857 - 867 |
A reduced mechanism for methanol oxidation in supercritical water Brock EE, Savage PE, Barker JR |
869 - 877 |
Self-diffusion of water in thermoreversible gels near volume transition : Model development and PFG NMR investigation Ray SS, Rajamohanan PR, Badiger MV, Devotta I, Ganapathy S, Mashelkar RA |
879 - 890 |
Hydrodynamic and colloidal interactions effects on the rejection of a particle larger than a pore in microfiltration and ultrafiltration membranes Bowen WR, Sharif AO |
891 - 898 |
On the mechanism of microbial cell disruption in high-pressure homogenisation Kleinig AR, Middelberg APJ |
899 - 917 |
Membrane-based solvent extraction in multicomponent systems Kubaczka A, Burghardt A, Mokrosz T |
919 - 931 |
Monte Carlo simulations of self-sustained oscillations of CO oxidation over non-isothermal supported catalysts Qin F, Tagliabue L, Piovesan L, Wolf EE |
933 - 946 |
Study on diffusion-reaction process inside a cylindrical catalyst pellet Pan TS, Zhu BC |
947 - 950 |
A simple analysis of heat transfer near an oscillating interface Chen ZD, Chen JJJ |
951 - 961 |
Analysis of the fluidization process of particle beds at high temperature Formisani B, Girimonte R, Mancuso L |
963 - 976 |
Influence of multicomponent mass transfer on homogeneous azeotropic distillation Castillo FJL, Towler GP |
977 - 993 |
Rise velocity of a Taylor bubble through concentric annulus Das G, Das PK, Purohit NK, Mitra AK |
995 - 1007 |
Dynamic modelling of a biogas tower reactor Pahl M, Lunze J |
1009 - 1013 |
Stability and integrity enforcement by integrating variable pairing and controller design Zhu ZX |
1015 - 1025 |
Liquid hold-up and backmixing in cocurrent upflow three-phase fixed-bed reactors Cassanello M, Martinez O, Cukierman AL |
1027 - 1039 |
Analysis of reactive melt infiltration in the processing of ceramics and ceramic composites Einset EO |
1041 - 1047 |
Simple new EOS mixing rules which incorporate lattice fluid excess functions Brandani F, Brandani S, Brandani V |
1049 - 1058 |
Gas transport in porous Vycor glass subjected to gradual pore narrowing Fernandes NE, Gavalas GR |
1059 - 1066 |
A population balance model for disperse systems : Drop size distribution in emulsion Chen Z, Pruss J, Warnecke HJ |
1067 - 1075 |
The production of diacetone alcohol with catalytic distillation - Part I : Catalytic distillation experiments Podrebarac GG, Ng FTT, Rempel GL |
1077 - 1088 |
The production of diacetone alcohol with catalytic distillation - Part II : A rate-based catalytic distillation model for the reaction zone Podrebarac GG, Ng FTT, Rempel GL |
1089 - 1095 |
A study of gas-liquid mass transfer in reactors with two disk turbines Wu H, Arcella V, Malavasi M |
1097 - 1101 |
Particle disruption of precipitated CaCO3 crystal agglomerates in turbulently agitated suspensions Wojcik JA, Jones AG |
1103 - 1105 |
Crystallization of fatty acids using binodal regions of two liquid phases Maeda K, Nomura Y, Guzman LA, Hirota S |
1107 - 1109 |
Flow between nested regular polygonal ducts Wang CY |