259 - 269 |
Mass transfer and kinetics of the three-phase hydrogenation of a dinitrile over a Raney-type nickel catalyst Hoffer BW, Schoenmakers PHJ, Mooijman PRA, Hamminga GM, Berger RJ, van Langeveld AD, Moulijn JA |
271 - 281 |
Simultaneous measurement of flow pattern and mass transfer coefficient in bubble columns Kulkarni AA, Joshi JB |
283 - 297 |
Modeling of volatile organic compounds condensation in fluidized bed Yazbek W, Delebarre A |
299 - 311 |
Investigations in mass transfer enhancement in textiles with ultrasound Moholkar VS, Warmoeskerken MMCG |
313 - 327 |
Optimization of batch cooling crystallization Choong KL, Smith R |
329 - 343 |
Novel strategies for optimization of batch, semi-batch and heating/cooling evaporative crystallization Choong KL, Smith R |
345 - 358 |
Simulation of aerosol dynamics and transport in chemically reacting particulate matter laden flows. Part I: Algorithm development and validation Kommu S, Khomami B, Biswas P |
359 - 371 |
Simulation of aerosol dynamics and transport in chemically reacting particulate matter laden flows. Part II: Application to CVD reactors Kommu S, Khomami B, Biswas P |
373 - 383 |
Immobilized lipase-catalysed esterification and transesterification reactions in non-aqueous media for the synthesis of tetrahydrofurfuryl butyrate: comparison and kinetic modeling Yadav GD, Devi KM |
385 - 396 |
Multiobjective optimization of an industrial grinding operation using elitist nondominated sorting genetic algorithm Mitra K, Gopinath R |
397 - 405 |
Kinetic model for lactose hidrolysis in a recirculation hollow-fibre bioreactor Jurado E, Camacho F, Luzon G, Vicaria JM |
407 - 415 |
Creeping motions of a composite sphere in a concentric spherical cavity Keh HJ, Chou J |
417 - 424 |
Purely viscous flow of a shear-thinning fluid between two rotating spheres Lee E, Ming JK, Hsu JP |
425 - 435 |
Distinct element modelling of non-spherical frictionless particle flow Langston PA, Al-Awamleh MA, Fraige FY, Asmar BN |
437 - 447 |
Numerical simulation of particle motion in vibrated fluidized bed Tatemoto Y, Mawatari Y, Yasukawa T, Noda K |
449 - 457 |
Modeling axial distributions of adsorbent particle size and local voidage in expanded bed Yun JX, Yao SJ, Lin DQ, Lu MH, Zhao WT |
459 - 478 |
Design and optimisation of batch and semi-batch reactors Zhang JH, Smith R |
479 - 483 |
Approximate model for diffusion and reaction in a porous pellet and an effectiveness factor Szukiewicz M, Petrus R |
485 - 485 |
Letter to the editor Moo-Young M |
487 - 487 |
Letter to the editor Jones JC |