Catalytic steam reforming of bio-oil model compounds for hydrogen production over coal ash supported Ni catalyst

2014 ◽  
Vol 39 (5) ◽  
pp. 2018-2025 ◽  
Author(s):  
Shurong Wang ◽  
Fan Zhang ◽  
Qinjie Cai ◽  
Xinbao Li ◽  
Lingjun Zhu ◽  
...  
2020 ◽  
Vol 28 (9) ◽  
pp. 2328-2336 ◽  
Author(s):  
Ammaru Ismaila ◽  
Huanhao Chen ◽  
Yan Shao ◽  
Shaojun Xu ◽  
Yilai Jiao ◽  
...  

2010 ◽  
Vol 1279 ◽  
Author(s):  
P. Lan ◽  
Q. L. Xu ◽  
L. H. Lan ◽  
Y. J. Yan ◽  
J. A. Wang

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.


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 (22) ◽  
pp. 9234-9244 ◽  
Author(s):  
L.F. Bobadilla ◽  
F. Romero-Sarria ◽  
M.A. Centeno ◽  
J.A. Odriozola

2021 ◽  
Vol 212 ◽  
pp. 106622 ◽  
Author(s):  
Ahmed Tijani F. Afolabi ◽  
Panagiotis N. Kechagiopoulos ◽  
Yurong Liu ◽  
Chun-Zhu Li

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