1 - 7 |
Fabrication of novel Pd-Ag-Ru/Al2O3 ternary alloy composite membrane with remarkably enhanced H-2 permeability Wang LS, Yoshiie R, Uemiya S |
8 - 15 |
Proton conductivity and methanol rejection by ceramic membranes derived from ferroxane and alumoxane precursors Tsui EM, Cortalezzi MM, Wiesner MR |
16 - 28 |
Materials dependence of mixed gas plasticization behavior in asymmetric membranes Visser T, Masetto N, Wessling M |
29 - 35 |
Catalytic dehydrogenation of ethylbenzene to styrene in a zeolite silicalite-1 membrane reactor Kong CL, Lu JM, Yang HH, Wang JQ |
36 - 46 |
Trimesoyl chloride crosslinked chitosan membranes for CO2/N-2 separation and pervaporation dehydration of isopropanol Xiao SD, Feng XS, Huang RYM |
47 - 55 |
Improved polybenzimidazole films for H3PO4-doped PBI-based high temperature PEMFC Lobato J, Canizares P, Rodrigo MA, Linares JJ, Aguilar JA |
56 - 65 |
Characterization of Pd-Ag membranes after exposure to hydrogen flux at high temperatures Bosko ML, Yepes D, Irusta S, Eloy P, Ruiz P, Lombardo EA, Cornaglia LM |
66 - 74 |
Diffusion of H through Pd membranes: Effects of non-ideality Flanagan TB, Wang D, Shanahan KL |
75 - 92 |
Pure and mixed gas CH4 and n-C4H10 permeability and diffusivity in poly (dimethylsiloxane) Raharjo RD, Freeman BD, Paul DR, Sarti GC, Sanders ES |
93 - 102 |
Dehydration of caprolactam-water mixtures through cross-linked PVA composite pervaporation membranes Zhang L, Yu P, Luo YB |
103 - 115 |
H-2 production from simulated coal syngas containing H2S in multi-tubular Pd and 80 wt% Pd-20 wt% Cu membrane reactors at 1173 K Iyoha O, Enick R, Killmeyer R, Howard B, Ciocco M, Morreale B |
116 - 124 |
Effects of molecular shape on osmotic reflection coefficients Bhalla G, Deen WM |
125 - 133 |
Deterministic model for matrix solidification in liquid-liquid thermally induced phase separation Hanks PL, Lloyd DR |
134 - 146 |
Flux enhancement in membrane distillation by fabrication of dual layer hydrophilic-hydrophobic hollow fiber membranes Bonyadi S, Chung TS |
147 - 158 |
Enhanced gas separation performance of dual-layer hollow fiber membranes via substructure resistance reduction using mixed matrix materials Widjojo N, Zhang SD, Chung TS, Liu Y |
159 - 165 |
Preparation of thin Pd-based composite membrane on planar metallic substrate - Part II. Preparation of membranes by electroless plating and characterization Li A, Grace JR, Lim CJ |
166 - 172 |
An experimental method to identify various oxygen species transported in oxides Dong Q |
173 - 185 |
Zeolite K-LTL-loaded sodium alginate mixed matrix membranes for pervaporation dehydration of aqueous-organic mixtures Bhat SD, Aminabhavi TM |
186 - 195 |
Non-equilibrium nanoblends via forced assembly for pervaporation separation of benzene from cyclohexane: UNIFAQ-FV group contribution calculations Nam SY, Dorgan JR |
196 - 208 |
Numerical simulations compared against experimental results for barrier membranes with lithographically printed flakes Goodyer CE, Bunge AL |
209 - 215 |
High permeability membranes for the dehydration of low water content ethanol by pervaporation Namboodiri VV, Vane LM |
216 - 227 |
Ultrathin, hydrogen-selective silica membranes deposited on alumina-graded structures prepared from size-controlled boehmite sols Gu YF, Oyama ST |
228 - 243 |
Numerical study of mass transfer in three-dimensional spacer-filled narrow channels with steady flow Fimbres-Weihs GA, Wiley DE |
244 - 252 |
Microfiltration of MS2 bacteriophage: Effect of ozone on membrane fouling Oh BS, Jang HY, Jung YJ, Kang JW |
253 - 260 |
Preparation and characterazition of poly(phthalazinone ether sulfone ketone) hollow fiber ultrafiltration membrane with high-molecular weight cut-off Jin Z, Yang DL, Zhang SH, Han XG |
261 - 266 |
Long-term hydrogen permeation tests of Pd-Cu-Ni/PNS with temperature cycles from room temperature to 773 K Ryi SK, Park JS, Kim SH, Kim DW, Moon JW |
267 - 276 |
Prediction of permeation behavior of CO2 and CH4 through silicalite-1 membranes in single-component or binary mixture systems using occupancy-dependent Maxwell-Stefan diffusivities Lee SC |
277 - 286 |
Assessing feasibility of polyarylate-clay nanocomposites towards improvement of gas selectivity Bhole YS, Wanjale SD, Kharul UK, Jog JP |
287 - 297 |
Sugarcane juice ultrafiltration: FTIR and SEM analysis of polysaccharide fouling Saha NK, Balakrishnan M, Ulbricht M |
298 - 306 |
Fabrication and characterization of improved PFSA/ePTFE composite polymer electrolyte membranes Tang HL, Wang XE, Pan M, Wang F |
307 - 317 |
Evaluation of cellulose-derived carbon molecular sieve membranes for hydrogen separation from light hydrocarbons Grainger D, Hagg MB |
318 - 328 |
Properties and performance of A-site deficient (Ba0.5Sr0.5)(1-x)Co0.8Fe0.2O3-delta for oxygen Ge L, Zhou W, Ran R, Liu S, Shao Z, Jin W, Xu N |
329 - 340 |
Simulation study of water gas shift reaction in a membrane reactor Brunetti A, Caravella A, Barbieri G, Drioli E |
341 - 348 |
A Monte Carlo simulation model for vacuum membrane distillation process Imdakm AO, Khayet M, Matsuura T |
349 - 354 |
Hydrogen-permeable membranes composed of zeolite nano-blocks Nishiyama N, Yamaguchi M, Katayama T, Hirota Y, Miyamoto M, Egashira Y, Ueyama K, Nakanishi K, Ohta T, Mizusawa A, Satoh T |
355 - 364 |
RO module RTD analyses based on directly processing conductivity signals Yang Q, Drak A, Hasson D, Serniat R |
365 - 365 |
Pervaporation of benzene/cyclohexane mixtures using ion-exchange membrane containing copper ions Lue SJ, Wang FJ, Hsiaw SY |