Multi-fluid reactive modeling of fluidized bed pyrolysis process

A multiphase reactive model of biomass pyrolysis process has been implemented by integrating the reaction kinetics of the thermo-chemical decomposition of biomass with the hydrodynamics of the fluidized bed. The model was validated with the experimental data of biomass pyrolysis in the presence of a...

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Main Authors: Sharma, Abhishek, Wang, Shaobin, Pareek, Vishnu, Yang, H., Zhang, D.
Format: Journal Article
Published: Pergamon 2015
Subjects:
Online Access:http://hdl.handle.net/20.500.11937/6520
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author Sharma, Abhishek
Wang, Shaobin
Pareek, Vishnu
Yang, H.
Zhang, D.
author_facet Sharma, Abhishek
Wang, Shaobin
Pareek, Vishnu
Yang, H.
Zhang, D.
author_sort Sharma, Abhishek
building Curtin Institutional Repository
collection Online Access
description A multiphase reactive model of biomass pyrolysis process has been implemented by integrating the reaction kinetics of the thermo-chemical decomposition of biomass with the hydrodynamics of the fluidized bed. The model was validated with the experimental data of biomass pyrolysis in the presence of a sand bed. The simulation results were examined to analyze the effect of reactor temperature, superficial gas velocity and biomass particle size on the bed hydrodynamics and product yields. It was found that at temperatures higher than 500 °C, there was a significant conversion of primary tar into NCG (non-condensable gases) due to thermal cracking inside the reactor. However, the increase in superficial gas velocity led to higher concentration of tar due to lower residence time for tar cracking reactions. Any increase in biomass particle size reduced the yield of volatile products due to decrease in the rate of heat transfer, which in turn increased the yield of biochar.
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institution Curtin University Malaysia
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publishDate 2015
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spelling curtin-20.500.11937-65202017-09-13T15:53:52Z Multi-fluid reactive modeling of fluidized bed pyrolysis process Sharma, Abhishek Wang, Shaobin Pareek, Vishnu Yang, H. Zhang, D. Pyrolysis Fluidized bed Computational fluid dynamics Multiphase Biomass A multiphase reactive model of biomass pyrolysis process has been implemented by integrating the reaction kinetics of the thermo-chemical decomposition of biomass with the hydrodynamics of the fluidized bed. The model was validated with the experimental data of biomass pyrolysis in the presence of a sand bed. The simulation results were examined to analyze the effect of reactor temperature, superficial gas velocity and biomass particle size on the bed hydrodynamics and product yields. It was found that at temperatures higher than 500 °C, there was a significant conversion of primary tar into NCG (non-condensable gases) due to thermal cracking inside the reactor. However, the increase in superficial gas velocity led to higher concentration of tar due to lower residence time for tar cracking reactions. Any increase in biomass particle size reduced the yield of volatile products due to decrease in the rate of heat transfer, which in turn increased the yield of biochar. 2015 Journal Article http://hdl.handle.net/20.500.11937/6520 10.1016/j.ces.2014.11.019 Pergamon restricted
spellingShingle Pyrolysis
Fluidized bed
Computational fluid dynamics
Multiphase
Biomass
Sharma, Abhishek
Wang, Shaobin
Pareek, Vishnu
Yang, H.
Zhang, D.
Multi-fluid reactive modeling of fluidized bed pyrolysis process
title Multi-fluid reactive modeling of fluidized bed pyrolysis process
title_full Multi-fluid reactive modeling of fluidized bed pyrolysis process
title_fullStr Multi-fluid reactive modeling of fluidized bed pyrolysis process
title_full_unstemmed Multi-fluid reactive modeling of fluidized bed pyrolysis process
title_short Multi-fluid reactive modeling of fluidized bed pyrolysis process
title_sort multi-fluid reactive modeling of fluidized bed pyrolysis process
topic Pyrolysis
Fluidized bed
Computational fluid dynamics
Multiphase
Biomass
url http://hdl.handle.net/20.500.11937/6520