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

被引:106
|
作者
Wang, Shurong [1 ]
Zhang, Fan [1 ]
Cai, Qinjie [1 ]
Li, Xinbao [1 ]
Zhu, Lingjun [1 ]
Wang, Qi [2 ]
Luo, Zhongyang [1 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Zhejiang, Peoples R China
[2] China Jiliang Univ, Coll Metrol Technol & Engn, Hangzhou 310018, Zhejiang, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrogen; Reforming; Coal ash; Bio-oil; Acetic acid; Phenol; BIOMASS PYROLYSIS OIL; ACETIC-ACID; FLUIDIZED-BED; RH CATALYSTS; FE CATALYSTS; GASIFICATION; TEMPERATURE; MECHANISM; PHENOL; FUEL;
D O I
10.1016/j.ijhydene.2013.11.129
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The development of a high performance and low cost catalyst is an important contribution to clean hydrogen production via the catalytic steam reforming of renewable bio-oil. Solid waste coal ash, which contains SiO2, Al2O3, Fe2O3 and many alkali and alkaline earth metal oxides, was selected as a superior support for a Ni-based catalyst. The chemical composition and textural structures of the ash and the Ni/Ash catalysts were systematically characterized. Acetic acid and phenol were selected as two typical bio-oil model compounds to test the catalyst activity and stability. The conversion of acetic acid and phenol reached as much as 98.4% and 83.5%, respectively, at 700 degrees C. It is shown that the performance of the Ni/Ash catalyst was comparable with other commercial Ni-based steam reforming catalysts. Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2018 / 2025
页数:8
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