Renewable hydrogen production from bio-oil derivative via catalytic steam reforming: An overview

2017 ◽  
Vol 79 ◽  
pp. 347-357 ◽  
Author(s):  
Walid Nabgan ◽  
Tuan Amran Tuan Abdullah ◽  
Ramli Mat ◽  
Bahador Nabgan ◽  
Yahya Gambo ◽  
...  
Author(s):  
Piyush Pratap Singh ◽  
Neelkanth Nirmalkar ◽  
Tarak Mondal

Catalytic steam reforming (SR) of agricultural waste derived bio-oil for hydrogen production is a unique technology, offering twin benefits of waste management as well as sustainable energy production. In the...


2016 ◽  
Vol 41 (4) ◽  
pp. 2345-2353 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Zongliang Zuo ◽  
Zhicheng Han ◽  
Xin Yao ◽  
...  

2013 ◽  
Vol 38 (10) ◽  
pp. 3948-3955 ◽  
Author(s):  
Shaomin Liu ◽  
Mingqiang Chen ◽  
Lei Chu ◽  
Zhonglian Yang ◽  
Chuanhao Zhu ◽  
...  

2016 ◽  
Vol 59 (15-16) ◽  
pp. 1343-1353 ◽  
Author(s):  
Tarak Mondal ◽  
Nidhi Kaul ◽  
Ritesh Mittal ◽  
Kamal K. Pant

2010 ◽  
Vol 24 (12) ◽  
pp. 6456-6462 ◽  
Author(s):  
Qingli Xu ◽  
Ping Lan ◽  
Baozhen Zhang ◽  
Zhizhong Ren ◽  
Yongjie Yan

2011 ◽  
Vol 347-353 ◽  
pp. 2231-2235 ◽  
Author(s):  
Ping Lan ◽  
Li Hong Lan ◽  
Tao Xie ◽  
An Ping Liao

Catalytic steam reforming of bio-oil is an economically feasible route producing renewable hydrogen. Ni/MgO-La2O3-Al2O3 catalyst was prepared with Ni as active agent, Al2O3 as support and MgO, La2O3 as promoters. The experiments were carried out in a fixed-bed reactor. The content of Ni, calcination temperature, and calcinations time, were investigated with hydrogen yield as index. The optimal preparation conditions were concluded as follows: the Ni content 18%, the calcination temperature 8500C and the calcinations time 6 h.


2019 ◽  
Vol 44 (29) ◽  
pp. 14671-14682 ◽  
Author(s):  
C. Italiano ◽  
K. Bizkarra ◽  
V.L. Barrio ◽  
J.F. Cambra ◽  
L. Pino ◽  
...  

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