The Manufacture of Hydrogen by the Partial Liquefaction of Water Gas and Coke-Oven Gas

1922 ◽  
Vol 14 (12) ◽  
pp. 1118-1118
Author(s):  
GEORGES. CLAUDE
Keyword(s):  
2016 ◽  
Vol 263 ◽  
pp. 46-51 ◽  
Author(s):  
Chunling Wang ◽  
Cheng Liu ◽  
Wei Fu ◽  
Zhenghong Bao ◽  
Jieyu Zhang ◽  
...  

2020 ◽  
Vol 33 (2) ◽  
pp. 183
Author(s):  
Hongqing Feng ◽  
Zhirong Nan ◽  
Xinyi Wang ◽  
Weiwen Zhang

2010 ◽  
Vol 35 (12) ◽  
pp. 6239-6247 ◽  
Author(s):  
Zhibin Yang ◽  
Weizhong Ding ◽  
Yunyan Zhang ◽  
Xionggang Lu ◽  
Yuwen Zhang ◽  
...  

2009 ◽  
Vol 18 (4) ◽  
pp. 407-414 ◽  
Author(s):  
Zhibin Yang ◽  
Yunyan Zhang ◽  
Weizhong Ding ◽  
Yuwen Zhang ◽  
Peijun Shen ◽  
...  

2010 ◽  
Vol 156-157 ◽  
pp. 1024-1028
Author(s):  
Da Hai Hu ◽  
Xiong Gang Lu ◽  
Hong Wei Cheng ◽  
Wei Zhong Ding

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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