Hydrogen production via steam reforming of bio-oil model compounds over supported nickel catalysts

2015 ◽  
Vol 24 (3) ◽  
pp. 299-308 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Xin Yao ◽  
Wenjun Duan ◽  
Zongliang Zuo ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Model Compounds ◽  
Bio Oil ◽  
Supported Nickel Catalysts

Hydrogen production from catalytic steam reforming of glycerol over various supported nickel catalysts

2017 ◽  
Vol 42 (14) ◽  
pp. 9087-9098 ◽  
Author(s):  
Nurul Huda Zamzuri ◽  
Ramli Mat ◽  
Nor Aishah Saidina Amin ◽  
Amin Talebian-Kiakalaieh
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Supported Nickel Catalysts ◽  
Catalytic Steam Reforming

Hydrogen production via steam reforming of ethylene glycol over Attapulgite supported nickel catalysts

2018 ◽  
Vol 43 (45) ◽  
pp. 20438-20450 ◽  
Author(s):  
Yishuang Wang ◽  
Mingqiang Chen ◽  
Xiaojing Li ◽  
Zhonglian Yang ◽  
Tian Liang ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Ethylene Glycol ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Supported Nickel Catalysts

Hydrogen Production by Catalytic Steam Reforming of Model Compounds of Biomass Fast Pyrolysis Oil

2010 ◽  
Vol 1279 ◽  
Author(s):  
P. Lan ◽  
Q. L. Xu ◽  
L. H. Lan ◽  
Y. J. Yan ◽  
J. A. Wang
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Space Velocity ◽  
Molar Ratio ◽  
Hydrogen Yield ◽  
Pyrolysis Oil ◽  
Model Compounds ◽  
Liquid Hourly Space Velocity ◽  
Bio Oil ◽  
Catalytic Steam Reforming

AbstractA Ni/MgO-La2O3-Al2O3 catalyst with Ni as active component, Al2O3 as support, MgO and La2O3 as additives was prepared and its catalytic activity was evaluated in the process of hydrogen production from catalytic steam reforming of bio-oil. In the catalytic evaluation, some typical components present in bio-oil such as acetic acid, butanol, furfural, cyclopentanone and m-cresol were mixed following a certain proportion as model compounds. Reaction parameters like temperature, steam to carbon molar ratio and liquid hourly space velocity were studied with hydrogen yield as index. The optimal reaction conditions were obtained as follows: temperature 750-850 °C, steam to carbon molar ratio 5-9, liquid hourly space velocity 1.5-2.5 h-1. The maximum hydrogen yield was 88.14%. The carbon deposits were formed on the catalyst surface but its content decreased as reaction temperature increased in the bio-oil steam reforming process.

Thermodynamic analysis of hydrogen production from model compounds of bio-oil through steam reforming

2013 ◽  
Vol 33 (3) ◽  
pp. 1008-1016 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Kun Wang ◽  
Xiaobo Shi ◽  
Xinhui Li
Keyword(s):  
Hydrogen Production ◽  
Thermodynamic Analysis ◽  
Steam Reforming ◽  
Model Compounds ◽  
Bio Oil

Hydrogen production from steam reforming of ethylene glycol over supported nickel catalysts

2015 ◽  
Vol 43 (5) ◽  
pp. 581-588 ◽  
Author(s):  
Xing-ling ZHAO ◽  
Yan-an LÜ ◽  
Wei-ping LIAO ◽  
Ming-shan JIN ◽  
Zhang-huai SUO
Keyword(s):  
Hydrogen Production ◽  
Ethylene Glycol ◽  
Steam Reforming ◽  
Nickel Catalysts ◽  
Supported Nickel Catalysts
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