Catalytic pyrolysis of pine needles: Role of zeolite structure and SiO2/Al2O3 ratio on bio-oil yield and product distribution

被引:1
作者
Yadav, Omvesh [1 ,2 ]
Jindal, Meenu [1 ,2 ]
Bhatt, Richa [3 ]
Agarwal, Akul [4 ]
Thallada, Bhaskar [1 ,2 ]
Palla, Venkata Chandra Sekhar [1 ,2 ]
机构
[1] Acad Sci & Innovat Res AcSIR, Ghaziabad, India
[2] Indian Inst Petr, Mat Resource Efficiency Div, CSIR, Dehra Dun, India
[3] Graph Era Deemed Univ, Dept Math, Dehra Dun, India
[4] Inst Chem Technol Mumbai, Dept Chem Engn, Indian Oil Odisha Campus, Bhubaneswar, India
关键词
bio-oil yield; catalytic pyrolysis; pine needles; silica-alumina; zeolites; COTTON STALKS; CO-PYROLYSIS; BED REACTOR; BIOMASS; CONVERSION; QUALITY; HYDROPYROLYSIS; PARAMETERS; MICROWAVE; AROMATICS;
D O I
10.1002/cjce.25453
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Renewable and sustainable energy production has gained significant attention to meet sustainable development goals (SDGs). Pine needles, an abundant typical forestry residue, can be used as a renewable biomass source for sustainable energy production. Pyrolysis is a well-established and commercialized technique for the thermochemical valorization of lignocellulosic biomass. The present work focuses on improving the bio-oil yield by introducing SiO2-Al2O3-based catalysts, including different zeolites and SiO2-Al2O3 materials with varying SiO2-Al2O3 ratios, during the pyrolysis. Bio-oil yield increased from 45.2 wt.% to 47.2 wt.% with the introduction of SiO2-Al2O3 catalysts and increased to 51.2 wt.% and 50.6 wt.% with HZSM-5 and Y-zeolite, respectively, and decreased to 40.0 wt.% with beta-zeolite catalyst. The pyrolysis experiments of physically mixed biomass and catalyst were carried out in a fixed-bed down-flow reactor. Various process parameters such as temperature, retention time, and catalyst-to-biomass ratio were examined to evaluate their effect on product yield. The catalyst's introduction slightly decreased phenolic compound content, enhancing carbonyl and hydrocarbon production. Maximum improvement in bio-oil yield by 6 wt.% was achieved using an H-ZSM-5 catalyst at 450 degrees C temperature and 30 min residence time with a catalyst-to-biomass ratio of 1:4.
引用
收藏
页码:3734 / 3743
页数:10
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