EFFECT OF EQUATION OF STATE ON PREDICTION OF TRICKLE BED REACTOR MODEL PERFORMANCE

1986 ◽  
Vol 49 (1-3) ◽  
pp. 133-143 ◽  
Author(s):  
AYDIN AKGERMAN ◽  
DONALD W. NETHERLAND
Keyword(s):  
Equation Of State ◽  
Model Performance ◽  
Reactor Model ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Trickle bed reactor model to simulate the performance of commercial diesel hydrotreating unit

Fuel ◽  
2007 ◽  
Vol 86 (7-8) ◽  
pp. 1176-1184 ◽  
Author(s):  
C. Murali ◽  
R.K. Voolapalli ◽  
N. Ravichander ◽  
D.T. Gokak ◽  
N.V. Choudary
Keyword(s):  
Reactor Model ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Trickle-bed reactor model for desulfurization and dearomatization of diesel

AIChE Journal ◽  
2002 ◽  
Vol 48 (1) ◽  
pp. 126-135 ◽  
Author(s):  
R. Chowdhury ◽  
E. Pedernera ◽  
R. Reimert
Keyword(s):  
Reactor Model ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Three-phase trickle-bed reactor model for industrial hydrotreating processes: CFD and experimental verification

2020 ◽  
Vol 208 ◽  
pp. 106496
Author(s):  
Antônio Tavernard Pereira Neto ◽  
Thalita Cristine Ribeiro Lucas Fernandes ◽  
Heleno Bispo da Silva Junior ◽  
Antônio Carlos Brandão de Araújo ◽  
José Jailson Nicácio Alves
Keyword(s):  
Experimental Verification ◽  
Reactor Model ◽  
Trickle Bed Reactor ◽  
Three Phase ◽  
Trickle Bed

A trickle-bed reactor model for hydrogenation of 2,4 dinitrotoluene: experimental verification

1998 ◽  
Vol 53 (4) ◽  
pp. 787-805 ◽  
Author(s):  
Malyala V. Rajashekharam ◽  
Rengaswamy Jaganathan ◽  
Raghunath V. Chaudhari
Keyword(s):  
Experimental Verification ◽  
Reactor Model ◽  
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

scholarly journals Hydrodynamics in a pressurized cocurrent gas-liquid trickle-bed reactor

1991 ◽  
Vol 14 (6) ◽  
pp. 406-413 ◽  
Author(s):  
Wino J. A. Wammes ◽  
K. Roel Westerterp
Keyword(s):  
Trickle Bed Reactor ◽  
Trickle Bed
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