Impact of using calcium oxide as a bed material on hydrogen production in two-stage fluidized bed gasification

被引:10
|
作者
Kuo, Jia-Hong [1 ,2 ]
Lin, Chiou-Liang [3 ]
Chang, Tsung-Jen [3 ]
Weng, Wang-Chang [3 ]
Liu, JingYong [1 ,2 ]
机构
[1] Guangdong Univ Technol, Sch Environm Sci & Engn, Guangzhou 510006, Guangdong, Peoples R China
[2] Guangdong Univ Technol, Inst Environm Hlth & Pollut Control, Guangzhou 510006, Guangdong, Peoples R China
[3] Natl Univ Kaohsiung, Dept Civil & Environm Engn, Kaohsiung 811, Taiwan
关键词
Biomass; Gasification; Calcium oxide; Syngas; Fluidized bed; ENRICHED-GAS-PRODUCTION; STEAM GASIFICATION; BIOMASS GASIFICATION; AIR GASIFICATION; HIGH-TEMPERATURE; WOODY BIOMASS; SYNGAS PRODUCTION; PERFORMANCE; PRETREATMENT; EFFICIENCY;
D O I
10.1016/j.ijhydene.2016.07.144
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
This paper describes the effect of equivalence ratio and steam/biomass ratio on the gas production of a two-stage fluidized bed gasifier. The calcium oxide was employed as bed material in the second stage to evaluate the influence of gasification efficiency. The result shows the H-2 molar percentage increased by approximately 2-3 mol% at the end of the second stage fluidized bed reactor without adding CaO. The second stage fluidized bed gasifier plays an important role of cracking and reforming of tar which generated from the first stage one. On the other hand, when the calcium oxide was used as the bed material in the second stage, it enhanced the generation of H2 under most parameters. Highest H-2 molar percentage in syngas was observed as 37 mol% at ER and S/B ratio is 0.3 and 2, respectively. Generally, more H-2 generation through second stage gasifier was found than that in first stage by 6.1-12.8%. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:17283 / 17289
页数:7
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