Modeling and Simulation of an Industrial Trickle-Bed Reactor for Benzene Hydrogenation: Model Validation against Plant Data

2009 ◽  
Vol 48 (4) ◽  
pp. 1866-1872 ◽  
Author(s):  
Jonas Roininen ◽  
Ville Alopaeus ◽  
Sami Toppinen ◽  
Juhani Aittamaa
Keyword(s):  
Modeling And Simulation ◽  
Model Validation ◽  
Benzene Hydrogenation ◽  
Trickle Bed Reactor ◽  
Plant Data ◽  
Trickle Bed

Mathematical modeling and simulation of an industrial adiabatic trickle-bed reactor for upgrading heavy crude oil by hydrotreatment process

2018 ◽  
Vol 126 (1) ◽  
pp. 31-48 ◽  
Author(s):  
Ignacio Elizalde ◽  
Fabián S. Mederos ◽  
Ma. del Carmen Monterrubio ◽  
Ninfa Casillas ◽  
Hugo Díaz ◽  
...  
Keyword(s):  
Mathematical Modeling ◽  
Crude Oil ◽  
Modeling And Simulation ◽  
Heavy Crude Oil ◽  
Trickle Bed Reactor ◽  
Heavy Crude ◽  
Trickle Bed

Estimation of kinetic parameters of benzene hydrogenation in a trickle bed reactor

1993 ◽  
Vol 16 (5) ◽  
pp. 347-359 ◽  
Author(s):  
Sunil Dutt Sharma ◽  
Kasturi Gadgil ◽  
Manoj Kumar Sarkar
Keyword(s):  
Kinetic Parameters ◽  
Benzene Hydrogenation ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Modeling and simulation of a small-scale trickle bed reactor for sugar hydrogenation

2014 ◽  
Vol 66 ◽  
pp. 22-35 ◽  
Author(s):  
Davide Durante ◽  
Teuvo Kilpiö ◽  
Petteri Suominen ◽  
Victor Sifontes Herrera ◽  
Johan Wärnå ◽  
...  
Keyword(s):  
Modeling And Simulation ◽  
Small Scale ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Kinetics and Mass Transfer of Benzene Hydrogenation in a Trickle-Bed Reactor

2006 ◽  
Vol 45 (21) ◽  
pp. 7110-7119 ◽  
Author(s):  
Kostas C. Metaxas ◽  
Nikos G. Papayannakos
Keyword(s):  
Mass Transfer ◽  
Benzene Hydrogenation ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Wall flow in trickle bed reactor

1975 ◽  
Vol 40 (10) ◽  
pp. 3145-3152 ◽  
Author(s):  
J. Prchlík ◽  
J. Soukup ◽  
V. Zapletal ◽  
V. Růžička ◽  
P. Kovařík
Keyword(s):  
Trickle Bed Reactor ◽  
Wall Flow ◽  
Trickle Bed

Mass Transfer Limited Wet Oxidation in Trickle-Bed Reactor

1998 ◽  
Vol 63 (11) ◽  
pp. 1938-1944 ◽  
Author(s):  
Vratislav Tukač ◽  
Jiří Vokál ◽  
Jiří Hanika
Keyword(s):  
Supported Catalyst ◽  
Reaction Rates ◽  
Gas Transfer ◽  
Wet Oxidation ◽  
Reactor Performance ◽  
Catalytic Wet Oxidation ◽  
Environmental Application ◽  
Trickle Bed Reactor ◽  
Fine Glass ◽  
Trickle Bed

Catalytic activity of CuO-supported catalyst in phenol oxidation, and the influence of reaction conditions, viz. temperature (125-170 °C), oxygen partial pressure (1-7 MPa) and liquid feed (30-760 ml h-1), in the continuous operation using 17.9 mm i.d. trickle-bed reactor is presented. The hydrodynamic impact on the three-phase trickle-bed reactor performance in an environmental application of catalytic wet oxidation was also investigated. The results of trickle-bed operation were strongly influenced by wetting efficiency. An insufficient catalyst wetting can be to compensated by filling the catalyst bed voids by fine glass spheres. In the case of the gas transfer limited reaction, a better wetting of the catalyst can lead to worse reactor performance due to lower reaction rates.

scholarly journals Selecting carrier material for efficient biomethanation of industrial biogas-CO2 in a trickle-bed reactor

2021 ◽  
Vol 51 ◽  
pp. 101611
Author(s):  
Mads Borgbjerg Jensen ◽  
Súsanna Poulsen ◽  
Bjarke Jensen ◽  
Anders Feilberg ◽  
Michael Vedel Wegener Kofoed
Keyword(s):  
Trickle Bed Reactor ◽  
Carrier Material ◽  
Trickle Bed
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