Experimental study on hydrogen production by lignite gasification in supercritical water fluidized bed reactor using external recycle of liquid residual

被引:107
作者
Jin, Hui [1 ]
Fan, Chao [1 ]
Guo, Liejin [1 ]
Liu, Shanke [1 ]
Cao, Changqing [1 ]
Wang, Runyu [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xianning West Rd, Xian 710049, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
Supercritical water gasification; Lignite; Fluidized bed; External recycle; Hydrogen production; CATALYTIC GASIFICATION; PHENOL MIXTURES; BIOMASS GASIFICATION; STEAM GASIFICATION; TAIHEIYO COAL; EXTRACTION; GENERATION; OXIDATION; GLUCOSE; EXPLORE;
D O I
10.1016/j.enconman.2017.04.102
中图分类号
O414.1 [热力学];
学科分类号
摘要
The technology of supercritical water gasification provides a novel way to convert high-moisture lignite to hydrogen-rich products directly. According to the energy analysis of the whole system for supercritical water gasification, the energy recovery of liquid residual played a key role in the energy efficiency improvement. Moreover, previous research findings showed that some chemical compounds such as phenols and formic acid contained in liquid residual can be recycled to increase the yield of hydrogen. Therefore, an external recycle of liquid residual was used in the supercritical water fluidized bed system to recover not only the heat energy but also the chemical energy by re-gasification of the liquid residual. Besides, the separation of gaseous products from the system enhanced the gasification process. Hydrogen production experiments were operated in this system and the influence of operating temperature 470550 C-omicron, pressure 23-27 MPa, concentration 3-35 wt% and cycling flow rate 0-70 g/min were studied. The experimental results showed that hydrogen yield and carbon gasification efficiency reached 32 mol/kg and 82%, respectively, at 530 C-omicron. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:214 / 219
页数:6
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