Abstract:Synthetic polymer membranes are enabling components in key technologies at the water–energy nexus, including desalination and energy conversion, because of their high water/salt selectivity or ionic conductivity. However, many applications at the water–energy nexus require ion selectivity, or separation of specific ionic species from other similar species. Here, the ion selectivity of conventional polymeric membrane materials is assessed and recent progress in enhancing selective transport via tailored free vo… Show more
“…The mechanisms underlying the delicate selectivity observed between similarly sized and charged monovalent ions have been increasingly studied in recent years. , Understanding the molecular details of these mechanisms is the key to design membranes for precise separations that can extend the use of polymeric membranes to applications beyond water desalination and purification. , While numerous experimental studies focused on explaining monovalent–monovalent ion selectivity by testing the permeation of monovalent anions, ,,, in the current study, we explored the transport and selectivity of monovalent cations, which demonstrate some intriguing transport phenomena, as we discuss below. More specifically, we measured the intrinsic permeability of four monovalent cations (i.e., lithium, sodium, potassium, and cesium; as chloride salts) at different pH and temperature values to extract their TST parameters using the methods described above (Figure ).…”
While polyamide reverse osmosis and nanofiltration membranes have been extensively utilized in water purification and desalination processes, the molecular details governing water and solute permeation in these membranes are not fully understood. In this study, we apply transition-state theory for transmembrane permeation to systematically break down the intrinsic permeabilities of water and small ions in loose and tight polyamide nanofiltration membranes into enthalpic and entropic components using an Eyring-type equation. We analyze trends in these components to elucidate molecular phenomena that induce water−salt, monovalent−divalent, and monovalent− monovalent selectivity at different pH values. Our results suggest that in pores that are either too small or contain an electrostatically repelling mouth, the thermal activation of ions in the form of ion dehydration is less likely, promoting entropically driven selectivity with steric exclusion of hydrated ions. Instead, larger uncharged pores enable ion dehydration, inducing enthalpic selectivity that is driven by differences in the ion hydration properties. We also demonstrate that electrostatic interactions between cations and intrapore carboxyl groups hinder salt permeability, increasing the enthalpic barrier of the transport. Last, permeation tests of monovalent cations in the loose and tight polyamide membranes expose opposite rejection trends that further support the phenomenon of ion dehydration in large subnanopores.
“…The mechanisms underlying the delicate selectivity observed between similarly sized and charged monovalent ions have been increasingly studied in recent years. , Understanding the molecular details of these mechanisms is the key to design membranes for precise separations that can extend the use of polymeric membranes to applications beyond water desalination and purification. , While numerous experimental studies focused on explaining monovalent–monovalent ion selectivity by testing the permeation of monovalent anions, ,,, in the current study, we explored the transport and selectivity of monovalent cations, which demonstrate some intriguing transport phenomena, as we discuss below. More specifically, we measured the intrinsic permeability of four monovalent cations (i.e., lithium, sodium, potassium, and cesium; as chloride salts) at different pH and temperature values to extract their TST parameters using the methods described above (Figure ).…”
While polyamide reverse osmosis and nanofiltration membranes have been extensively utilized in water purification and desalination processes, the molecular details governing water and solute permeation in these membranes are not fully understood. In this study, we apply transition-state theory for transmembrane permeation to systematically break down the intrinsic permeabilities of water and small ions in loose and tight polyamide nanofiltration membranes into enthalpic and entropic components using an Eyring-type equation. We analyze trends in these components to elucidate molecular phenomena that induce water−salt, monovalent−divalent, and monovalent− monovalent selectivity at different pH values. Our results suggest that in pores that are either too small or contain an electrostatically repelling mouth, the thermal activation of ions in the form of ion dehydration is less likely, promoting entropically driven selectivity with steric exclusion of hydrated ions. Instead, larger uncharged pores enable ion dehydration, inducing enthalpic selectivity that is driven by differences in the ion hydration properties. We also demonstrate that electrostatic interactions between cations and intrapore carboxyl groups hinder salt permeability, increasing the enthalpic barrier of the transport. Last, permeation tests of monovalent cations in the loose and tight polyamide membranes expose opposite rejection trends that further support the phenomenon of ion dehydration in large subnanopores.
“…Filtration using polymer membranes is an essential technology for water purification and for supplying safe water at low cost and with low energy consumption [ 3 – 5 ]. Aromatic polyamide thin films have been used as the separation layer of membranes.…”
Section: Introductionmentioning
confidence: 99%
“…Aromatic polyamide thin films have been used as the separation layer of membranes. Recently, advanced water filtration membranes [ 5 ] with materials such as liquid-crystalline (LC) polymers [ 6 – 14 ], carbon nanotubes [ 15 ], and block polymers [ 16 ] have been proposed. For example, we developed nanostructured membranes with three-dimensional (3D) nano ionic channels from an ionic bicontinuous cubic (Cub bi ) LC monomer with a taper-shaped mesogen [ 10 ].…”
Liquid-crystalline (LC) water-treatment membranes obtained by in situ photopolymerization of ionic mesogenic monomers have been shown to efficiently remove viruses. In our previous works, bicontinuous cubic (Cub
bi
) and smectic (Sm) LC membranes prepared from ionic taper- and rod-shaped polymerizable mesogens, respectively, were used for this purpose. Here, we report the results of virus removal by columnar (Col) LC water-treatment membranes having ionic nanochannels obtained from ionic taper-shaped mesogens. These effects are compared with those obtained for Cub
bi
membranes. The effects of these Col and Cub
bi
LC ionic membranes on the removal of several viruses from their cocktail solution are also examined.
“…Extraordinarily, Membrane distillation is a developing membrane separation technology through which combined membrane technique with distillation process (Liu et al, 1998;Meindersma et al, 2006;Liao et al, 2021), which has been indicated that the membrane distillation possessed excellent advantages, e.g., high separation efficiency, simple operation conditions, mild requirements on the interaction between membrane, and raw feed liquid (Smolders and Franken, 1989;Rezaei et al, 2018). Therefore, it is widely applied to seawater desalination, ultra-pure water preparation, and separation of an azeotropic mixture the like (Gong et al, 2019;Karahan et al, 2020;DuChanois et al, 2021). However, refrigerating capacity required for the membrane distillation process is generally supplied by mechanical refrigeration, which causes a membrane distillation system to have a complex structure and higher power consumption.…”
Thermoelectric Refrigeration Membrane Distillation (TERMD) is an emerging membrane-based evaporation technology with excellent prospects for separation industries. However, the development of the TERMD system was further limited by excellent membrane component properties. In this paper, a cold chamber component of a TERMD is manufactured. Then, the cooling performance of the component is studied to examine the coupling between the Thermoelectric Refrigeration (TER) and the Membrane Distillation (MD) process. Moreover, the effects of the membrane components properties are studied by changing the water flow rate, and the input current of thermoelectric refrigeration. The results showed that when the TERMD cold room inlet current is maintained stable and the heat dissipation intensity increases, the cooling temperature gradually decreases. Also, the temperature on the cold side tends to stabilize while the flow rate exceeds 600 L/h. In addition, the input power decreases as the heat dissipation intensity increases in the cooling dissipation intensity of the Thermoelectric Refrigeration Component (TERC) cold chamber is kept stable. And, the input power will reach a critical value while the water volume flow rate is over 500 L/h. Furthermore, the cooling rate reaches the maximum of 1.59 at the water volume flow rate of 700 L/h while the operating current of the TERC is 12 A. It is concluded that the thermoelectric refrigeration component can supply great refrigeration power and a high Coefficient of Performance (COP) under small current conditions for the analysis of the thermoelectric performance of the TERC.
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