1 - 7 |
Steam stability of a silica membrane prepared by counter-diffusion chemical vapor deposition Nomura M, Aida H, Gopatakrishnan S, Sugawara T, Nakao S, Yamazaki S, Inada T, Iwamoto Y |
8 - 13 |
Solvent selection for manufacture of fluorinated polyimide composite membranes Qin JJ, Chung TS, Cao YM |
14 - 24 |
Zeolite-filled PMMA composite membranes: influence of coupling agent addition on gas separation properties Hu CC, Liu TC, Lee KR, Ruaan RC, Lai JY |
25 - 34 |
Modelling of water/organic vapor dehydration by glassy polymer membranes Salem A, Ghoreyshi AA |
35 - 42 |
A multicomponent transport model for dehydration of organic vapors by zeolite membranes Salem A, Ghoreyshi AA, Jahanshahi M |
43 - 50 |
Morphology and carbon dioxide transport properties of polyurethane blend membranes Kim MJ, Sea B, Youm KH, Lee KH |
51 - 57 |
Effects of oxidation curing on the permeation performances of polyphenylene oxide-derived carbon membranes Lee HJ, Yoshimune M, Suda H, Haraya K |
58 - 65 |
Ultra-thin asymmetric gas separation membranes of modified PEEK prepared by the dry-wet phase inversion technique Jansen JC, Buonomenna MG, Figoli A, Drioli E |
66 - 72 |
Gas transport properties of carbon molecular sieve membranes derived from metal containing sulfonated poly(phenylene oxide) Yoshimune M, Fujiwara I, Suda H, Haraya K |
73 - 81 |
The effect of oxygen membranes from enriched air obtained by gas separation the emission gas of diesel engines Byun H, Hong B, Lee B |
82 - 89 |
Modeling gas sorption in amorphous Teflon through the non equilibrium thermodynamics for glassy polymers (NET-GP) approach De Angelis MG, Doghieri F, Sarti GC, Freeman BD |
90 - 96 |
Facilitated transport of CO2 through polyvinylamine/polyethlene glycol blend membranes Yi CH, Wang Z, Li M, Wang JX, Wang SC |
97 - 102 |
Comparison of SiO2-ZrO2-50% and commercial SiO2 membranes on the pervaporative dehydration of organic solvents Urtiaga A, Casado C, Asaeda M, Ortiz I |
103 - 108 |
Effect of residual sugars in fermentation broth on pervaporation flux and selectivity for ethanol Aroujalian A, Belkacemi K, Davids SJ, Turcotte G, Pouliot Y |
109 - 118 |
Application of poly(ethylene terephthalate)-graft-polystyrene membranes in pervaporation Khayet M, Nasef MM, Mengual JI |
119 - 128 |
Separation of ethanol/water mixtures by pervaporation through zeolite-filled polysulfone membrane containing 3-aminopropyltrimethoxysilane Fu YJ, Hu CC, Lee KR, Lai JY |
129 - 136 |
Study of the separation properties of chitosan/polysulfone composite hollow-fiber membranes Tsai HA, Chen HC, Lee KR, Lai JY |
137 - 143 |
Separation of xylene mixtures using polyurethane-zeolite composite membranes Lue SJ, Liaw TH |
144 - 151 |
Permselectivities of 3,3',4,4' benzhydrol tetraacarboxylic dianhydride based polyimide membrane for pervaporation Teng MY, Li CL, Lee KR, Lai JY |
152 - 159 |
Optimum design of PV processes for dehydration of organic mixtures Gomez P, Ibanez R, Ortiz I, Grossmann I |
160 - 165 |
Bergamot essential oil extraction by pervaporation Figoli A, Donato L, Camevale R, Tundis R, Statti GA, Menichini F, Drioli E |
166 - 170 |
Effect of pervaporation module structure on separation performance Zhang L, Huang JX, Zhou ZJ, Chen HL, Pan ZR |
171 - 181 |
Chitosan-poly (vinyl alcohol)/poly (acrylonitrile) (CS-PVA/PAN) composite pervaporation membranes for the separation of ethanol-water solutions Li BB, Xu ZL, Qusay FA, Li R |
182 - 192 |
Pervaporation of benzene/cyclohexane mixtures through poly(vinyl alcohol) membranes with and without beta-cyclodextrin Peng FB, Jiang ZY, Hu CL, Wang YQ, Lu LY, Wu H |
193 - 201 |
Preparation and pervaporation of a palygorskite/polyacrylamide inorganic-organic hybrid membrane for separating m-/p-xylene isomers Yang Y, Qian JW, Xuan LJ, An AF, Zhang L, Gao CJ |
202 - 210 |
Preparation of poly(vinyl alcohol)-sodium alginate hollow-fiber composite membranes and pervaporation dehydration characterization of aqueous alcohol mixtures Dong YQ, Zhang L, Shen JN, Song MY, Chen HL |
211 - 214 |
Gas permeation properties of carbon molecular sieve membranes dispersed with palladium nano particles via supercritical CO2 impregnation Suda H, Yoda S, Hasegawa A, Tsuji T, Otake K, Haraya K |
215 - 223 |
Moments method applied to the in-situ characterisation of normal butane mass transfer in MFI zeolite membranes Courthial L, Baudot A, Jolimaitre E, Tayakout M, Jallut C |
224 - 229 |
High flux palladium-copper composite membranes for hydrogen separations Thoen PM, Roa F, Way JD |
230 - 235 |
Preparation of a multi-membrane module for high-temperature hydrogen separation Gopalakrishnan S, Nomura M, Sugawara T, Nakao S |
236 - 243 |
Mechanical properties and structural stability of perovskite-type, oxygen-permeable, dense membranes Lee S, Woo SK, Lee KS, Kim DK |
244 - 251 |
Pervaporation of an aqueous ethanol solution through hydrophilic zeolite membranes Ahn H, Lee H, Lee SB, Lee Y |
252 - 255 |
Preparation and gas permeation properties of silicon carbide-based inorganic membranes for hydrogen separation Suda H, Yamauchi H, Uchimaru Y, Fujiwara I, Haraya K |
256 - 259 |
Preparation and characterization of ultrathin alumina hollow fiber microfiltration membrane Choi IH, Kim IC, Min BR, Lee KH |
260 - 266 |
Enzymatic synthesis of sugar esters in organic solvent coupled with pervaporation Sakaki K, Aoyama A, Nakane T, Ikegami T, Negishi H, Watanabe K, Yanagishita H |
267 - 279 |
Analysis of safety aspects in a membrane reactor Chiappetta G, Clarizia G, Drioli E |
280 - 285 |
New hydrophobic membranes for contactor processes - Applications to isothermal concentration of solutions Romero J, Draga H, Belleville MP, Sanchez J, Combe-James C, Dornier M, Rios GM |
286 - 290 |
Gas absorption in a hollow-fiber membrane contactor with pseudo-plastic liquid as an absorbent Todorovic J, Krstic DM, Vatai GN, Tekic MN |
291 - 298 |
Selective pertraction of isomers using membranes having fixed cyclodextrin as molecular recognition sites Touil S, Tingry S, Bouchtalla S, Deratani A |
299 - 303 |
Effect of heat cross-linking on carbon dioxide fixed-carrier membrane structure and performance Zhang Y, Wang Z, Wang JX, Wang SC |
304 - 312 |
Facilitated transport of organic acid through a supported liquid membrane with a carrier Park SW, Choi BS, Kim SS, Lee JW |
313 - 320 |
CO2 facilitated transport through an acrylamide and maleic anhydride copolymer membrane Wu LG, Shen JN, Chen HL, Gao CJ |
321 - 326 |
Transport of silver metal ions through a liquid membrane gel using a solvating extractant (TOPO) Taoualit N, Hadj-Boussaad DE |
327 - 334 |
Selective permeation of CO2 through a composite membrane with a separation layer of 2-N,N-dimethyl aminoethyl methacrylate and acrylic acid copolymer Shen JN, Wu LG, Zhang L, Dong YQ, Chen HL, Gao CJ |
335 - 343 |
Concentration of aqueous ethanol solutions by porous poly(dimethylsiloxane) membranes during temperature-difference controlling evapomeation Uragami T |
344 - 349 |
Reservoir water treatment using hybrid coagulation-ultrafiltration Qin HJ, Oo MH, Kekre KA, Knops F, Miller P |
350 - 360 |
Nitrate removal from contaminated water using polyelectrolyte-enhanced ultrafiltration Zhu XS, Choo KH, Park JM |
361 - 366 |
Adsorptive membranes vs. resins for acetic acid removal from biomass hydrolysates Han B, Carvalho W, Canilha L, da Silva SS, Silva JBAE, McMillan JD, Wickramasinghe SR |
367 - 374 |
Microfiltration membrane of polymer blend of poly(L-lactic acid) and poly(epsilon-caprolactone) Tanaka T, Tsuchiya T, Takahashi H, Masayuki T, Lloyd DR |
375 - 380 |
Membrane processes for the efficient recovery of anionic pollutants Ortiz I, Bringas E, Samaniego H, San Roman F, Urtiaga A |
381 - 386 |
Preparation of W/O emulsions by membrane emulsification with a mullite ceramic membrane Wu J, Jing WH, Xing WH, Xu NP |
387 - 397 |
Proton conductivity and characterization of novel composite membranes for medium-temperature fuel cells Ahmad MI, Zaidi SMJ, Rahman SU |
398 - 404 |
Water sorption and diffusion in a short-side-chain perfluorosulfonic acid ionomer membrane for PEMFCS: effect of temperature and pre-treatment De Angelis MG, Lodge S, Baschetti MG, Sarti GC, Doghieri F, Sanguineti A, Fossati P |
405 - 410 |
Use of cation-exchange membranes for simultaneous recovery of lead and EDTA during electrokinetic extraction Amrate S, Akretche DE, Innocent C, Seta P |
411 - 421 |
Influence of voltage and flow rate on electrodeionization (EDI) process efficiency Bouhidel KE, Lakehal A |
422 - 425 |
Use of membranes in copper hydrometallurgy Sabba N, Akretche DE |