Characteristics of biomass gasification using chemical looping with iron ore as an oxygen carrier

被引:81
|
作者
Huang, Zhen [1 ]
He, Fang [1 ]
Feng, Yipeng [1 ]
Liu, Rundong [2 ]
Zhao, Kun [1 ]
Zheng, Anqing [1 ]
Chang, Sheng [1 ]
Zhao, Zengli [1 ]
Li, Haibin [1 ]
机构
[1] Chinese Acad Sci, Guangzhou Inst Energy Convers, Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Guangdong, Peoples R China
[2] Univ Toledo, Dept Environm Sci, Toledo, OH 43606 USA
基金
中国国家自然科学基金;
关键词
Biomass gasification; Chemical looping; Lattice oxygen; Iron ore; SYNTHESIS GAS-PRODUCTION; FLUIDIZED-BED; COMBUSTION; COAL; FE; OXIDE; CONVERSION; MINERALS; REACTOR; SCALE;
D O I
10.1016/j.ijhydene.2013.09.022
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
Experiments regarding to biomass gasification using chemical looping (BGCL) were carried out in a fluidized bed reactor under argon atmosphere. Iron ore (natural hematite) was used as an oxygen carrier in the study. Similar to steam, a performance of oxygen carrier which provided oxygen source for biomass gasification by acting as a gasifying medium was found. An optimum Fe2O3/C molar ratio of 0.23 was determined with the aim of obtaining maximum gas yield of 1.06 Nm(3)/kg and gasification efficiency of 83.31%. The oxygen carrier was gradually deactivated with reduction time increasing, inhibiting the carbon and hydrogen in biomass from being converted into synthesis gas. The fraction of Fe2+ increased from 0 to 47.12% after reduction time of 45 min, which implied that active lattice oxygen of 49.75% was consumed. The oxygen carrier of fresh and reacted was analyzed by a series of characterization methods, such as X-ray diffraction (XRD), Scanning electron microscopy (SEM), and Energy-dispersive X-ray spectroscopy (EDX). Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:14568 / 14575
页数:8
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