| 239 - 258 |
The analysis of the mathematical criteria of the hydrodynamic regimes changeover in the three-phase reactors
Burghardt A, Bartelmus G, Janecki D |
| 259 - 279 |
Hydrodynamics of the cocurrent gas-liquid flow through a three-phase reactor
Burghardt A, Bartelmus G, Szlemp A, Janecki D |
| 281 - 287 |
Determination of propylene hydroformylation reaction rate
Tic WJ |
| 289 - 307 |
Cfd modelling of kinetics of drying in a spouted bed apparatus
Szafran RG |
| 309 - 316 |
Impact of the method and conditions of drying on the survival of bacteria Lactobacillus plantarum
Miecznikowski A, Lenart A |
| 317 - 323 |
Coating of ring elements with an active mass coat in the spouted bed apparatus
Ludwig W, Kmiec A |
| 325 - 338 |
The influence of biofilm density and diffusivity of substrates in the biofilm on stationary properties of a fluidized bed bioreactor
Tabis B |
| 339 - 351 |
Two-phase thermosyphon loop laterally heated
Bielinski H, Mikielewicz J |
| 353 - 362 |
Visualisation of marangoni effects during deformation of the gas-liquid interface
Sosnowski TR, Gradon L |
| 363 - 376 |
Determination of the chemical reaction kinetics based on calorimetric measurements and amount of gaseous products evolved
Godala M, Nowicki L |
| 377 - 390 |
A new method of determination of the shape coefficient with the use of densimetric measurements
Vogt E |
