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

Author:

Yadav Omvesh12,Jindal Meenu12,Bhatt Richa3,Agarwal Akul4,Thallada Bhaskar12,Palla Venkata Chandra Sekhar12

Affiliation:

1. Academy of Scientific and Innovative Research (AcSIR) Ghaziabad India

2. Material Resource Efficiency Division CSIR–Indian Institute of Petroleum Dehradun India

3. Department of Chemistry Graphic Era (Deemed to be) University Dehradun India

4. Department of Chemical Engineering Institute of Chemical Technology Mumbai‐Indian Oil Odisha Campus Bhubaneswar India

Abstract

AbstractRenewable 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 β‐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°C temperature and 30 min residence time with a catalyst‐to‐biomass ratio of 1:4.

Publisher

Wiley

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