Biomass CO2 gasification with CaO looping for syngas production in a fixed-bed reactor

被引:56
作者
Gao, Ningbo [1 ]
Sliz, Maciej [2 ]
Quan, Cui [1 ]
Bieniek, Artur [2 ]
Magdziarz, Aneta [2 ]
机构
[1] Xi An Jiao Tong Univ, Sch Energy & Power Engn, Xian 710049, Peoples R China
[2] AGH Univ Sci & Technol, 30 Mickiewicza Av, PL-30059 Krakow, Poland
基金
欧盟地平线“2020”;
关键词
gasification; CO2; capture; CaO looping; TG-FTIR; ENRICHED-GAS-PRODUCTION; PURITY HYDROGEN-PRODUCTION; STEAM GASIFICATION; TG-FTIR; CAPTURE; PYROLYSIS; COAL; TECHNOLOGY; EMISSIONS; SAWDUST;
D O I
10.1016/j.renene.2020.11.134
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The most important challenge in solid feedstock thermal conversion methods is minimising CO2 emissions. In this work, the gasification of pine sawdust in a mixture of N-2 and CO2 was investigated for the reduction of CO2 by a calcium oxide loop. The experiments were conducted at 600, 700, and 800 degrees C in a fixed-bed reactor. The biomass was mixed with the calcium oxide at a ratio of 1:1. The chemical composition of the syngas was analysed using gas chromatography. Moreover, the high heating values of the received gas samples were calculated, and thermogravimetric analysis and Fourier-transform infrared spectroscopy analysis were performed to investigate the absorption of CO2 by CaO. The results of the gasification process showed that the syngas contained CO, CH4, CO2, H-2, N-2, and other low hydrocarbons. The most significant results were obtained for a 2:1 ratio of N-2 to CO2 at 700 degrees C, and a CO2 reduction of 25% was observed. Moreover, the catalytic properties of CaO increased the concentration of H-2 in the produced syngas by up to 10%. A temperature of 800 degrees C was too high for the carbonation reaction of CaO. This study presents a possible solution for achieving negative carbon emissions. (c) 2020 The Author(s). Published by Elsevier Ltd. This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0/).
引用
收藏
页码:652 / 661
页数:10
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