Development of activated biochar supported Ni catalyst for enhancing toluene steam reforming

被引:41
|
作者
Quan, Cui [1 ]
Wang, Huihui [1 ]
Gao, Ningbo [1 ]
机构
[1] Xi An Jiao Tong Univ, Sch Energy & Power Engn, Xian 710049, Peoples R China
基金
欧盟地平线“2020”; 中国国家自然科学基金;
关键词
activated biochar; hydrogen production; steam reforming; toluene; TAR MODEL-COMPOUND; RICH SYNGAS PRODUCTION; HYDROGEN-PRODUCTION; BIOMASS TAR; BIO-OIL; PYROLYSIS; PERFORMANCE; CHAR; CO; DECOMPOSITION;
D O I
10.1002/er.5335
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Catalytic steam reforming of tar is considered to be an attractive pathway for tar removal and H-2 production in the modern world. In this study, activation of biochar (B) from pine wood pyrolysis was performed to boost its specific surface area and pore structure. The activated biochar (AB) was used as a catalyst support with the aim to enhance the catalytic activity. The catalytic reforming performance of toluene over Ni/AB catalyst was investigated, and the catalytic behavior of Ni/AB catalysts was compared with Ni/Al2O3 and Ni/B. The effect of potassium hydroxide (KOH) to biochar ratio, Ni loading, reforming temperature, weight hourly space velocity and steam to carbon ratio(S/C) on the performance of Ni/AB catalysts were studied. The results showed that Ni/AB catalysts exhibited a superior catalytic activity for carbon conversion and H-2 production to Ni/B and Ni/Al2O3 catalysts. In addition, high carbon conversion (86.2%) and H-2 production (64.3%) can be achieved with Ni/AB catalyst under the optimal operating conditions. Furthermore, in order to improve the stability of the Ni/AB catalyst, Ce was introduced to Ni/AB catalyst. According to stability tests, the H-2 concentration of Ni-Ce/AB catalysts was still higher than 2.24 mmol/min even after 20 hours reaction.
引用
收藏
页码:5749 / 5764
页数:16
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