Ni-CaO bifunctional catalyst for biomass catalytic pyrolysis to produce hydrogen-rich gas

被引:35
|
作者
Yue, Wenchang [1 ,2 ]
Ma, Xiaoqian [1 ,2 ]
Yu, Zhaosheng [1 ,2 ]
Liu, Hongyu [1 ,2 ]
Li, Meirong [1 ,2 ]
Lu, Xiaoluan [1 ,2 ]
机构
[1] South China Univ Technol, Sch Elect Power, Guangzhou 510640, Peoples R China
[2] Guangdong Prov Key Lab Efficient & Clean Energy Ut, Guangzhou 510640, Peoples R China
关键词
Corn cob; Catalytic pyrolysis; Ni-CaO bifunctional catalyst; CO2; capture; Hydrogen-rich pyrolysis gas; SYNGAS PRODUCTION; CO2; CAPTURE; PERFORMANCE; WASTE; DECOMPOSITION; NANOPARTICLES; CE1-XNIXO2-Y; CRACKING; SORBENT; METHANE;
D O I
10.1016/j.jaap.2023.105872
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
In this study, high-value conversion of biomass energy was achieved by catalytic pyrolysis of corn cob in a fixed-bed reaction system to produce hydrogen-rich gas. Specifically, the effects of synthesis temperature and catalyst metal ratio of Ni-CaO bifunctional adsorption catalyst on pyrolysis gas composition, yield, and hydrogen con -version were explored. The results show that the Ni1Ca7-750 catalyst has a uniform morphology, small partic-ulate size, large specific surface area, and good pore size distribution at a synthesis temperature of 750 degrees C and metal ratio of Ni/Ca = 1/7. Under the conditions of pyrolysis temperature of 600 degrees C and catalyst/biomass = 1/1, the syngas percentage of Ni1Ca7-750 was 85.81 vol. %, and the total pyrolysis gas yield reached 661.63 mL/ gbiomass with the highest H2 concentration (68.62 vol. %), hydrogen yield (450.15 mL/gbiomass) and hydrogen conversion (65.97 wt. %). The percentage of CO2 in the pyrolysis gas was 9.11 vol. %, which was 65.4 % lower than that of the corn cob pyrolysis blank group. Thus, this study provides a specific reference for catalytic py-rolysis technology for biomass resource development and clean production.
引用
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页数:11
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