Nickel supported on low-rank coal for steam reforming of ethyl acetate

被引:12
作者
Ruhswurmova, Nikola [1 ]
Kim, Soohyun [2 ]
Yoo, Jiho [2 ]
Chun, Donghyuk [2 ]
Rhim, Youngjoon [2 ]
Lim, Jeonghwan [2 ]
Kim, Sangdo [2 ]
Choi, Hokyung [2 ]
Lee, Sihyun [2 ]
机构
[1] Mondi Steti As, Litomericka 272, Steti 41108, Czech Republic
[2] Korea Inst Energy Res, Clean Fuel Lab, Daejeon 34129, South Korea
关键词
Low-rank coal; Carbon support; Catalytic support; Steam reforming; Nickel; Ethyl acetate; HYDROGEN-PRODUCTION; BROWN-COAL; CATALYTIC GASIFICATION; CARBON MATERIALS; SYNTHESIS GAS; BIO-OIL; METAL; TAR; PYROLYSIS; CHAR;
D O I
10.1016/j.ijhydene.2018.06.104
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
Ethyl acetate is a volatile organic compound (VOC) that has emerged as a major environmental pollutant and also one of representative components of bio-oil. In this study, mostly metallic Ni particles (size: <10 nm) were finely dispersed on low-rank coal (LRC) by the ion-exchange process. Catalytic steam reforming of ethyl acetate (EA) was performed over Ni supported on Eco LRC (Ni/Eco) to reduce EA emissions and simultaneously produce H-2. EA reforming over 17.7 wt% Ni/Eco at 400 degrees C results in H-2 yield of 70%-80%; this is comparable to that achieved with reforming over commercial Ni/Al2O3. Advantageously, metallic Ni particles are dominant over Ni oxides on LRC, and therefore, the pre-reduction step routinely required for an alumina-supported catalyst can be skipped. Furthermore, deactivation by coking is slower with Ni/Eco than with Ni/Al2O3 during long-term operation, probably because of the smaller particle size and preferential adsorption on the coal support. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:15880 / 15890
页数:11
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