key: cord-0868357-izacsial
authors: Duy Nguyen, Bao Tran; Nguyen Thi, Hai Yen; Nguyen Thi, Bich Phuong; Kang, Dong-Ku; Kim, Jeong F.
title: The Roles of Membrane Technology in Artificial Organs: Current Challenges and Perspectives
date: 2021-03-28
journal: Membranes (Basel)
DOI: 10.3390/membranes11040239
sha: c0fbec7f83f8e19848a1226d30a169d7be85bff5
doc_id: 868357
cord_uid: izacsial

The recent outbreak of the COVID-19 pandemic in 2020 reasserted the necessity of artificial lung membrane technology to treat patients with acute lung failure. In addition, the aging world population inevitably leads to higher demand for better artificial organ (AO) devices. Membrane technology is the central component in many of the AO devices including lung, kidney, liver and pancreas. Although AO technology has improved significantly in the past few decades, the quality of life of organ failure patients is still poor and the technology must be improved further. Most of the current AO literature focuses on the treatment and the clinical use of AO, while the research on the membrane development aspect of AO is relatively scarce. One of the speculated reasons is the wide interdisciplinary spectrum of AO technology, ranging from biotechnology to polymer chemistry and process engineering. In this review, in order to facilitate the membrane aspects of the AO research, the roles of membrane technology in the AO devices, along with the current challenges, are summarized. This review shows that there is a clear need for better membranes in terms of biocompatibility, permselectivity, module design, and process configuration.

Every living organism strives to maintain homeostasis with the surrounding environments. The cells, tissues, and organs of a living organism control its internal environments to maintain safe concentration ranges in order to maintain life. In cases of unexpected tissue damage or organ failures, cells have an extraordinary ability to repair themselves and to regain homeostasis. However, some acute and chronic damages can be irreversible, leading to life-threatening failures that require medical intervention and treatment.

The median age of the world population has increased steadily ( Figure 1 ). Such an aging population inevitably leads to higher chances of organ failures, and the best available treatment for such patients now is organ transplantation. However, as shown in Figure 1 , the gap between the number of organ donors and the number of patients has expanded steadily and is only expected to get wider. In addition, although the stem-cell-derived treatment could be a promising option in the future [1] [2] [3] [4] , it has not been fully developed yet. Hence, currently, the optimal solution for organ failure patients in the short-term is artificial organ (AO) technology, until the patient recovers (i.e., bridge-to-recovery) or until the patient receives an organ transplant (i.e., bridge-to-transplantation).

The advancements in AO technology are truly astonishing, and they are increasingly becoming important, even necessary, in the modern medical treatments. Nowadays, AO technology can partly augment the functions of the human organs by maintaining physiochemical gradients in the safe range. Many of these AOs employ synthetic polymeric Figure 1 . Number of people receiving transplants, waiting for transplants, and donors in the US (data obtained from [5] ), plotted together with the statistic of the World Median Age (data obtained from [6] ).

The advancements in AO technology are truly astonishing, and they are increasingly becoming important, even necessary, in the modern medical treatments. Nowadays, AO technology can partly augment the functions of the human organs by maintaining physiochemical gradients in the safe range. Many of these AOs employ synthetic polymeric membranes to assist the physical and chemical functions of the failed organs. Particularly, AOs that employ membrane technology includes artificial lung, kidney, liver, and pancreas.

Membrane technology has also made incredible strides in the past few decades. Notably, water purification and desalination membranes have reached the state-of-the-art, dominating more than half of the desalination market [7] . Ion exchange membranes such as Nafion have become a main component for fuel cell technology. Moreover, gas separation membranes are now a key player in many fields including CO2 capture and hydrogen purification [8] . As a separate front, membranes for the healthcare and biomedical markets, which are the main topic of this review, have steadily increased their market share [9] .

The market size of the artificial kidney (e.g., hemodialysis) reached USD 74 billion in 2019 [10] . As for the artificial lung market, also commonly known as ECMO (extracorporeal membrane oxygenator), is expected to grow up to USD 305 million by 2021 [11] . However, this forecast may have changed with the recent outbreak of COVID-19 in 2020, as ECMO is one of the key treatments for severe COVID-19 patients. The artificial liver and pancreas markets are still relatively small because the technology is not mature enough and is as yet without firm clinical effectiveness data.

Surprisingly, despite the considerable market size of the healthcare industries, the literature on membrane research in such fields is relatively scarce compared to other applications such as water and gas separation membranes. In fact, there is a large amount of literature that reports the use of AO for clinical research, but not as many that actually develop AO membranes. One of the reasons may be that AO research requires interdisciplinary knowledge and there exists a wide gap between the membrane field and biomedical technology. Membrane researchers are primarily from the nonbiomedical disciplines, and vice versa. [5] ), plotted together with the statistic of the World Median Age (data obtained from [6] ).

Membrane technology has also made incredible strides in the past few decades. Notably, water purification and desalination membranes have reached the state-of-the-art, dominating more than half of the desalination market [7] . Ion exchange membranes such as Nafion have become a main component for fuel cell technology. Moreover, gas separation membranes are now a key player in many fields including CO 2 capture and hydrogen purification [8] . As a separate front, membranes for the healthcare and biomedical markets, which are the main topic of this review, have steadily increased their market share [9] .

The market size of the artificial kidney (e.g., hemodialysis) reached USD 74 billion in 2019 [10] . As for the artificial lung market, also commonly known as ECMO (extracorporeal membrane oxygenator), is expected to grow up to USD 305 million by 2021 [11] . However, this forecast may have changed with the recent outbreak of COVID-19 in 2020, as ECMO is one of the key treatments for severe COVID-19 patients. The artificial liver and pancreas markets are still relatively small because the technology is not mature enough and is as yet without firm clinical effectiveness data.

Surprisingly, despite the considerable market size of the healthcare industries, the literature on membrane research in such fields is relatively scarce compared to other applications such as water and gas separation membranes. In fact, there is a large amount of literature that reports the use of AO for clinical research, but not as many that actually develop AO membranes. One of the reasons may be that AO research requires interdisciplinary knowledge and there exists a wide gap between the membrane field and biomedical technology. Membrane researchers are primarily from the nonbiomedical disciplines, and vice versa.

Although the artificial kidney technology can be considered as mature clinically, other types of membrane-based AOs, such as artificial lung, liver, and pancreas, still suffer from many technical challenges that must be resolved urgently. Needless to say, such challenges are very complex, requiring interdisciplinary collaboration across the fields of chemistry, biology, materials, and engineering. In addition, the quality of life of organ failure patients, albeit improved, is still poor. The AO technology must continuously improve not only from the membrane perspective, but also from the biocompatibility fronts to improve the quality of life and well-being of the patients.

Hence, in this review, in an attempt to narrow the gap between the membrane research and biomedical fields, the current status and challenges of membrane technology applied to artificial organs were compiled. More specifically, this review was written from a membrane researcher perspective, in order to aid and to facilitate future research on better membrane materials and module design.

It is very important to clearly distinguish the key roles of an organ. Most organs are multifunctional and they perform physical, chemical and biological roles simultaneously with incredible precision. Generally, the physical roles of an organ can be partly or fully augmented with membrane technology; however, currently, the chemical and biological roles cannot be replaced in most cases.

The lungs are part of the respiratory system, and their main function is to oxygenate the bloodstream while removing carbon dioxide in tandem. Hence, the lungs can roughly be considered as a gas exchange membrane, and the physical functions of the lungs can be partly augmented using membrane technology. Similar to the lung alveoli, a membrane can provide an interface between the air (oxygen) and the blood to facilitate the exchange of gases (Figure 2a ). other types of membrane-based AOs, such as artificial lung, liver, and pancreas, still suffer from many technical challenges that must be resolved urgently. Needless to say, such challenges are very complex, requiring interdisciplinary collaboration across the fields of chemistry, biology, materials, and engineering. In addition, the quality of life of organ failure patients, albeit improved, is still poor. The AO technology must continuously improve not only from the membrane perspective, but also from the biocompatibility fronts to improve the quality of life and well-being of the patients.

Hence, in this review, in an attempt to narrow the gap between the membrane research and biomedical fields, the current status and challenges of membrane technology applied to artificial organs were compiled. More specifically, this review was written from a membrane researcher perspective, in order to aid and to facilitate future research on better membrane materials and module design.

It is very important to clearly distinguish the key roles of an organ. Most organs are multifunctional and they perform physical, chemical and biological roles simultaneously with incredible precision. Generally, the physical roles of an organ can be partly or fully augmented with membrane technology; however, currently, the chemical and biological roles cannot be replaced in most cases.

The lungs are part of the respiratory system, and their main function is to oxygenate the bloodstream while removing carbon dioxide in tandem. Hence, the lungs can roughly be considered as a gas exchange membrane, and the physical functions of the lungs can be partly augmented using membrane technology. Similar to the lung alveoli, a membrane can provide an interface between the air (oxygen) and the blood to facilitate the exchange of gases (Figure 2a ). One of the iconic artificial lung devices was the bubble oxygenator proposed by De Wall and Lillehei in 1955 [12, 13] . However, bubble oxygenators led to unwanted hemolysis (i.e., lysis or breakage of red blood cells) and air embolism, which was overcome with the use of membranes. Continuous improvements in the membrane permeance performance reduced the required surface area dramatically from 25 m 2 of multilayer flat sheet One of the iconic artificial lung devices was the bubble oxygenator proposed by De Wall and Lillehei in 1955 [12, 13] . However, bubble oxygenators led to unwanted hemolysis (i.e., lysis or breakage of red blood cells) and air embolism, which was overcome with the use of membranes. Continuous improvements in the membrane permeance performance reduced the required surface area dramatically from 25 m 2 of multilayer flat sheet membranes [14] down to about 2 m 2 in the form of hollow fiber membranes [15, 16] . Currently, the bottleneck is not caused by the membrane gas transport performance, but the blood side mass transfer resistance limits the blood oxygenation efficiency (discussed in detail below).

The artificial lung technology can be roughly split into two categories: a short-term and a long-term respiratory support. The short-term supports include open-heart bypass surgery, of which about 1.5 million cases are performed annually [9] . The venous blood from the patient is circulated extracorporeally (i.e., outside the body) using a heart-lung machine, also known as the cardiopulmonary bypass system (CPB). The blood gets oxy-genated inside a membrane module (i.e., oxygenator) then returns to the patient. The operation lasts about six hours, and the purpose of the CPB is to temporarily augment both the heart and lung functions.

The long-term respiratory support is carried out using the extracorporeal membrane oxygenation (ECMO) system. This treatment is reserved for severe lung failure patients, due to either aging, chronic lung diseases, or acute virus infection (e.g., MERS and COVID-19) [17] , where mechanical ventilator treatment cannot supply the necessary oxygen demand. The components of an ECMO are similar to those of a CPB, but the term ECMO is generally reserved for long-term respiratory treatment (days to weeks). The main purpose of the ECMO system is to provide support until the body naturally recovers (bridge-torecovery) [18] . Its clinical efficiency has been proved many times, as it can increase the survival rate of the patients by up to 75% relative to conventional treatment [17, [19] [20] [21] [22] [23] [24] [25] [26] [27] [28] [29] . The O 2 /CO 2 exchange rate of an average adult human lung is in the range of 200-250 mL/min (at rest) to 6 L/min (active work-out) [30] .

The exchange of gases between atmosphere and blood follows series of steps. The atmospheric oxygen is first inhaled into the lung, which then diffuses through the alveolus wall into the blood (Figure 3a ). The oxygen then dissolves into the blood plasma, and is subsequently taken up by red blood cells. The dissolved oxygen inside red blood cells then binds to the hemoglobin proteins. The oxygenated blood is then carried around the body to aid cell aerobic metabolism. On the other hand, CO 2 gas follows the opposite path (Figure 3b ), except that most of the CO 2 is carried by blood as carbonate and bicarbonate ions, not bound to the hemoglobin proteins (only about 5%).

The key difference between the two gases is the solubility (Figure 3b ). The oxygen is only sparingly soluble in blood plasma (Henry's constant of 0.0031 mL/mmHg O 2 /dL of blood), necessitating an oxygen carrier protein known as hemoglobin. The amount of dissolved O 2 in plasma is commonly expressed in partial pressure unit. Assuming equilibrium, the partial pressure of oxygen can be conveniently correlated with the blood saturation level by the Hill equation [31, 32] Hb saturation (%) = 100

where x (mmHg) is the partial pressure of O 2; and K and ∝ are the parameter values (K = 0.01455 and ∝ = 1.405) [31] . Hence, by measuring the oxygen concentration in blood plasma, the hemoglobin saturation percentage of the blood can be estimated [33] . The minimal metabolic O 2 requirement of an adult is about 11 mmol/min, and approximately 9 mmol/min of CO 2 must be removed from the body [34] . Hence, the CO 2 /O 2 exchange ratio needs to be about 0.8, and the artificial lung performance must be carefully tuned to meet this exchange ratio to avoid unwanted hyper-or hypocapnia [34] . The maximum driving force attainable in normal physiological condition and in membrane module is graphically illustrated in The key difference between the two gases is the solubility (Figure 3b ). The oxygen is only sparingly soluble in blood plasma (Henry's constant of 0.0031 mL/mmHg O2/dL of blood), necessitating an oxygen carrier protein known as hemoglobin. The amount of dissolved O2 in plasma is commonly expressed in partial pressure unit. Assuming equilibrium, the partial pressure of oxygen can be conveniently correlated with the blood saturation level by the Hill equation [31, 32] Hb saturation (%) = 100

(mmHg) is the partial pressure of O2; and and ∝ are the parameter values ( = 0.01455 and ∝ = 1.405) [31] .

Hence, by measuring the oxygen concentration in blood plasma, the hemoglobin saturation percentage of the blood can be estimated [33] . The minimal metabolic O2 requirement of an adult is about 11 mmol/min, and approximately 9 mmol/min of CO2 must be removed from the body [34] . Hence, the CO2/O2 exchange ratio needs to be about 0.8, and the artificial lung performance must be carefully tuned to meet this exchange ratio to avoid unwanted hyper-or hypocapnia [34] . The maximum driving force attainable in normal physiological condition and in membrane module is graphically illustrated in Figure  4 . Compared to the alveoli conditions, the blood is exposed to steeper partial pressure gradients of O2 and CO2 in oxygenator membranes (Figure 4b ). The deoxygenated blood enters the membrane with the partial pressures of O2 and CO2 at 40 and 46 mmHg, respectively. The feed gas flows through the bore side of the oxygenator membrane, and CO2/O2 exchange occurs at the membrane-blood interface. The oxygenated bloodstream exits the Compared to the alveoli conditions, the blood is exposed to steeper partial pressure gradients of O 2 and CO 2 in oxygenator membranes (Figure 4b ). The deoxygenated blood enters the membrane with the partial pressures of O 2 and CO 2 at 40 and 46 mmHg, respectively. The feed gas flows through the bore side of the oxygenator membrane, and CO 2 /O 2 exchange occurs at the membrane-blood interface. The oxygenated bloodstream exits the membrane with the partial pressures of 100-150 mmHg for O 2 and 30-40 mmHg for CO 2 [34] . It is important to note here that the driving force for CO 2 exchange is lower than that of O 2 . Hence, the gas flowrate must be sufficiently high to meet the CO 2 removal requirement and to satisfy the CO 2 /O 2 exchange ratio of 0.8. It will be stressed several times in this review that the membrane permeance is not the bottleneck in the current artificial lung technology. Instead, fixing the exchange ratio to 0.8 is more of an engineering aspect of controlling the driving force for gas exchange. A comparison of the key parameters of human lungs and current oxygenator membranes is summarized in Table 1 . [35] Similar to the lung physiology, the blood oxygenator system also consists of three phases: gas phase, membrane phase and blood phase. The most important parameter is the oxygen transfer rate, N (mol s −1 ) within the membrane oxygenator. The total oxygen transfer rate can be calculated by measuring the oxygen partial pressures of inlet and outlet bloodstreams (using a blood gas analyzer device). It can also be represented from the membrane perspective using the overall mass transfer coefficient, K (mol m −2 s −1 Pa −1 ), as follows:

where A (m 2 ) is the effective membrane surface area, ∆P LM (Pa) is the logarithmic mean difference of oxygen partial pressures. The oxygen transfer rate, N, is directly proportional to the mass transfer coefficient, and by definition, inversely proportional to the sum of resistances within the membrane oxygenator. The total mass transport resistance R total contains three main resistances: gas phase resistance, membrane phase resistance, and blood phase resistance.

The total mass transport resistance R total can also be written as:

where = 1 K ; G, M and B are gas, membrane and blood phases, respectively. δ (m) is the membrane thickness, and B (mol m m −2 s −1 Pa −1 ) is the permeability of the membrane.

The gas transfer rate of the oxygenation device can be improved by reducing these three mass transport resistances ( Figure 5 ). Among the resistances, the gas phase boundary layer resistance is negligible [9, 34, 36] . On the other hand, the blood phase boundary layer resistance can be as high as 100 times larger than the membrane resistance [9] . Hence, for current hollow fiber modules, the total mass transfer coefficient of the device K can simply be approximated to the mass transfer coefficient of the blood boundary layer K B [36] .

oxygenator. The total mass transport resistance contains three main resistances: gas phase resistance, membrane phase resistance, and blood phase resistance.

(3)

The total mass transport resistance can also be written as:

where = ; G, M and B are gas, membrane and blood phases, respectively. (m) is the membrane thickness, and (mol m m -2 s -1 Pa -1 ) is the permeability of the membrane. The gas transfer rate of the oxygenation device can be improved by reducing these three mass transport resistances ( Figure 5 ). Among the resistances, the gas phase boundary layer resistance is negligible [9, 34, 36] . On the other hand, the blood phase boundary layer resistance can be as high as 100 times larger than the membrane resistance [9] . Hence, for current hollow fiber modules, the total mass transfer coefficient of the device can simply be approximated to the mass transfer coefficient of the blood boundary layer [36] .

The above analysis clearly shows that the focus must be given to lower the blood phase resistance, by providing better mixing for the bloodstream. Although higher velocity can give better mixing, it is also important to consider the pressure drop along the oxygenator, as high shear stress can cause blood trauma, which leads to unwanted hemolysis. There is a tradeoff between gas transfer rate and blood trauma. Many studies have also been carried out to optimize oxygenator geometries that give more complex flow patterns [36] [37] [38] [39] [40] , as shown in Figure 6 . The above analysis clearly shows that the focus must be given to lower the blood phase resistance, by providing better mixing for the bloodstream. Although higher velocity can give better mixing, it is also important to consider the pressure drop along the oxygenator, as high shear stress can cause blood trauma, which leads to unwanted hemolysis. There is a tradeoff between gas transfer rate and blood trauma. Many studies have also been carried out to optimize oxygenator geometries that give more complex flow patterns [36] [37] [38] [39] [40] , as shown in Figure 6 .

The mass transfer performance can be analyzed and cross-compared using the Sherwood number (Sh)-a dimensionless parameter as a function of the Reynold number (Re) and the Schmidt number (Sc). The Sherwood number for hollow fiber membrane module can be expressed as follows [36] :

The Sherwood number can be also written as:

where k B,L (m s −1 ) is the mass transfer coefficient which depends on the oxygen concentration in liquid (k B,L = Hk B ); d 0 (m) is the outer diameter of hollow fiber membrane, u 0 (m s −1 ) is the superficial velocity of blood, v (m 2 s −1 ) is the kinematic viscosity, and D B (m 2 s −1 ) is the diffusion coefficient of oxygen in blood. Moreover, the Sherwood number for blood flowing in a thin channel, such as a microfluidic device, can be expressed as follows:

where Gz is the Graetz number, a dimensionless number represents for the laminar flow in a conduit, d h (m) is the hydraulic diameter, and L (m) is the length of fiber. The Sherwood numberdepends on the number of hollow fiber in a bundle or the fiber orientation in the device ( Table 2) . The mass transfer performance can be analyzed and cross-compared using the Sherwood number (Sh)-a dimensionless parameter as a function of the Reynold number (Re) and the Schmidt number (Sc). The Sherwood number for hollow fiber membrane module can be expressed as follows [36] :

The Sherwood number can be also written as:

where , (m s -1 ) is the mass transfer coefficient which depends on the oxygen concentration in liquid ( , = ); (m) is the outer diameter of hollow fiber membrane, (m s -1 ) is the superficial velocity of blood, (m 2 s -1 ) is the kinematic viscosity, and (m 2 s -1 ) is the diffusion coefficient of oxygen in blood.

Moreover, the Sherwood number for blood flowing in a thin channel, such as a microfluidic device, can be expressed as follows: Many experiments on various configurations have been conducted to obtain reliable Sherwood correlations. Generally, the gas transfer rate is better for the transverse flow compared to the parallel flow configuration. More recently, a generalized model for both the transverse and parallel flow for the oxygenators was reported to predict the oxygenation performance [37] , as summarized in Table 3 . The authors showed that the oxygenator void fraction of hollow fiber bundles (ε f ) affects the mass transfer coefficient in several ways. For example, when ε f is between 0.3 to 0.5, the mass transfer coefficient of the square fiber arrangement with perpendicular flow is better than the staggered arrangement. However, for the parallel flow, the behavior tends to be the opposite [37] . [36] PP /Hollow fibers Across a perpendicular hollow fibers Sh = 0.14 Re 0.9 Sc 0.33 [36] PMP /Hollow fibers Across a parallel hollow fibers Sh = 0.39 Re 0.76 Sc 0.33 [40] Table 3 . Generalized mass transfer correlations with parallel and transverse flow for hollow fiber blood oxygenator in square or staggered arrangement (with ε f is the void fraction of the bundle of hollow fibers) (equations obtained from [37] ).

Parallel flow

Currently, the two main polymers used for artificial lung membranes are polypropylene (PP) and poly-4-methylpentene (PMP). The first generation artificial lung is a PP-based microporous membrane with hydrophobic characteristics. These membranes are highly porous with excellent gas permeance but have a short lifetime of about six hours [41, 42] , after which the membrane gets wet. They are mostly fabricated via the melt-extrusionstretching method, which gives an average pore size between 0.05 to 0.1 µm. Another widely employed fabrication method is the TIPS process (i.e., thermally induced phase separation, which gives narrower pore size distribution [43] .

As the PP membrane is intrinsically hydrophobic, the blood only contacts the surface of the membrane to facilitate the gas exchange; hence, the blood does not (and should not) leak through the membrane [41] . This type of membrane process is also commonly known as the membrane contactor process. For the open-heart surgery application, the microporous membranes are reliable. However, in long-term treatment, the plasma proteins adsorb onto the membrane surface, which increases the surface energy of the membrane material, eventually allowing unwanted membrane wetting and allowing the blood plasma to break through [41, 44, 45] .

In the early 2000s, the second generation artificial lung membrane was developed based on the PMP material with a remarkably longer lifetime (last 2-4 weeks) [46] [47] [48] . Compared to the porous PP membrane, PMP membranes have a thin dense layer that can effectively prevent the plasma leakage [46, 48] . As PMP is generally insoluble in organic solvents, these membranes are also prepared via melt-extrusion or TIPS method. From the membrane technology perspective, the formation of such skin layer with TIPS is interesting, as the thin skin layer of a semicrystalline polymer can only be formed via combination of NIPS (nonsolvent-induced phase separation) and TIPS technique, so called N-TIPS method [43, 49] .

Expectedly, the presence of a thin dense layer significantly reduces the gas permeance. Compared to the porous PP membrane, where gas molecules can freely permeate through, PMP membranes with a dense skin layer exhibit two orders of magnitude lower gas permeance as the gas molecules must diffuse through the dense PMP material. [45] . Nevertheless, compared to other polymeric materials, PMP has high intrinsic gas permeability, as summarized in Table 4 . It is important to clearly distinguish the term membrane gas permeance from material intrinsic gas permeability. The gas permeance is typically in the unit of GPU (gas permeation unit) and it represents the performance of a membrane. On the other hand, the gas permeability is in the unit of barrer, and it characterizes the intrinsic gas permeability of a dense material.

Additionally, as discussed previously, the membrane permeance is not the bottleneck in the process of blood oxygenation. Hence, even with such low permeance, the blood oxygenation efficiency is not compromised. PMP also exhibit good hydrophobicity, preventing the unwanted wetting of the membrane by the blood plasma. Due to these advantages, PMP membranes can be applied to long-term treatment including ECMO, continuously for more than 42 days [39, 40] .

More recently, third generation artificial lung membranes have been proposed using fluoropolymers [50] . The characteristic low surface energy of fluoropolymers prevents unwanted protein adsorption onto the membrane surface, potentially improving the longterm hemocompatibility of artificial lung membranes. Among the known fluoropolymers, polytetrafluoroethylene (PTFE), also known by its tradename Teflon, exhibits outstanding characteristics such as low surface energy, chemical stability, mechanical rigidity, and high biocompatibility. However, it is technically difficult to process PTFE polymer into a thin, hollow fiber shape due to its high melt viscosity. Kim et al. [50] have shown that other fluoropolymers with better processability, such as PVDF and P(VDF-co-HFP), can be processed into membranes with target pore size.

Apart from these options, many possible possibilities exist in the realm of fluoropolymers, yet to be explored for artificial lung membranes.

It has been clinically proven that the artificial lung treatment can increase the survival rate of lung failure patients [54] . Despite such improvements, many challenges remain to further improve the survival rate and quality of life of the patients. Future membrane research must focus on three fronts: (1) better hemocompatibility, (2) better module design with lower prime volume, and (3) smaller and more portable systems.

Blood Compatibility (Hemocompatibility)

The concept of blood compatibility, or hemocompatibility, has been one of the most daunting challenges in the field of biomaterial research. In spite of 50 years of intensive research, biomaterial researchers even coined the term "blood compatibility catastrophe" [55] to show that there is no consensus as to which materials are even "blood compatible." The term biocompatibility is a broader concept that includes hemocompatibility, and these two terms are often used interchangeably in the blood-contacting materials literature.

Inside an artificial lung membrane module, the blood comes in contact with the membrane (among other parts), and the proteins inside the blood, such as albumin, fibrinogen, fibronectin, and many others, immediately bind to the surface. As illustrated in Figure 7 , the initial adsorption step sets off cascades of complex immune response and blood clot formation (e.g., thrombosis) processes [18, [56] [57] [58] . Hence, the protein-material interaction is an important indicator of hemocompatibility.

The key issues in artificial lung membranes are the formation of blood clots and inflammatory response. These mechanisms, although vital for our survival, can cause a variety of adverse issues during clinical treatments. Particularly, blood clots can block the blood pathway and dramatically lower the oxygenation efficiency. Current state-of-the-art artificial lung membranes can last for a few weeks before blood clots (thrombosis) adversely affect patients [59] [60] [61] . As the protein adsorption is the first step that initiates both the blood coagulation pathway and the inflammatory response [63] , many works have focused on minimizing the protein adsorption onto blood-contacting devices [50, [64] [65] [66] [67] . Generally, proteins bind to a surface via hydrophobic interaction, and hence the hydrophilic modification of a surface effectively lowers the protein adsorption, which in turn improves the hemocompati- As the protein adsorption is the first step that initiates both the blood coagulation pathway and the inflammatory response [63] , many works have focused on minimizing the protein adsorption onto blood-contacting devices [50, [64] [65] [66] [67] . Generally, proteins bind to a surface via hydrophobic interaction, and hence the hydrophilic modification of a surface effectively lowers the protein adsorption, which in turn improves the hemocompatibility [62] . However, artificial lung membranes require hydrophobic properties to avoid pore wetting and plasma breakthrough. This is precisely the reason why the current artificial lung membranes are mostly based on hydrophobic materials such as PP and PMP.

Another strategy to prevent the protein adsorption, particularly for artificial lung membranes, is to minimize the surface energy. It has been shown that the amount of protein adsorption is inversely proportional to the membrane surface energy [50] . Figure 8 clearly shows that a fluorinated surface, although hydrophobic, can effectively prevent protein adsorption and potentially improve the hemocompatibility. Hence, fluorinated polymers could be a promising alternative to the current PP and PMP materials. Protein adsorption can be further inhibited with super liquid-repellent surfaces, also known as superamphiphobic surfaces [50, [67] [68] [69] [70] . The superarmphiphobic surface can only be realized with appropriate surface roughness modification and surface energy modification. The first step is to implement the right roughness with nanostructures in order to create the capillary force at the blood-surface interface [71] [72] [73] . The nanostructure creates an air gap between the liquid and the surface of the material, transforming the surface from the Wenzel state to the Cassie-Baxter state [71, [74] [75] [76] [77] [78] [79] [80] (Figure 9 ). There are many ways to fabricate nanostructures, such as spray particle coating [57, [81] [82] [83] or etching methods (plasma, laser, chemical, and electrochemical etching) [71, 78, [84] [85] [86] [87] [88] [89] [90] [91] .

To realize a superamphiphobic surface, the surface energy must also be minimized in tandem, typically using fluorochemicals. The most commonly used ones are fluorocarbon-based compounds, (-CF2-)n, where n is between 4 and 10. These perfluorochemicals exhibit extremely low surface energy but can be toxic to the environment and health [92] , and cannot be applied for healthcare materials. Alternative perfluorochemicals are being sought which are safer but with similar low surface energy characteristics [92] . The lowest surface energy reported is 9.3 mN/m using fluorinated polyhedral oligomeric silsesquioxanes (POSS) [93] . Protein adsorption can be further inhibited with super liquid-repellent surfaces, also known as superamphiphobic surfaces [50, [67] [68] [69] [70] . The superarmphiphobic surface can only be realized with appropriate surface roughness modification and surface energy modification. The first step is to implement the right roughness with nanostructures in order to create the capillary force at the blood-surface interface [71] [72] [73] . The nanostructure creates an air gap between the liquid and the surface of the material, transforming the surface from the Wenzel state to the Cassie-Baxter state [71, [74] [75] [76] [77] [78] [79] [80] (Figure 9 ). There are many ways to fabricate nanostructures, such as spray particle coating [57, [81] [82] [83] or etching methods (plasma, laser, chemical, and electrochemical etching) [71, 78, [84] [85] [86] [87] [88] [89] [90] [91] . exhibit extremely low surface energy but can be toxic to the environment and health [92] , and cannot be applied for healthcare materials. Alternative perfluorochemicals are being sought which are safer but with similar low surface energy characteristics [92] . The lowest surface energy reported is 9.3 mN/m using fluorinated polyhedral oligomeric silsesquioxanes (POSS) [93] . To realize a superamphiphobic surface, the surface energy must also be minimized in tandem, typically using fluorochemicals. The most commonly used ones are fluorocarbonbased compounds, (-CF 2 -) n , where n is between 4 and 10. These perfluorochemicals exhibit extremely low surface energy but can be toxic to the environment and health [92] , and cannot be applied for healthcare materials. Alternative perfluorochemicals are being sought which are safer but with similar low surface energy characteristics [92] . The lowest surface energy reported is 9.3 mN/m using fluorinated polyhedral oligomeric silsesquioxanes (POSS) [93] .

Apart from controlling the protein adsorption, hemocompatibility can be achieved by controlling other factors within the blood physiology. For example, blood coagulation cascades can be inhibited using nitric oxide (NO) [94] or by coating heparin derivatives [95] . Coating the membrane with phosphorylcholine (PC) compound has also been reported to decrease thrombosis [96] [97] [98] . A considerable reduction of platelet adhesion was reported when coating the membrane with poly(2-methoxyethylacrylate) (PMEA) [99, 100] . One of the most promising methods is to form a thin endothelial cell layer on the membrane surface to mimic the actual blood vessels. Hypothetically, a monolayer of endothelial cells on membranes can achieve complete hemocompatibility [101] . Many interesting pieces of research have been carried out [101] [102] [103] [104] [105] [106] [107] , but its efficacy and clinical safety must be proven before it can be implemented in commercial products.

Despite several decades of hemocompatible research, it is as yet difficult to obtain membranes that can completely avoid blood coagulation and inflammation. In fact, this challenge is not only in the artificial lung field, but in the entire discipline of bloodcontacting biomaterials. Many promising developments are being reported but have yet to be implemented into artificial lung technology.

The performance of current commercial ECMO modules is summarized in Table 5 . It can be seen that there is still a wide gap between the oxygenator membrane performance and that of human lungs (Table 1 ). There are several ways to improve the oxygenator membrane performance. First, the blood oxygenation efficiency can be improved by optimizing the blood's fluid dynamics within the module. Many articles reported different strategies for better module designs [39, [108] [109] [110] [111] [112] . Most of the blood oxygenator modules are designed with hollow fiber bundles with the blood flowing outside the fiber membranes. In this way, the contact area and the gas transfer efficiency of the artificial lung can be maximized [39, 109] . In order to avoid unwanted blood trauma due to shear flow [113] , computational fluid dynamics (CFD) tools have been applied to optimize the module design and to improve the ECMO performance [110, 112, 114, 115] . Secondly, the prime volume, or the amount of extracorporeal blood, must be minimized. Simultaneously, the contact area and contact time with foreign materials must also be minimized to improve the blood hemostasis. One obvious strategy is to minimize the hollow fiber thickness (100 µm) similar to that of alveolus thickness (2 µm), but materials with strong enough mechanical properties must be developed. Theoretically, this strategy could lower the prime volume quite significantly.

Apart from the hollow fiber membrane modules, other types of artificial lung are being developed, such as paracorporeal, introthoracic and intravenous artificial lungs [116] [117] [118] [119] , some reaching clinical trials [120] . In particular, microfluidic devices are now considered as the most promising artificial lung platform for the future [121] [122] [123] [124] [125] [126] [127] . Mostly fabricated with PDMS material, the membrane thickness can be controlled within 6 to 130 µm [128] , and the oxygen exchange rate can reach as high as 329 mL·min −1 ·m −2 [129] (Figure 10 ). In addition, the blood paths can be customized to maximize the contact area and residence time.

However, main challenges of the microfluidic artificial lung are, again, related to hemocompatibility [128] . Additionally, although the photolithographic fabrication step can be cumbersome, the recent development of the PDMS fabrication technique could lead to a breakthrough [130] . Apart from the hollow fiber membrane modules, other types of artificial lung are 1 being developed, such as paracorporeal, introthoracic and intravenous artificial lungs 2 [116] [117] [118] [119] , some reaching clinical trials [120] . In particular, microfluidic devices are now 3 considered as the most promising artificial lung platform for the future [121] [122] [123] [124] [125] [126] [127] . Mostly 4 fabricated with PDMS material, the membrane thickness can be controlled within 6 to 130 5 μm [128] , and the oxygen exchange rate can reach as high as 329 ml·min −1 ·m −2 [129] (Figure 6 10). In addition, the blood paths can be customized to maximize the contact area and res-7 idence time. 8 However, main challenges of the microfluidic artificial lung are, again, related to he-9 mocompatibility [128] . Additionally, although the photolithographic fabrication step can 10 be cumbersome, the recent development of the PDMS fabrication technique could lead to 11 a breakthrough [130] . 15 technology-an ambulatory pumpless extracorporeal lung assist system (reprinted with permis- 16 sion from [128] ); (b) a multilayer PDMS microfluidic blood oxygenator (reprinted with permission 17 from [131] .). 18 Wearable and Implantable Artificial Lung 19 To improve the quality of life of lung-failure patients, the device must become 20 smaller and more portable. For instance, a wearable or implantable artificial lung could 21 be a preferred treatment. Several different types of such devices have been reported. In 22 2012, researchers reported results on a wearable artificial lung, tested with sheep for 30 23 days with stable oxygen saturation levels [132] . In 2019, a paracorporeal ambulatory assist 24 lung (PAAL) was tested with sheep for six hours [133] and for five days [134] . Another 25 wearable ECMO device, compliant thoracic artificial lung (cTAL), was tested on sheep for 26 14 days [135] . Additionally, intravenacaval oxygenator and carbon dioxide removal de-27 vice (IVOX) [136] and the Hattler respiratory gas exchange catheter [137] were also re-28 ported but these artificial lungs failed during clinical tests. The wearable and implantable 29 artificial lung devices are still in the early stages of development. Expectedly, the main 30 challenge is the hemocompatibility of the materials. In order to achieve safety over the 31 long-term, better understanding of the blood-material interaction is required. 32 33 The kidneys are bean-shaped organs in the renal system, located on both sides of the 34 lower spine. They are made up of nephrons that act as a physical filter to remove biologi- 35 cal waste and excess water from the blood to maintain homeostasis. In addition, human 36 kidneys perform biological roles, such as hormone production, to make new red blood 37 Figure 10 . (a) A conceptual drawing of an initial clinical application of microfluidic artificial lung technology-an ambulatory pumpless extracorporeal lung assist system (reprinted with permission from [128] ); (b) a multilayer PDMS microfluidic blood oxygenator (reprinted with permission from [131] .).

To improve the quality of life of lung-failure patients, the device must become smaller and more portable. For instance, a wearable or implantable artificial lung could be a preferred treatment. Several different types of such devices have been reported. In 2012, researchers reported results on a wearable artificial lung, tested with sheep for 30 days with stable oxygen saturation levels [132] . In 2019, a paracorporeal ambulatory assist lung (PAAL) was tested with sheep for six hours [133] and for five days [134] . Another wearable ECMO device, compliant thoracic artificial lung (cTAL), was tested on sheep for 14 days [135] . Additionally, intravenacaval oxygenator and carbon dioxide removal device (IVOX) [136] and the Hattler respiratory gas exchange catheter [137] were also reported but these artificial lungs failed during clinical tests. The wearable and implantable artificial lung devices are still in the early stages of development. Expectedly, the main challenge is the hemocompatibility of the materials. In order to achieve safety over the long-term, better understanding of the blood-material interaction is required.

The kidneys are bean-shaped organs in the renal system, located on both sides of the lower spine. They are made up of nephrons that act as a physical filter to remove biological waste and excess water from the blood to maintain homeostasis. In addition, human kidneys perform biological roles, such as hormone production, to make new red blood cells (erythropoietin), to promote bone health, and to regulate blood pressure. These biological roles cannot be augmented with membrane technology yet.

In the case of kidney failure, the patient must be treated with artificial kidney technology at least twice a week for blood purification. The artificial kidney, also known as the dialyzer (Figure 11 ), is one of the most important technologies that helps millions of people around the world. The term "dialyzer" was first coined in the middle of the 19th century [138] , but the first real success in prolonging a patient's life was reported in 1945 [139] . Since then, artificial kidney membranes underwent tremendous improvements in treating renal diseases (i.e., kidney failures). After many module designs, such as coil and plate types, the current state-of-the-art artificial kidney membranes are mostly in the form of hollow fiber modules. cells (erythropoietin), to promote bone health, and to regulate blood pressure. These bio-38 logical roles cannot be augmented with membrane technology yet. 39 In the case of kidney failure, the patient must be treated with artificial kidney tech-40 nology at least twice a week for blood purification. The artificial kidney, also known as 41 the dialyzer (Figure 11 ), is one of the most important technologies that helps millions of 42 people around the world. The term "dialyzer" was first coined in the middle of the 19th 43 century [138] , but the first real success in prolonging a patient's life was reported in 1945 44 [139] . Since then, artificial kidney membranes underwent tremendous improvements in 45 treating renal diseases (i.e., kidney failures). After many module designs, such as coil and 46 plate types, the current state-of-the-art artificial kidney membranes are mostly in the form 47 of hollow fiber modules. 48 One of the key roles of artificial kidney is to purify blood, also known as extracorpo-49 real (e.g., outside the body) blood purification, and it can be further classified as hemodi-50 alysis (HD), hemofiltration (HF), and hemodiafiltration (HDF). As illustrated in Figure 12 , 51 hemodialysis is a blood purification method that requires a separate dialysate stream, and 52 toxins are extracted from the blood into the dialysate stream via natural diffusion down 53 the concentration gradient. Normally, the MWCO (molecular weight cut off) of dialyzer 54 membranes is from 3000 Da to more than 15 kDa [140, 141] . In recent times, the super high 55 flux dialyzer membrane can have a MWCO of around 65 kDa [142] . It is interesting to note 56 that dialysate production occupies a considerable market portion of the reverse osmosis 57 membranes, as ultrapure water is required to make the dialysate solution. 58 59 Figure 11 . Membrane-based artificial kidney schematic. 60 Hemofiltration is similar to hemodialysis, but a transmembrane pressure is applied 61 across the membrane to push the waste solutes and water through the membrane. Unlike 62 hemodialysis, hemofiltration does not require a dialysate stream, but a substitution fluid 63 is used to make up the lost blood volume. Additionally, as the applied pressure induces 64 liquid convection through the membrane, hemofiltration can permeate large solutes faster 65 than hemodialysis [143] . On the other hand, hemodiafiltration is a hybrid of the hemodi-66 alysis and hemofiltration methods. This method can improve the permeance by applying 67 the pressure gradient and increase the performance of the membrane [144] . 68 Figure 11 . Membrane-based artificial kidney schematic.

One of the key roles of artificial kidney is to purify blood, also known as extracorporeal (e.g., outside the body) blood purification, and it can be further classified as hemodialysis (HD), hemofiltration (HF), and hemodiafiltration (HDF). As illustrated in Figure 12 , hemodialysis is a blood purification method that requires a separate dialysate stream, and toxins are extracted from the blood into the dialysate stream via natural diffusion down the concentration gradient. Normally, the MWCO (molecular weight cut off) of dialyzer membranes is from 3000 Da to more than 15 kDa [140, 141] . In recent times, the super high flux dialyzer membrane can have a MWCO of around 65 kDa [142] . It is interesting to note that dialysate production occupies a considerable market portion of the reverse osmosis membranes, as ultrapure water is required to make the dialysate solution. Figure 12 . Schematic illustration of hemodialysis, hemodiafiltration and hemofiltration. 70 Currently, there are many different types of polymers to fabricate dialysis mem-71 branes, and it can be divided into five different groups-namely, cellulose derivatives, 72 polysulfone derivatives (PSU), polyacrylontrile (PAN), polymethylmethacrylate (PMMA) 73 and ethyl-vinyl-acetate copolymer (EVAL). 74 The first group is the cellulose derivatives. Most of the hemodialysis membranes 75 were made from cellulose materials in the early days (around 1950) of artificial kidney 76 technology. In 1985, Henderson et al. [145] published an article which reported concerns 77 over the blood biocompatibility of the regenerated cellulose membranes used for artificial 78 kidneys [145] . This paper initiated researchers searching for new biomaterials with higher 79 biocompatibility to apply in dialysis membranes. Nowadays, synthetic membranes with 80 better biocompatibility have mostly replaced the cellulosic membranes. As of 2016, syn-81 thetic membranes such as polysulfone (PSU), polyethersulfone (PES), PAN, PMMA and 82 EVAL make up 95% of the dialysis membrane market share [9] . Interestingly, acetylated 83 cellulose polymers, such as cellulose triacetate (CTA), exhibit reasonable biocompatibility 84 [146] and hence still hold 5% of the dialysis membrane market [147] . 85 The second group is the polysulfone-based polymers such as polysulfone (PSU) and 86 polyethersulfone (PES), and they currently dominate the hemodialysis market. PSU-based 87 dialysis membranes are proven to have higher biocompatibility and better clinical perfor-88 mance. Long years of research have shown that a delicate balance is required between 89 hydrophilic and hydrophobic properties to obtain adequate biocompatibility. As PSU pol-90 ymers are intrinsically hydrophobic, researchers have blended polyvinylpyrrolidone 91 (PVP) additives to increase the PSU membrane hydrophilicity, and its positive effect on 92 biocompatibility have been clinically proven [148] . 93 The third group, PAN dialysis membranes were first reported in 1972 by the Rhone- 94 Poulenc company as "AN69" with high flux. The AN69 was made with PAN and hydro-95 philic sodium-meth-allyl-sulfonate additives with high biocompatibility [149] . The fourth 96 group is PMMA hemodialysis, which is known as a biocompatible adsorbent membrane 97 [150] . PMMA membranes show excellent adsorption of biological middle molecule (β2 98 microglobulin) at the wall and the inner surface of membranes [150] . Lastly, EVAL and 99 EVOH polymers are promising dialysis materials with remarkable blood compatibility, 100 based on their strong hydrophilic properties. Notably, protein adsorption onto the EVAL 101 membrane is extremely slow [151] . Hemofiltration is similar to hemodialysis, but a transmembrane pressure is applied across the membrane to push the waste solutes and water through the membrane. Unlike hemodialysis, hemofiltration does not require a dialysate stream, but a substitution fluid is used to make up the lost blood volume. Additionally, as the applied pressure induces liquid convection through the membrane, hemofiltration can permeate large solutes faster than hemodialysis [143] . On the other hand, hemodiafiltration is a hybrid of the hemodialysis and hemofiltration methods. This method can improve the permeance by applying the pressure gradient and increase the performance of the membrane [144] .

Currently, there are many different types of polymers to fabricate dialysis membranes, and it can be divided into five different groups-namely, cellulose derivatives, polysulfone derivatives (PSU), polyacrylontrile (PAN), polymethylmethacrylate (PMMA) and ethylvinyl-acetate copolymer (EVAL).

The first group is the cellulose derivatives. Most of the hemodialysis membranes were made from cellulose materials in the early days (around 1950) of artificial kidney technology. In 1985, Henderson et al. [145] published an article which reported concerns over the blood biocompatibility of the regenerated cellulose membranes used for artificial kidneys [145] . This paper initiated researchers searching for new biomaterials with higher biocompatibility to apply in dialysis membranes. Nowadays, synthetic membranes with better biocompatibility have mostly replaced the cellulosic membranes. As of 2016, synthetic membranes such as polysulfone (PSU), polyethersulfone (PES), PAN, PMMA and EVAL make up 95% of the dialysis membrane market share [9] . Interestingly, acetylated cellulose polymers, such as cellulose triacetate (CTA), exhibit reasonable biocompatibility [146] and hence still hold 5% of the dialysis membrane market [147] .

The second group is the polysulfone-based polymers such as polysulfone (PSU) and polyethersulfone (PES), and they currently dominate the hemodialysis market. PSUbased dialysis membranes are proven to have higher biocompatibility and better clinical performance. Long years of research have shown that a delicate balance is required between hydrophilic and hydrophobic properties to obtain adequate biocompatibility. As PSU polymers are intrinsically hydrophobic, researchers have blended polyvinylpyrrolidone (PVP) additives to increase the PSU membrane hydrophilicity, and its positive effect on biocompatibility have been clinically proven [148] .

The third group, PAN dialysis membranes were first reported in 1972 by the Rhone-Poulenc company as "AN69" with high flux. The AN69 was made with PAN and hydrophilic sodium-meth-allyl-sulfonate additives with high biocompatibility [149] . The fourth group is PMMA hemodialysis, which is known as a biocompatible adsorbent membrane [150] . PMMA membranes show excellent adsorption of biological middle molecule (β 2 microglobulin) at the wall and the inner surface of membranes [150] . Lastly, EVAL and EVOH polymers are promising dialysis materials with remarkable blood compatibility, based on their strong hydrophilic properties. Notably, protein adsorption onto the EVAL membrane is extremely slow [151] .

The cell-free artificial kidney system has been employed for a long time, and the basic principle of the dialysis system is to eliminate the toxins from the blood using a membrane. However, this system cannot replace the endocrine, homeostatic, metabolic and regulatory functions of the human kidney (biological and chemical functions). Hence, researchers have tried to combine the polymeric membranes with kidney cells, known as the bioartificial kidney (BAK). The first BAK prototype was presented in 1987 [152] . A BAK device is composed of two parts ( Figure 13 ): a hemofiltration device and a renal tubule assist device (RAD). A patient's blood is first separated by a hemofilter into the blood and the ultrafiltrate streams. Then, both streams enter the RAD, where the valuable components in the ultrafiltrate are reabsorbed into the bloodstream. A hollow fiber module incorporating renal cells is used. The commonly employed polymers are PSU [153, 154] , PAES [154] and PES [155] . The cell-free artificial kidney system has been employed for a long time, and the basic 103 principle of the dialysis system is to eliminate the toxins from the blood using a mem-104 brane. However, this system cannot replace the endocrine, homeostatic, metabolic and 105 regulatory functions of the human kidney (biological and chemical functions). Hence, re-106 searchers have tried to combine the polymeric membranes with kidney cells, known as 107 the bioartificial kidney (BAK). The first BAK prototype was presented in 1987 [152] . A 108 BAK device is composed of two parts ( Figure 13 ): a hemofiltration device and a renal tu-109 bule assist device (RAD). A patient's blood is first separated by a hemofilter into the blood 110 and the ultrafiltrate streams. Then, both streams enter the RAD, where the valuable com-111 ponents in the ultrafiltrate are reabsorbed into the bloodstream. A hollow fiber module 112 incorporating renal cells is used. The commonly employed polymers are PSU [153, 154] , 113 PAES [154] and PES [155] . 114 115 Figure 13 . Bioartificial kidney (BAK) schematic. 116 The source of renal cells can be from porcine [156, 157] , canine [158] or human renal 117 cells [153] [154] [155] . More recently, 3D printing technologies were applied to mimic a more 118 kidney-like structure [159] in combination with the microfluidic technology [160] . On the 119 other hand, wearable artificial kidney (WAK) devices are actively being developed to im-120 prove the quality of life of the patients while reducing the financial burden of long-term 121 treatments [161] [162] [163] . An ideal WAK devices should weigh under 8 kg and the total vol-122 ume should be less than 0.1m 3 [164] . Several urea removal strategies have been reported 123 in the WAK such as sorbents [165] , photo-oxidation [166] and electro-oxidation [167] . An 124 exciting work that applies artificial intelligence (AI) techniques to improve dialysis ther-125 apy has been reported by real-time feedback responses and life and death making deci-126 sions [168, 169] . 127 128 The liver is a multifunctional organ with more than 200 functions that is essential for 129 survival. It is the largest internal human organ, weighting about 1.5 kg, and is composed 130 mostly of hepatocytes (liver cells). The liver performs many essential metabolic functions, 131 along with nutrient storage, blood detoxification, plasma protein synthesis, and hormone 132 control [170] . 133 Liver failure can be acute and/or chronic, and it can occur due to many reasons; com-134 mon causes are the ingestion of a toxic substance, medicine, drug overdose, alcohol con-135 The source of renal cells can be from porcine [156, 157] , canine [158] or human renal cells [153] [154] [155] . More recently, 3D printing technologies were applied to mimic a more kidney-like structure [159] in combination with the microfluidic technology [160] . On the other hand, wearable artificial kidney (WAK) devices are actively being developed to improve the quality of life of the patients while reducing the financial burden of long-term treatments [161] [162] [163] . An ideal WAK devices should weigh under 8 kg and the total volume should be less than 0.1m 3 [164] . Several urea removal strategies have been reported in the WAK such as sorbents [165] , photo-oxidation [166] and electro-oxidation [167] . An exciting work that applies artificial intelligence (AI) techniques to improve dialysis therapy has been reported by real-time feedback responses and life and death making decisions [168, 169] .

The liver is a multifunctional organ with more than 200 functions that is essential for survival. It is the largest internal human organ, weighting about 1.5 kg, and is composed mostly of hepatocytes (liver cells). The liver performs many essential metabolic functions, along with nutrient storage, blood detoxification, plasma protein synthesis, and hormone control [170] .

Liver failure can be acute and/or chronic, and it can occur due to many reasons; common causes are the ingestion of a toxic substance, medicine, drug overdose, alcohol consumption, and viral hepatitis. Liver damage can lead to a variety of life-threatening physiologic and metabolic abnormalities like hemorrhage, hypoglycemia and hyperammonemia [171] . Fortunately, the liver is one of the unique organs that can regenerate, and it can recover itself from minor damages (e.g., binge drinking). However, as the roles of liver are primarily biochemical functions requiring hepatocytes, the most effective treatment for severe liver failure patients is, again, organ transplantation.

Researchers have tried to develop various artificial liver support devices for liver failure patients. The current liver support systems can be divided into two main types: (1) nonbiological artificial liver systems that augment the blood detoxification role of the liver, and (2) bioartificial liver with hepatocytes that can also augment the biological roles.

The first type is the conventional artificial liver support which is a nonbiological membrane system-that is, without any cellular (hepatocyte) functions. Its main role is to augment liver detoxification function. To achieve blood homeostasis, two different classes of blood toxins must be removed from the body. There are low MW hydrosoluble toxins such as urea and ammonia. These toxins can be effectively removed by the kidneys or by hemodialysis. On the other hand, there are protein-bound toxins that are too big to be removed by kidney or hemodialysis. These protein-bound toxins must be treated by the liver prior to excretion.

Some of the biological waste toxins (e.g., bilirubin, aromatic amino acids, endotoxins, etc.) are hydrophobic and sparingly soluble in blood plasma. These toxins in the blood are transported to the liver as protein-bound, mostly bound to albumin proteins. It is important to note here that albumin is the most abundant protein in the blood plasma with many important roles including osmotic pressure control and toxin scavenging.

Particularly, bilirubin is a chemical compound produced during the breakdown of old red blood cells. The produced bilirubin binds to albumin in the blood, and is transported to the liver, where it becomes conjugated with glucuronic acid, after which it can be degraded and excreted. The blood bilirubin concentration is commonly considered as an important marker for liver malfunction, as high bilirubin concentration can lead to hepatic encephalopathy (brain damage), or coma. Hence, the main objective of the current artificial liver systems is to eliminate these albumin-bound toxins in the blood, as this is the most urgent issue in the event of liver failure.

From membrane engineering perspective, the challenge is the difficulty in discriminating the albumin-bound toxins from other important chemicals inside the blood. These toxins (e.g., bilirubin and tryptophan) are strongly bound to albumin proteins, and albumin itself should not be removed from the bloodstream for homeostasis. The MW of albumin is approximately 69 kDa. It is possible to simply replace the entire plasma (plasmapheresis), but it is not practical as it requires large amounts of fresh plasma continuously [172] . Additionally, the blood can be pushed through an absorbent column (hemoperfusion) to remove toxins but this is relatively nonspecific (low selectivity) and it can inadvertently remove other important biomolecules in tandem [173] .

Currently, two different strategies have been developed ( Figure 14 ). The first strategy, known as MARS (molecular absorbent recirculation system), was first applied in 1996 and it utilizes a technique called albumin dialysis [174] . Although bilirubin exists as albuminbound form in the blood plasma, it is strictly in thermodynamic equilibrium between the free bilirubin form and albumin-bound bilirubin form. Hence, the only way to selectively push free bilirubin through a membrane is by circulating highly concentrated free albumin (unbound) solution on the dialysate side of the membrane, as illustrated in Figure 14 . Generally, 20 wt% albumin (unbound) solution is used as the dialysate. Hence, due to the free albumin concentration gradient, bilirubin unbinds itself from blood plasma albumin, diffuses through the membrane, then subsequently binds to a free albumin in the dialysate solution. For this process, a conventional hemodialysis membrane (albumin-impregnated) is used with MWCO of 50~60 kDa. Hence, this membrane blocks albumin permeation while allowing bilirubin (MW of 584 Da) to permeate freely. 190 The driving force for bilirubin permeation is purely by the concentration gradient of 191 the free albumin across the membrane. Hence, the phase equilibria of the albumin-toxin 192 systems must be understood. It has been reported that the binding constants (Keq) for bil- 193 irubin and tryptophan, two of the most problematic liver failure toxins, are 10 7 L/mole 194 [175] and 10 4 L/mole [176] , respectively. These values indicate that basically all bilirubin 195 and tryptophan molecules exist as albumin-bound form. Therefore, the toxin removal ef-196 ficiency is primarily a function of albumin dialysate concentration. 197 The albumin dialysate solution circulates around a loop and albumin is regenerated 198 using two adsorption columns, mostly with an activated carbon column to adsorb un-199 charged toxins (e.g., tryptophan), and an anion exchange column to remove negatively 200 charged compounds (e.g., bilirubin). Apart from bilirubin, other low MW compounds also 201 permeate the MARS membrane into the albumin dialysate solution. Such compounds are 202 then removed in the second dialysis membrane ( Figure 14) . Hence, MARS also performs 203 artificial kidney functions, but not as effectively. This system can only last about 6-8 204 hours, after which the adsorption columns must be replaced. 205 Another strategy of artificial liver system is called Prometheus, or FPSA (Fractionated 206 Plasma Separation and Adsorption), first proposed in 1999 [177] and clinically commer-207 cialized in 2003 [174] . The key difference of this process compared to MARS is the use of 208 a loose polysulfone membrane with MWCO of about 250 kDa (MARS employs a 65 kDa 209 membrane). Instead of using albumin dialysate, the membrane allows the toxin-bound 210 albumin proteins in the blood to selectively permeate. The albumin filtrate is then treated 211 with adsorption resins to regenerate the albumin (toxin removed). The regenerated albu-212 min stream is then recombined with the blood, and the bloodstream is further dialyzed 213 with a conventional hemodialyzer. The driving force for bilirubin permeation is purely by the concentration gradient of the free albumin across the membrane. Hence, the phase equilibria of the albumin-toxin systems must be understood. It has been reported that the binding constants (K eq ) for bilirubin and tryptophan, two of the most problematic liver failure toxins, are 10 7 L/mole [175] and 10 4 L/mole [176] , respectively. These values indicate that basically all bilirubin and tryptophan molecules exist as albumin-bound form. Therefore, the toxin removal efficiency is primarily a function of albumin dialysate concentration.

The albumin dialysate solution circulates around a loop and albumin is regenerated using two adsorption columns, mostly with an activated carbon column to adsorb uncharged toxins (e.g., tryptophan), and an anion exchange column to remove negatively charged compounds (e.g., bilirubin). Apart from bilirubin, other low MW compounds also permeate the MARS membrane into the albumin dialysate solution. Such compounds are then removed in the second dialysis membrane ( Figure 14) . Hence, MARS also performs artificial kidney functions, but not as effectively. This system can only last about 6-8 hours, after which the adsorption columns must be replaced.

Another strategy of artificial liver system is called Prometheus, or FPSA (Fractionated Plasma Separation and Adsorption), first proposed in 1999 [177] and clinically commercialized in 2003 [174] . The key difference of this process compared to MARS is the use of a loose polysulfone membrane with MWCO of about 250 kDa (MARS employs a 65 kDa membrane). Instead of using albumin dialysate, the membrane allows the toxin-bound albumin proteins in the blood to selectively permeate. The albumin filtrate is then treated with adsorption resins to regenerate the albumin (toxin removed). The regenerated albu-min stream is then recombined with the blood, and the bloodstream is further dialyzed with a conventional hemodialyzer.

The clinical data for the MARS and Prometheus systems showed that the treatments clearly improve the biochemical homeostasis (e.g., bilirubin concentration), but unfortunately these treatments did not improve the survival rate of the patients [178, 179] . Such an outcome may be because the liver performs many other important functions besides maintaining blood homeostasis. Hence, simply augmenting the blood detoxification role of the liver cannot guarantee the patient's survival. Liver failure almost always leads to multiorgan failures which are, currently, difficult to predict and to treat. From membrane performance perspectives, the use of facilitated transport membranes can be applied to the MARS system to enhance the toxin removal rate, and membranes with better selectivity between albumin and fibrinogen could improve the Prometheus performance.

There are also other artificial liver systems such as SPAD [180] , and SEPET [9] ; however, conventional artificial liver systems have clear limitations and their role is primarily to temporarily treat acute liver failure patients. These treatments cannot be applied in the long-term for severe liver failure patients. Hence, future research must focus on bioartificial liver (BAL) systems with hepatocytes that can also perform the biological roles of the liver, such as regulation and synthesis.

A BAL system combines the membrane technology with a compartmentalized bioreactor that contains hepatocytes ( Figure 15 ). The key role of the membrane in BAL is to protect the hepatocytes (foreign source) from the immune system. The membrane needs to prevent blood immune cells from passing through the membrane, while allowing other biomolecules and nutrients to permeate and come into contact with the hepatocytes; however, it should be noted that the membrane itself can also initiate the immune response and blood coagulation [181, 182] , and necessary measures (anticoagulation) must be implemented. Again, hemocompatibility is the key challenge.

Many BAL systems have been tested, such as ELAD (Extracorporeal Liver Assist Devices) [183] , BLSS (bioartificial liver support system) [184] , and BIOLIV A3A [185] . Although considerable improvements have been made, BAL systems are still in early stages of development with countless challenges. The development of BAL is very challenging as many parameters must be considered simultaneously, such as hepatocyte source, bioreactor design, immune response, and blood homeostasis. In addition, many difficult challenges must be overcome from the bioreactor component as well.

From the membrane perspective, the rate of mass transfer of biomolecules through the membrane must be controlled to maintain hepatocyte survival and cellular metabolism, while effectively suppressing the immune response and blood coagulation. Hence, membrane properties such as the pore size, surface charge, and wettability must be optimized for this purpose [186, 187] . The current BAL membranes are fabricated from rather conventional materials such as polysulfone [188] [189] [190] [191] , cellulose [192] , and cellulose acetate [193, 194] . Ideally, more application-specific materials must be developed.

actor that contains hepatocytes ( Figure 15 ). The key role of the membrane in BAL is to 232 protect the hepatocytes (foreign source) from the immune system. The membrane needs 233 to prevent blood immune cells from passing through the membrane, while allowing other 234 biomolecules and nutrients to permeate and come into contact with the hepatocytes; how-235 ever, it should be noted that the membrane itself can also initiate the immune response 236 and blood coagulation [181, 182] , and necessary measures (anticoagulation) must be im-237 plemented. Again, hemocompatibility is the key challenge. 

The primary role of the pancreas is to maintain glucose homeostasis in the blood by controlling the concentration of endocrine hormones (e.g., insulin and glucagon). Pancreas failure can lead to diabetes, one of the most well-known diseases in the world. Upon pancreas failure, the body loses control of its insulin production, causing various types of diabetes. Type 1 diabetes, which mostly occurs in young children, is caused by a pancreas disorder where insulin production cannot meet the body's demand. On the other hand, type 2 diabetes, which is much more prevalent in adults, occurs when the body develops insulin resistance and the blood sugar level remains high for prolonged periods.

There are several treatment methods to control the sugar levels and insulin concentrations for patients with the type 1 diabetes. The method can range from simple injection of the required insulin to cutting-edge islet (pancreatic cell) transplantation technology. Instead of the transplantation of the whole pancreas, only the islet (pancreas) cells can be transplanted from the donor, known as the Clinical Islet Transplantation (CIT) [195] . The CIT technology has been improving, with its five-year success rate increasing from only 15% to approximately 60% [196] [197] [198] [199] .

The bioartificial pancreas (BAP) technology, similarly to BAL, combines membrane technology with islet cell transplantation technology. A BAP consists of islet cells encapsulated within a semipermeable membrane capsule that acts as an immune system barrier [200, 201] .

An ideal BAP needs to meet the following requirements: (1) segregate and protect the islet cells from the immune system; (2) allow glucose, nutrients and oxygen to permeate, so that the response time to blood glucose level is minimized; (3) exhibit high hemocom-patibility with minimal inflammatory response by the host body to ensure prolonged use inside the body; (4) easily implantable and retrievable in case of failures.

As illustrated in Figure 16a , the capsule that encapsulates the islet cells is a semipermeable membrane which can protect the islet cells from immunoglobin while providing the necessary nutrients, oxygen and glucose to the cells. The smallest immunoglobin, IgG, has a MW of 150 kDa [202] . Hence, the optimal membrane MWCO (or pore size) to achieve these objectives is around 50-150 kDa (of course, solute MW alone cannot and should not be the sole factor that determines the selectivity). There are various types of membrane materials applied for the intravascular devices 296 (Table 6 ) such as polyacrylontrile-polyvinylchloride (PAN-PVC) copolymer, polycar-297 bonate, EVAL fibers, poly-animo-urethane, nonwoven PTFE fabric and nylon mi-298 croporous membrane to encapsulate the islet cells [203] [204] [205] [206] . 299 As for the extravascular devices, inorganic materials have been reported, such as sil-300 ica [207] , aluminum/aluminum oxide [208, 209] and titanium/titanium oxide [209] . How-301 ever, the use of inorganic membranes for BAP is still relatively new and has not been 302 clinically proven. Polymeric membranes are more widely used to encapsulate the islet 303 cells (Table 6 ). Current membrane permselectivity is poor; it must be improved to decrease 304 the insulin-release time delay. Depending on the size and type of islet cells, there are three types of islet encapsulation: macroencapsulation (10-100 mm), microencapsulation (0.2-1 mm), and nanoencapsulation (<0.1 mm) (Figure 16b ). Macroencapsulation devices can be further classified into two different types-intravascular and extravascular-depending on the implant position. The intravascular device consists of islet cells encapsulated in hollow fiber membranes, implanted directly into the patient's cardiovascular system. The extravascular device is mostly implanted in the peritoneal cavity of the patient.

There are various types of membrane materials applied for the intravascular devices (Table 6 ) such as polyacrylontrile-polyvinylchloride (PAN-PVC) copolymer, polycarbonate, EVAL fibers, poly-animo-urethane, nonwoven PTFE fabric and nylon microporous membrane to encapsulate the islet cells [203] [204] [205] [206] .

As for the extravascular devices, inorganic materials have been reported, such as silica [207] , aluminum/aluminum oxide [208, 209] and titanium/titanium oxide [209] . However, the use of inorganic membranes for BAP is still relatively new and has not been clinically proven. Polymeric membranes are more widely used to encapsulate the islet cells (Table 6 ). Current membrane permselectivity is poor; it must be improved to decrease the insulin-release time delay. 

Artificial organ (AO) technology has become an indispensable tool for the treatment of organ failures. As summarized in this review, there have been incredible strides in many of AO devices that employ membrane technology including lung, kidney, liver, and pancreas. Every organ has its own unique functions, and the membrane must be tailor-developed for each organ. It is important to reiterate that the key bottleneck in membrane-based AO technology is not the permselectivity of the membrane (although better performance is still desired), but the hemocompatibility of the membrane material at the blood-material interface. The strategy to achieve better hemocompatibility must also be tailor-developed for each organ, as the requirements for kidney and lungs, for example, can be drastically different. In addition, particularly for artificial lungs, effective module design to improve the mass transfer coefficient is the most important parameter. Additionally, the development of a hemocompatible superamphiphobic membrane could be an important breakthrough. Unfortunately, only the physical functions of human organs can be partly augmented with the membrane technology. Bioartificial organ technology, which incorporates live cells, has been improving to replace the biochemical aspects of failed organs. Future research must focus on developing better bioartificial organs, precisely controlling the selective permeation of solutes in and out of the membrane to suppress the unwanted immune response. Additionally, future AO research needs to improve the well-being and quality of life of organ failure patients, until bridge-to-recovery or bridge-to-transplantation. 

The authors declare no conflict of interest. 

The future of organ replacement: Needs, potential applications, and obstacles to application

Stem cell culture and differentiation in microfluidic devices toward organ-on-a-chip

Concise reviews: Stem cells and kidney regeneration: An update

Concise review: Hurdles in a successful example of limbal stem cell-based regenerative medicine

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Porous inorganic membranes for CO 2 capture: Present and prospects

Hemodialysis and Peritoneal Dialysis Market by Product (Machines, Dialyzers, Concentrates, Dialysates, Catheters) Services, Modality (Conventional, CAPD, Nocturnal)

Extracorporeal Membrane Oxygenation Machine Market by Modality, Application and Region-Analysis & Forecasts to 2021

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The helix reservoir pump-oxygenator

An artificial lung dependent upon diffusion of oxygen and carbon dioxide through plastic membrane

Evaluation of three types of membrane oxygenators and their suitability for use with pulsatile flow

Medical applications of membranes: Drug delivery, artificial organs and tissue engineering

Outcome Prediction in Patients with Severe COVID-19 Requiring Extracorporeal Membrane Oxygenation-A Retrospective International Multicenter Study

The science and practice of cardiopulmonary bypass: From cross circulation to ECMO and SIRS

Extracorporeal life support for severe acute respiratory distress syndrome in adults

Extracorporeal membrane oxygenation for adult respiratory failure

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Extracorporeal membrane oxygenation for adult respiratory distress syndrome in trauma patients: A case series and systematic literature review

Extracorporeal Life Support for Severe Acute Chest Syndrome in Adult Sickle Cell Disease: A Preliminary Report

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Anatomy and Physiology of the Human Respiratory System

The Hill equation: A review of its capabilities in pharmacological modelling

The possible effects of the aggregation of the molecules of haemoglobin on its dissociation curves

Lung inflammatory response syndrome after cardiac-operations and treatment of lornoxicam

Oxygen transfer performance of a membrane oxygenator composed of crossed and parallel hollow fibers

Formulation of generalized mass transfer correlations for blood oxygenator design

Designing blood oxygenators

Blood flow and oxygen transfer rate of an outside blood flow membrane oxygenator

Pulsatile flow and oxygen transport past cylindrical fiber arrays for an artificial lung: Computational and experimental studies

artificial: Basic principles and current applications

Pumpless respiratory assistance using a membrane oxygenator as an artificial placenta: A preliminary study in newborn and preterm lambs

Thermally induced phase separation and electrospinning methods for emerging membrane applications: A review

Membranes for artificial lungs

Performance of a MedArray silicone hollow fiber oxygenator

A Polymethylpentene Fiber Gas Exchanger for Long-Term Extracorporeal Life Support

Poly-Methyl Pentene Oxygenators Have Improved Gas Exchange Capability and Reduced Transfusion Requirements in Adult Extracorporeal Membrane Oxygenation

Understanding the non-solvent induced phase separation (NIPS) effect during the fabrication of microporous PVDF membranes via thermally induced phase separation (TIPS)

Blood Oxygenation Using Fluoropolymer-Based Artificial Lung Membranes

Discussion about the use of relative values of permeabilities between two gases for high molecular weight polymers

The barrier properties of polyacrylonitrile

Gas Separation Membranes: Polymeric and Inorganic by AF Ismail

Efficacy of extracorporeal membrane oxygenation as a bridge to lung transplantation

The Blood Compatibility Catastrophe

Systemic inflammatory response syndrome

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Host Responses to Biomaterials and Anti-Inflammatory Design-a Brief Review

Review of ECMO (extra corporeal membrane oxygenation) support in critically ill adult patients. Heartlung Circ

Pump-induced haemolysis: A comparison of short-term ventricular assist devices

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The mechanisms of platelet dysfunction during extracorporeal membrane oxygenation in critically ill neonates

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Candle Soot as a Template for a Transparent Robust Superamphiphobic Coating

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Biocompatibility in cardiopulmonary bypass

Extracorporeal circulation, hemocompatibility, and biomaterials

Design of Highly Oleophobic Cellulose Surfaces from Structured Silicon Templates

Principles of Adsorption and Adsorption Processes

Capillary forces between surfaces with nanoscale roughness

Superhydrophobicity and superoleophobicity from hierarchical silica sphere stacking layers

Solution spraying of poly(methyl methacrylate) blends to fabricate microtextured, superoleophobic surfaces

Designing Superoleophobic Surfaces

Fabrication, Surface Properties, and Origin of Superoleophobicity for a Model Textured Surface

Influence of surface roughness on water-and oil-repellent surfaces coated with nanoparticles

Wetting of textured surfaces

Robust omniphobic surfaces

Superoleophobic Nanocomposite Coatings by Spray Atomization

Bio-inspired superoleophobic and smart materials: Design, fabrication, and application

RF-PACVD of water repellent and protective HMDSO coatings on bell metal surfaces: Correlation between discharge parameters and film properties

Super water-and oil-repellencies from silica-based nanocoatings

Preparation of a superamphiphobic surface on a common cast iron substrate

From Superamphiphobic to Amphiphilic Polymeric Surfaces with Ordered Hierarchical Roughness Fabricated with Colloidal Lithography and Plasma Nanotexturing

Engineering a Titanium Surface with Controllable Oleophobicity and Switchable Oil Adhesion

Superoleophobic Coatings with Ultralow Sliding Angles Based on Silicone Nanofilaments

Atmospheric plasma treatment to improve durability of a water and oil repellent finishing for acrylic fabrics

Bioinspired fabrication of stable and robust superhydrophobic steel surface with hierarchical flowerlike structure

Facile fabrication of superoleophobic surfaces with enhanced corrosion resistance and easy repairability

Properties, performance and associated hazards of state-of-the-art durable water repellent (DWR) chemistry for textile finishing

Anomalous macromolecular assembly of partially fluorinated polyhedral oligomeric silsesquioxanes

Assessing and improving the biocompatibility of microfluidic artificial lungs

Hemocompatibility of heparin-coated surfaces and the role of selective plasma protein adsorption

Phosphorylcholine coating offers natural platelet preservation during cardiopulmonary bypass

Reduced systemic heparin dose with phosphorylcholine coated closed circuit in coronary operations

Closed, phosphorylcholine-coated circuit and reduction of systemic heparinization for cardiopulmonary bypass: The intraoperative ECMO concept

Design of a new plasma separation membrane by graft copolymerization

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The influence of biomaterials on endothelial cell thrombogenicity

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Enhanced adhesion of endothelial cells onto a polypropylene hollow-fiber membrane by plasma discharge treatment and high inoculum cell density

Development of hybrid artificial lung with gene transfected biological cells

Endothelialization and characterization of titanium dioxide-coated gas-exchange membranes for application in the bioartificial lung

A biohybrid artificial lung prototype with active mixing of endothelialized microporous hollow fibers

Developing a biohybrid lung-sufficient endothelialization of poly-4-methly-1-pentene gas exchange hollow-fiber membranes

Comparison of oxygenation and flow characteristics of inside and outside blood flow membrane oxygenators

Effects of hollow fiber packing fraction on blood flow pattern and gas transfer rate of an intravascular oxygenator (IVOX)

Flow vectorial analysis in an artificial implantable lung

Turbulent flow technique for the estimation of oxygen diffusive permeability of membranes for the oxygenation of blood and other cell suspensions

Characterization of membrane blood oxygenation devices using computational fluid dynamics

In vitro characterization of the occurrence of hemolysis during extracorporeal blood circulation using a mini hemodialyzer

A theoretical model for evaluation of the design of a hollow-fiber membrane oxygenator

Flow uniformity in oxygenators with different outlet port design

Artificial lung basics: Fundamental challenges, alternative designs and future innovations

Development of the MC3 BioLung/spl trade

Flow mixing enhancement from balloon pulsations in an intravenous oxygenator

Development of an intravenous membrane oxygenator: Enhanced intravenous gas exchange through convective mixing of blood around hollow fiber membranes

Major findings from the clinical trials of the intravascular oxygenator

Construction and evaluation of an alveolar membrane artificial heart-lung

Transport and flow phenomena in a microchannel membrane oxygenator

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Microchannel technologies for artificial lungs: (2) screen-filled wide rectangular channels

Microchannel technologies for artificial lungs: (3) open rectangular channels

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The promise of microfluidic artificial lungs. Lab. A Chip

Performance and scaling effects in a multilayer microfluidic extracorporeal lung oxygenation device

Monolithic digital patterning of polydimethylsiloxane with successive laser pyrolysis

Engineering tissue with BioMEMS

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In vitro and in vivo evaluation of a novel integrated wearable artificial lung

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A respiratory gas exchange catheter: In vitro and in vivo tests in large animals

The Bakerian lecture.-On osmotic force

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Advances in hemodialysis techniques

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Chapter 48-Liver

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Chapter 1-Artificial kidney: A chemical engineering challenge

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The specific binding of L-tryptophan to serum albumin

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The bioartificial pancreas (BAP): Biological, chemical and engineering challenges

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The use, in diabetic rats and monkeys, of artificial capillary units containing cultured islets of Langerhans (artificial endocrine pancreas)

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Biocompatibility of nanoporous alumina membranes for immunoisolation

In vitro inflammatory response of nanostructured titania, silicon oxide, and polycaprolactone

Studies of hereditary-obese mice (obob) after implantation of pancreatic islets in Millipore filter capsules

Hydrogels for encapsulation of pancreatic islet cells

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Maintenance of normoglycemia in diabetic mice by subcutaneous xenografts of encapsulated islets

In vitro and in vivo studies of the properties of an artificial membrane for pancreatic islet encapsulation

vitro test of new biomaterials for the development of a bioartificial pancreas