Steam reforming of tar from raw coke oven gas over bifunctional catalysts: Reforming performance for H 2 production

Author(s):  
Weidong Zhang ◽  
Huaqing Xie ◽  
Zhenyu Yu ◽  
Panlei Wang ◽  
Zhengyu Wang ◽  
...  
2018 ◽  
Vol 38 (1) ◽  
pp. 89-97 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Han Lu ◽  
Liang Ji ◽  
Hao Chen ◽  
...  

2019 ◽  
Vol 258 ◽  
pp. 117977 ◽  
Author(s):  
Asbel David Hernandez ◽  
Noora Kaisalo ◽  
Pekka Simell ◽  
Marco Scarsella

2016 ◽  
Vol 36 (3) ◽  
pp. 729-735 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Jianrong Zhang ◽  
Jialin Liu ◽  
Zongliang Zuo ◽  
...  

2016 ◽  
Vol 126 (3) ◽  
pp. 1621-1631 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Zongliang Zuo ◽  
Jianrong Zhang ◽  
Zhicheng Han ◽  
...  

2019 ◽  
Vol 33 (11) ◽  
pp. 11420-11438 ◽  
Author(s):  
Yumin Chen ◽  
Ruifeng Peng ◽  
Yao Xiao ◽  
Baoxu Zhang ◽  
Weijie Yan ◽  
...  

Fuel ◽  
2006 ◽  
Vol 85 (2) ◽  
pp. 143-149 ◽  
Author(s):  
M ONOZAKI ◽  
K WATANABE ◽  
T HASHIMOTO ◽  
H SAEGUSA ◽  
Y KATAYAMA

2010 ◽  
Vol 152-153 ◽  
pp. 817-820 ◽  
Author(s):  
Hong Wei Cheng ◽  
Xiong Gang Lu ◽  
Wei Zhong Ding

The steam reforming of simulated coke oven gas (COG) with toluene as a model tar compound for syngas production was investigated over Ni/Al2O3-MgO catalysts. XRD results showed that the catalysts with high calcination temperature and Al2O3 content after calcination formed (Ni,Mg)Al2O4 spinel and Ni-Mg-O solid solution structure. At optimized reaction conditions, toluene and CH4 can be completely converted, while a H2 yield of 71.8% and a CO yield of 76.1% have been achieved at 800 oC. The catalysts with appropriate calcination temperature and Al2O3 content showed better catalytic activity and resistance to coking, which will be promising catalysts in the catalytic reforming of COG.


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