National Repository of Grey Literature 25 records found  beginprevious16 - 25  jump to record: Search took 0.02 seconds. 
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.
Styrene Hydrogenation in Bench and Pilot Plant Trickle Bed Reactor.
Tukač, V. ; Hanika, Jiří ; Chyba, V. ; Šimíčková, M. ; Lederer, J. ; Kolena, J. ; Šimek, J. ; Jiřičný, Vladimír ; Staněk, Vladimír ; Stavárek, Petr
Paper brings data on styrene hydrogenation using palladium catalyst measured using two trickle bed reactors of different dimensions. The data were applied to formulation and solution dynamic models of reactor under forced periodic feed rate modulation of reaction mixture. Adequate agreement between model solution and pilot plant adiabatic trickle bed reactor has been confirmed.
Transition Events in Trickle Bed Reactor under Conditions of Steady State and Pulse Regime. Part 2
Jiřičný, Vladimír ; Staněk, Vladimír ; Hanika, Jiří ; Vychodilová, Hana ; Stavárek, Petr ; Vlček, Dalibor ; Karfík, David ; Tukač, V. ; Lederer, J. ; Chyba, V.
Transition events in trickle bed reactor under conditions of steady state and pulse regime has been studied experimentally in pilot plant trickle bed reactor at elevated pressures 2 and 5bar and temperatures 20 and 50oC. From hydrodynamic dependencies of pressure drops on gas and liquid velocities the transients lines between film and pulse regime have been determined. The effects of various variables flow rates, temperature, pressure, length of period and spilt have been verified with respect to pressure drop and pressure drop profile along trickle bed reactor operated in pulse regime.
Scale Up of Styrene and Dicyclopentadiene Hydrogenation in Trickle Bed Reactor
Tukač, V. ; Chyba, V. ; Šimíčková, M. ; Lederer, J. ; Kolena, J. ; Šimek, J. ; Hanika, Jiří
Experimental study brings evidence that rate of hydrogenation of both unsaturated hydrocarbons is proportional to hydrogen partial pressure and depends on wetting efficiency of catalyst by liquid. Parameters of empirical model for laboratory data scale up to pilot plant reactor were identified.
Mathematical Modeling and Simulation of Trickle Bed Reactors, Part 1
Tukač, V. ; Hanika, Jiří ; Chyba, V. ; Šimíčková, M. ; Jiřičný, Vladimír
Formulation of mathematical models of trickle bed reactors is a part of the report. Numerical metods for solution of math models and determination of parameters of TBR are presented.
Reaction Kinetics, Part 1
Tukač, V. ; Hanika, Jiří ; Chyba, V. ; Šimíčková, M. ; Lederer, J. ; Kolena, J. ; Šimek, J. ; Jiřičný, Vladimír
Following results are published in this report: Selection of reaction system and Catalysts. determination of activities and selectivities selected catalysts. Experimental verification of reaction kinetics on pilot plant experimental station.
Selectivity of Wet Oxidation in Trickle Bed Reactor under Periodically Modulated Feed Rate
Chyba, V. ; Tukač, V. ; Hanika, Jiří
Wet air oxidation of phenol in water solution using active carbon catalyst pellets was used as a model reaction of the process. Experiments were made using bench scale stainless steal trickle bed reactor at temperature 125 ů 170 oC and pressure 1 ů 7 MPa intervals. The higher reactor throughput at periodically modulated liquid feed rate in comparison to the continuous reactor regime was observed. The optimal reactor control parameters ůperiod length and split- were determined in the study.
Selektivita mokré oxidace v periodicky řízeném zkrápěném reaktoru
Tukač, V. ; Chyba, V. ; Hanika, Jiří
The objective of this work was to investigate the impact of dynamically changing extent of wetted catalyst surface and mass-transfer of gaseous oxygen on oxidation of the aqueous phenol under periodic modulated liquid feed rate. Selectivity of oxidation and reactor productivity was also under consideration in this study.

National Repository of Grey Literature : 25 records found   beginprevious16 - 25  jump to record:
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