scholarly journals Plasmachemical Trace‐Oxygen Removal in a Coke Oven Gas with a Coaxial Packed‐Bed‐DBD Reactor

2020 ◽  
Vol 92 (10) ◽  
pp. 1559-1566
Author(s):  
Tim Nitsche ◽  
Marcus Budt ◽  
Ulf‐Peter Apfel
Keyword(s):  
Coke Oven ◽  
Packed Bed ◽  
Oxygen Removal ◽  
Coke Oven Gas ◽  
Dbd Reactor

Removal of hydrogen sulfide from coke oven gas by catalytic oxidative absorption in a rotating packed bed

Fuel ◽  
2017 ◽  
Vol 204 ◽  
pp. 47-53 ◽  
Author(s):  
Haikui Zou ◽  
Miaopeng Sheng ◽  
Xiaofei Sun ◽  
Zihao Ding ◽  
Moses Arowo ◽  
...  
Keyword(s):  
Hydrogen Sulfide ◽  
Coke Oven ◽  
Packed Bed ◽  
Coke Oven Gas ◽  
Rotating Packed Bed

scholarly journals Catalytic Oxygen Removal from Synthetic Coke Oven Gas: A Comparison of Sulfided CoMo/γ‐Al 2 O 3 and NiMo/γ‐Al 2 O 3 Catalysts with Pt/γ‐Al 2 O 3 as Benchmark Catalyst

2020 ◽  
Vol 92 (10) ◽  
pp. 1533-1541
Author(s):  
Thomas Wiesmann ◽  
Sung Youn Suh ◽  
Stefan Kaluza ◽  
Heiko Lohmann ◽  
Barbara Zeidler‐Fandrich
Keyword(s):  
Coke Oven ◽  
Oxygen Removal ◽  
Coke Oven Gas

An exergy study on compression ignition engine operating with biogas gas and coke oven gas

2020 ◽  
Vol 33 (2) ◽  
pp. 183
Author(s):  
Hongqing Feng ◽  
Zhirong Nan ◽  
Xinyi Wang ◽  
Weiwen Zhang
Keyword(s):  
Coke Oven ◽  
Compression Ignition ◽  
Coke Oven Gas ◽  
Compression Ignition Engine

Catalytic Partial Oxidation of Coke Oven Gas to Syngas over Ni/SiO2 Catalyst Modified by Rare Earth Metal Oxide in a Membrane Reactor

2010 ◽  
Vol 156-157 ◽  
pp. 1024-1028
Author(s):  
Da Hai Hu ◽  
Xiong Gang Lu ◽  
Hong Wei Cheng ◽  
Wei Zhong Ding
Keyword(s):  
Rare Earth ◽  
Partial Oxidation ◽  
Membrane Reactor ◽  
Coke Oven ◽  
Oxygen Permeation ◽  
Catalytic Partial Oxidation ◽  
Permeation Flux ◽  
Coke Oven Gas ◽  
Permeable Membrane ◽  
Oxygen Permeation Flux

The performance of Ni/SiO2 Catalysts modified by La2O3, ZrO2 and CeO2 were tested in a BaCo0.7Fe0.2Nb0.1O3-δ (BCFNO) membrane reactor by catalytic partial oxidation of coke oven gas (COG) under atmospheric pressure. The results show that the oxygen permeation flux increased dramatically with Ni/RxOy/SiO2 (R = La, Zr or Ce) catalysts by adding the element of rare earth especially the La during the reforming reaction. At optimized reaction conditions, the dense oxygen permeable membrane had an oxygen permeation flux around 16.4 ml/cm2•min and a CH4 conversion of 99.2% have been achieved at 900 oC.

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