1 - 13 |
Experimental investigation and mathematical modeling of CO2 sequestration from CO2/CH4 gaseous mixture using MEA and TEA aqueous absorbents through polypropylene hollow fiber membrane contactor Nakhjiri AT, Heydarinasab A, Bakhtiari O, Mohammadi T |
14 - 24 |
Theoretical modeling and simulation of AGMD and LGMD desalination processes using a composite membrane Im BG, Lee JG, Kim YD, Kim WS |
25 - 32 |
Hydrogen production via natural gas steam reforming in a Pd-Au membrane reactor. Investigation of reaction temperature and GHSV effects and long-term stability Anzelmo B, Wilcox J, Liguori S |
33 - 41 |
Temperature-dependent on/off PVP@TiO2 separator for safe Li-storage Jiang YH, Ding YH, Zhang P, Li F, Yang ZM |
42 - 49 |
Porous polyetherimide membranes with tunable morphology for lithium-ion battery Li D, Zhang HM, Li XF |
50 - 60 |
Tri-layer nonwoven membrane with shutdown property and high robustness as a high-safety lithium ion battery separator Li Z, Xiong Y, Sun SP, Zhang L, Li SS, Liu XG, Xu ZH, Xu SM |
61 - 71 |
Transport and reaction phenomena in multilayer membranes functioning as bioartificial kidney devices Refoyo R, Skouras ED, Chevtchik NV, Stamatialis D, Burganos VN |
72 - 84 |
Advances in water breakthrough measurement at high temperature in macroporous hydrophobic ceramic/polymeric membranes Varela-Corredor F, Bandini S |
85 - 94 |
Superwettable Coprinus comatus coated membranes used toward the controllable separation of emulsified oil/water mixtures Long YF, Shen YQ, Tian HF, Yang YX, Feng H, Li J |
95 - 103 |
Plasticization behavior in polymers of intrinsic microporosity (PIM-1): A simulation study from combined Monte Carlo and molecular dynamics Kupgan G, Demidov AG, Colina CM |
104 - 111 |
A non-MPD-type reverse osmosis membrane with enhanced permselectivity for brackish water desalination Zheng JF, Yao YJ, Li M, Wang LJ, Zhang X |
112 - 118 |
Gas permeation, diffusion, sorption and free volume of poly(2-trifluoromethyl-2-pentafluoroethyl-1,3-perfluorodioxole) Belov N, Nikiforov R, Polunin E, Pogodina Y, Zavarzin I, Shantarovich V, Yampolskii Y |
119 - 130 |
Controlling the zwitterionization degree of alternate copolymers for minimizing biofouling on PVDF membranes Lien CC, Yeh LC, Venault A, Tsai SC, Hsu CH, Dizon GV, Huang YT, Higuchi A, Chang Y |
131 - 144 |
Graphene oxide/PVDF VIPS membranes for switchable, versatile and gravity-driven separation of oil and water Venault A, Chiang CH, Chang HY, Hung WS, Chang Y |
145 - 156 |
Preparation of polyamide thin film nanocomposite membranes containing silica nanoparticles via an in-situ polymerization of SiCl4 in organic solution Shen HM, Wang SH, Xu H, Zhou Y, Gao CJ |
157 - 168 |
Flow battery based on reverse electrodialysis with bipolar membranes: Single cell experiments Xia JB, Eigenberger G, Strathmann H, Nieken U |
169 - 178 |
Organic solvent nanofiltration (OSN) membranes made from plasma grafting of polyethylene glycol on cross-linked polyimide ultrafiltration substrates Gao ZF, Shi GM, Cui Y, Chung TS |
179 - 185 |
Electrophoretic fabrication of proton exchange membranes in fuel cells Fang FF, Zhao SX, Zhang W, Zhang CY, Min LF, Wang YX |
186 - 193 |
Zeolite-like MOF nanocrystals incorporated 6FDA-polyimide mixed-matrix membranes for CO2/CH4 separation Liu GP, Labreche Y, Chernikova V, Shekhah O, Zhang C, Belmabkhout Y, Eddaoudi M, Koros WJ |
194 - 202 |
Efficient biogas upgrading by a novel membrane-cryogenic hybrid process: Experiment and simulation study Song CF, Fan ZC, Li R, Liu QL, Kitamura Y |
203 - 212 |
Supported bicyclic amidine ionic liquids as a potential CO2/N-2 separation medium Schott JA, Do-Thanh CL, Mahurin SM, Tian ZQ, Onishi NC, Jiang DE, Dai S |
213 - 225 |
Effect of morphology on anion conductive properties in self-assembled polystyrene-based copolymer membranes Tuli SK, Roy AL, Elgammal RA, Tian MK, Zawodzinski TA, Fujiwara T |
226 - 232 |
Mixed matrix membranes composed of WS2 nanosheets and fluorinated poly (2,6-dimethyl-1,4-phenylene oxide) via Suzuki reaction for improved CO2 separation Geng ZM, Song QQ, Zhang XM, Yu B, Shen YQ, Cong HL |
233 - 240 |
Incorporating imidazolium-functionalized graphene oxide into imidazolium-functionalized poly(ether ether ketone) for enhanced hydroxide conductivity Li JZ, Zhang B, Wu H, Cao L, He XY, Li Y, Xu MZ, Jiang ZY |
241 - 253 |
Exploring the differences between forward osmosis and reverse osmosis fouling Siddiqui FA, She QH, Fane AG, Field RW |
254 - 265 |
Photothermal-enhanced and fouling-resistant membrane for solar-assisted membrane distillation Tan YZ, Wang H, Han L, Tanis-Kanbur MB, Pranav MV, Chew JW |
266 - 280 |
Development of high flux ultrafiltration polyphenylsulfone membranes applying the systems with upper and lower critical solution temperatures: Effect of polyethylene glycol molecular weight and coagulation bath temperature Plisko TV, Bildyukevich AV, Karslyan YA, Ovcharova AA, Volkov VV |
281 - 292 |
Metal-organic framework anchored sulfonated poly(ether sulfone) as a high temperature proton exchange membrane for fuel cells Anahidzade N, Abdolmaleki A, Dinari M, Tadavani KF, Zhiani M |
293 - 302 |
Functionalization of ultrafiltration membrane with polyampholyte hydrogel and graphene oxide to achieve dual antifouling and antibacterial properties Zhang W, Cheng W, Ziemann E, Be'er A, Lu XL, Elimelech M, Bernstein R |
303 - 310 |
Underwater superoleophobic-underoil superhydrophobic Janus ceramic membrane with its switchable separation in oil/water emulsions Ding D, Mao HY, Chen XF, Qiu MH, Fan YQ |
311 - 321 |
Vapor separation of methanol-dimethyl carbonate mixture on SAPO-34 zeolite membrane Wang MQ, Li M, Chang N, Gao LY, Wang MX, Zhang YF |
322 - 330 |
Novel high-flux polyamide/TiO2 composite nanofiltration membranes on ceramic hollow fibre substrates Li YX, Cao Y, Wang M, Xu ZL, Zhang HZ, Liu XW, Li Z |
331 - 341 |
Highly water-selective membranes based on hollow covalent organic frameworks with fast transport pathways Yang H, Cheng XP, Cheng XX, Pan FS, Wu H, Liu GH, Song YM, Cao XZ, Jiang ZY |
342 - 357 |
Effect of ceria loading on performance and durability of sulfonated poly (ether ether ketone) nanocomposite membranes for proton exchange membrane fuel cell applications Parnian MJ, Rowshanzamir S, Prasad AK, Advani SG |
358 - 369 |
High-flux CHA zeolite membranes for H-2 separations Mei WL, Du Y, Wu TY, Gao F, Wang B, Duan JG, Zhou JJ, Zhou RF |
370 - 379 |
Pebax/ionic liquid modified graphene oxide mixed matrix membranes for enhanced CO2 capture Huang GJ, Isfahani AP, Muchtar A, Sakurai K, Shrestha BB, Qin DT, Yamaguch D, Sivaniah E, Ghalei B |
380 - 389 |
Graphene oxide incorporated thin film nanocomposite membrane at low concentration monomers Zhao W, Liu HY, Meng N, Jian MP, Wang HT, Zhang XW |
390 - 401 |
Study on the formation of thin film nanocomposite (TFN) membranes of polymers of intrinsic microporosity and graphene-like fillers: Effect of lateral flake size and chemical functionalization Alberto M, Bhavsar R, Luque-Alled JM, Prestat E, Gao L, Budd PM, Vijayaraghavan A, Szekely G, Holmes SM, Gorgojo P |
402 - 410 |
How to select the optimal membrane distillation system for industrial applications Cassard HM, Park HG |
411 - 424 |
Development of Nb-Ti-Co alloy for high-performance hydrogen separating membrane Yan EH, Huang HR, Sun SH, Zou YJ, Chu HL, Sun LX |
425 - 438 |
Next generation in vitro liver model design: Combining a permeable polystyrene membrane with a transdifferentiated cell line Luetchford KA, Wung N, Argyle IS, Storm MP, Weston SD, Tosh D, Ellis MJ |
439 - 449 |
Hydrophilic and morphological modification of nanoporous polyethersulfone substrates for composite membranes in CO2 separation Wu DZ, Han Y, Salim W, Chen KK, Li JX, Ho WSW |
450 - 462 |
Effect of fouling on performance of pressure retarded osmosis (PRO) and forward osmosis (FO) Nagy E, Hegedus I, Tow EW, Lienhard VJH |
463 - 479 |
Improved conductivity and anti(bio)fouling of cation exchange membranes by AgNPs-GO nanocomposites Lopez-Cazares MI, Perez-Rodriguez F, Rangel-Mendez JR, Centeno-Sanchez M, Chazaro-Ruiz LF |
480 - 487 |
Nernst-Planck transport theory for (reverse) electrodialysis: III. Optimal membrane thickness for enhanced process performance Tedesco M, Hamelers HVM, Biesheuvel PM |