| 1 - 12 |
Pareto design of fluidized bed dryers
Krokida MK, Kiranoudis CT |
| 13 - 21 |
Analysis of controlled CSTR models with fluctuating parameters and uncertain parameters
Ratto M, Paladino O |
| 23 - 30 |
Mixing time for a reciprocating plate agitator with flapping blades
Masiuk S |
| 31 - 39 |
Size reduction of polystyrene in a shaker bead mill - kinetic aspects
Molina-Boisseau S, Le Bolay N |
| 41 - 52 |
Phase holdup and gas-to-liquid mass transfer coefficient in magneto stabilized G-L-S airlift fermenter
Al-Qodah Z, Al-Hassan M |
| 53 - 59 |
Liquid inclusions in crystals produced in suspension crystallization
Saito N, Yokota M, Fujiwara T, Kubota N |
| 61 - 67 |
Continuous extraction of penicillin G by emulsion liquid membranes with optimal surfactant compositions
Lee SC |
| 69 - 72 |
Estimation of liquid viscosity at ambient temperature of pure organic compounds by using group-interaction contributions
Marrero-Morejon J, Pardillo-Fontdevila E |
| 73 - 77 |
Heat transfer to viscous Newtonian and non-Newtonian fluids using helical ribbon agitator
Rai CL, Devotta I, Rao PG |
| 79 - 79 |
Comments on the article "Turbulent characteristics in turbine tanks of different sizes and geometries" by E. Stahl and C. Tragardh
Fort I |
| 81 - 81 |
Reply to "Comments on the article 'Turbulence characteristics in turbine agitated tanks of different sizes and geometries' by Ivan Fort, Czech Technical University"
Tragardh C |
