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Transition Phenomena in Trickle Bed Reactor, Part IV, Intermediate Research Report, Task C, Project FT-TA/039, 2007
Jiřičný, Vladimír ; Staněk, Vladimír ; Hanika, Jiří ; Vychodilová, Hana ; Stavárek, Petr ; Vlček, Dalibor ; Karfík, David ; Tukač, V. ; Chyba, V. ; Lederer, J. ; Kubička, D.
This report sumarizes project results obtained from December 10th 2006 to July 31st 2007. Working team effort was concentraced on residence time distribution measurement by refractometric method in laboratory trickle bed reactor with organic liquid. Method was tested giving reproducible results.
Pressure and Temperature Waves in Periodically Operated Hydrogenation Reactor.
Stavárek, Petr ; Jiřičný, Vladimír ; Staněk, Vladimír ; Hanika, Jiří ; Tukač, V. ; Chyba, V. ; Lederer, J. ; Kolena, J. ; Kubička, D.
Paper deals with behaviour investigation of trickle bed reactor with periodically modulated feed rate of liquid reaction mixture. Dicyclopentadiene hydrogenation using palladium supported catalyst was used as a model reaction. Feed rate modulation parameters – period length and its split – have effect on pressure and temperature waves travelling down along catalyst bed.
Pyrolysis Gasoline Hydrogenation in Trickle Bed Reactor with Periodically Modulated Feed Rate.
Tukač, V. ; Hanika, Jiří ; Chyba, V. ; Handlová, M. ; Sazanov, Z. ; Lederer, J. ; Kolena, J. ; Jiřičný, Vladimír ; Stavárek, Petr ; Staněk, Vladimír
The effect of feed rate modulation on efficiency of pilot plant trickle bed reactor during pyrolysis gasoline hydrogenation using palladium supported catalyst was investigated. Enhancement factors for unsaturated hydrocarbon components were evaluated from experiments made both in steady state and dynamic operation modes. Feed rate modulation mode prefered hydrogenation of minority components of the feed.
Internal Diffusion Effect on Styrene and Dicyclopentadiene Hydrogenation.
Sazanov, S. ; Tukač, V. ; Chyba, V. ; Handlová, M. ; Hanika, Jiří ; Lederer, J. ; Kolena, J.
Internal efficiency factors of palladium on alumina catalyst have been evaluated for hydrogenation of unsaturated hydrocarbons – styrene and dicyclopentadienene - representing key components of pyrolysis gasoline. Effect of catalyst particle diameter and temperature on reaction rate has been investigated in the study.
Hydrogenatoion of Nonsaturated Hydrocarbons in Pilot Plant TBR, Part III, Final Research Report, Task E, Project FT-TA/039, 2006.
Lederer, J. ; Kolena, J. ; Kubička, D. ; Kubičková, I. ; Tukač, V. ; Chyba, V. ; Jiřičný, Vladimír ; Stavárek, Petr
Experimental study oh hydrogenation of olefines in pilot plant TBR under conditions of constant and pulse liquid flow. Determination of the effect of operation conditions, as phase flow rates, pulse period, split and pressure on the hydrogenation conversion and selectivity.
Transition Phenomena in Trickle Bed Reactor, Part III, Final Research Report, Task B and C, Project FT-TA039, 2006.
Jiřičný, Vladimír ; Staněk, Vladimír ; Hanika, Jiří ; Vychodilová, Hana ; Stavárek, Petr ; Vlček, Dalibor ; Karfík, David ; Tukač, V. ; Chyba, V. ; Lederer, J. ; Kubička, D.
Experimental study of trasition of liquid film to pulse flow regime in TBR. Determination of presssure drop profiles, temperature profiles, liquid hold up and RTD and mixing in liquid phase at constant and pulse flow liquid rate.
4th Reaction Kinetics, Part III, Final Research Report, Task A, Project FT-TA/039, 2006.
Chyba, V. ; Tukač, V. ; Hanika, Jiří ; Šimíčková, M. ; Lederer, J. ; Kolena, J. ; Šimek, J. ; Jiřičný, Vladimír ; Sazanov, Z.
Determination of hydrogenation reaction kinetics of styrene, DCPD and and heavy gasoline fraction in Trickle bed reactor.
Transition Phenomena in Trickle Bed Reactor, Part III, Intermediate Research Report, Task B and C, Project FT-TA/039, 2006.
Jiřičný, Vladimír ; Staněk, Vladimír ; Hanika, Jiří ; Vychodilová, Hana ; Stavárek, Petr ; Vlček, Dalibor ; Karfík, David ; Tukač, V. ; Chyba, V. ; Lederer, J. ; Kubička, D.
Experimental study of trasition of liquid film to pulse flow regime in TBR. Determination of presssure drop profiles, temperature profiles, liquid hold up and RTD and mixing in liquid phase at constant and pulse flow liquid rate.

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