Comprehensive study of alkali lignin pyrolysis catalyzed by composite metal-modified molecular sieves for the preparation of hydrocarbon liquid fuels

被引:4
|
作者
Liu, Huan [1 ,2 ]
Liu, Huili [1 ,2 ]
Hu, Jianhang [1 ,2 ]
Zhong, Wenrui [1 ,2 ]
Hu, Zhikai [3 ]
Wang, Hua [1 ,2 ]
机构
[1] Kunming Univ Sci & Technol, Engn Res Ctr, Minist Educ Met Energy Conservat & Emiss Reduct, Kunming 650093, Yunnan, Peoples R China
[2] Kunming Univ Sci & Technol, State Key Lab Complex Nonferrous Met Resources Cle, Kunming, Peoples R China
[3] Kunming Univ Sci & Technol, Sch Met & Energy Engn, Kunming, Peoples R China
关键词
Alkali lignin; Composite metal-modified molecular sieve; Catalyst pyrolysis characteristics; Product analysis; Hydrocarbon liquid fuels; BIO-OIL; METHYL MERCAPTAN; KINETICS; BIOMASS; SELECTIVITY; PARAMETERS; AROMATICS; HZSM-5; ZSM-5; H2S;
D O I
10.1016/j.jaap.2024.106608
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Catalytic lignin pyrolysis for hydrocarbon liquid fuel production offers a viable alternative to fossil fuels. This study investigated the effects of transition metal (Fe, Co, Ni, Cu) modified composite molecular sieve catalysts on the pyrolysis product distribution and behavior of alkali lignin (AL). AL pyrolysis achieved the highest liquid product yield of 24.50 % at 600 degrees C, with high temperatures favoring hydrocarbon product formation. Volatile gaseous products from AL pyrolysis included H2, CO, CO2, phenolic compounds, heteroatomic compounds, and hydrocarbons. Molecular sieve catalyst additions were all favorable to the increase in hydrocarbon content. Compared with ZSM-5 and SBA-15, catalysts processed through acid etching and metal modification exhibited optimized pore structure, acid site distribution, and catalytic performance. Metal-modified composite molecular sieve catalysts (FeZS, CoZS, NiZS, and CuZS) generated more liquid products and promoted hydrocarbon formation. Notably, Cu-modified ZS catalysts exhibited superior acid site distribution and specific surface area, considerably reducing oxygenated compounds in the products. A higher catalyst-to-feedstock ratio increased the number of catalytically active sites, facilitating the cracking and deoxygenation of oxygenated components and generating more hydrocarbon products. The highest hydrocarbon yield for AL with a catalyst-to-biomass ratio of 10:1 under CuZS was 92.25 %, with 66.07 % being monocyclic aromatic hydrocarbons (MAHs) and 61.72 % benzene, toluene, ethylbenzene, and xylenes (BTEX). Additionally, kinetic and thermodynamic analyses revealed a substantial decrease in the average activation energy (E alpha) of AL and a reduction in entropy value with the CuZS catalyst, indicating enhanced pyrolytic reactivity of AL. Therefore, the proposed method is highly effective for producing highly selective hydrocarbons through catalytic pyrolysis of AL.
引用
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页数:15
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