CO2 capture by double metal modified CaO-based sorbents from pyrolysis gases

被引:0
|
作者
Chen, Xiaobin
Tang, Yuting [1 ]
Ke, Chuncheng
Zhang, Chaoyue
Ding, Sichun
Ma, Xiaoqian
机构
[1] South China Univ Technol, Sch Elect Power, Guangzhou 510640, Peoples R China
关键词
Pyrolysis gas; CO2; capture; Co-precipitation; CaO-based sorbents; Modified sorbents; CALCIUM-BASED SORBENT; CARBIDE SLAG PELLETS; FIXED-BED REACTOR; SEWAGE-SLUDGE; FLY-ASH; PERFORMANCE; STABILITY; WASTE; CALCINATION; CARBONATION;
D O I
10.1016/j.cjche.2021.09.002
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
High-temperature pyrolysis technology can effectively solve the problem of municipal solid waste pollution. However, the pyrolysis gas contains a large amount of CO2, which would adversely affect the subsequent utilization. To address this problem, a novel method of co-precipitation modification with Ca, Mg and Zr metals was proposed to improve the CO2 capture performance. X-ray diffraction (XRD) patterns and energy dispersive X-ray spectroscopy analysis showed that the two inert supports MgO and CaZrO3 were uniformly distributed in the modified calcium-based sorbents. In addition, the XRD results indicated that CaZrO3 was produced by the reaction of ZrO2 and CaO at high temperatures. The effects of doping ratios, adsorption temperature, calcination temperature, CO2 concentration and calcination atmosphere on the adsorption capacity and cycle stability of the modified calcium-based sorbent were studied. The modified calcium-based sorbent achieved the best CO(2 )capture performance when the doping ratio was 10:1:1 with carbonation at 700 degrees C under 20% CO2/80% N-2 atmosphere and calcination at 900 degrees C under 100% N-2 atmosphere. After ten cycles, the average carbonation conversion rate of Ca-10 sorbent was 72%. Finally, the modified calcium-based sorbents successfully reduced the CO2 concentration of the pyrolysis gas from 37% to 5%. (C) 2021 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:40 / 49
页数:10
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