1 - 6 |
Fluidized bed granulation - the importance of a drying zone for the particle growth mechanism Becher RD, Schlunder EU |
7 - 21 |
Computational fluid dynamics studies of fixed bed heat transfer Logtenberg SA, Dixon AG |
23 - 32 |
The influence of the tube and particle diameters at constant ratio on heat transfer in packed beds Dixon AG, van Dongeren JH |
33 - 46 |
Modelling of the reaction of N-oxidation of 2-methylpyridine using hydrogen peroxide and a complex metal catalyst Sempere J, Nomen R, Rodriguez JL, Papadaki M |
47 - 54 |
Mass transfer model for the film countercurrent flow of two liquid phases in a packed bed column Wronski S, Molga E |
55 - 59 |
Runaway phenomena in the ethylene/vinylacetate copolymerization under high pressure Albert J, Luft G |
61 - 67 |
A reaction calorimeter with compensation heater and differential cooling Schlegel H, Lowe A |
69 - 78 |
A new absorbent for carbon dioxide and hydrogen sulphide absorption process Pohorecki R, Mozenski C |
79 - 88 |
Convective drying of porous material containing a partially miscible mixture Steinbeck MJ, Schlunder EU |
89 - 101 |
Modelling of heavy metals adsorption to a chelating resin in a fluidized bed reactor Menoud P, Cavin L, Renken A |
103 - 107 |
Analogy between heat and momentum transfer Schlunder EU |
109 - 114 |
Comparison of kinetic data obtained from integral fixed bed reactor and differential recycle reactor Estenfelder M, Lintz HG, Stein B, Gaube J |