977 - 987 |
Computation of the flow and reactive mixing in dual-Rushton ethoxylation reactor Chiu YN, Naser J, Ngian KF, Pratt KC |
988 - 996 |
Influence of filtration superficial velocity on cake compression and cake formation Chen YS, Hsiau SS |
997 - 1003 |
The microwave processing of wood using a continuous microwave belt drier Vongpradubchai S, Rattanadecho P |
1004 - 1011 |
Conventional and modified fluidized bed: Comparison of the fluid dynamics and application in particle granulation da Cunha RLG, Pereira MMC, Rocha SCS |
1012 - 1019 |
Mixing in milli torus reactor under aerated conditions Rihani R, Legrand J, Bensmaili A |
1020 - 1029 |
Separation of isopropyl alcohol-water mixtures by pervaporation using crosslink IPN membranes Singha NR, Kar S, Ray S, Ray SK |
1030 - 1039 |
Phase distribution measurements in metallic foam packing using X-ray radiography and micro-tomography Calvo S, Beugre D, Crine M, Leonard A, Marchot R, Toye D |
1040 - 1046 |
Steady-state biofilter performance under non-isothermal conditions Shareefdeen Z, Shaikh AA, Ahmed A |
1047 - 1060 |
Integrated solvent and process selection for separation and reactive separation systems Papadopoulos AI, Linke P |
1061 - 1071 |
Interfacial polycondensation of polyarylate in Taylor-Couette-Reactor Wolinski J, Wronski S |
1072 - 1079 |
Technical and economical feasibility of zeolite NaA membrane-based reactors in liquid-phase etherification reactions Pera-Titus M, Llorens J, Cunill F |
1080 - 1087 |
Catalytic distillation for simultaneous hydrolysis of methyl acetate and etherification of methanol Dirk-Faitakis CB, An WZ, Lin TB, Chuang KT |