Biomass:polystyrene co-pyrolysis coupled with metal-modified zeolite catalysis for liquid fuel and chemical production

被引:28
作者
Dyer, Andrew C. [1 ]
Nahil, Mohamad A. [1 ]
Williams, Paul T. [1 ]
机构
[1] Univ Leeds, Sch Chem & Proc Engn, Leeds LS2 9JT, W Yorkshire, England
基金
英国工程与自然科学研究理事会;
关键词
Biomass; Waste plastic; zeolite; Catalyst; Bio-oil; BIO-OIL PRODUCTION; BIOMASS PYROLYSIS; RECENT PROGRESS; WASTE PLASTICS; LIGNOCELLULOSIC BIOMASS; POLYSTYRENE; GASIFICATION; POLYETHYLENE; CONVERSION; CELLULOSE;
D O I
10.1007/s10163-021-01334-0
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Biomass and waste polystyrene plastic (ratio 1:1) were co-pyrolysed followed by catalysis in a two-stage fixed bed reactor system to produce upgraded bio-oils for production of liquid fuel and aromatic chemicals. The catalysts investigated were ZSM-5 impregnated with different metals, Ga, Co, Cu, Fe and Ni to determine their influence on bio-oil upgrading. The results showed that the different added metals had a different impact on the yield and composition of the product oils and gases. Deoxygenation of the bio-oils was mainly via formation of CO2 and CO via decarboxylation and decarbonylation with the Ni-ZSM-5 and Co-ZSM-5 catalysts whereas higher water yield and lower CO2 and CO was obtained with the ZSM-5, Ga-ZSM-5, Cu-ZSM-5 and Fe-ZSM-5 catalysts suggesting hydrodeoxygenation was dominant. Compared to the unmodified ZSM-5, the yield of single-ring aromatic compounds in the product oil was increased for the Co-ZSM-5, Cu-ZSM-5, Fe-ZSM-5 and Ni-ZSM-5 catalysts. However, for the Ga-ZSM-5 catalyst, single-ring aromatic compounds were reduced, but the highest yield of polycyclic aromatic hydrocarbons was produced. A higher biomass to polystyrene ratio (4:1) resulted in a markedly lower oil yield with a consequent increased yield of gas.
引用
收藏
页码:477 / 490
页数:14
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