511 - 529 |
Adaptive control of multiple-fraction batch distillation for tracking optimal a priori policies Li P, Wozny G |
531 - 549 |
Resistance of liquid-liquid two phase flow Hapanowicz J, Troniewski L |
551 - 555 |
Comparison of the calculation methods of the nitrogen diffusion coefficients in cyclohexane Moniuk W, Pohorecki R |
557 - 573 |
A model of the two-phase gas-solids flow in fluidizing apparatus with the draft tube. I. Model development Kmiec A, Ludwig W |
575 - 589 |
A model of the two-phase gas-solids flow in fluidizing apparatus with the draft tube. II. Model solution Kmiec A, Ludwig W |
591 - 604 |
Kinetics of solids mixing. The model of chemical sequence reaction Boss J, Szatko W |
605 - 619 |
Non-linear dynamics of a continuous stirred tank bioreactor for a process in a predator-prey system. Yield of the uncontrolled reactor Tabis B |
621 - 634 |
Mathematical model of dehydrocyclization of n-heptane in the conditions of reforming Szczygiel J |
635 - 652 |
The thermoanemometric measurements in slowly flowing gas Dolata M, Krajewska M, Michalski JA |
653 - 665 |
Selection of a model and its parameters to the description of activation and thermal destruction of spores Iciek J, Cywinska U, Jaworska A, Libudzisz Z, Nowicki L, Oltuszak E, Stobinska H, Stolarek P |
667 - 683 |
Selective pneumatic classifier Bryczkowski A, Bandrowski J |
685 - 697 |
Nucleation and caprolactam crystal growth in suspension melt crystallization apparatus Misztal S |