317 - 318 |
Special issue - Fluid mixing Azzopardi B |
319 - 326 |
Solids suspension in three-phase stirred tanks Micale G, Carrara V, Grisafi F, Brucato A |
327 - 333 |
CFD study of homogenization with dual Rushton turbines -Comparison with experimental results part I: Initial studies Jaworski Z, Bujalski W, Otomo N, Nienow AW |
334 - 341 |
Observations on the distribution of energy dissipation in stirred vessels Ng K, Yianneskis M |
342 - 347 |
Gas-liquid mass transfer using surface-aeration in stirred vessels, with dual impellers Lines PC |
348 - 353 |
Visual 3-D modelling of stirred vessel mixing for an inclined-blade impeller Rahimi M, Senior PR, Mann R |
354 - 362 |
Macro-mixing and Streptomyces fradiae - Modelling oxygen and nutrient segregation in an industrial bioreactor Vlaev D, Mann R, Lossev V, Vlaev SD, Zahradnik J, Seichter P |
363 - 370 |
The transition from homogeneous to heterogeneous flow in a gassed, stirred vessel Gezork KM, Bujalski W, Cooke M, Nienow AW |
371 - 377 |
The influence of a lamellar structure upon the yield of a chemical reaction Clifford MJ, Cox SM, Roberts EPL |
378 - 388 |
Modelling and simulation of flow maldistribution in random packed columns with gas-liquid countercurrent flow Sun CG, Yin FH, Afacan A, Nandakumar K, Chuang KT |
389 - 396 |
A comparative assessment of the performance of the Kenics and SMX static mixers Rauline D, Le Blevec JM, Bousquet J, Tanguy PA |
397 - 403 |
Prediction of liquid holdup in countercurrent-flow rotating packed bed Lin CC, Chen YS, Liu HS |
404 - 418 |
Flow pattern, holdup and pressure drop in vertical and near vertical two- and three-phase upflow Spedding PL, Woods GS, Raghunathan RS, Watterson JK |
419 - 424 |
Comparison between models used in the determination of rheological parameters of suspensions with a helical screw impeller Zumalacarregui L, Valverde JL, Santana R, de Lucas A, Rodriguez L |
425 - 434 |
Measurement of gas hold-up profiles in bubble column by gamma ray tomography - Effect of liquid phase properties Veera UP, Joshi JB |
435 - 444 |
CFD simulation of particle distribution in stirred vessels Micale G, Montante G, Grisafi F, Brucato A, Godfrey J |
445 - 453 |
Power consumption in a double planetary mixer with non-Newtonian and viscoelastic materials Zhou G, Tanguy PA, Dubois C |
454 - 464 |
A method to draw fully thermally coupled distillation column configurations for multicomponent distillation Agrawal R |
465 - 472 |
Gas channelling and heat transfer in moving beds of spherical particles Crawshaw JP, Paterson WR, Scott DM |
473 - 480 |
Simplified methodology for calculating dump tank volumes McIntosh RD, Nolan PF, Rogers RL, Lindsay D |
481 - 491 |
Effect of process design/operation on the steady-state operability of a CSTR - Reactions A -> B -> C Gamboa-Torres AE, Flores-Tlacuahuac A |
492 - 498 |
Stability analysis of the ethylene dimerization reactor for the selective production of butene-1 Alhumaizi KI |
499 - 505 |
An experimental investigation into the motion of a single drop in a pulsed DC electric field Bailes PJ, Lee JGM, Parsons AR |