Catalytic conversion of tar from hot coke oven gas using 1-methylnaphthalene as a tar model compound

2010 ◽  
Vol 96 (1-2) ◽  
pp. 232-237 ◽  
Author(s):  
Jun Yang ◽  
Xueguang Wang ◽  
Lin Li ◽  
Kui Shen ◽  
Xionggang Lu ◽  
...  
Keyword(s):  
Model Compound ◽  
Catalytic Conversion ◽  
Coke Oven ◽  
Coke Oven Gas ◽  
Tar Model Compound

Catalytic Conversion of Tar Components in Hot Coke Oven Gas over Ni/MgO-Al2O3 Catalysts

2009 ◽  
Vol 25 (08) ◽  
pp. 1517-1522 ◽  
Author(s):  
AI Xin-Peng ◽  
◽  
◽  
YUE Bao-Hua ◽  
WANG Xue-Guang ◽  
...  
Keyword(s):  
Catalytic Conversion ◽  
Coke Oven ◽  
Coke Oven Gas

Catalytic Conversion of Tar Components from Hot Coke Oven Gas over Ni/MgAl(O) Catalyst

2010 ◽  
Vol 31 (2) ◽  
pp. 218-224 ◽  
Author(s):  
Baohua YUE ◽  
Linghua KONG ◽  
Xueguang WANG ◽  
Xionggang LU ◽  
Weizhong DING
Keyword(s):  
Catalytic Conversion ◽  
Coke Oven ◽  
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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