| 4125 - 4136 |
A new kinetic model for the NO-carbon reaction
Li YH, Radovic LR, Lu GQ, Rudolph V |
| 4137 - 4144 |
Tracer dispersion in packings of porous activated carbon grains
Drazer G, Chertcoff R, Bruno L, Rosen M, Hulin JP |
| 4145 - 4164 |
Screening models for batch process development Part I. Design targets for reaction/distillation networks
Allgor RJ, Evans LB, Barton PI |
| 4165 - 4178 |
A mathematical model of the self-heating of spray-dried food powders containing fat, protein, sugar and moisture
Chong LV, Chen XD |
| 4179 - 4187 |
The onset of convection induced by buoyancy during gas diffusion in deep fluids
Tan KK, Thorpe RB |
| 4189 - 4197 |
Solid acid catalysed acylation of 2-methoxy-naphthalene: role of intraparticle diffusional resistance
Yadav GD, Krishnan MS |
| 4199 - 4209 |
Evaluation of effective thermal conductivity from the structure of a packed bed
Cheng GJ, Yu AB, Zulli P |
| 4211 - 4222 |
The influence of impeller type on mean drop size and drop size distribution in an agitated vessel
Pacek AW, Chamsart S, Nienow AW, Bakker A |
| 4223 - 4232 |
Kinetics of oxidation of ferrous sulfate with molecular oxygen
Ronnholm MR, Warna J, Salmi T, Turunen I, Luoma M |
| 4233 - 4243 |
Heat and mass transfer in fixed-bed drying
Wang ZH, Chen GH |
| 4245 - 4256 |
Scale-up of Rushton turbine-agitated tanks
Wernersson ES, Tragardh C |
| 4257 - 4265 |
Effect of solute parameters on wick action in concrete
Puyate YT, Lawrence CJ |
| 4267 - 4271 |
Approximate high flux corrections for multicomponent mass transfer models and some explicit methods
Alopaeus V, Aittamaa J, Norden HV |
| 4273 - 4284 |
Suspended solids distribution in agitated, baffled vessels containing three concentric cooling coils
Skelland AHP, Hassan NM |
| 4285 - 4291 |
Concentration dependence of diffusion-adsorption rate in activated carbon
Drazer G, Chertcoff R, Bruno L, Rosen M |
