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	Enzymová hydrolýza oleje z černého rybízu v superkritickém oxidu uhličitém Sovová, Helena ; Bernášek, Prokop ; Zarevúcka, Marie Oil conversion to free fatty acids was measured for the reaction of refined blackcurrant oil and water, both dissolved in supercritical carbon dioxide, in a continuous-flow packed-bed reactor filled with immobilised lipase Lipozyme and glass beads at 15 MPa and 40 C. The enzyme amount and the flow rate were varied. The reaction kinetics was simulated with mathematical models for plug flow and ideal mixer. Detailed record
	Binární adsorpce směsí propanu, butanu a oxidu uhličitého ve vycorovém skle. Čermáková, Jiřina ; Markovic, A. ; Uchytil, Petr ; Seidel-Morgenstern, A. Detailed record
	Semiempirický model transportu toluenu polyethylenovou membránou. Fialová, Kateřina ; Petričkovič, Roman ; Uchytil, Petr Detailed record
	Transportní jevy v polymerní membráně. Fialová, Kateřina ; Petričkovič, Roman ; Uchytil, Petr Detailed record
	Kyselost nosiče a její vliv na vlastnosti molybdenových hydrorafinačních katalyzátorů modifikovaných platinou Gulková, Daniela ; Vít, Zdeněk ; Zdražil, Miroslav It is known that acidity of supports plays a positive role in HDN. Thus, the Pt-Mo system was now deposited on a more acidic support than alumina, i.e. on an amorphous silica-alumina (ASA) in attempt to further enhance the HDN activity and HDN/HDS selectivity. The objective was to find how acidic support may affect the catalytic properties of the Pt-Mo system. The strongest effect was observed in HDN. Detailed record
	Hydrogenace styrenu a dicyklopentadienu ve zkrápěném reaktoru s katalyzátorem typu „egg shell“. Model a experiment Tukač, V. ; Šimíčková, M. ; Chyba, V. ; Lederer, J. ; Kolena, J. ; Hanika, Jiří Experimental study has been carried out of hydrogenation of styrene and dicyclopentadiene in a catalytic egg-shell type catalyst reactor under elevated pressure on a pilot plant scale. A mathematical model has been developed of the hydrogenation under periodic variations of the inlet liquid rate. Detailed record
	Rozdělení dob prodlení nevodné kapaliny při dvoufázovém souproudém toku ve zkrápěném reaktoru Stavárek, Petr ; Jiřičný, Vladimír ; Staněk, Vladimír ; Hanika, Jiří ; Vychodilová, Hana Residence time distribution has been studied under two phase cocurrent flow in a trickle bed reactor with toluene as the liquid phase. Electric conductivity using ethanol solution of sodium chloride was used as a tracer. Detailed record
	Hydrodynamika dvoufázového pulzního toku v náplňové koloně Jiřičný, Vladimír ; Stavárek, Petr ; Staněk, Vladimír ; Hanika, Jiří ; Vychodilová, Hana Hydrodynamics has been studied of the two-phase flow in cocurrent packed bed column while forcing pulsations of the regime by pulsations of inlet liquid velocity. Detailed record
	Matematický model katalytického hydrogenačního reaktoru za periodických změn vstupní rychlosti kapaliny Staněk, Vladimír ; Hanika, Jiří ; Jiřičný, Vladimír ; Tukač, V. ; Stavárek, Petr A mathematical model has been developed of the cocurrent trickle bed hydrogenation reactor operating under periodically variable inlet feed rate of liquid. The model calculates the periodic changes of the hydrodynamics of the reactor and the time variations of the temperature and conversion profile within the bed and at the reactor outlet. Detailed record
	Intensifikace, bezpečný provoz a řízení zkrápěného katalytického reaktoru Hanika, Jiří ; Jiřičný, Vladimír ; Kolena, J. ; Lederer, J. ; Staněk, Vladimír ; Stavárek, Petr ; Tukač, V. An experimental and theoretical study has been carried out of the aspects of the safe operation and control of an industrial trickle bed reactor. The study was mainly focused on the operation of the reactor under forced pulsations of inlet liquid feed. Detailed record

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