| 847 - 848 |
Special Topic Issue - Heat and Mass-Transfer
Whalley P |
| 849 - 852 |
Heat-Exchanger Design Through Parameter Plotting
Poddar TK, Polley GT |
| 853 - 855 |
Effect of Agitation Intensity on Gas-Liquid Reaction in Variable Volume Systems
Lu WM, Ju SJ |
| 856 - 862 |
An Ultrathin Skinned Hollow-Fiber Module for Gas-Absorption at Elevated Pressures
Li K, Teo WK |
| 863 - 871 |
Batch Distillation of Multicomponent Systems with Constant Relative Volatilities
Barolo M, Guarise GB |
| 872 - 881 |
The Gas-Liquid Mass-Transfer Coefficient (K(L)A) in the Gas-Liquid Multistage Agitated Contactor (Mac)
Breman BB, Beenackers AA, Bouma MJ, Vanderwerf MH |
| 882 - 892 |
Influence of Local Variations of Air Velocity and Flow Direction Reversals on the Drying of Stacked Timber Boards in Kilns
Nijdam JJ, Keey RB |
| 893 - 900 |
Prediction of Packed Sieve Tray Efficiency in Distillation
Xu ZP, Afacan A, Chuang KT |
| 901 - 912 |
Simulation and Control of an Industrial Rotary Calciner with a Heat Shield Around the Combustion Zone
Ciftci S, Kim NK |
| 913 - 933 |
A Dynamic-Model for the Energy-Balance of an Electrolysis Cell
Taylor MP, Zhang WD, Wills V, Schmid S |
| 934 - 943 |
Designing Dryers Using Heat and Mass-Exchange Networks - An Application to Conveyor Belt Dryers
Sebastian P, Nadeau JP, Puiggali JR |
| 944 - 952 |
Wave Concept in the Theory of Hydrodynamical Dispersion - A Maxwellian Type Approach
Westerterp KR, Kronberg AE, Benneker AH, Dilman VV |
