1095 - 1102 |
Pollutant destruction in a reverse-flow chromatographic reactor Jeong YO, Luss D |
1103 - 1111 |
Mass transfer characteristics of wire-mesh honeycomb reactors Jiang ZD, Chung KS, Kim GR, Chung JS |
1113 - 1124 |
Modeling of monolithic and trickle-bed reactors for the hydrogenation of styrene Nijhuis TA, Dautzenberg FM, Moulijn JA |
1125 - 1133 |
Semi-batch reactive crystallization of sodium perborate tetrahydrate: effect of mixing parameters on crystal size Mandare PN, Pangarkar VG |
1135 - 1146 |
Flow-rate effects in flow-reversal reactors: experiments, simulations and approximations Ben-Tullilah M, Alajem E, Gal R, Sheintuch M |
1147 - 1161 |
Transport equations for distillation of ethanol and water from the entropy production rate Kjelstrup S, de Koeijer GM |
1163 - 1176 |
Nitroxide-mediated radical polymerization of styrene in miniemulsion: model studies of alkoxyamine-initiated systems Ma JW, Smith JA, McAuley KB, Cunningham MF, Keoshkerian B, Georges MK |
1177 - 1190 |
Nitroxide mediated living radical polymerization of styrene in miniemulsion - modelling persulfate-initiated systems Ma JW, Cunningham MF, McAuley KB, Keoshkerian B, Georges M |
1191 - 1196 |
Unsteady mass transfer in the continuous phase around axisymmetric drops of revolution Favelukis M, Mudunuri RR |
1197 - 1205 |
Hydrodynamic modelling of binary mixture in a gas bubbling fluidized bed using the kinetic theory of granular flow Lu HL, He YR, Gidaspow D |
1207 - 1221 |
Control of a solution copolymerization reactor using multi-model predictive control Ozkan L, Kothare MV, Georgakis C |
1223 - 1233 |
Interfacial tensions of ethanol-carbon dioxide and ethanol-nitrogen. Dependence of the interfacial tension on the fluid density - prerequisites and physical reasoning Dittmar D, Fredenhagen A, Oei SB, Eggers R |
1235 - 1250 |
An analytical study of heat-transfer efficiency in laminar counterflow concentric circular tubes with external refluxes Ho CD, Yang WY |
1251 - 1269 |
Optimal moving and fixed grids for the solution of discretized population balances in batch and continuous systems: droplet breakage Attarakih MM, Bart HJ, Faqir NM |
1271 - 1288 |
Explicit numerical simulation of suspension flow with deposition in porous media: influence of local flow field variation on deposition processes predicted by trajectory methods Biggs MJ, Humby SJ, Buts A, Tuzun U |
1289 - 1300 |
Simultaneous kinetic resolution of chiral propylene oxide and propylene glycol in a continuous reactive distillation column Okasinski MJ, Doherty MF |
1301 - 1314 |
Adsorption of chlorinated hydrocarbons from aqueous solutions by wetted and non-wetted synthetic sorbents: dynamics Rexwinkel G, Berkhout JTAM, Heesink ABM |
1315 - 1322 |
Mechanism of deactivation of iron-molybdate catalysts prepared by coprecipitation and sol-gel techniques in methanol to formaldehyde oxidation Soares APV, Portela MF, Kiennemann A, Hilaire L |
1323 - 1336 |
An assessment of the conventional cake filtration theory Tien C, Bai RB |
1337 - 1351 |
Modeling the controlled release of microencapsulated drugs: theory and experimental validation Manca D, Rovaglio M |
1353 - 1363 |
Experimental study of drop size distributions at high phase ratio in liquid-liquid dispersions Desnoyer C, Masbernat O, Gourdon C |
1365 - 1372 |
A note on pressure drop for the cross-flow of power-law liquids and air/power law liquid mixtures past a bundle of circular rods Rao TVM, Chhabra RP |
1373 - 1380 |
Two-fluid model for counter-current dumped packing-containing columns Iliuta I, Grandjean BPA, Piche S, Larachi F |