The effect of addition of Ca, K and Mn over Ni-based catalyst on steam reforming of toluene as model tar compound

被引:61
作者
Heo, Dong Hyun [1 ]
Lee, Roosse [1 ]
Hwang, Jong Ha [1 ]
Sohn, Jung Min [1 ]
机构
[1] Chonbuk Natl Univ, Dept Mineral Resources & Energy Engn, 567 Baekje Daero, Jeonju 54896, South Korea
基金
新加坡国家研究基金会;
关键词
Steam reforming; Toluene; Tar; Ni; Mn; Dolomite; Carbon deposition; BIOMASS-DERIVED SYNGAS; FLUIDIZED-BED; NI/OLIVINE CATALYST; GASIFICATION; DOLOMITE; OLIVINE; DECOMPOSITION; CONVERSION; PROMOTER; BEHAVIOR;
D O I
10.1016/j.cattod.2015.09.057
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The catalytic activity and carbon deposition for toluene steam reforming were investigated by adding promoters such as K, Ca and Mn on 10 wt% Ni-based catalysts. The toluene steam reforming experiments were carried out at temperature of 800 degrees C under S/C ratio = 3. Catalyst characteristics were evaluated using XRD, BET, TPR and TGA. Ni/dolomite showed the highest hydrogen production and the toluene conversion efficiency to CO and CO2 among the catalysts. A slight enhancement effect was observed by adding K or Ca. By adding Mn on Ni/dolomite, the better toluene conversion efficiency to CO and CO2 was obtained than K and Ca and maintained constantly because of the resistance of carbon deposition. Conclusively, the addition of Mn on Ni/dolomite could give the stable catalytic activity for toluene steam reforming by suppressing the carbon deposition. (C) 2015 Published by Elsevier B.V.
引用
收藏
页码:95 / 102
页数:8
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