The production of hydrogen-rich gas by catalytic pyrolysis of biomass using waste heat from blast-furnace slag

被引:55
|
作者
Luo, Siyi [1 ]
Fu, Jie [2 ]
Zhou, Yangmin [1 ]
Yi, Chuijie [1 ]
机构
[1] Qingdao Technol Univ, Sch Environm & Municipal Engn, 11 Fushun Rd, Qingdao 266033, Peoples R China
[2] Georgia Inst Technol, Sch Civil & Environm Engn, Atlanta, GA 30332 USA
基金
中国国家自然科学基金; 中国博士后科学基金;
关键词
Biomass; Catalytic pyrolysis; Waste heat; Molten slag; MOLTEN SLAG; STEAM GASIFICATION; FLUIDIZED-BED; FEASIBILITY; GRANULATION; RECOVERY; COAL;
D O I
10.1016/j.renene.2016.09.072
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The granulation for molten slag produces a large amount of sensible and recoverable heat. In this paper, a system was proposed to simultaneously produce glassy slag and reuse the heat for production of hydrogen-rich gas via biomass catalytic pyrolysis. A variety of parameters, including slag temperature, mass ratio of slag to biomass (S/B), particles size, and rotor speed, were evaluated for their effects on pyrolysis product yields and gas characteristics. The catalytic activity of blast-furnace (BF) slag for improving tar cracking was also addressed. The conditions of 1000 degrees C of slag temperature and 0.6 of S/B achieved a complete pyrolysis of biomass. When the S/B value increased to 0.8, a lower slag temperature (700 degrees C) can afford a complete pyrolysis of biomass. The maximum gas yield was gained at a rotor speed of 16 rpm/min, when slag particles in reactor showed a "cascading" movement. BF slag exhibited a catalytic activity in tar cracking and CnHm reforming during biomass pyrolysis process. Furthermore, decreasing the slag particle size favored to produce more light gases, and less char and condensate. However, the effect of slag particle size became not evident in the subsequent catalytic reforming process. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1030 / 1036
页数:7
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