Enhancement of depolymerization slag gasification in supercritical water and its gasification performance in fluidized bed reactor

被引:63
作者
Wang, Cui [1 ]
Zhu, Chao [2 ]
Huang, Jianbing [1 ]
Li, Linfeng [1 ]
Jin, Hui [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, 28 Xianning West Rd, Xian 710049, Peoples R China
[2] State Grid Shaanxi Elect Power Res Inst, 669 Middle Aerosp Rd, Xian 710100, Peoples R China
基金
中国国家自然科学基金;
关键词
Depolymerization slag; Supercritical water gasification; Mechanism; Fluidized bed reactor; HYDROGEN-PRODUCTION; BIOMASS GASIFICATION; BLACK LIQUOR; COAL; CONVERSION; MECHANISM; WASTE; MODEL; CHAR;
D O I
10.1016/j.renene.2020.12.104
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Supercritical water gasification (SCWG) can achieve efficient utilization of solid wastes, including depolymerization slag, biomass, municipal sludge, and others, and can produce hydrogen-rich gas. But phenolic intermediates produced during the gasification process are difficult to be gasified. It restricted the increase of conversion efficiency. Thus, in this paper, two effective schemes were put forward to raise the gasification efficiency of depolymerization slag. The first one was to add oxidants to promote the decomposition of hydrolysates. Carbon gasification efficiency (CGE) and hydrogen gasification efficiency (HGE) reached 71% and 74% respectively at the time of 1200 s. They raised by 41.6% and 60.5%, separately compared with non-oxidants addition. The second one was to raise the reaction temperature since a higher temperature can accelerate the reaction rate and obtain a high hydrogen yield. The results showed that hydrogen percentage increased by 32.82% and CGE and HGE increased by 35.39% and 219.85%, respectively when the reaction temperature raised by 200 degrees C. Based on the obtained gasification mechanism, the catalytic gasification. (c) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页码:829 / 837
页数:9
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