Investigation of flow dynamics of liquid phase in a pilot-scale trickle bed reactor using radiotracer technique

2016 ◽  
Vol 116 ◽  
pp. 163-173 ◽  
Author(s):  
H.J. Pant ◽  
V.K. Sharma
Keyword(s):  
Liquid Phase ◽  
Pilot Scale ◽  
Flow Dynamics ◽  
Radiotracer Technique ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Investigation of flow dynamics of wastewater in a pilot-scale constructed wetland using radiotracer technique

2019 ◽  
Vol 147 ◽  
pp. 70-75 ◽  
Author(s):  
S. Goswami ◽  
H.J. Pant ◽  
D. Poswal ◽  
J.S. Samantray ◽  
S.R. Asolekar
Keyword(s):  
Constructed Wetland ◽  
Pilot Scale ◽  
Flow Dynamics ◽  
Radiotracer Technique

Hydrogenation of Ethylbenzene Over Ru/γ-Al2O3 Catalyst in Trickle-Bed Reactor

2021 ◽  
Vol 21 (7) ◽  
pp. 4116-4120
Author(s):  
Seung Kyo Oh ◽  
Huiji Ku ◽  
Gi Bo Han ◽  
Byunghun Jeong ◽  
Young-Kwon Park ◽  
...  
Keyword(s):  
Liquid Phase ◽  
Active Sites ◽  
Catalytic Performance ◽  
Hydrogenation Reaction ◽  
Impregnation Method ◽  
Average Pore ◽  
Wet Impregnation ◽  
Trickle Bed Reactor ◽  
Liquid Phase Hydrogenation ◽  
Trickle Bed

The objective of this study is to evaluate the catalytic performance of pellet-type Ru/γ-Al2O3 as a catalyst during liquid-phase hydrogenation of the aromatic hydrocarbon. The Ru/γ-Al2O3 catalyst was prepared using a wet impregnation method. After adding a binder to Ru/γ-Al2O3, a pellet-type catalyst was obtained through an extrusion method. Nanoporous structures are well developed in the pellet-type Ru/γ-Al2O3 catalyst. The average pore sizes of the Ru/γ-Al2O3 catalysts were approximately 10 nm. The catalytic performance of the pellet-type Ru/γ-Al2O3 catalyst during ethylbenzene hydrogenation was evaluated in a trickle-bed reactor. When the ruthenium loading increased from 1 to 5 wt%, the number of active sites effective for the hydrogenation of ethylbenzene increased proportionally. In order to maximize the conversion of ethylbenzene to ethylcyclohexane, it was necessary to maintain a liquid phase hydrogenation reaction in the trickle bed reactor. In this regards, the reaction temperature should be lower than 90 °C. The conversion of ethylbenzene to ethylcyclohexane on the Ru(5 wt%)/γ-Al2O3 catalyst was highest, which is ascribed to the largest number of active sites of the catalyst.

Modeling of a pilot-scale trickle bed reactor for the catalytic oxidation of phenol

2009 ◽  
Vol 67 (2) ◽  
pp. 158-165 ◽  
Author(s):  
Qiang Wu ◽  
Xijun Hu ◽  
Po Lock Yue ◽  
Jian Feng ◽  
Xi Chen ◽  
...  
Keyword(s):  
Catalytic Oxidation ◽  
Pilot Scale ◽  
Trickle Bed Reactor ◽  
Oxidation Of Phenol ◽  
Trickle Bed ◽  
Catalytic Oxidation Of Phenol
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