Preparation and characterization of furfural residue derived char-based catalysts for biomass tar cracking.

Waste Manag

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 Manufacturing of Biobased Chemicals, Puyang, Henan 457000, China.

Published: April 2024

AI Article Synopsis

  • This study explored a new method to improve the catalytic cracking of tar during biomass pyrolysis using biochar-based catalysts made from furfural residue.
  • The metal-modified catalysts (FRC-Fe, FRC-Co, FRC-Ni) showed significantly better tar conversion efficiencies at higher temperatures, with FRC-Ni achieving the best results at 800 °C.
  • FRC-Ni exhibited high gas yields, excellent stability across multiple cycles, and uniform particle distribution, making it the most effective catalyst in terms of performance and durability.

Article 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 (H, CO, CH, CO) 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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http://dx.doi.org/10.1016/j.wasman.2024.03.013DOI Listing

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