355 - 378 |
Rate-based model for chemical absorption and desorption developed in a cooperation between the university and the industry in the coke oven gas purification sector Thiele R, Brettschneider O, Thielert H, Wozny G |
379 - 390 |
Effect of non-ideal phase separation on a multi-unit crystallization process performance Dudczak J |
391 - 409 |
Approach to cyclic steady state in simulations of the catalytic reverse-flow combustion of methane Gosiewski K |
411 - 427 |
Application of the equation-of-state methods for chemical equilibria calculations in strongly non-ideal liquid phase Wyczesany A |
429 - 439 |
Analysis of the phase equilibrium in the system H2O-NH3-CO2 Koziol A, Budzianowski W |
441 - 448 |
Kinetics of the esterification of levulinic acid with n-hexanol and n-decanol in the presence of sulfuric acid Lachowska M, Grzesik M, Skrzypek J, Moroz H |
449 - 467 |
CFD modelling of two-phase flows in an SMX static mixer Pianko-Oprych P, Jaworski Z |
469 - 486 |
Adhesion mechanisms in particulate systems at different contact separation rates. Part I. Experimental Opalinski I, Chutkowski M, Petrus R |
487 - 507 |
Modelling of a one-dimensional sedimentation in suspensions Kowalski SJ, Sikorski M |
509 - 523 |
Influence of roasting conditions on selected physico-chemical properties of cocoa bean Krysiak W, Iciek J, Motyl-Patelska L |
525 - 532 |
Determination of the coefficients of diffusion for sodium chloride in silica gel Rogacki G, Plaskota D, Dziubinski M |
533 - 543 |
Shape of gas bubbles rising in non-Newtonian liquids Budzynski P, Dziubinski M, Orczykowska M |
545 - 550 |
Storage of hydrogen in commercial activated carbon Buczek B, Czepirski L |