1 - 9 |
Effect of bubble contamination on rise velocity and mass transfer Alves SS, Orvalho SP, Vasconcelos JMT |
11 - 25 |
Prediction of aggregation kinetics based on surface properties of nanoparticles Schwarzer HC, Peukert W |
27 - 40 |
Numerical study of cluster and particle rebound effects in a circulating fluidised bed Helland E, Occelli R, Tadrist L |
41 - 55 |
The continuous self stirred tank reactor: measurement of the cracking kinetics of biomass pyrolysis vapours Baumlin S, Broust F, Ferrer M, Meunier N, Marty E, Lede J |
57 - 72 |
Critical comparison of hydrodynamic models for gas-solid fluidized beds - Part I: bubbling gas-solid fluidized beds operated with a jet Patil DJ, Annaland MV, Kuipers JAM |
73 - 84 |
Critical comparison of hydrodynamic models for gas-solid fluidized beds - Part II: freely bubbling gas-solid fluidized beds Patil DJ, Annaland AV, Kuipers JAM |
85 - 94 |
Experimental investigation of phase inversion in a stirred vessel using LIF Liu L, Matar OK, de Ortiz ESP, Hewitt GF |
95 - 102 |
Spray-dried ceramic powders: A quantitative correlation between slurry characteristics and shapes of the granules Bertrand G, Roy P, Filiatre C, Coddet C |
103 - 109 |
Indoor air purification by photocatalyst TiO2 immobilized on an activated carbon filter installed in an air cleaner Ao CH, Lee SC |
111 - 122 |
Oscillatory flow and axial dispersion in packed beds of spheres Crittenden BD, Lau A, Brinkmann T, Field RW |
123 - 134 |
Stagnation-point flows in a porous medium Wu Q, Weinbaum S, Andreopoulos Y |
135 - 149 |
Charged droplet and particle-mixing studies in liquid-liquid systems in the presence of non-linear electrical fields Petera J, Strzelecki W, Agrawal D, Weatherley LR |
151 - 166 |
Mass transfer enhancement in the Membrane Aromatic Recovery System (MARS): theoretical analysis Ferreira FC, Peeva LG, Livingston AG |
167 - 177 |
Effect of recycle-barrier location on membrane extraction in a parallel-flow rectangular module with internal reflux Yeh HM, Hung FC, Chen CH, Hung CR |
179 - 186 |
An improved model for bubble formation using the boundary-integral method Xiao ZY, Tan RBH |
187 - 199 |
Transport property measurements in sheared granular flows Hsiau SS, Yang WL |
201 - 211 |
Purification of polycrystalline e-caprolactam particles van der Gun MA, Bruinsma OSL, Jansens PJ |
213 - 218 |
A generalized approach to model oxygen transfer in bioreactors using population balances and computational fluid dynamics Dhanasekharan KM, Sanyal J, Jain A, Haidari A |
219 - 230 |
Velocity and concentration field measurements in a turbulent, impinging flammable jet Birch AD, Cleaver RP, Fairweather M, Hargrave GK |
231 - 238 |
Drop breakage model in static mixers at low and intermediate Reynolds number Das PK, Legrand J, Morancais P, Carnelle G |
239 - 253 |
Neural network model-based predictive control of liquid-liquid extraction contactors Mjalli FS |
255 - 268 |
Targeting and design of water networks for fixed flowrate and fixed contaminant load operations Prakash R, Shenoy UV |
269 - 277 |
Errors associated with swelling in the analysis of polymer-solvent diffusion measurements Altinkaya SA |
279 - 288 |
Fault identification for process monitoring using kernel principal component analysis Cho JH, Lee JM, Choi SW, Lee D, Lee IB |
289 - 292 |
Measurement of the size, shape and orientation of convex bodies Brown DJ, Vickers G, Collier AP, Reynolds GK |
293 - 298 |
Lorentz force influence on momentum and mass transfer in natural convection copper electrolysis Weier T, Huller R, Gerbeth G, Weiss FP |
299 - 300 |
Reply to the comments by D. Stevenson on "Physical insight into the Ergun and Wen and Yu equations for fluid flow in packed and fluidised beds" by RK Niven [Chemical Engineering Science, 57 (2002), 527-534] Niven RK |