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Preparation and characterization of furfural residue derived char-based catalysts for biomass tar cracking.
Bai, Jing; He, Zheng; Yang, Luying; Wei, Xianyun; Hu, Junhao; Li, Pan; Yan, Zhenli; Chen, Zhijuan; Chang, Chun.
Afiliação
  • Bai J; School of Mechanical and Power Engineering, Zhengzhou University, Zhengzhou, Henan 450001, China.
  • He Z; School of Mechanical and Power Engineering, Zhengzhou University, Zhengzhou, Henan 450001, China.
  • Yang L; School of Chemical Engineering, Zhengzhou University, Zhengzhou, Henan 450001, China.
  • Wei X; School of Mechanical and Power Engineering, Zhengzhou University, Zhengzhou, Henan 450001, China.
  • Hu J; School of Mechanical and Power Engineering, Zhengzhou University, Zhengzhou, Henan 450001, China; National Key Laboratory of Biobased Transport Fuel Technology, Zhengzhou, Henan 450001, China; Hubei Key Laboratory of Industrial Fume and Dust Pollution Control, Jianghan University, Wuhan, Hubei 43005
  • Li P; School of Mechanical and Power Engineering, Zhengzhou University, Zhengzhou, Henan 450001, China.
  • Yan Z; National Key Laboratory of Biobased Transport Fuel Technology, Zhengzhou, Henan 450001, China.
  • Chen Z; Henan Key Laboratory of Green Manufacturing of Biobased Chemicals, Puyang, Henan 457000, China.
  • Chang C; School of Chemical Engineering, Zhengzhou University, Zhengzhou, Henan 450001, China; National Key Laboratory of Biobased Transport Fuel Technology, Zhengzhou, Henan 450001, China; Henan Center for Outstanding Overseas Scientists, Zhengzhou, Henan 450001, China; Henan Key Laboratory of Green Manufac
Waste Manag ; 179: 182-191, 2024 Apr 30.
Article em En | MEDLINE | ID: mdl-38479257
ABSTRACT
This study proposed an innovative strategy of catalytic cracking of tar during biomass pyrolysis/gasification using furfural residue derived biochar-based catalysts. Fe, Co, and Ni modified furfural residue char (FRC-Fe, FRC-Co, and FRC-Ni) were prepared by one-step impregnation method. The influences of cracking temperature and metal species on the tar cracking characteristics were investigated. The results showed that the tar conversion efficiency for all catalysts were improved with the cracking temperature increasing, the higher tar conversion efficiency achieved at 800 °C were 66.72 %, 89.58 %, 84.58 %, and 94.70 % for FRC, FRC-Fe, FRC-Co, and FRC-Ni respectively. FRC-Ni achieved the higher gas (H2, CO, CH4, CO2) yield 681.81 mL/g. At 800 °C, the catalyst (FRC-Ni) still reached a high tar conversion efficiency over 85.90 % after 5 cycles. SEM-EDS results showed that the distribution of Ni particles on the biochar support was uniform. TGA results demonstrated that FRC-Ni exhibited better thermal stability. XRD results indicated that there was no significant change in the grain size of Ni before and after the reaction. The FRC-Ni catalyst was reasonably stable due to its better anti-sintering and coke-resistant capabilities.
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Texto completo: 1 Base de dados: MEDLINE Assunto principal: Carvão Vegetal / Furaldeído / Gases Idioma: En Ano de publicação: 2024 Tipo de documento: Article

Texto completo: 1 Base de dados: MEDLINE Assunto principal: Carvão Vegetal / Furaldeído / Gases Idioma: En Ano de publicação: 2024 Tipo de documento: Article