Integration of biomass catalytic pyrolysis and methane aromatization over Mo/HZSM-5 catalysts

被引:48
|
作者
Yang, Zixu [1 ]
Kumar, Ajay [1 ]
Apblett, Allen [2 ]
机构
[1] Oklahoma State Univ, Biosyst & Agr Engn Dept, Biobased Prod & Energy Ctr, Stillwater, OK 74078 USA
[2] Oklahoma State Univ, Dept Chem, Stillwater, OK 74078 USA
基金
美国食品与农业研究所;
关键词
Biomass catalytic pyrolysis; Methane aromatization; Aromatic hydrocarbons; Bifunctional catalysts; Biofuels; DIRECT CONVERSION; COAL PYROLYSIS; ZSM-5; CO2; BENZENE; VAPORS; FUELS; OIL;
D O I
10.1016/j.jaap.2016.06.021
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
The development of an effective process to convert bio-oil into intermediate platforms that are compatible with the existing refinery infrastructure is highly needed. To overcome the high cost of hydrogen consumption in conventional bio-oil upgrading processes, this paper reports a novel process that converts three major biomass constituents (cellulose, hemicellulose and lignin) directly into liquid fuels via pyrolysis in the presence of methane over molybdenum impregnated HZSM-5 catalysts. The carbon yield of total aromatics from lignin increased from 12.80 to 15.13% when pyrolysis atmosphere switched from helium to methane in the presence of HZSM-5 support. However, methane was not effective in improving the aromatics yield from cellulose and hemicellulose in the presence of Mo-modified HZSM-5 catalysts. The molybdenum impregnated catalyst was found to promote deoxygenation of lignin-derived phenols. The carbon yield of polyaromatics from lignin was 5.47% in the presence of HZSM-5 support under methane, compared to 2.61% that obtained in the presence of Mo2C/HZSM-5. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:484 / 492
页数:9
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