| 435 - 444 |
A study of gain scheduling control applied to an exothermic CSTR
Lagerberg A, Breitholtz C |
| 445 - 454 |
Caprolactam production: a comparison of different layouts of the liquid-liquid extraction section
Alessi V, Penzo R, Slater MJ, Tessari R |
| 455 - 461 |
Comparison of two-phase upflow and downflow fixed bed reactors performance: Catalytic SO2 oxidation
Iliuta I, Iliuta MC |
| 462 - 468 |
Oxidation of aqueous sulfide solutions by dioxygen .1. Autoxidation reaction
Fischer H, SchulzEkloff G, Wohrle D |
| 469 - 474 |
Influence of dust particles on the hydrodynamic behavior and mass transfer in droplet column
Muller N, Benadda B, Otterbein M |
| 475 - 477 |
Prediction of settling velocity of drops in a concentrated batch liquid-liquid dispersion
Das PK |
| 478 - 484 |
Effect of two-pass trays on distillation efficiencies
Klemola KT, Ilme JK |
| 485 - 490 |
Modeling of multi-solid liquid fluidized bed
Asif M |
| 491 - 494 |
Slip velocity characteristics in the riser of circulating fluidised bed
Subramanian NB, Kannan CS |
| 495 - 501 |
Application of mathematical modelling in a two-component layer crystallisation process
Guardani R, Belline A |
| 502 - 509 |
Models for minimum explosible concentration of organic dust clouds handled in industries
Mittal M |
