2167 - 2179 |
Ten years of sustainability: where do we go from here Batterham RJ |
2181 - 2202 |
Particle residence time distributions in circulating fluidised beds Harris AT, Davidson JF, Thorpe RB |
2203 - 2214 |
Multiple steady states in two-phase reactors under boiling conditions Waschler R, Pushpavanam S, Kienle A |
2215 - 2227 |
Uniformity in a thin-zone multi-pulse TAP experiment: numerical analysis Phanawadee P, Shekhtman SO, Jarungmanorom C, Yablonsky GS, Gleaves JT |
2229 - 2244 |
Chemical kinetics of alkaline peroxide brightening of mechanical pulps Liu SJ |
2245 - 2253 |
Measurement of liquid film thickness and the determination of spin-up radius on a rotating disc using an electrical resistance technique Burns JR, Ramshaw C, Jachuck RJ |
2255 - 2267 |
Gas-solid adsorption of selected volatile organic compounds on titanium dioxide Degussa P25 Demeestere K, Dewulf J, Van Langenhove H, Sercu B |
2269 - 2281 |
Modelling and design of thin-film slurry photocatalytic reactors for water purification Puma GL, Yue PL |
2283 - 2296 |
Optimisation of fed-batch bioreactors using genetic algorithms Sarkar D, Modak JM |
2297 - 2311 |
Low frequency macroinstabilities in a stirred tank: scale-up and prediction based on large eddy simulations Roussinova V, Kresta SM, Weetman R |
2313 - 2323 |
Measurement of lyophilisation primary drying rates by freeze-drying microscopy Zhai S, Taylor R, Sanches R, Slater NKH |
2325 - 2338 |
Application of the general rate model with the Maxwell-Stefan equations for the prediction of the band profiles of the 1-indanol enantiomers Kaczmarski K, Gubernak M, Zhou DM, Guiochon G |
2339 - 2350 |
Lipase-catalysed hydrolysis of blackcurrant oil in supercritical carbon dioxide Sovova H, Zarevucka M |
2351 - 2363 |
A numerical procedure for calculating droplet deformation in dispersing flows and experimental verification Feigl K, Kaufmann SFM, Fischer P, Windhab EJ |
2365 - 2376 |
Interfacial area and volumetric mass transfer coefficient in a bubble reactor at elevated pressures Maalej S, Benadda B, Otterbein A |
2377 - 2388 |
Multicomponent mass transfer across water films during hydrocarbon gas injection Bijeljic B, Muggeridge AH, Blunt MJ |
2389 - 2401 |
Model predictive control relevant identification and validation Huang B, Malhotra A, Tamayo EC |
2403 - 2408 |
Catalyst surface at a fractal of cost - a quest for optimal catalyst loading Phillips C, Ben-Richou A, Ambari A, Fedorov A |
2409 - 2419 |
Multiscale fluid transport theory for swelling biopolymers Singh PP, Cushman JH, Maier DE |
2421 - 2432 |
An experimental investigation of the convective instability of a jet Chauhan A, Maldarelli C, Rumschitzki DS, Papageorgiou DT |
2433 - 2440 |
Approximate formulas for nonlinear diffusion and adsorption of a spherical particle Hsuen HK |
2441 - 2443 |
Comments on bubble rising velocity in non-Newtonian liquids Dziubinski M, Orczykowska M, Budzynski P |
2445 - 2447 |
Morphology of conducting polymeric coatings: quantitative comparison between theory and experiment Lin B, Sureshkumar R, Kardos JL |
2449 - 2454 |
Experimental validation of a correlation-based model for permeability Adrover A, Giona M |
2455 - 2459 |
Mass transfer time in a deep bubble bed Nedeltchev S, Ookawara S, Ogawa K |
2461 - 2463 |
Comments on "Gas permeation through a glassy polymer membrane: Chemical potential gradient or dual mobility model?" by M.A. Islam and H. Buschatz [Chemical Engineering Science 57 (2002) 2089-2099 Koros W, Madden W |