.2
1271.9
1270.3
1268.6
12.66
12.82
12.99
270
269
268
41.84
41.16
40.49
144.2
141.8
139.4
1240.2
1238.7
1237.2
12.32
12.47
12.63
162.5
160.0
157.5
1248.8
1247.2
1245.7
12.60
12.76
12.92
181.7
179.1
176.5
1258.0
1256.4
1254.8
12.86
13.02
13.20
200.6
198.0
195.4
1266.9
1265.3
1263.7
13.15
13.31
13.49
267
266
265
39.83
39.17
38.53
137.0
134.5
132.1
1235.7
1234.2
1232.6
12.79
12.95
13.12
155.0
152.6
150.1
1244.1
1242.6
1241.0
13.08
13.25
13.42
174.0
171.5
169.0
1253.2
1251.6
1250.0
13.36
13.53
13.70
192.8
190.2
187.7
1262.0
1260.4
1258.8
13.66
13.83
14.01
264
263
262
37.89
37.26
36.64
129.7
127.3
124.9
1231.0
1229.5
1228.0
13.29
13.46
13.64
147.7
145^2
142.8
1239.5
1237.9
1236.4
13.58
13.76
13.94
166.4
163.9
161.3
1248.4
1246.7
1245.1
13.88
14.06
14.23
185.1
182.5
179.9
1257.2
1255.6
1254.0
14.19
14.38
14.56
261
260
259
36.02
35.42
34.83
122.5
120.1
117.7
1226.4
1224.9
1223.3
13.81
13.99
14.17
140.3
137.8
135.3
1234.8
1233.2
1231.7
14.11
14.30
14.49
158.8
156.2
153.6
1243.5
1241.9
1240.3
14.41
14.60
14.79
177.3
174.7
172.1
1252.4
1250.8
1249.1
14.75
14.95
15.14
258
257
256
34.24
33.66
33.09
115.3
112.9
110.5
1221.7
1220.2
1218.6
14.35
14.54
14.74
132.9
130.4
128.0
1230.1
1228.6
1227.0
14.67
14.86
15.05
151.0
148.4
145.8
1238.7
1237.0
1235.4
14.99
15.18
15.38
169.5
166.9
164.3
1247.4
1245.8
1244.2
15.33
15.53
15.74
255
254
253
32.53
31.97
31.42
108.1
105.7
103.3
1217.1
1215.6
1214.1
14.93
15.11
15.31
125.4
123.0
120.4
1225.5
1224.0
1222.4
15.25
15.44
15.65
143.2
140.6
138.1
1233.8
1232.1
1230.5
15.58
15.78
15.99
161.8
159.2
156.5
1242.6
1241.0
1239.3
15.94
16.15
16.36
252
251
250
30.88
30.35
29.82
100.9
98.5
96.1
1212.5
1211.0
1209.4
15.52
15.72
15.94
118.0
115.5
113.0
J1220.8
1219.2
1217.6
15.86
16.06
16.27
135.5
133.0
130.4
1228.9
1227.3
1225.7
16.20
16.40
16.62
153.9
151.3
148.7
1237.7
1236.1
1234.4
16.58
16.80
17.02
249
248
247
29.30
28.79
28.29
93.7
91.3
88.9
1207.9
1206.4
1204.8
16.14
16.36
16.57
110.5
108.0
105.6
1216.0
1214.4
1212.9
16.49
16.70
16.92
127.9
125.4
122.9
1224.1
1222.6
1221.0
16.84
17.06
17.29
146.1
143.5
140.9
1232.8
1231.2
1229.6
17.24
17.47
17.70
246
245
244
27.80
27.31
26.83
86.5
84.0
81.6
1203.3
1201.8
1200.3
16.79
17.01
17.23
103.1
100.6
98.2
1211.4
1209.9
1208.3
17.14
17.35
17.60
120.4
117.8
115.3
1219.5
1217.9
1216.3
17.51
17.75
17.99
138.3
135.7
133.1
1227.9
1226.3
1224.7
17.93
18.17
18.41
243
242
241
26.35
25.88
25.42
79.2
76.8
74.4
1198.8
1197.3
1195.8
17.47
17.70
17.94
95.7
93.3
90.9
1206.7
1205.1
1203.6
17.83
18.07
18.30
112.8
110.3
107.8
1214.7
1213.1
1211.5
18.23
18.48
18.72
130.5
127.9
125.3
1223.1
1221.4
1219.8
18.67
18.91
19.17
240
239
238
24.97
24.52
24.08
72.0
69.6
67.2
1194.3
1192.8
1191.3
18.18
18.41
18.67
88.4
85.9
83.4
1202.0
1200.5
1198.9
18.56
18.80
19.06
105.2
102.7
100.2
1209.9
1208.3
1206.8
18.99
19.23
19.50
122.6
120.0
117.5
1218.2
1216.6
1215.0
19.43
19.70
19.97
237
236
235
23.64
23.21
22.79
64.8
62.4
60.0
1189.7
1188.2
1186.6
18.93
19.19
19.44
81.0
78.5
76.0
1197.4
1195.8
1194.3
19.31
19.59
19.85
97.7
95.2
92.7
1205.2
1203.6
1202.0
19.76
20.04
20.30
115.0
112.4
109.7
1213.4
1211.8
1200.1
20.24
20.50
20.80
234
233
232
22.38
21.97
21.57
57.6
55.2
52.8
1185.1
1183.6
1182.1
19.70
19.99
20.26
73.5
71.0
68.6
1192.7
1191.2
1189.6
20.12
20.40
20.69
90.1
87.6
85.1
1200.4
1198.8
1197.3
20.60
20.89
21.17
107.1
104.5
101.9
1208.5
1206.9
1205.3
21.10
21.39
21.69
231
230
229
21.17
20.78
20.40
50.4
48.0
45.7
1180.6
1179.1
1177.6
20.54
20.83
21.11
66.1
63.6
61.2
1188.0
1186.4
1184.9
20.99
21.29
21.58
82.6
80.1
77.7
1195.8
1194.3
1192.8
21.47
21.77
22.10
99.3
96.8
94.3
1203.7
1202.1
1200.5
22.00
22.30
22.61
TEMPERATURE-ENTROPY TABLE.
123
Temperature,
Degrees Fahr. 1
Pressure, Pounds!
per Square
Inch.
1.80
1.81
1.82
1.83
>>
I
4 j
11
w
fi
QD
>*
I
a
3s
13
w
*!
p
02
I
!<2
*!
0> **
w
ij
P
02
1
1
s*
11
B
o 1
S -
3 o
i*
02
276
275
274
46.13
45.39
44.67
235.4
232.8
230.2
1286.3
1284.7
1283.0
12.45
12.60
12.76
255.5
252.8
250.1
1296.1
1294.4
1292.7
12.71
12.87
13.03
276.3
273.5
270.8
1306.0
1304.2
1302.5
13.00
13.16
13.33
296.0
293.2
290.4
1315.6
1313.8
1312.0
13.26
13.43
13.60
273
272
271
43.95
43.24
42.54
227.6
224.9
222.2
1281.3
1279.6
1277.9
12.93
13.10
13.26
247.4
244.7
242.0
1291.0
1289.3
1287.6
13.20
13.36
13.54
268.0
265.2
262.5
1300.7
1299.0
1297.3
13.50
13.67
13.84
287.7
284.9
282.1
1310.2
1308.5
1306.7
13.77
13.95
14.13
270
269
268
41.84
41.16
40.49
219.5
216.9
214.3
1276.2
1274.5
1272.8
13.43
13.60
13.78
239.4
236.7
234.0
1285.9
1284.2
1282.5
13.70
13.89
14.06
259.7
257.0
254.2
1295.5
1293.7
1292.0
14.02
14.20
14.39
279.3
276.5
273.8
1304.9
1303.2
1301.4
14.31
14.50
14.68
267
266
265
39.83
39.17
38.53
211.6
209.0
206.3
1271.1
1269.4
1267.7
13.95
14.13
14.31
231.3
228.6
225.9
1280.8
1279.1
1277.4
14.24
14.43
14.60
251.4
248.7
246.0
129D.3
1288.5
1286.8
14.57
14.76
14.94
271.0
268.2
265.5
1299.7
1297.9
1296.1
14.87
15.06
15.26
264
263
262
37.89
37.26
36.64
203.6
200.9
198.3
1266.0
1264.3
1262.6
14.50
14.70
14.89
223.2
220.5
217.8
1275.7
1274.0
1272.3
14.80
15.00
15.19
243.3
240.5
237.7
1285.1
1283.3
1281.6
15.13
15.33
15.53
262.7
260.0
257.2
1294.4
1292.6
1290.9
15.45
15.65
15.86
261
260
259
36.02
35.42
34.83
195.6
193.0
190.4
1261.0
1259.4
1257.7
15.07
15.27
15.47
215.1
212.4
209.7
1270.6
1268.9
1267.1
15.39
15.58
15.79
235.0
232.2
229.5
1279.8
1278.1
1276.4
15.73
15.94
16.15
254.4
251.6
248.9
1289.2
1287.4
1285.6
16.07
16.27
16.49
258
257
256
34.24
33.66
33.09
187.9
185.4
182.9
1256.1
1254.5
1252.9
15.67
15.88
16.09
207.0
204.3
201.5
1265.4
1263.6
1261.9
16.00
16.20
16.41
226.7
224.0
221.2
1274.7
1273.0
1271.2
16.36
16.57
16.79
246.1
243.3
240.5
1283.9
1282.2
1280.5
16.70
16.93
17.15
255
254
253
32.53
31.97
31.42
180.2
177.6
174.9
1251.3
1249.6
1247.9
16.30
16.52
16.73
198.8
196.1
193.4
1260.2
1258.5
1256.8
16.62
16.84
17.06
218.5
215.7
213.0
1269.5
1267.8
1266.1
17.01
17.23
17.46
237.8
235.0
232.3
1278.7
1277.0
1275.2
17.39
17.60
17.84
252
251
250
30.88
30.35
29.82
172.2
169.5
166.8
1246.2
1244.5
1242.9
16.95
17.18
17.40
190.7
188.0
185.3
1255.1
1253.3
1251.6
17.29
17.52
17.75
210.3
207.5
204.7
1264.3
1262.6
1260.9
17.69
17.92
18.16
229.5
226.7
224.0
1273.5
1271.7
1269.9
18.09
18.32
18.56
249
248
247
29.30
28.79
28.29
164.2
161.5
158.8
1241.2
1239.5
1237.8
17.63
17.86
18.10
182.5
179.8
177.1
1249.9
1248.2
1246.6
18.00
18.23
18.48
202.0
199.2
196.4
1259.2
1257.4
1255.7
18.40
18.65
18.90
221.2
218.4
215.7
1268.2
1266.5
1264.8
18.80
19.06
19.32
246
245
244
27.80
27.31
26.83
156.1
153.4
150.7
1236.2
1234.6
1232.9
18.34
18.59
18.84
174.4
171.7
169.0
1244.9
1243.2
1241.5
18.73
18.99
19.23
193.6
190.9
188.1
1254.0
1252.3
1250.5
19.14
19.40
19.66
213.0
210.2
207.4
1263.1
1261.3
1259.6
19.59
19.84
20.11
243
242
241
26.35
25.88
25.42
148.0
145.4
142.8
1231.2
1229.5
1227.8
19.10
19.35
19.61
166.3
163.7
161.0
1239.8
1238.1
1236.4
19.49
19.76
20.03
185.3
182.6
179.9
1248.8
1247.1
1245.4
19.93
20.20
20.47
204.6
201.9
199.1
1257.9
1256.2
1254.5
20.39
20.67
20.95
240
239
238
24.97
24.52
24.08
140.1
137.3
134.5
1226.1
1224.4
1222.7
19.88
20.15
20.42
158.3
155.6
152.9
1234.7
1233.0
1231.4
20.31
20.59
20.87
177.1
174.3
171.5
1243.7
1242.0
1240.3
20.76
21.03
21.32
196.3
193.5
190.7
1252.8
1251.1
1249.3
21.25
21.53
21.82
237
236
235
23.64
23.21
22.79
131.8
129.1
126.5
1221.1
1219.4
1217.7
20.70
20.99
21.29
150.2
147.4
144.7
1239.7
1228.0
1226.3
21.16
21.45
21.76
168.8
166.0
163.2
1238.6
1236.9
1235.2
21.62
21.93
22.23
188.0
185.2
182.4
1247.6
1245.9
1244.2
22.13
22.44
22.76
234
233
232
22.38
21.97
21.57
123.8
121.1
118.4
1216.1
1214.5
1212.8
21.59
21.89
22.19
142.0
139.3
136.6
1224.6
1222.9
1221.2
22.06
22.38
22.69
160.4
157.6
154.9
1233.5
1231.7
1230.0
22.54
22.86
23.20
179.6
176.9
174.1
1242.4
1240.7
1238.9
23.09
23.41
23.74
231
230
229
21.17
20.78
20.40
115.8
113.2
110.7
1211.2
1209.6
1208.0
22.50
22.83
23.17
133.9
131.2
128.5
1219.5
1217.8
1216.1
23.02
23.35
23.68
152.1
149.3
146.6
1228.2
1226.4
1224.7
23.52
23.87
24.20
171.3
168.5
165.7
1237.2
1235.4
1233.7
24.10
24.45
24.79
124
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr.
T3
k
"o*
9 .d
m
1.76
1.77
1.78
1.79
tf>
j*
|J
i
Ss
d
o |
S-g
>>
J*
!
|
I*
,1
1
r
V
<
V
|*
m
1
r
r
1
gs
||
OQ
228
227
226
20.02
19.64
19.28
43.3
40.9
38.5
1176.1
1174.6
1173.1
21.41
21.71
22.02
58.8
56.4
54.0
1183.3
1181.8
1180.3
21.90
22.20
22.53
75.2
72.7
70.2
1191.2
1189.6
1188.0
22.40
22.74
23.06
91.8
89.2
86.6
1198.9
1197.2
1195.6
22.94
23.29
23.61
225
224
223
18.91
18.56
18.21
36.1
33.7
31.3
1171.6
1160.1
1168.6
22.32
22.64
22.98
51.5
49.0
46.6
1178.8
1177.3
1175.8
22.87
23.20
23.54
67.7
65.2
62.7
1186.4
1184.9
1183.3
23.40
23.74
24.09
84.0
81.4
78.8
1194.0
1192.4
1190.8
23.96
24.30
24.67
222
221
220
17.86
17.52
17.19
29.0
26.6
24.2
1167.1
1165.6
1164.1
23.32
23.67
24.01
44.2
41.8
39.4
1174.3
1172.8
1171.3
23.90
24.25
24.60
60.2
57.7
55.1
1181.7
1180.1
1178.6
24.44
24.80
25.17
76.2
73.6
71.0
1189.2
1187.6
1186.0
25.01
25.40
25.79,
219
218
217
16.86
16.54
16.22
21.7
19.3
16.9
1162.6
1161.1
1159.6
24.37
24.73
25.10
37.0
34.6
32.2
1169.8
1168.3
1166.8
24.96
25.33
25.72
52.6
50.1
47.6
1177.0
1175.5
1174.0
25.55
25.93
26.31
68.5
65.9
63.4
1184.4
1182.8
1181.2
26.15
26.55
26.94
216
215
214
15.90
15.60
15.29
14.5
12.1
9.8
1158.2
1156.7
1155.2
25.47
25.83
26.22
29.8
27.4
25.0
1165.3
1163.8
1162.3
26.10
26.50
26.90
45.1
42.7
40.3
1172.4
1170.9
1169.4
26.72
27.13
27.54
60.9
58.3
55.7
1179.7
1178.1
1176.5
27.35
27.77
28.20
213
212
211
14.99
14.70
14.41
7.4
5.0
2.6
1153.8
1152.3
1150.8
26.60
26.98
27.38
22.6
20.2
17.9
1160.8
1159.3
1157.8
27.31
27.73
28.16
37.9
35.5
33.0
1167.9
1166.3
1164.8
27.95
28.38
28.80
53.1
50.6
48.0
1174.9
1173.3
1171.7
28.61
29.04
29.47
210
209
208
14.13
13.85
13.57
0.2
1149.4
27.80
15.5
13.1
10.7
1156.3
1154.9
1153.4
28.59
29.00
29.43
30.5
28.1
25.6
1163.3
1161.8
1160.3
29.23
29.67
30.11
45.5
43.0
40.5
1170.1
1168.6
1167.0
29.92
30.38
30.83
9991
9980
1148.0
1146.5
28.29
28.80
207
206
205
13.30
13.03
12.77
9969
9958
9947
1145.1
1143.6
1142.1
29.32
29.85
30.40
8.3
5.9
3.5
1151.9
1150.4
1148.9
29.87
30.30
30.75
23.2
20.7
18.2
1158.7
1157.2
1155.7
30.59
31.05
31.51
38.0
35.6
33.1
1165.5
1164.0
1162.5
31.30
31.79
32.28
204
203
202
12.51
12.26
12.01
9936
9924
9914
1140.6
1139.2
1137.8
30.95
31.51
32.09
0.7
1147.4
31.20
15.8
13.3
10.8
1154.2
1152.7
1151.2
31.99
32.48
32.97
30.6
28.1
25.6
1161.0
1159.4
1157.8
32.78
33.27
33.78
9992
9982
1145.9
1144.4
31.72
32.31
201
200
199
11.77
11.53
11.29
9903
9892
9881
1136.3
1134.8
1133.4
32.67
33.26
33.86
9971
9959
9948
1142.9
1141.4
1139.9
32.89
33.48
34.09
8.3
5.9
3.4
1149.6
1148.0
1146.5
33.46
33.98
34.48
23.1
20.6
18.1
1156.2
1154.7
1153.2
34.30
34.82
35.35
198
197
196
11.06
10.83
10.61
9870
9859
9848
1131.9
1130.4
1128.9
34.48
35.11
35.76
9937
9926
9915
1138.5
1136.9
1135.4
34.71
35.35
36.00
1.0
1145.0
35.00
15.6
13.1
10.7
1151.8
1150.3
1148.8
35.90
36.45
37.02
9993
9981
1143.5
1142.0
35. 5y
36.24
195
194
193
10.39
10.17
9.96
9837
9826
9815
1127.4
1125.9
1124.5
36.43
37.11
37.82
9904
9893
9882
1134.0
1132.5
1131.0
36.67
37.36
38.07
9971
9959
9948
1140.5
1139.0
1137.6
36.92
37.62
38.33
8.2
5.7
3.2
1147.3
1145.7
1144.2
37.60
38.18
38.78
192
191
190
9.75
9.54
9.34
9804
9793
9782
1123.0
1121.5
1120.1
38.54
39.28
40.03
9870
9859
9848
1129.5
1128.0
1126.6
38.80
39.54
40.30
9937
9925.
9914
1136.0
1134.5
1133.1
39. D6
39.81
40.57
0.6
1142.7
39.39
9991
9980
1141.1
1139.6
40.07
40.84
189
188
187
9.14
8.95
8.76
9771
9760
9749
1118.6
1117.1
1115.7
40.79
41.57
42.36
9837
9826
9815
1125.1
1123.6
1122.1
41.07
41.85
42.64
9903
9891
9880
1131.6
1130.1
1128.6
41.35
42.13
42.93
9969
9957
9946
1138.1
1136.5
1135.1
41.62
42.41
43.21
186
185
184
8.57
8.38
8.20
9738
9727
9716
1114.2
1112.7
1111.2
43.17
43.99
44.86
9803
9792
9781
1120.6
1119.1
1117.6
43.46
44.29
45.16
9869
9858
9846
1127.1
1125.6
1124.0
43.75
44.59
45.46
9934
9923
9911
1133.5
1132.0
1130.5
44.04
44.88
45.76
183
182
181
8.02
7.85
7.68
9705
9695
9684
1109.7
1108.2
1106.7
45.73
46.64
47.58
9770
9760
9749
1116.1
1114.7
1113.1
46.04
46.95
47.90
9835
9824
9814
1122.6
1121.1
1119.5
46.34
47.27
48.21
9900
9889
9878
1129.0
1127.5
1125.9
46.65
47.58
48.53
TEMPERATURE-ENTROPY TABLE.
I2S
ll
^3
1
1.80
1.81
1.82
1.83
Et2
11
f
H
3
K4
||
<cJ
g
6 3
|
6
j*
s|
c3
ll
i
III
1
1*
!>
1
** -
ll
;3
1 1
1
i ^
H
fi
<y
H
OQ
<y
**
GO
<
H
OB
m
CQ
228
20.02
108.1
1206.3
23.50
125.9
1214.4
24.01
143.9
1223.1
24.55
162.9
1232.0
25.13
227
19.64
105.5
1204.6
23.84
123.2
1212.7
24.37
141.211221.4
24.90
160.1
1230.2
25.50
226
19.28
103.0
1203.0
24.19
120.5
1211.1
24.73
138.4
1219.7
25.27
157.2
1228.4
25.89
225
18.91
100.4
1201.4
24.53
117.8
1209.5
25.09
135.5
1217.9
25.64
154.4
1226.6
26.28
224
18.56
97.8
1199.8
24.90
115.1
1207.9
25.45
132.7
1216.2
26.02
151.5
1224.9
26.65
223
18.21
95.2
1198.2
25.26
112.4
1206.3
25.82
129.9
1214.4
26.40
148.7
1223.2
27.04
222
17.86
92.6
1196.6
25.64
109.8
1204.7
26.20
127.1
1212.7
26.80
145.9
1221.4
27.43
221
17.52
90.0
1195.0
26.01
107.2
1203.0
26.60
124.4
1211.0
27.20
143.1
1219.7
27.83
220
17.19
87.4
1193.3
26.40
104.5
1201.3
26.99
121.6
1209.3
27.60
140.3
1218.0
28.25
219
16.86
84.8
1191.7
26.80
101.9
1199.7
27.39
118.9
1207.6
28.00
137.5
1216.3
28.67
218
16.54
82.1
1190.1
27.20
99.3
1198.1
27.80
116.2
1205.9
28.43
134.7
1214.5
29.10
217
16.22
79.5
1188.5
27.60
96.7
1196.5
28.20
113.5
1204.3
28.86
131.9
1212.8
29.53
216
15.90
76.9
1186.9
28.02
94.0
1194.9
28.61
110.8
1202.6
29.30
129.1
1211.0
29.98
215
15.60
74.4
1185.3
28.46
91.4
1193.3
29.05
108.1
1201.0
29.73
126.2
1209.3
30.43
214
15.29
71.9
1183.8
28.88
88.8
1191.7
29.49
105.4
1199.3
30.18
123.4
1207.5
30.89
213
14.99
69.4
1182.2
29.31
86.2
1190.0
29.93
102.8
1197.7
30.63
120.5
1205.8
31.35
212
14.70
66.9
1180.7
29.75
83.6
1188.4
30.39
100.1
1196.0
31.10
117.7
1204.1
31.83
211
14.41
64.3
1179.1
30.20
81.0
1186.8
30.85
97.4
1194.4
31.56
114.9
1202.3
32.30
210
14.13
61.7
1177.5
30.66
78.4
1185.2
31.31
94.8
1192.7
32.05
112.1
1200.7
32.79
209
13.85
59.1
1175.9
31.11
75.8
1183.6
31.80
92.1
1191.1
32.51
109.3
1199.0
33.30
208
13.57
56.5
1174.3
31.60
73.2
1182.0
32.29
89.4
1189.5
33.00
106.5
1197.3
33.80
207
13.30
53.9
1172.7
32.08
70.6
1180.4
32.77
86.8
1187.8
33.51
103.8
1195.6
34.31
206
13.03
51.3
1171.1
32.56
68.0
1178.8
33.29
84.1
1186.2
34.02
101.0
1193.9
34.84
205
12.77
48.7
1169.5
33.05
65.3
1177.2
33.78
81.5
1184.6
34.56
98.2
1192.2
35.39
204
12.51
46.2
1168.0
33.55
62.6
1175.6
34.30
78.9
1183.0
35.10
95.5
1190.5
35.93
203
12.26
43.6
1166.4
34.06
60.0
1174.0
34.83
76.3
1181.4
35.63
92.8
1188.8
36.49
202
12.01
41.0
1164.8
34.58
57-4
1172.3
35.39
73.6
1179.7
36.19
90.0
1187.2
37.06
201
11.77
38.4
1163.2
35.10
54.8
1170.7
35.94
71.0
1178.0
36.78
87.3
1185.5
37.63
200
11.53
35.8
1161.7
35.66
52.1
1169.0
36.51
68.3
1176.3
37.37
84.6
1183.8
38.21
199
11.29
33.2
1160.1
36.20
49.4
1167.4
37.10
65.6
1174.7
37.92
82.0
1182.2
38.80
198
11.06
30.7
1158.5
36.77
46.8
1165.8
37.69
62.9
1173..0
38.56
79.3
1180.6
39.40
197
10.83
28.1
1156.9
37.33
44.1
1164.2
38.30
60.1
1171.3
39.18
76.7
1179.0
40.04
196
10.61
25.6
1155.4
37.92
41.5
1162.6
38.90
57.4
1169.7
39.80
74.1
1177.4
40.67
195
10.39
23.0
1153.8
38.50
38.9
1161.0
39.52
54.7
1168.1
40.43
71.4
1175.8
41.30
194
10.17
20.5
1152.3
39.11
36.3
1159.4140.17
52.0
1166.5
41.07
68.8
1174.2
41.95
193
9.96
18.0
1150.8
39.72
33.7
1157.8
40.83
49.3
1164.9
41.75
66.2
1172.6
42.60
192
9.75
15.5
1149.3
40.39
31.0
1156.2
41.48
46.6
1163.3
42.43
63.6
1171.0
43.30
191
9.54
13.01147.7
41.00
28.3
1154.6
42.12
44.0
1161.7
43.10
61.0
1169.4
44.00
190
9.34
10.4
1146.2
41.65
25.7
1153.1
42.83
41.3
1160.1
43.78
58.3
1167.8
44.70
189
'9.14
7.9
1144.7
42.30
23.1
1151.5
43.52
38.6
1158.5
44.50
55.5
1166.1
45.40
188
8.95
5.3 1143.2
42.99
20.5
1149.9
44.22
36.0
1156.9
45.20
52.7
1164.5
46.10
187
8.76
2.7
1141.7
43.68
17.9
1148.3
44.95
33.3
1155.3
45.90
50.0
1162.8
46.90
186
8.57
0.1
1140.0
44.33
15.3
1146.7
45.68
30.6
1153.7
46.65
47.2
1161.1
47.70
185
8.38
9988 1138. 4i45. 18
12.7
1145.2
46.40
28.0
1152.1
47.40
44.4
1159.4
48.50
184
8.20
9976
1136.9
46.06
10.1
1143.7
47.15
25.3
1150.5
48.15
41.6
1157.7
49.30
183
8.02
9965
1135.3
46.96
7.5
1142.1
47.90
22.6
1148.8
48.90
38.8
1156.1
50.15
182
7.85 9954
1133.8
47.89
4.9
1140.5
48.70
20.0
1147.2
49.65
36.0J1154.5
51.05
181
7.68i 9943
1132.2
48.85
2.2
1138.9
49.45
17.3
1145.6
50.40
33.2
1152.8
51.95
126
TEMPERATURE-ENTROPY TABLE.
T5
a
1.76
1.77
1.78
1.79
a
o 2
3 _
||
&T.
&
e
< i
a
|
|
o5
a
y3 3
Is
|l
ioJ
1
-*> o
l>
1
-u C
w -^
ll
3
ll
'3 "3
1
3
11
1^
H
a
**
02
<
w
02
M
OQ
O"
a
OQ
180
7.51
9673
105.1
48.56
9737
1111.5
48.88
9802
1117.9
49.21
9867
1124.3
49.53
179
7.35
9662
103.7
49.47
9727
1110.0
49.80
9791
116.4
50.1
9856
1122.8
50.5
178
7.19
9651
102.2
50.4
9716
1108.6
50.8
9780
1114.9
51.1
9844
1121.3
51.5
177
7.03
9641
100.7
51.5
9705
1107.1
51.8
9769
1113.4
52.2
9833
1119.8
52.5
176
6.87
9629
099.2
52.5
9693
1105.5
52.8
9757
1111.9
53.2
9821
1118.2
53.5
175
6.71
9619
097.7
53.6
9683
1104.0
53.9
9747
1110.4
54.3
9811
1116.7
54.6
174
6.56
9608
096.2
54.7
9672
1102.5
55.0
9736
1108.8
55.4
9799
1115.2
55.8
173
6.42
9597
1094.7
55.8
9661
1101.0
56.1
9725
1107.3
56.5
9788
1113.7
56.9
172
6.27
9587
1093.2
56.8
9650
1099.5
57.2
9714
1105.8
57.6
9777
1112.1
58.0
171
6.13
9575
1091.6
58.0
9638
1097.9
58.4
9702
1104.2
58.8
9765
1110.5
59.2
170
5.99
9564
1090.1
59.3
9627
1096.4
59.7
9691
1102.7
60.1
9754
1109.0
60.5
169
5.85
9553
1088.6
60.6
9616
1094.9
61.0
9680
1101.2
61.4
9743
1107.5
61.8
168
5.72
9543
1087.1
61.8
9606
1093.4
62.2
9669
1099.7
62.7
9732
1105.9
63.1
167
5.59
9532
1085.6
63.1
9595
1091.9
63.5
9657
1098.1
63.9
9720
1104.4
64.3
166
5.46
9521
1084.1
64.5
9584
1090.3
64.9
9646
1096.6
65.3
9709
1102.8
65.7
165
5.33
9510
1082.6
65.7
9573
1088.8
66.1
9636
1095.0
66.6
9698
1101.3
67.0
164
5.21
9500
1081.0
67.1
9562
1087.3
67.5
9624
1093.5
67.9
9687
1099.7
68.4
163
5.09
9489
1079.5
68.4
9551
1085.7
68.9
9613
1092.0
69.3
9676
1098.2
69.8
162
4.969
9478
1078.0
69.9
9540
1084.2
70.3
9602
1090.4
70.8
9664
1096.6
71.2
161
4.852
9467
1076.5
71.4
9529
1082.7
71.9
9591
1088.9
72.3
9653
1095.1
72.8
160
4.738
9457
1075.0
73.0
9518
1081.2
73.5
9580
1087.4
74.0
9642
1093.6
74.4
159
4.626
9446
1073.4
74.5
9508
1079.6
75.0
9569
1085.8
75.5
9631
1092.0
76.0
158
4.517
9435
1071.9
76.1
9497
1078.1
76.6
9558
1084.2
77.1
9620
1090.4
77.6
157
4.409
9425
1070.4
77.8
9486
1076.6
78.4
9547
1082.7
78.9
9609
1088.9
79.4
156
4.303
9414
1068.9
79.5
9475
1075.0
80.1
9536
1081.2
80.6
9598
1087.3
81.1
155
4.200
9402
1067.3
81.2
9464
1073.4
81.8
9525
1079.6
82.3
9586
1085.7
82.8
154
4.099
9391
1065.7
83.0
9453
1071.9
83.6
9514
1078.0
84.1
9575
1084.2
84.6
153
4.000
9381
1064.2
84.8
9442
1070.4
85.4
9503
1076.5
85.9
9564
1082.6
86.5
152
3.903
9370
1062.7
86.7
9431
1068.8
87.2
9491
1074.9
87.8
9552
1081.0
88.4
151
3.808
9359
1061.1
88.6
9419
1067.2
89.2
9480
1073.3
89.8
9541
1079.4
90.3
150
3.715
9348
1059.6
90.6
9409
1065.7
91.2
9469
1071.8
91.8
9530
1077.9
92.3
149
3.624
9337
1058.0
92.6
9398
1064.1
93.2
9458
1070.2
93.8
9518
1076.3
94.4
148
3.535
9327
1056.5
94.8
9387
1062.6
95.4
9447
1068.7
96.0
9508
1074.8
96.6
147
3.447
9316
1055.0
96.9
9376
1061.0
97.5
9436
1067.1
98.1
9496
1073.1
98.8
146
3.361
9305
1053.4
99.1
9365
1059.5
99.7
9425
1065.5
100.4
9485
1071.6
101.0
145
3.278
9294
1051.8
101.3
9354
1057.9
102.0
9413
1063.9
102.6
9473
1070.0
103.3
144
3.196
9283
1050.3
103.6
9343
1056.4
104.3
9403
1062.4
104.9
9462
1068.4
105.6
143
3.116
9272
1048.7
106.0
9332
1054.8
106.7
9391
1060.8
107.3
9451
1066.8
108.0
142
3.037
9262
1047.2
108.5
9321
1053.2
109.1
9380
1059.2
109.8
9440
1065.2
110.5
141
2.960
9251
1045.7
110.9
9310
1051.7
111.6
9369
1057.7
112.3
9429
1063.7
113.1
140
2.885
9240
1044.1
113.5
9299
1050.1
114.2
9358
1056.0
114.9
9417
1062.0
115.6
139
2.812
9229
1042.5
116.2
9288
1048.5
117.0
9347
1054.5
117.7
9406
1060.5
118.5
138
2.740
9219
1041.0
118.8
9278
1047.0
119.6
9337
1053.0
120.3
9396
1058.9
121.1
137
2.669
9207
1039.4
121.6
9266
1045.3
122.4
9325
1051.3
123.2
9384
1057.3
124.0
136
2.600
9197
1037.8
124.5
9256
1043.8
125.3
9314
1049.7
126.1
9372
1055.7
126.9
135
2.533
9186
1036.2
127.5
9245
1042.2
128.3
9303
1048.1
129.1
9362
1054.1
129.9
134
2.467
9175
1034.6
130.5
9233
1040.6
131.3
9292
1046.5
132.1
9350
1052.4
133.0
133
2.403
9164
1033.1
133.6
9223
1039.0
134.5
9281
1044.9
135.3
9339
1050.8
136.2
TEMPERATURE-ENTROPY TABLE.
u
a
1.80
1.81
1.82
1.83
r d
o
f!
a _
ol
a
6-
V
a
i
c
a!
II
H
ill
I M
^
3
<y
11
do
1
-S
n
do
1
a
Jl
F
$
1
2
V
GO
180
7.51
9931
1130.7
49.85
9996
1137.2
50.1
14.6
1144.0
51.2
30.4
1151.1
52.9
179
7.35
9920
1129.250.79
9985
1135.6
51.1
12.0
1142.5
52.0
27.6
1149.4
53.8
178
7.19
9909
1127.751.82
9973
1134.1
52.2
9.3
1140.9
52.8
24.7
1147.8
54.6
177
7.03
9897
1126.2
52.9
9962
1132.5
53.2
6.6
1139.3
53.5
21.8
1146.0
55.6
176
6.87
9886
1124.6
53.9
9950
1130.9
54.2
3.9
1137.7
54.3
18.9
1144.3
56.5
175
6.71
9874
1123.0
55.0
9938
1129.4
55.4
1 .1
1136.0
55.1
16.0
1142.6
57.5
174
6.56
9863
1121.5
56.1
9927
1127.9
56.5
9991
1134.3
56.8
13.1
1140.9
58.4
173
6.42
9852
1120.0
57.2
9916
1126.3
57.6
9979
1132.6
58.0
10.2
1139.2
59.4
172
6.27
9841
1118.4
58.4
9904
1124.8
58.7
9968
1131.1
59.1
7.3
1137.5
60.4
171
6.13
9829
1116.8
59.6
9892
1123.1
59.9
9955
1129.5
60.3
4.4
1135.8
61.4
170
5.99
9817
1115.3
60.9
9880
1121.6
61.3
9944
1127.9
61.6
1.5
1134.2
62.4
169
5.85
9806
1113.8
62.2
9869
1120.0
62.6
9932
1126.3
63.0
9995
1132.6
63.4
168
5.72
9795
1112.2
63.5
9858
1118.5
63.9
9921
1124.8
64.3
9984
1131.0
64.7
167
5.59
9783
1110.6
64.8
9846
1116.9
65.2
9909
1123.2
65.6
9971
1129.4
66.0
166
5.46
9772
1109.1
66.2
9835
1115.3
66.6
9897
1121.6
67.0
9960
1127.9
67.4
165
5.33
9761
1107.5
67.4
9823
1113.8
67.9
9886
1120.0
68.3
9948
1126.
68.7
164
5.21
9749
1106.0
68.8
9812
1112.2
69.3
9874
1118.4
69.7
9936
1124.
70.2
163
5.09
9738
1104.4
70.2
9800
1110.6
70.7
9862
1116.9
71.1
9925
1123.
71.6
162
4.969
9726
1102.8
71.7
9789
1109.0
72.1
9851
1115.3
72.6
9913
1121.
73.1
161
4.852
9715
1101.3
73.3
9777
1107.5
73.7
9839
1113.7
74.2
9901
1119.
74.7
160
4.738
9704
1099.7
74.9
9766
1105.9
75.4
9828
1112.1
75.9
9890
1118.
76.3
159
4.626
9693
1098.2
76.5
9755
1104.4
77.0
9816
1110.5
77.4
9878
1116.
77.9
158
4.517
9681
1096.6
78.1
9743
1102.8
78.6
9805
1108.9
79.1
9866
1115.1
79.6
157
4.409
9670
1095.1
79.9
9732
1101.2
80.4
9793
1107.4
80.9
9855
1113.6
81.4
156
4.303
9659
1093.5
81.6
9720
1099.6
82.1
9782
1105.8
82.7
9843
1111.9
83.2
155
4.200
9647
1091.9
83.4
9708
1098.0
83.9
9770
1104.2
84.4
9831
1110.3
84.9
154
4.099
9636
1090.3
85.2
9697
1096.4
85.7
9758
1102.6
86.3
9819
1108.7
86.8
153
4.000
9625
1088.7
87.0
9685
1094.9
87.6
9746
llOliO
88.1
9807
1107.1
88.7
152
3.903
9613
1087.1
88.9
9674
1093.3
89.5
9734
1099.4
90.0
9795
1105.5
90.6
151
3.808
9601
1085.5
90.9
9662
1091.6
91.5
9722
1097.8
92.1
9783
1103.9
92.6
150
3.715
9590
1084.0
92.9
9651
1090.1
93.5
9711
1096.2
94.1
9772
1102.3
94.7
149
3.624
9579
1082.4
95.0
9639
1088.5
95.6
9700
1094.6
96.2
9760
1100.6
96.8
148
3.535
9568
1080.8
97.2
9628
1086.9
97.8
9688
1093.0
98.4
9749
1099.1
99.0
147
3.447
9556
1079.2
99.4
9616
1085.3
100.0
9676
1091.3
100.6
9736
1097.4
101.3
146
3.361
9545
1077.71101.7
9605
1083.7
102.3
9665
1089.8
102.9
9725
1095.8
103.6
145
3.278
9533
1076.0
103.9
9593
1082.1
104.6
9653
1088.1
105.2
9713
1094.2
105.9
144
3.196
9522
1074.5
106.3
9582
1080.5
106.9
9641
1086.5
107.6
9701
1092.6
108.3
143
3.116
9510
1072.8 108.7
9570
1078.9
109.4
9630
1084.9
110.1
9689
1090.9
110.7
142
3.037
9499
1071.3
111.2
9559
1077.3
111.9
9618
1083.3
112.6
9678
1089.3
113.3
141
2.960
9488
1069.7
113.8
9547
1075.7
114.5
9607
1081.7
115.2
9666
1087.7
115.9
140
2.885
9476
1068.0 116.41 9536
1074.0
117.1
9595
1080.0
117.8
9654
1086.0
118.6
139
2.812
9465
1066.5
119.2
9524
1072.4
120.0
9584
1078.4
120.7
9643
1084.4
121.5
138
2.740
9454
1064.9
121.9
9513
1070.8
122.6
9572
1076.8
123.4
9631
1082.8
124.1
137
2.669
9443
1063.2
124.7
9501
1069.2
125.5
9560
1075.1
126.3
9619
1081.1
127.1
136
2.600
9431
1061.6
127.7
9490
1067.6
128.5
9549
1073.5
129.3
9607
1079.5
130.1
135
2.533
9420
1060.0
130.8
9479
1066.0
131.6
9538
1071.9
132.4
9596
1077.9
133.2
134
2.467
9409
1058.4 133.8
9467
1064.3
134.6
9525
1070.2
135.4
9584
076.2
36.3
133
2.403
9397
1056.8(137.0 9456
1062.7
137.9
9514
1068.6 138.7
9572
074.5
39.6
128
TEMPERATURE-ENTROPY TABLE.
Temperature,
Degrees Fahr. I
1
*l
Ki
jt,
1.76
1.77
1.78
1.79
|j
5
J
11
H
1
c 3.
\>
02
|
.1
I*
i 1
!
p
>>
"eS
3
O"
6 4S
II
ll
02
*j
e
6 2
ll
!
'5 ,0
^
02
132
131
130
2.341
2.280
2.220
9154
9143
9133
1031.5
1029.9
1028.3
136.9
140.1
143.5
9212
9201
9191
1037.4
1035.8
1034.2
137.7
141.0
144.4
9270
9259
9248
1043.3
1041.7
1040.1
138.6
141.9
145.3
9328
9317
9306
1049.2
1047.6
1046.0
139.5
142.7
146.2
129
128
127
2.161
2.103
2.047
9122
9111
9100
1026.8
1025.2
1023.6
147.0
150.5
154.2
9180
9169
9158
1032.7
1031.1
1029.5
147.9
151.5
155.1
9237
9226
9215
1038.5
1036.9
1035.3
148.8
152.4
156.1
9295
9284
9273
1044.4
1042.8
1041.2
149.7
153.4
157.1
126
125
124
1.992
1.938
1.886
9089
9079
9068
1022.0
1020.5
1018.8
158.0
161.9
165.8
9147
9136
9125
1027.9
1026.3
1024.7
159.0
162.9
166.9
9204
9193
9182
1033.7
1032.2
1030.5
160.0
163.9
167.9
9261
9250
9239
1039.6
1038.0
1036.3
161.0
164.9
169.0
123
122
121
1.835
1.785
1.737
9057
9046
9036
1017.3
1015.6
1014.0
170.0
174.3
178.7
9114
9103
9092
1023.1
1021.4
1019.9
171.1
175.4
179.8
9171
9160
9149
1029.0
1027.3
1025.7
172.1
176.5
181.0
9228
9217
9206
1034.8
1033.1
1031.5
173.2
177.6
182.1
120
119
118
.689
.642
.597
9025
9014
9003
1012.5
1010.9
1009.3
183.2
187.8
192.6
9081
9070
9060
1018.3
1016.7
1015.1
184.4
189.0
193.8
9138
9127
9116
1024.1
1022.5
1020.9
185.5
190.2
195.0
9195
9183
9172
1029.9
1028.3
1026.6
186.6
191.4
196.2
117
116
115
.552
.509
.467
8992
8981
8971
1007.7
1006.1
1004.5
197.6
202.7
207.9
9048
9037
9027
1013.5
1011.8
1010.2
198.9
204.0
209.2
9105
9093
9082
1019.2
1017.5
1015.9
200.1
205.2
210.5
9161
9149
9138
1025.0
1023.3
1021.7
201.4
206.5
211.8
114
113
112
1.426
1.386
1.347
8959
8948
8938
1002.9
1001.3
999.7
213.2
218.7
224.4
9015
9004
8993
1008.6
1007.0
1005.4
214.6
220.1
225.8
9071
9060
9049
1014.3
1012.7
1011.1
215.9
221.4
227.2
9127
9115
9104
1020.1
1018.4
1016.8
217.2
222.8
228.6
111
110
109
1.308
1.271
1.235
8926
8916
8905
998.1
996.4
994.8
230.3
236.4
242.7
8982
8971
8960
1003.8
1002.1
1000.5
231.7
237.9
244.2
9037
9027
9015
1009.5
1007.8
1006.2
233.2
239.4
245.7
9093
9082
9070
1015.2
1013.5
1011.9
234.6
240.8
247.2
108
107
106
1.200
.165
.131
8894
8883
8872
993.2
991.6
989.9
249.2
256.0
263.0
8949
8938
8927
998.9
997.3
995.6
250.8
257.6
264.6
9004
8993
8982
1004.5
1002.9
1001.2
252.3
259.2
266.2
9059
9048
9037
1010.2
1008.6
1006.9
253.8
260.8
267.8
105
104
103
.098
.066
.035
8862
8850
8840
988.3
986.7
985.1
270.1
277.5
285.0
8916
8905
8894
994.0
992.3
990.7
271.8
279.2
286.7
8971
8959
8949
999.6
997.9
996.3
273.4
280.9
288.5
9026
9014
9003
1005.3
1003.6
1002.0
275.1
282.6
290.3
102
101
100
1.005
0.975
0.946
8829
8818
8807
983.4
981.8
980.2
292.8
300.8
309.0
8883
8873
8861
989.1
987.4
985.7
294.6
302.6
310.8
8938
8927
8915
994.7
993.0
991.3
296.4
304.5
312.7
8992
8981
8969
1000.3
998.6
996.9
298.2
306.3
314.6
99
98
97
0.918
0.891
0.864
8796
8786
8775
978.6
976.9
975.3
317.5
326.2
335.3
8850
8839
8828
984.1
982.5
980.9
319.4
328.2
337.3
8904
8893
8882
989.7
988.0
986.4
321.4
330.2
339.4
8958
8947
8936
995.3
993.6
992.0
323.3
332.2
341.4
96
95
94
0.838
0.813
0.788
8764
8753
8743
973.7
972.1
970.4
344.7
354.3
364.3
8818
8807
8796
979.3
977.7
976.0
346.8
356.5
366.5
8871
8860
8849
984.8
983.2
981.5
348.9
358.7
368.7
8925
8914
8902
990.4
988.8
987.1
351.0
360.8
371.0
93
92
91
0.764
0.741
0.718
8732
8721
8710
968.8
967.2
965.5
374.7
385.5
396.7
8785
8774
8763
974.4
972.7
971.0
377.0
387.8
399.1
8838
8827
8816
979.9
978.2
976.5
379.2
390.1
401.5
8891
8880
8869
985.4
983.7
982.0
381.5
392.5
403.9
90
89
88
0.696
0.675
0.654
8699
8688
8678
963.8
962.2
960.5
408.2
420.0
432.1
8752
8741
8730
969.3
967.7
966.0
410.6
422.5
434.8
8805
8794
8783
974.8
973.2
971.5
413.1
425.1
437.4
8858
8846
8835
980.3
978.6
976.9
415.6
427.6
440.0
87
86
85
0.633
0.613
0.594
8667
8656
8645
958.9
957.2
955.6
444.6
457.0
470.3
8719
8708
8697
964.4
962.7
961.0
447.3
459.8
473.1
8772
8761
8750
969.8
968.1
966.4
450.0
462.6
476.0
8824
8813
8802
975.3
973.6
971.9
452.7
465.3
478.8
TEMPERATURE-ENTROPY TABLE.
I2 9
Temperature,
Degrees Fahr.
Pressure, Pounds!
per Square
Inch.
1.80
1.81
1.82
1.83
>.
1
a
5 3
gS
H
*!
|
ll
r
sl
&
I
ll
2
H
||
>*
*/
1 S
o S
s
*o o
132
131
130
2.341
2.280
2.220
9386
9375
9364
1055.2
1053.5
1051.9
140.3
143.6
147.1
9445
9433
9422
1061.1
1059.4
1057.8
141.2
144.5
148.0
9503
9491
9480
1067.0
1065.4
1063.7
142.1
145.4
148.9
9561
9549
9538
1072.9
1071.3
1069.6
142.9
146.3
149.8
129
128
127
2.161
2.103
2.047
9353
9342
9330
1050.3
1048.7
1047.1
150.7
154.3
158.1
9411
9399
9388
1056.2
1054.6
1053.0
151.6
155.3
159.0
9468
9457
9445
1062.1
1060.4
1058.8
152.5
156.2
160.0
9526
9514
9503
1068.0
1066.3
1064.7
153.5
157.2
161.0
126
125
124
1.992
1.938
1.886
9319
9307
9296
1045.4
1043.8
1042.2
162.0
166.0
170.0
9376
9365
9353
1051.3
1049.7
1048.0
163.0
167.0
171.1
9433
9422
9410
1057.1
1055.5
1053.8
164.0
168.0
172.1
9491
9479
9467
1063.0
1061.4
1059.7
164.9
169.0
173.2
123
122
121
1.835
1.785
1.737
9285
9273
9263
1040.6
1038.9
1037.3
174.3
178.7
183.2
9342
9330
9319
1046.4
1044.7
1043.1
175.3
179.8
184.3
9398
9387
9376
1052.2
1050.5
1048.9
176.4
180.9
185.5
9455
9444
9433
1058.1
1056.3
1054.7
177.5
182.0
186.6
120
119
118
1.689
1.642
1.597
9251
9240
9229
1035.7
1034.1
1032.4
187.8
192.6
197.4
9308
9296
9285
1041.5
1039.9
1038.2
188.9
193.7
198.6
9364
9352
9341
1047.2
1045.6
1044.0
190.1
194.9
199.8
9421
9409
9397
1053.0
1051.4
1049.7
191.2
196.1
201.0
117
116
115
1.552
1.509
1.467
9217
9205
9194
1030.8
1029.1
1027.5
202.6
207.8
213.1
9273
9262
9250
1036.5
1034.8
1033.2
203.8
209.0
214.4
9329
9318
9306
1042.3
1040.6
1039.0
205.1
210.3
215.7
9385
9374
9362
1048.0
1046.3
1044.7
206.3
211.6
217.0
114
113
112
1.426
1.386
1.347
9183
9171
9160
1025.8
1024.2
1022.5
218.5
224.1
230.0
9238
9227
9215
1031.5
1029.9
1028.2
219.9
225.5
231.4
9294
9282
9271
1037.3
1035.6
1033.9
221.2
226.9
232.8
9350
9338
9326
1043.0
1040.4
1039.7
222.5
228.2
234.2
111
110
109
1.308
1.271
1.235
9148
9137
9125
1020.9
1019.2
1017.6
236.0
242.3
248.8
9203
9192
9180
1026.6
1024.9
1023.3
237.4
243.8
250.3
9259
9248
9236
1032.3
1030.6
1028.9
238.9
245.2
251.8
9314
9303
9291
1038.0
1036.3
1034.7
240.3
246.7
253.3
108
107
106
1.200
1.165
1.131
9114
9103
9091
1015.9
1014.3
1012.6
255.4
262.3
269.5
9169
9157
9146
1021.6
1019.9
1018.2
256.9
263.9
271.1
9224
9212
9201
1027.2
1025.6
1023.9
258.5
265.5
272.7
9279
9267
9256
1032.9
1031.2
1029.5
260.0
267.1
274.3
105
104
103
1.098
1.066
1.035
9080
9068
9057
1010.9
1009.2
1007.6
276.8
284.3
292.0
9135
9123
9112
1016.5
1014.8
1013.2
278.4
286.0
293.8
9189
9177
9166
1022.2
1020.5
1018.8
280.1
287.7
295.5
9244
9232
9221
1027.8
1026.1
1024.5
281.8
289.4
297.3
102
101
100
1.005
0.975
0.946
9046
9035
9023
1005.9
1004.2
1002.5
300.0
308.2
316.5
9100
9089
9077
1011.5301.8
1009.8310.0
1008.1318.4
9155
9143
9131
1017.1
1015.4
1013.7
303.6
311.9
320.3
9209
9197
9185
1022.8
1021.1
1019.3
305.4
313.7
322.2
99
98
97
0.918
0.891
0.864
9012
9001
8989
1000.9
999.2
997.6
325.2
334.2
343.5
9066
9055
9043
1006.5
1004.8
1003.2
327.2
336.2
345.5
9120
9108
9097
1012.0
1010.3
1008.7
329.1
338.2
347.6
9174
9162
9150
1017.6
1015.9
1014.3
331. T
340.2
349.6
96
95
94
0.838
0.813
0.788
8978
8967
8956
996.0
994. 3
992.6
353.1
363.0
373.2
9032
9020
9009
1001.5
999.8
998.1
355.2
365.1
375.4
9085
9074
9062
1007.1
1005.4
1003.7
357.3
367.3
377.6
9139
9127
9115
1012.6
1010.9
1009.2
359.4
369.5
379.8
93
92
91
0.764
0.741
0.718
8945
8933
8922
990.9
989.2
987.5
383.8
394.8
406.3
8998
8986
8975
996.4
994.7
993.0
386.1
397.2
408.7
9051
9039
9027
1001.9388.4
1000.2)399.5
998.5411.1
9104
9092
9080
1007.5
1005.8
1004.1
390.6
401.9
413.5
90
89
88
0.696
0.675
0.654
8910
8899
8888
985.8
984.1
982.4
418.1
430.2
442.6
8963
8952
8940
991.3
989.6
987.9
420.6
432.7
445.2
9016
9004
8993
996.8
995.1
993.4
423.0
435.3
447.8
9069
9057
9045
1002.3
1000.6
998.8
425.5
437.8
450.4
87
86
85
0.633
0.613
0.594
8877
8865
8854
980.7
979.0
977.3
455.4
468.1
481.6
8929
8918
8906
986.2
984.5
982.8
458.1
470.8
484.5
8982
8970
8958
991.7
990.0
988.2
460.8
473.6
487.3
9034
9022
9010
997.1
995.4
993.7
463.4
476.4
490.2
130
NAPERIAN LOGARITHMS.
e =2.7182818 log e = 0.4342945 = M
1
2
3
4
5
6
7
s
9
1.0
0. 0000
0.0099^
0.0198(
0.0295(
0.03925
1 0. 0487<
0.0582
0.0676(
.0.0769
0.08618
1.1
1.2
1.3
0.09531
0.1823
0.2624
0.1044
0.1906
0.2700
0.1133
0.1988
0.2776
0.1222
0.2070
0.2852
0.1310
0.2151
0.2927
0.1398
0.2231
0.3001
0.1484
0.2311
0.3075
0.1570
0.2390
0.3148
0.1655
0.2469
0.3221
0.1739
0.2546
0. 3293
1.4
1.5
1.6
0.3365
0.4055
0.4700
0.3436
0.4121
0.4762
0.3507
0.4187
0.4824
0.3577
0.4253
0.4886
0.3646
0.4318
0.4947
0.3716
0.4382
0.5008
0.3784
0.4447
0.5068
0.3853
0.4511
0.5128
0.3920
0.4574
0.5188
0.3988
0.4637
0.5247
1.7
1.8
1.9
0.5306
0.5878
0.6418
0.5365
0.5933
0.6471
0.5423
0.5988
0.6523
0.5481
0.6043
0.6575
0.5539
0.6098
0.6627
0-5596
0.6152
0.6678
0.5653
0.6206
0-6729
0.5710
0.6259
0.6780
0. 5766
0.6313
0.6831
0.5822
0.6366
0.6881
2.0
2.1
2.2
2.3
0.6931
0.7419
0.7884
0.8329
0.6981
0.7467
0.7930
0.8372
0.7031
0.7514
0.7975
0.8416
0.7080
0.7561
0.8020
0.8459
0.7129
0.7608
0. 8065
0. 8502
0.7178
0.7655
0.8109
0.8544
0.7227
0.7701
0.8154
0.8587
0.7275
0.7747
0.8198
0.8629
0.7324
0.7793
0.8242
0.8671
0. 7372
0.7839
0.8286
0.8713
2.4
2.5
2.6
0.8755
0.9163
0.9555
0.8796
0.9203
0.9594
0.8838
0.9243
0.9632
0.8879
0.9282
0.9670
0.8920
0.9322
0.9708
0.8961
0.9361
0.9746
0.9002
0.9400
0.9783
0.9042
0.9439
0.9821
0.9083
0.9478
0.9858
0.9123
0.9517
0.9895
2.7
2.8
2.9
0.9933
1.0296
1.0647
0.9969
.0332
.0682
1.0006
1.0367
.0716
1.0043
1.0403
1.0750
1.0080
1.0438
1.0784
1.0116
1.0473
1.0818
1.0152
1:0508
.0852
1.0188
1.0543
1.0886
1.0225
1.0578
1.0919
1.0260
1.0613
1.0953
3.0
1.0986
.1019
.1053
1.1086
1.1119
1.1151
.1184
1.1217
1.1249
1.1282
3.1
3.2
3.3
1.1314
.1632
.1939
.1346
1.1663
1.1969
.1378
1.1694
1.2000
.1410
1.1725
1.2030
.1442
.1756
.2060
1.1474
1.1787
1.2090
.1506
1.1817
1.2119
.1537
.1848
.2149
1.1569
1.1878
1.2179
1.1600
.1909
.2208
3.4
3.5
3.6
.2238
.2528
.2809
1.2267
1.2556
1.2837
1.2296
1.2585
1.2865
1.2326
1.2613
1.2892
.2355
.2641
.2920
.2384
.2669
.2947
1.2413
1.2698
1.2975
.2442
.2726
.3002
1.2470
1.2754
1.3029
.2499
.2782
.3056
3.7
3.8
3.9
.3083
.3350
.3610
1.3110
1.3376
1.3635
1.3137
1.3403
1.3661
1.3164
1.3429
1.3686
.3191
.3455
.3712
.3218
.3481
.3737
1.3244
1.3507
1.3762
.3271
.3533
.3788
1.3297
1.3558
1.3813
.3324
.3584
.3838
4.0
.3863
1.3888
1.3913
1.3938
.3962
.3987
1.4012
.4036
1.4061
.4085
4.1
4.2
4.3
.4110
.4351
.4586
1.4134
1.4375
1.4609
1.4159
1.4398
1.4633
1.4183
1.4422
1.4656
.4207
.4446
.4679
.4231
.4469
.4702
1.4255
1.4493
1.4725
.4279
.4516
.4748
1.4303
1.4540
1.4770
.4327
.4563
.4793
4.4
4.5
4.6
.4816
.5041
.5261
1.4839
1.5063
1.5282
1.4861
1.5085
1.5304
1.4884
1.5107
1.5326
.4907
.5129
.5347
.4929
.5151
.5369
1.4951
1.5173
1.5390
.4974
.5195
.5412
1.4996
1.5217
1.5433
.5019
.5239
.5454
4.7
4.8
4.9
.5476
.5686
.5892
1.5497
1.5707
1.5913
1.5518
1.5728
1.5933
1.5539
1.5748
1.5953
.5560
.5769
.5974
.5581
.5790
.5994
1.5602
1.5810
1.6014
.5623
.5831
.6034
1.5644
1.5851
1.6054
.5665
.5872
.6074
5.0
.6094
[.6114
1.6134
1.6154
.6174
.6194
1.6214
.6233
1.6253
.6273
5.1
5.2
5.3
.6292
.6487
.6677
1.6312
1.6506
1.6696
.6332
.6525
.6715
1.6351
1.6544
1.6734
.6371
.6563
.6752
.6390
.6582
.6771
1.6409
1.6601
1.6790
.6429
.6620
.6808
1.6448
1.6639
1.6827
.6467
.6658
.6845
5.4
5.5
5.6
.6864
.7047
.7228
1.6882
1.7066
1.7246
.6901
.7884
.7263
1.6919
1.7102
1.7281
.6938
.7120
.7299
.6956
.7138
.7317
1.6974
L.7156
L.7334
.6993
.7174
.7352
1.7011
1.7192
L.7370
.7029
.7210
.7387
PROPERTIES OF STEAM AND OTHER VAPORS..
NAPERIAN LOGARITHMS.
1
2.
3
4
5
6
7
8
9
5.7
5.8
5.9
1 . 7405
1.7579
1.7750
1.7422
1.7596
1.7766
1.7440
1.7613
1.7783
1.7457
1.7630
1.7800
1.7475
1.7647
1.7817
1.7492
1.7664
1.7834
1.7509
1.7681
1.7851
1.7527
1,7699
1.7867
1.7544
1.7716
1.7884
1.7561
1.7733
1.7901
6.0
1.7918
1.7934
1.7951
1.7967
1.7984
1.8001
1.8017
1.8034
1.8050
1.8066
6.1
6.2
6.3
1.8083
1.8245
1.8405
1.8099
1.8262
1.8421
1.8116
1.8278
1.8437
1.8132
1.8294
1.8453
1.8148
1.8310
1.8469
1.8165
1.8326
1.8485
1.8181
1.8342
1.8500
1.8197
1.8358
1.8516
1.8213
1.8374
1.8532
1.8229
1.8390
1.8547
6.4
6.5
6.6
1.8563
1.8718
1.8871
1.8579
1.8733
1.8886
1.8594
1.8749
1.8901
1.8610
1.8764
1.8916
1.8625
1.8779
1.8931
1.8641
1.8795
1.8946
1.8656
1.8810
1.8961
1.8672
1.8825
1.8976
1.8687
1.8840
1.8991
1.8703
1.8856
1.9006
6.7
6.8
6.9
1.9021
1.9169
1.9315
1.9036
1.9184
1.9330
1.9051
1.9199
1.9344
1.9066
1.9213
1.9359
1.9081
1.9228
1.9373
1.9095
1.9242
1.9387
1.9110
1.9257
1.9402
1.9125
1.9272
1.9416
1.9140
1.9286
1.9430
1.9155
1.9301
1.9445
7.0
1.9459
1.9473
1.9488
1.9502
1.9516
1.9530
1.9544
1.9559
1.9573
1.9587
7.1
7.2
7.3
1.9601
1.9741
1.9879
1.9615
1.9755
1.9892
1.9629
1.9769
1.9906
1.9643
1.9782
1.9920
1.9657
1.9796
1.9933
1.9671
1.9810
1.9947
1.9685
1.9824
1.9961
1.9699
1.9838
1.9974
1.9713
1.9851
1.9988
1.9727
1.9865
2.0001
7.4
7.5
7.6
2.0015
2.0149
2.0281
2.0028
2.0162
2.0295
2.0042
2.0176
2.0308
2.0055
2.0189
2.0321
2.0069
2.0202
2.0334
2.0082
2.0215
2.0347
2. 0096
2.0229
2.0360
2.0109
2.0242
2.0373
2.0122
2.0255
2.0386
2.0136
2.0268
2.0399
7.7
7.8
7.9
2.0412
2.0541
2.0668
2. 0425
2.0554
2.0681
2.0438
2.0567
2.0694
2.0451
2.0580
2.0707
2.0464
2.0592
2.0719
2.0477
2.0605
2.0732
2. 0490
2.0618
2.0744
2.0503
2.0631
2.0757
2.0516
2.0643
2.0769
2.0528
2.0656
2.0782
8.0
2.0794
2.0807
2.0819
2.0832
2.0844
2.0857
2.0869
2.0881
2.0894
2.0906
8.1
8.2
8.3
2.0919
2.1041
2.1163
2.0931
2.1054
2.1175
2.0943
2. 1066
2.1187
2.0956
2.1078
2.1199
2.0968
2.1090
2.1211
2.0980
2.1102
2.1223
2.0992
2.1114
2.1235
2. 1005
2.1126
2.1247
2.1017
2.1138
2. 1258
2. 1029
2.1150
2.1270
8.4
8.5
8.6
2. 1282
2.1401
2.1518
2.1294
2.1412
2.1529
.1306
.1424
.1541
2.1318
2.1436
2.1552
2.1330
2. 1448
2.1564
2.1342
2.1459
2.1576
2.1353
2.1471
2.1587
2.1365
2.1483
2.1599
2.1377
2. 1494
2.1610
2.1389
2. 1506
2.1622
8.7
8.8
8.9
2.1633
2. 1748
2.1861
2.1645
2.1759
2.1872
.1656
.1770
.1883
2.1668
2.1782
2.1894
2.1679
2.1793
2. 1905
2.1691
2. 1804
2.1917
2.1702
2.1815
2.1928
2.1713
2.1827
2.1939
2.1725
2.1838
2.1950
2.1736
2. 1849
2.1961
9.0
2.1972
2. 1983
.1994
2. 2006
2.2017
2. 2028
2.2039
2. 2050
2.2061
2.2072
9.1
9.2
9.3
2.2083
2.2192
2. 2300
2.2094
2.2203
2.2311
.2105
.2214
.2322
2.2116
2.2225
2.2332
2.2127
2.2235
2.2343
2.2138
2. 2246
2.2354
2.2148
2.2257
2.2364
2.2159
2. 2268
2.2375
2.2170
2.2279
2.2386
2.2181
2. 2289
2.2396
9.4
9.5
9.6
2. 2407
2.25J3
2.2618
2.2418
2.2523
2.2628
.2428
.2534
.2638
2.2439
2.2544
2.2649
2. 2450
2.2555
2.2659
2.2460
2.2565
2.2670
2.2471
2.2576
2. 2680
2.2481
2.2586
2.2690
2.2492
2.2597
2.2701
2. 2502
2. 2607
2.2711
9.7
9.8
9.9
2.2721
2.2824
2.2925
2.2732
2.2834
2.2935
.2742
.2844
2.2946
2.2752
2.2854
2.2956
2.2762
2.2865
2.2966
2.2773
2.2875
2.2976
2.2783
2.2885
2.2986
2. 2793
2.2895
2.2996
2.2803
2.2905
2.3006
2.2814
2.2915
2.3016
10.0
2.3026
132
PROPERTIES OF STEAM AND OTHER VAPORS.
LOGARITHMS.
Nat
Proportional Parts.
IN at.
Nos.
1
2
3
4
5
6
7
8
9
123
456
789
10
0000
0043
0086
0128
0170
0212
0253
0294
0334
0374
4 8 12
17 21 25
29 33 37
11
0414
0453
0492
0531
0569
0607
0645
0682
0719
0755
4 8 11
15 19 23
26 30 34
12
0792
0828
0864
0899
0934
0969
1004
1038
1072
1106
3 7 10
14 17 21
24 28 31
13
1139
1173
1206
1239
1271
1303
1335
1367
1399
1430
3 6 10
13 16 19
23 26 29
14
1461
1492
1523
1553
1584
1614
1644
1673
1703
1732
369
12 15 18
21 24 27
15
1761
1790
1818
1847
1875
1903
1931
1959
1987
2014
368
11 14 17
20 22 25
16
2041
2068
2095
2122
2148
2175
2201
2227
2253
2279
358
11 13 16
18 21 24
17
2304
2330
2355
2380
2405
2430
2455
2480
2504
2529
257
10 12 15
17 20 22
18
2553
2577
2601
2625
2648
2672
2695
2718
2742
2765
257
9 12 14
16 19 21
19
2788
2810
2833
2856
2878
2900
2923
2945
2967
2989
247
9 11 13
16 18 20
20
3010
3032
3054
3075
3096
3118
3139
3160
3181
3201
246
8 11 13
15 17 19
21
3222
3243
3263
3284
3304
3324
3345
3365
3385
3404
246
8 10 12
14 16 18
22
3424
3444
3464
3483
3502
3522
3541
3560
3579
3598
246
8 10 12
14 15 17
23
3617
3636
3655
3674
3692
3711
3729
3747
3766
3784
246
7 9 11
13 15 17
24
3802
3820
3838
3856
3874
3892
3909
3927
3945
3962
245
7 9 11
12 14 16
25
3979
3997
4014
4031
4048
4065
4082
4099
4116
4133
235
7 9 10
12 14 15
26
4150
4166
4183
4200
4216
4232
4249
4265
4281
4298
235
7 8 10
11 13 15
27
4314
4330
4346
4362
4378
4393
4409
4425
4440
4456
235
689
11 13 14
28
4472
4487
4502
4518
4533
4548
4564
4579
4594
4609
235
689
11 12 14
29
4624
4639
4654
4669
4683
4698
4713
4728
4742
4757
1 3 4
679
10 12 13
30
4771
4786
4800
4814
4829
4843
4857
4871
4886
4900
1 3 4
679
10 11 13
31
4914
4928
4942
4955
4969
4983
4997
5011
5024
5038
1 3 4
678
10 11 12
32
5051
5065
5079
5092
5105
5119
5132
5145
5159
5172
1 3 4
578
9 11 12
33
5185
5198
5211
5224
5237
5250
5263
5276
5289
5302
1 3 4
568
9 10 12
'34
5315
5328
5340
5353
5366
5378
5391
5403
5416
5428
1 3 4
568
9 10 11
35
5441
5453
5465
5478
5490
5502
5514
5527
5539
5551
1 2 4
567
9 10 11
36
5563
5575
5587
5599
5611
5623
5635
5647
5658
5670
1 2 4
567
8 10 11
37
5682
5694
5705
5717
5729
5740
5752
5763
5775
5786
1 2 3
567
8 9 10
38
5798
5809
5821
5832
5843
5855
5866
5877
5888
5899
1 2 3
567
8 9 10
39
5911
5922
5933
5944
5955
5966
5977
5988
5999
6010
1 2 3
457
8 9 10
40
6021
6031
6042
6053
6064
6075
6085
6096
6107
6117
1 2 3
456
8 9 10
41
6128
6138
6149
6160
6170
6180
6191
6201
6212
6222
1 2 3
456
789
42
6232
6243
6253
6263
6274
6284
6294
6304
6314
6325
1 2 3
456
789
43
6335
6345
6355
6365
6375
6385
6395
6405
6415
6425
1 2 3
456
789
44
6435
6444
6454
6464
6474
6484
6493
6503
6513
6522
1 2 3
456
789
45
6532
6542
6551
6561
6571
6580
6590
6599
6609
6618
1 2 3
456
789
46
6628
6637
6646
6656
6665
6675
6684
6693
6702
6712
1 2 3
456
778
47
6721
6730
6739
6749
6758
6767
6776
6785
6794
6803
1 2 3
455
678
48
6812
6821
6830
6839
6848
6857
6866
6875
6884
6893
1 2 3
445
678
49
6902
6911
6920
6928
6937
6946
6955
6964
6972
6981
1 2 3
445
678
50
6990
6998
7007
7016
7024
7033
7042
7050
7059
7067
1 2 3
345
678
51
7076
7084
7093
7101
7110
7118
7126
7135
7143
7152
1 2 3
345
678
52
7160
7168
7177
7185
7193
7202
7210
7218
7226
7235
1 2 2
345
6 7 7
53
7243
7251
7259
7267
7275
7284
7292
7300
7308
7316
1 2 2
345
667
54
7324
7332
7340
7348
7356
7364
7372
7380
7388
7396
1 2 2
345
667
PROPERTIES OF STEAM AND OTHER VAPORS.
133
LOGARITHMS.
Proportional Parts.
Nat,
Nos.
1
2
3
4
6
6
7
8
9
123
456
789
55
7404
7412
7419
7427
7435
7443
7451
7459
7466
7474
2 2
345
567
56
57
7482
7559
7490 7497 7505
7566 7574J7582
7513
7589
7520
7597
7528
7604
7536
7612
7543J7551
7619 7627
2 2
2 2
345
345
567
567
58
7634
764217649 7657
7664
7672
7679
7686
769417701
1 2
344
567
59
7709
7716
7723 7731
7738
7745
7752
7760
7767
7774
1 2
344
567
60
7782
7789
77967803
7810
7818
7825
7832
7839
7846
1 2
3 4
566
61
7853
7860:78687875
7882
7889
7896
7903
7910
7917
1 2
3 4
566
62
7924
793179387945
7952 7959
7966
7973
7980 7987
1 2
3 3
566
63
64
7993
8062
8000
8069
8007
8075
8014
8082
8021
8089
8028
8096
8035
8102
8041
8109
8048
8116
8055
8122
1 2
1 2
3 3
3 3
556
556
65
8129
8136
8142
8149
8156
8162
8189
8176
8182
8189
1 2
3 3
556
66
8195
8202
8209
8215
8222
8228
8235
8241
8248
8254
1 2
3 3
556
67
8261
8267
8274
8280
8287
8293
8299
8306
8312
8319
1 2
3 3
556
68
8325
8331
8338
8344
8351
8357
8363
8370
8376
8382
1 2
3 3
456
69
8388
8395
8401
8407
8414
8420
8426
8432
8439
8445
1 2
234
456
70
8451
8457
8463
8470
8476
8482
8488
8494
8500
8506
1 1 2
234
456
71
85 i 3
8519 8525
8531
8537
8543
8549
8555
8561J8567
1 1 2
234
4 5
72
8573
8579 8585
8591
8597
8603 8609
8615
8621 8627
1 2
234
4 5
73
8633
863986458651
8657
8663:8669
8675
8681 8686
1 2
234
4 5
74
8692
8698
8704;8710
8716
8722
8727
8733
8739
8745
1 2
234
4 5
75
8751
8756
8762 8768
8774
8779
8785
8791
8797
8802
1 2
233
455
76
8808
8814 8820 8825
8831
8837 8842
8848
8854
8859
1 2
233
455
77
8865
8871 8876
8882
8887
8893 8899
8904
8910
8915
2
233
445
78
8921
8927
8932
8938
8943
8949
8954
8960
8965
8971
2
233
445
79
8976
8982
8987
8993
8998
9004
9009
9015
9020
9025
2
233
445
80
9031
9036
9042
9047
9053
9058
9063
9069
9074
9079
2
233
445
81
9085
9090
9096
9101
9106
9112
9117
9122
9128
9133
2
233
445
82
9138
9143
9149
9154
9159
9165
9170
9175
9180
9186
2
233
445
83
9191
9196
9201
9206
9212
9217
9222
9227
9232
9238
2
233
445
84
9243
9248
9253
9258
9263
9269
9274
9279
9284
9289
2
233
445
85
9294
9299 9304
9309
9315
9320
9325
9330
9335
9340
2
233
445
86
9345
9350 9355 9360
936593709375
9380
9385
9390
2
233
445
87
9395
9400 9405i9410
9<15'9420 9425
9430
9435
9440
1
223
344
88
9445
9450 ! 9455 9460
946594699474
9479
9484
9489
1
223
344
89
9494
9499
9504
9509
9513
951S
9523
9528
9533
9538
1
223
344
90
9542
9547
9552
9557
9562
9566
9571
9576
9581
9586
1
223
344
91
9590
9595,9600 9605
9609 9614,9619
9624 9628
9633
1
223
344
92
9638
9643 9647|9652
965796619666
967l'9675
9680
1
223
344
93
9685
9689 9694 9699
97039708
9713
97179722
9727
1
223
344
94 9731
9736
9741 9745
97509754
9759
9763
9768
9773
1
223
344
1
95
9777
9782
9786
9791
9795:9800
9805
9809
9814
9818
1
223
344
96
9823
9827
9832 9836
984119845
9850
9854
9859
9863
1
223
344
97
9868
9872 9877 9881
98869890
9894
9899
9903
9908
1
223
344
98
9912
9917 9921 9926
9930 9934 9939
9943
9948
9952
1
223
344
99
9956
9961
9965
9969
9974
9978 9983
9987
9991
9996
1
223
334
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BRIDGES AND ROOFS.
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Howe's Design of Simple Roof- trusses in Wood and Steel 8vo. 2 00
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HYDRAULICS.
Barnes's Ice Formation 8vo, 3 00
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Treatise on Masonry Construction 8vo, 5 00
Black's United States Public Works Oblong 4to, 5 00
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Church's Mechanics of Engineering 8vo, 6 00
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* Eckel's Cements, Limes, and Plasters 8vo, 6 00
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Fowler's Ordinary Foundations 8vo, 3 50
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Holley and Ladd's Analysis of Mixed Paints, Color Pigments and Varnishes.
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Johnson's (J. B.) Materials of Construction Large 8vo, 6 00
Keep's Cast Iron 8vo, 2 50
Lanza's Applied Mechanics 8vo, 7 50
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Martens's Handbook on Testing Materials. (Henning.) 2 vols 8vo, 7 50
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Metcalf's Steel. A Manual for Steel-users 12mo, 2 00
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Smith's Strength of Material 12mo,
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Spalding's Hydraulic Cement 12mo, 2 00
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Taylor and Thompson's Treatise on Concrete, Plain and Reinforced 8vo, 5 00
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Tillson's Street Pavements and Paving Materials 8vo, 4 00
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Waterbury's Cement Laboratory Manual 12mo, 1 00
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RAILWAY ENGINEERING.
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Butts's Civil Engineer's Field-book 16mo, mor. 2 50
Crandall's Railway and Other Earthwork Tables 8vo, 1 50
Transition Curve 16mo, mor. 1 50
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Dredge's History of the Pennsylvania Railroad. (1879) Papei 5 00
Fisher's Table of Cubic Yards Cardboard, 25
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Hudson's Tables for Calculating the Cubic Contents of Excavations and Em-
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Molitor and Beard's Manual for Resident Engineers 16mo, 1 00
Nagle's Field Manual for Railroad Engineers 16mo, mor. 3 00
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Philbrick's Field Manual for Engineers Itimo, mor. 3 00
Raymond's Railroad Engineering. 3 volumes.
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9
DRAWING.
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* " Abridged Ed 8vo, 150
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Durley's Kinematics of Machines 8vo, 4 00
Emch's Introduction to Protective Geometry and its Application 8vo, 2 50
French and Ives' Stereotomy 8vo, 2 50
Hill's Text-book on Shades and Shadows, and Perspective 8vo, 2 00
Jamison's Advanced Mechanical Drawing 8vo, 2 00
Elements of Mechanical Drawing 8vo, 2 50
Jones's Machine Design:
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Kimball and Barr's Machine Design. (In Press.)
MacCord's Elements of Descritpive Geometry .8vo, 3 00
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Moyer's Descriptive Geometry 8vo, 2 00
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Reid's Course in Mechanical Drawing 8vo, 2 00
Text-book of Mechanical Drawing and Elementary Machine Design.. 8vo, 3 00
Robinson's Principles of Mechanism 8vo, 3 00
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Smith (A. W.) and Marx's Machine Design 8vo, 3 00
Smith's (R. S.) Manual of Topographical Drawing. (McMillan) 8vo, 2 50
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Elements of Descriptive Geometry, Shadows, and Perspective 8vo, 3 50
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Wilson's (H. M.) Topographic Surveying 8vo, 3 50
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ELECTRICITY AND PHYSICS.
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Andrews's Hand-book for Street Railway Engineering 3X5 inches, mor. 1 25
Anthony and Brackett's Text-book of Physics. (Magie.) ... .Large 12mo, 3 00
Anthony and Ball's Lecture-notes on the Theory of Electrical Measure-
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Benjamin's History of Electricity 8vo, 3 00
Voltaic Cell 8vo, 3 00
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Dawson's "Engineering" and Electric Traction Pocket-book. . . .16mo, mor. 5 00
Dolezalek's Theory of the Lead Accumulator (Storage Battery), (von Ende.)
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Duhem's Thermodynamics and Chemistry. (Burgess.) 8vo, 4 00
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Getman's Introduction to Physical Science 12mo,
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Landauer's Spectrum Analysis. (Tingle.) 8vo, 3 00
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Morgan's Outline of the Theory of Solution and its Results 12mo, 1 00
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Norris and Dennison's Course of Problems on the Electrical Characteristics of
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* Parshall and Hobart's Electric Machine Design 4to, half mor, 12 50
Reagan's Locomotives: Simple, Compound, and Electric. New Edition.
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Ryan, Norris, and Hoxie's Electrical Machinery. Vol. 1 8vo, 2 50
Schapper's Laboratory Guide for Students in Physical Chemistry 12mo, 1 00
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LAW.
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MATHEMATICS.
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Byerley's Harmonic Functions 8vo, $1 00
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12
MECHANICAL ENGINEERING.
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13
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14
Kneass's Practice and Theory of the Injector 8vo, $1 50
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MECHANICS PURE AND APPLIED.
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15
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METALLURGY.
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16
MINERALOGY.
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Groth's Introduction to Chemical Crystallography (Marshall) 12mo, 1 25
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Iddings's Igneous Rocks 8vo, 5 00
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MINING.
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SANITARY SCIENCE.
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