2821 - 2829 |
Deep desulfurization of diesel oil: kinetic studies and process-improvement by the use of a two-phase reactor with pre-saturator Schmitz C, Datsevitch L, Jess A |
2831 - 2839 |
Extremes of conversion in continuous-flow reactors Buffham BA, Nauman EB |
2841 - 2852 |
The effect of seed preparation on the chirality of the secondary nuclei Qian RY, Botsaris GD |
2853 - 2861 |
A versatile flow visualisation technique for quantifying mixing in a binary system: application to continuous supercritical water hydrothermal synthesis (SWHS) Blood PJ, Denyer JP, Azzopardi BJ, Poliakoff M, Lester E |
2863 - 2879 |
Residue curve maps of reactive membrane separation Huang YS, Sundmacher K, Qi ZW, Schlunder EU |
2881 - 2890 |
Propylene glycol and ethylene glycol recovery from aqueous solution via reactive distillation Dhale AD, Myrant LK, Chopade SP, Jackson JE, Miller DJ |
2891 - 2898 |
Investigation of phase trapping by secondary imbibition within Fontainebleau sandstone Holmes WA, Packer KJ |
2899 - 2912 |
Simulation of algae growth in a bench scale internal loop airlift reactor Wu XX, Merchuk JC |
2913 - 2920 |
New approach to the formulation of hydrogel beads by emulsification/thermal gelation using a static mixer Belyaeva E, Della Valle D, Neufeld RJ, Poncelet D |
2921 - 2928 |
Conjugate heat and mass transfer process within porous media with dielectric cores in microwave freeze drying Wu HW, Tao Z, Chen GH, Deng HW, Xu GQ, Ding ST |
2929 - 2936 |
Convective diffusion of particles deposition under electrostatics from turbulently-mixed conditions Lai ACK, Yu SCM, Chen FZ |
2937 - 2945 |
Artificial neural network based modelling of head and power characteristics of pump-mixer Singh KK, Shenoy KT, Mahendra AK, Ghosh SK |
2947 - 2960 |
The effects of diffusion mechanism and void structure on transport rates and tortuosity factors in complex porous structures Zalc JM, Reyes SC, Iglesia E |
2961 - 2968 |
Distribution of particles during solvent evaporation from films Routh AF, Zimmerman WB |
2969 - 2982 |
Gas displacing liquids from tubes: high capillary number flow of a power law liquid including inertia effects Polynkin A, Pittman JFT, Sienz J |
2983 - 2993 |
Determination of the intrinsic rate constant and activation energy of CO2 gas hydrate decomposition using in-situ particle size analysis Clarke MA, Bishnoi PR |
2995 - 3006 |
Statistical monitoring of dynamic processes based on dynamic independent component analysis Lee JM, Yoo C, Lee IB |
3007 - 3012 |
On a segregation intensity parameter in continuous-velocity lattice gas cellular automata for immiscible binary fluid Kitakawa A |
3013 - 3020 |
General solution of the dispersion model for a one-dimensional stirred flow system using Danckwerts' boundary conditions Kudrna V, Jahoda M, Siyakatshana N, Cermakova J, Machon V |
3021 - 3028 |
Superior mixing performance for airlift reactor with a net draft tube Fu CC, Lu SY, Hsu YJ, Chen GC, Lin YR, Wu WT |
3029 - 3036 |
Correction of the secondary flow effect for binary diffusion coefficients using coated/uncoated diffusion columns Funazukuri T, Kong CY, Kagei S |
3037 - 3040 |
Wall effects for the pressure drop in fixed beds Di Felice R, Gibilaro LG |
3041 - 3043 |
Comments on "A mechanistic model to determine the critical flow velocity required to initiate the movement of spherical bed particles in inclined channels" by A. Ramadan, P. Skalle and S.T. Johansen -(Chemical Engineering Science 2003, 58 2153-2163) Stevenson P |