| 305 - 313 |
A new effective combination of a thin-film extractor and gravity setter
Berman Y, Tamir A |
| 314 - 321 |
Flow of solids in an interconnected fluidized beds system investigated using positron emission particle tracking
Stellema CS, Gerritsen AW, Kolar ZI, de Goeij JJM, van den Bleek CM |
| 322 - 328 |
Comparison of experimental results and numerical predictions of drop diameter from a single submerged nozzle in a liquid-liquid system
Hamad FA, Khan MK, Pierscionek BK, Bruun HH |
| 329 - 340 |
Modelling of transient mass transfer in liquid and liquid-solid pulsating systems: Applications and extension to heat transfer
Maucci E, Martinuzzi RJ, Briens CL, Wild G |
| 341 - 348 |
Diffusion and reactivity of gas oil in FCC catalysts
Al-Khattaf S, de Lasa HI |
| 349 - 355 |
Mathematical modelling and its use for design of feeding strategies for L-sorbose fermentation
Giridhar RN, Srivastava AK |
| 356 - 366 |
Strength development due to long term sulfation and carbonation/sulfation phenomena
Anthony EJ, Jia LF, Laursen K |
| 367 - 373 |
An accurate model for prediction of gas hydrate formation conditions in mixtures of aqueous electrolyte solutions and alcohol
Javanmardi J, Moshfeghian M, Maddox RN |
| 374 - 383 |
Experimental influence of kinetic inhibitors on methane hydrate particle size distribution during batch crystallization in water
Pic JS, Herri JM, Cournil M |
| 384 - 391 |
Structure-H gas hydrates in petroleum reservoir fluids
Tohidi B, Ostergaard KK, Danesh A, Todd AC, Burgass RW |
| 392 - 401 |
The activity coefficients of glycine, DL-serine and DL-valine in aqueous solutions containing nitrates at 298.15 K
Gao CX, Vera JH |
| 402 - 411 |
On the prediction of surface tension for multicomponent mixtures
Li ZB, Lu BCY |
| 412 - 421 |
On the costs of parameter uncertainties. Part 2: Impact of EVOP procedures on the optimization and design of experiments
Pinto JC |
| 422 - 429 |
Hydrodynamic modelling of the axial density profile in the riser of a low-density circulating fluidized bed
Smolders K, Baeyens J |
| 430 - 437 |
Fluidization regimes in two- and three-phase fluidized beds: Comparison between measurement techniques
Barghi S, Briens CL |
| 438 - 443 |
Modelling of trickle-bed reactors in foaming regime
Turco F, Hudgins RR, Silveston PL, Sicardi S, Manna L, Banchero M |
| 444 - 448 |
Scale-up of single phase axial dispersion coefficients in batch and continuous oscillatory baffled tubes
Ni XW, de Gelicourt YS, Baird MHI, Rao NVR |
| 449 - 454 |
Centrifugal degassing of highly viscous Newtonian liquids
Kiljanski T, Dziubinski M |
| 455 - 457 |
Rheological evolution of a particular sol-gel system
Fernandez-Torres MJ, Ghirisan AL, Tipan-Lepetich JM |
| 458 - 462 |
Heat transfer between an isolated bubble and the dense phase in a fluidized bed
Hartman G, Wu WY, Chen ZM, Agarwal PK |
| 463 - 467 |
Enhancement of the overall volumetric oxygen transfer coefficient in a stirred tank bioreactor using ethanol
Bi YH, Hill GA, Sumner RJ |
| 468 - 470 |
An investigation of the effect of air addition during oil sand conditioning
Flynn M, Bara B, Czarnecki J, Masliyah J |
| 473 - 473 |
Letter to the Editor
Grandjean BPA, Larachi F |
| 474 - 475 |
Letter to the Editor
Mitrovic J |
| 476 - 477 |
Letter to the Editor - Reply
Littman H, Day JY, Morgan MH |
| 478 - 478 |
Heat and mass transfer in granular potash fertilizer with a surface dissolution reaction (vol 78, pg 1076, 2000)
Peng SW, Besant RW, Strathdee G |
| 479 - 479 |
Chemical engineering processes via art
Tamir A |
