Steam Reforming of Model Compounds and Fast Pyrolysis Bio-oil on Supported Nickle Metal Catalysts for Hydrogen Production

2012 ◽  
Vol 34 (21) ◽  
pp. 2004-2015 ◽  
Author(s):  
P. Lan ◽  
Q.-L. Xu ◽  
L.-H. Lan ◽  
D. Xie ◽  
S.-P. Zhang ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Fast Pyrolysis ◽  
Metal Catalysts ◽  
Model Compounds ◽  
Bio Oil

Steam reforming of model compounds and fast pyrolysis bio-oil on supported noble metal catalysts

2005 ◽  
Vol 61 (1-2) ◽  
pp. 130-139 ◽  
Author(s):  
Cyrille Rioche ◽  
Shrikant Kulkarni ◽  
Frederic C. Meunier ◽  
John P. Breen ◽  
Robbie Burch
Keyword(s):  
Noble Metal ◽  
Steam Reforming ◽  
Fast Pyrolysis ◽  
Metal Catalysts ◽  
Model Compounds ◽  
Noble Metal Catalysts ◽  
Bio Oil

Hydrogen Production via Catalytic Steam Reforming of Fast Pyrolysis Bio-oil in a Fluidized-Bed Reactor

2010 ◽  
Vol 24 (12) ◽  
pp. 6456-6462 ◽  
Author(s):  
Qingli Xu ◽  
Ping Lan ◽  
Baozhen Zhang ◽  
Zhizhong Ren ◽  
Yongjie Yan
Keyword(s):  
Hydrogen Production ◽  
Fluidized Bed ◽  
Steam Reforming ◽  
Fast Pyrolysis ◽  
Fluidized Bed Reactor ◽  
Bio Oil ◽  
Catalytic Steam Reforming

Steam reforming of bio-oil from rice husks fast pyrolysis for hydrogen production

2011 ◽  
Vol 102 (19) ◽  
pp. 9236-9240 ◽  
Author(s):  
Tianju Chen ◽  
Ceng Wu ◽  
Ronghou Liu
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Fast Pyrolysis ◽  
Rice Husks ◽  
Bio Oil

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

Investigation on hydrogen production by catalytic steam reforming of maize stalk fast pyrolysis bio-oil

2014 ◽  
Vol 39 (26) ◽  
pp. 13962-13971 ◽  
Author(s):  
Peng Fu ◽  
Weiming Yi ◽  
Zhihe Li ◽  
Xueyuan Bai ◽  
Andong Zhang ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Fast Pyrolysis ◽  
Bio Oil ◽  
Catalytic Steam Reforming

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
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