Evaluation of Engineered Biochar-Based Catalysts for Syngas Production in a Biomass Pyrolysis and Catalytic Reforming Process

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作者
Yang, Hanmin [1 ]
Cui, Yuxiao [2 ]
Jin, Yanghao [1 ]
Lu, Xincheng [3 ]
Han, Tong [1 ]
Sandstrom, Linda [4 ]
Jonsson, Par G. [1 ]
Yang, Weihong [1 ]
机构
[1] KTH Royal Inst Technol, Dept Mat Sci & Engn, S-11428 Stockholm, Sweden
[2] KTH Royal Inst Technol, Dept Fibre & Polymer Technol, S-10044 Stockholm, Sweden
[3] CAF, Inst Chem Ind Forest Prod, Nanjing 210042, Jiangsu, Peoples R China
[4] RISE Energy Technol Ctr AB, SE-94128 Pitea, Sweden
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中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Biochar, originating from biomass pyrolysis, has been proven a promising catalyst for tar cracking/reforming with great coke resistance. This work aims to evaluate various engineered biochar-based catalysts on syngas production in a biomass pyrolysis and catalytic reforming process without feeding extra steam. The tested engineered biochar catalysts include physical-and chemical-activated, nitrogen-doped, and nickel-doped biochars. The results illustrated that the syngas yields were comparable when using biochar and activated biochar as catalysts. A relatively high specific surface area (SSA) and a hierarchical porous structure are beneficial for syngas and hydrogen production. A 2 h physical-activated biochar catalyst induced the syngas with the highest H2/CO ratio (1.5). The use of N-doped biochar decreased the syngas yield sharply due to the collapse of the pore structure but obtained syngas with the highest LHVgas (18.5MJ/Nm3). The use of Ni-doped biochar facilitated high syngas and hydrogen yields (78.2 wt % and 26 mmol H2/g-biomass) and improved gas energy conversion efficiency (73%). Its stability and durability test showed a slight decrease in performance after a three-time repetitive use. A future experiment with a longer time is suggested to determine when the catalyst will finally deactivate and how to reduce the catalyst deterioration.
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页数:11
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