Influence of coal bottom ash additives on catalytic reforming of biomass pyrolysis gaseous tar and biochar/steam gasification reactivity

被引:10
作者
Li, Jie [1 ,2 ,4 ]
Chang, Guozhang [3 ,4 ]
Song, Ke [1 ]
Hao, Bolun [1 ]
Wang, Cuiping [3 ]
Zhang, Jian [1 ,4 ]
Yue, Guangxi [3 ,5 ]
Hu, Shugang [1 ]
机构
[1] Shandong Univ Sci & Technol, Coll Safety & Environm Engn, Qingdao 266590, Shandong, Peoples R China
[2] Guangzhou Inst Energy Convers, CAS Key Lab Renewable Energy, Guangzhou 510640, Guangdong Provi, Peoples R China
[3] Shandong Univ Sci & Technol, Coll Civil Engn & Architecture, Clean Energy Lab, Qingdao 266590, Shandong Provin, Peoples R China
[4] Shandong Univ Sci & Technol, Inst Yellow River Delta Earth Surface Proc & Ecol, Qingdao 266590, Shandong, Peoples R China
[5] Tsinghua Univ, Dept Energy & Power Engn, Beijing 10084, Peoples R China
基金
中国国家自然科学基金;
关键词
Biomass; Gasification; Coal bottom ash; Catalytic reforming; Tar removal; Kinetics; BUBBLING FLUIDIZED-BED; STEAM GASIFICATION; THERMOCHEMICAL CONVERSION; CHAR GASIFICATION; SOLID REACTIONS; CO2; MODEL; TOLUENE; OPTIMIZATION; COCOMBUSTION;
D O I
10.1016/j.renene.2022.12.037
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This work investigated the effect of CBA additives as bed material in gasification process on gaseous tar catalytic reforming characteristic and biochar/steam gasification reactivity adopting a lab-scale dual-stage fixed bed furnace and a thermogravimetric analyzer equipped with water vapor furnace. Results showed that CBA additive exhibited good catalytic performance for tar cracking and gas upgrading effect on the basis of larger specific surface area as well as higher content of metallic matters. Particularly, tar conversion efficiency and syngas acquired peaking at 92.39% and 594.3 mL/g adopting mixing biochar (PSC) with CBA at ratio of 1:15 (PSC-15CBA) as catalyst at reforming temperature of 900 degrees C, respectively, in which the main components of syngas are H2, CO and CH4. It is noted that PSC-nCBA exhibited higher deoxygenation extent and single-ring aromatics and aliphatic selectivity in tar, and the polycyclic aromatics selectivity evidently decreased. The CBA additive has a beneficial impact on the biochar/steam gasification reactivity. Interestingly, a relatively high proportion of CBA additive has a negative impact on promoting reactivity. Result from kinetics analysis that CBA additive had ability to reduce the activation energy of PSC gasification process.
引用
收藏
页码:434 / 444
页数:11
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