Steam reforming of toluene as model compounds of biomass tar by Fe-K-based biochar nano-catalysts at mild temperatures

被引:1
作者
Yu, Zhihao [1 ,2 ]
Guo, Zizhao [1 ,2 ]
Lang, Lin [1 ,2 ]
Yu, Yang [3 ]
Wei, Jian [3 ]
Yin, Xiuli [1 ,2 ]
Wu, Chuangzhi [2 ]
机构
[1] Univ Sci & Technol China, Sch Energy Sci & Engn, Hefei 230026, Peoples R China
[2] Chinese Acad Sci, Guangzhou Inst Energy Convers, CAS Key Lab Renewable Energy, Guangdong Prov Key Lab Renewable Energy, Guangzhou 510640, Peoples R China
[3] Chinese Acad Sci, Dalian Inst Chem Phys, Dalian Natl Lab Clean Energy, Dalian 116023, Peoples R China
关键词
Biomass gasification; Toluene; Steam reforming; Biochar catalyst; Tar removal; HYDROGEN-PRODUCTION; IN-SITU; GASIFICATION; PYROLYSIS; CARBON; CONVERSION; SYNGAS; GAS; DECOMPOSITION; REACTIVITY;
D O I
10.1016/j.ijhydene.2024.10.365
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
Development of efficient catalysts for steam reforming of biomass tar is crucial for the widespread application of biomass gasification. In this work, a novel biochar nano-catalyst (BN) is conveniently prepared via one-step catalytic pyrolysis, using K and Fe to adjust the surface structure of the biochar, thereby enhancing the activity for toluene reforming. Fe-K/BN is tested in a fixed-bed reactor for steam reforming of toluene, a model compound of biomass tar, achieving a 100% toluene conversion rate at 650 degrees C. Fe-K/BN is activated in situ with steam to increase their specific surface area and enhance the O-containing functional groups on the surface, improving toluene adsorption and reforming. Finally, the stability of Fe-K/BN is tested in the simulated syngas, maintaining a 100% toluene conversion rate during a 26-h continuous catalytic reforming experiment. This work provides a promising strategy for the design of an active and stable catalyst for toluene reforming, which has potential for application of tar steam reforming during biomass gasification.
引用
收藏
页码:238 / 249
页数:12
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