2117 - 2128 |
Structure-flow correlations in packed beds Sederman AJ, Johns ML, Alexander P, Gladden LF |
2129 - 2134 |
Controlling particle size by self-sustained oscillations in continuous emulsion polymerization of vinyl acetate Ohmura N, Kataoka K, Watanabe S, Okubo M |
2137 - 2142 |
Simulation of imperfect micromixing for first-order adiabatic reactions : the coalescence-dispersion model Sheikh F, Vigil RD |
2143 - 2151 |
Partitioning of styrene, butyl acrylate and methacrylic acid in emulsion systems Santos AM, Guillot J, McKenna TF |
2153 - 2166 |
A Maxwell-Stefan approach to modelling the cross-flow ultrafiltration of protein solutions in tubular membranes Bellara SR, Cui ZF |
2167 - 2176 |
Influence of pressure, fluidization velocity and particle size on the hydrodynamics of a freely bubbling fluidized bed Wiman J, Almstedt AE |
2177 - 2185 |
Agglomeration gibbsite Al(OH)(3) crystals in Bayer liquors. Influence of the process parameters Seyssiecq I, Veesler S, Boistelle R, Lamerant JM |
2187 - 2194 |
Micromixing of solids and fluid in an aggregating precipitator Wynn EJW, Hounslow MJ, Ilievski D |
2195 - 2210 |
Kinetically induced multiplicity of steady states in integral catalytic reactors Nibbelke RH, Hoebink JHBJ, Marin GB |
2211 - 2218 |
Water flow in filter paper and capillary suction time Smiles DE |
2219 - 2229 |
Evidence for in-line bubble interactions in non-Newtonian fluids Li HZ, Mouline Y, Funfschilling D, Marchal P, Choplin L, Midoux N |
2231 - 2239 |
Small-angle light scattering study of droplet break-up in emulsions and polymer blends Mewis J, Yang H, Van Puyvelde P, Moldenaers P, Walker LM |
2241 - 2256 |
Modelling of the glass transition temperature of free radical copolymers : An approach for control purposes Fevotte G, McKenna TF, Santos AM |
2257 - 2268 |
Numerical and experimental network study of evaporation in capillary porous media. Drying rates Laurindo JB, Prat M |