| 5633 - 5645 |
Gas-liquid interfacial mass transfer in trickle-bed reactors: state-of-the-art correlations
Iliuta I, Larachi F, Grandjean BPA, Wild G |
| 5647 - 5666 |
Particle-bed model for multicomponent adsorption-based separations: application to pressure swing adsorption
Serbezov A, Sotirchos SV |
| 5667 - 5675 |
Drop coalescence in turbulent dispersions
Liu SP, Li DM |
| 5677 - 5709 |
Feedback control of nonlinear differential difference equation systems
Antoniades C, Christofides PD |
| 5711 - 5715 |
An alternative to the concept of the interval of quiescence (IQ) in the Monte Carlo simulation of population balances
Song M, Qiu XJ |
| 5717 - 5722 |
Highly porous sphere moving through centerline of circular tube filled with Newtonian fluid
Wu RM, Lee DJ |
| 5723 - 5735 |
Characterisation of gas-liquid two-phase flow inside capillaries
Laborie S, Cabassud C, Durand-Bourlier L, Laine JM |
| 5737 - 5754 |
Particle and bubble movements around tubes immersed in fluidized beds - a numerical study
Rong DG, Mikami T, Horio M |
| 5755 - 5760 |
A method for the measurement of gas concentration distribution in the adsorptive bed
Wang ZX, Mo FZ, Shi YQ, Zhou M, Yu GC |
| 5761 - 5775 |
Experimental investigation of Taylor bubble acceleration mechanism in slug flow
Tudose ET, Kawaji M |
| 5777 - 5786 |
Pressure gradient, liquid hold-up and mass transfer in a graphite fibre bed with cocurrent upward gas-liquid flow
Hodgson I, Oloman C |
| 5787 - 5790 |
Effect of adsorbent shape on adsorption dynamics in a batch adsorber
Wang ZL |
