Catalytic upgrading of intermediate pyrolysis bio-oil to hydrocarbon-rich liquid biofuel via a novel two-stage solvent-assisted process

被引:12
|
作者
Onwudili, Jude A. [1 ]
Scaldaferri, Cristiane A. [1 ]
机构
[1] Aston Univ, Energy & Bioprod Res Inst, Coll Engn & Phys Sci, Birmingham B4 7ET, England
关键词
Intermediate pyrolysis bio-oil; Catalytic upgrading; Liquid hydrocarbon biofuel; Two-stage process; Hydrotreatment (stabilisation); Hydrodeoxygenation; HYDROTHERMAL LIQUEFACTION; BIOMASS; HYDROTREATMENT; FUELS; ACID; DECARBOXYLATION; KETONIZATION; TEMPERATURE; SELECTIVITY; COMPONENTS;
D O I
10.1016/j.fuel.2023.129015
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
A novel two-stage solvent-assisted batch catalytic hydroprocessing method has been developed for upgrading intermediate pyrolysis bio-oil to produce blended liquid fuels with & AP;23 wt% hydrocarbon-rich biofuel content. Stage I reactions (160 degrees C for 3 h, then 300 degrees C for 3 h) involving mixtures of dodecane and bio-oil (mass ratio = 3:2), hydrogen gas and 5 wt%-metal supported catalysts (Pd/C, Pt/Al2O3 Pd/Al2O3, Ru/Al2O3) suppressed char formation. Up to 80 wt% liquid organic products were obtained, with the biofuel component dominated by ketones and phenols. Significant amounts of water and gas (mainly CO2) were also produced. Stage II reactions (300 degrees C for 3 h; 5 wt% Pt/Al2O3; hydrogen gas) with Stage I organic liquid products gave >90 wt% of blended liquid fuel. Overall, up to 96 wt% bio-oil deoxygenation and 53.4 wt% bio-carbon retention were achieved in the final organic liquid product via a combination of various reaction mechanisms. Pt/Al2O3 catalyst deactivated via hydrolysis of alumina and coking in stage I but remained stable during Stage II.
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页数:18
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