Mechanism of In-Situ Catalytic Cracking of Biomass Tar over Biochar with Multiple Active Sites

D. Feng, Yu Zhang, Yijun Zhao, Shaozeng Sun
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引用次数: 2

Abstract

Biomass tar is the bottleneck in the development of efficient utilization of biomass syngas. The in-situ catalytic cracking biomass tar with multi-active biochar is investigated in a two-stage fluidized bed-fixed bed reactor. It indicates that adding H 2 O or CO 2 is found to improve the homogeneous and heterogeneous cracking of biomass tar. Activation of biochar by H 2 O or CO 2 impacted the morphology of biochar surface and distribution of metal species. H 2 O or CO 2 affects the creation and regeneration of pore structures, influencing the biochar structure and dynami-cal distribution of alkali and alkaline earth metal species (AAEMs), which ensure enough surface active sites to maintain the catalytic activity of biochar. The tar cracking into low-quality tar or small-molecule gas may be catalyzed by K, while the combination of tar with biochar would be promoted by Ca. The volatilizations of K and Ca, due to their reaction with volatiles, are to a large extent in accordance with their valences and boiling points. The subsequent transformation from the small aromatic ring systems to the larger ones occurs due to the volatile-biochar interaction. During tar cracking over biochar, K and Ca act as the active sites on biochar surface to promote the increase of active intermediates (C ▬ O bonds and C ▬ O ▬ K/Ca).
多活性位点生物炭原位催化裂解生物质焦油机理研究
生物质焦油是发展生物质合成气高效利用的瓶颈。在两级流化床固定床反应器上研究了多活性生物炭原位催化裂化生物质焦油的工艺。结果表明,加入h2o或co2均能改善生物质焦油的均相和非均相裂解。h2o或co2对生物炭的活化影响了生物炭表面的形态和金属的分布。h2o或CO 2影响孔隙结构的形成和再生,影响生物炭的结构和碱和碱土金属(aaem)的动态分布,从而保证生物炭有足够的表面活性位点维持催化活性。K可催化焦油裂解为低质量焦油或小分子气体,而Ca可促进焦油与生物炭的结合。K和Ca与挥发物发生反应,其挥发量在很大程度上与它们的价和沸点有关。由于挥发物与生物炭的相互作用,随后由小芳环系统向大芳环系统转变。在生物炭的焦油裂解过程中,K和Ca作为生物炭表面的活性位点,促进活性中间体(C - O键和C - O - K/Ca)的增加。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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