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Enhancement of aromatics from catalytic pyrolysis of yellow poplar: Role of hydrogen and methane decomposition
  • Moogi, Surendar ;
  • Jae, Jungho ;
  • Kannapu, Hari Prasad Reddy ;
  • Ahmed, Ashfaq ;
  • Park, Eun Duck ;
  • Park, Young Kwon
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Publication Year
2020-11-01
Publisher
Elsevier Ltd
Citation
Bioresource Technology, Vol.315
Keyword
AromaticsCatalytic co-pyrolysisCH4 decompositionGa/HZSM-5Yellow poplar
Mesh Keyword
Benzene , toluene , ethylbenzene , and xylenesCatalytic pyrolysisCatalytic upgradingGas environmentHydrodeoxygenationMethane decompositionMethoxyphenolsZeolite catalystBiomassCatalysisHot TemperatureHydrogenLiriodendronMethanePyrolysis
All Science Classification Codes (ASJC)
BioengineeringEnvironmental EngineeringRenewable Energy, Sustainability and the EnvironmentWaste Management and Disposal
Abstract
The present study examined the effects of the pyrolysis environment on BTEX (benzene, toluene, ethylbenzene, and xylenes) production in the catalytic upgrading of yellow poplar pyrolysis vapors. Three different gas environments, N2, CH4, and pre-decomposed CH4 stream (10 wt%-Ni/5 wt%-La2O3-5 wt% CeO2-Al2O3), which is a mixture of H2 (55.62%) and CH4, were studied using two types of zeolite catalysts, HZSM-5, and 1 wt% Ga/HZSM-5. The BTEX yields were enhanced linearly in the order N2 < CH4 < CH4 ex-situ decomposition. The highest BTEX yield of 9.58 wt% was obtained under the CH4 ex-situ decomposition environment over 1 wt% Ga/HZSM-5. The methane and hydrocarbons derived from biomass were activated on highly dispersed (GaO)+ sites and transformed smoothly to BTEX by aromatization on the BrØnsted acid sites of Ga/HZSM-5. The hydrogen produced from methane decomposition also assisted in aromatics production through the hydrodeoxygenation of methoxyphenols, guaiacols and catechols.
Language
eng
URI
https://dspace.ajou.ac.kr/dev/handle/2018.oak/31426
DOI
https://doi.org/10.1016/j.biortech.2020.123835
Fulltext

Type
Article
Funding
This work was supported by the C1 Gas Refinery Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science and ICT (2015M3D3A1A01064899).This work was supported by the C1 Gas Refinery Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science and ICT ( 2015M3D3A1A01064899 ).
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PARK, EUN DUCK박은덕
Department of Chemical Engineering
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