3 - 28 |
Comparison of various mass transport models in multicomponent condensation without inerts Burghardt A, Klepacka K |
29 - 50 |
Disintegration of Saccharomyces cerevisiae yeasts' cells in a flow pearl mill with a bell-shape impeller Heim A, Czerski R |
51 - 60 |
Power consumption for viscous liquids mixed in a vibratory agitator Masiuk S, Damra T |
61 - 77 |
Recognition and assessment of states of an industrial plant using artificial neural network Gosiewski K, Ogonowski Z, Paradowski J |
79 - 97 |
Measurement errors in multi-stage cascade impactors .1. Characteristic size of particles Maszek L |
99 - 119 |
Measurement errors in multistage cascade impactors .2. Fractional composition of solution. Range efficiency Maszek L |
121 - 131 |
Exothermic processes in a fluidized-bed catalytic reactor with recycle Tabis B, Georgiou A |
133 - 150 |
Investigation of dynamics of sorption processes in fluidized beds Tabis B, Kupiec K, Ciesielczyk W |
151 - 158 |
Separation of steady states of an adiabatic homogeneous CSTR Berezowski M |
159 - 173 |
Heat transfer in membrane distillation Gryta M, Tomaszewska M, Morawski W |