Experimental investigation on methanation reaction based on coal gasification in supercritical water

被引:49
作者
Jin Hui [1 ]
Zhao Xiao [1 ]
Guo Liejin [1 ]
Zhu Chao [1 ]
Cao Changqing [1 ]
Wu Zhenqun [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn SKLMF, 28 Xianning West Rd, Xian 710049, Shaanxi, Peoples R China
基金
中国国家自然科学基金;
关键词
Supercritical water gasification; Methanation; Synthetic natural gas; SNG; Coal; HYDROGEN-PRODUCTION; HETEROGENEOUS CATALYSIS; BIOMASS GASIFICATION; MEDIA; SYNGAS; PYROLYSIS;
D O I
10.1016/j.ijhydene.2016.06.216
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
Supercritical water gasification is a promising technology because it can convert coal into H-2 and CO2 which has potential for CH4 production. In order to obtain the optimal operating parameter for methane production, experimental investigations were conducted in the typical operating parameters: reaction temperature 380-520 degrees C, reaction residence time 6-10 min with different type of Raney-Ni. Gas mixture with volume ratio of 4:1 of H-2 and CO2 as a typical production of coal gasification in supercritical water was used as feedstock. The experiments results showed that Raney-Ni 4110 has the best performance in the methanation reaction and 400 degrees C reaction temperature and long residence time favored CH4 production. Based on the obtained optimal operation parameter, one-step CH4 production by Hongliulin gasification in one reactor with certain residence time at 400 degrees C was conducted. The results showed that one-step coal gasification was an efficient way to produce a high yield of CH4, and carbon gasification efficiency above 99% was achieved. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4636 / 4641
页数:6
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