Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor

This study investigates bed agglomeration during fast pyrolysis of bio-oil in a fluidized-bed reactor at temperatures of 500-800 °C. The samples used include bio-oil, bio-oil water-soluble fraction (WSF), bio-oil water-insoluble fraction (WIF), and selected model compounds. Increasing pyrolysis temp...

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Main Authors: Gao, Wenran, Zhang, Mingming, Wu, Hongwei
Format: Journal Article
Published: American Chemical Society 2018
Online Access:http://hdl.handle.net/20.500.11937/67417
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author Gao, Wenran
Zhang, Mingming
Wu, Hongwei
author_facet Gao, Wenran
Zhang, Mingming
Wu, Hongwei
author_sort Gao, Wenran
building Curtin Institutional Repository
collection Online Access
description This study investigates bed agglomeration during fast pyrolysis of bio-oil in a fluidized-bed reactor at temperatures of 500-800 °C. The samples used include bio-oil, bio-oil water-soluble fraction (WSF), bio-oil water-insoluble fraction (WIF), and selected model compounds. Increasing pyrolysis temperature from 500 to 800 °C decreases the agglomeration yields of biooil, WSF, and WIF from 40% to 15%, 26.2% to 11.6%, and 15.0% to 5.2%, respectively. Investigation using model compounds suggests that the interactions between lignin-derived oligomers and sugar are mainly responsible for the high bed agglomeration yields of bio-oil and WSF, and such interactions weaken as pyrolysis temperature increases. Water has an insignificant effect on bed agglomeration during bio-oil or WSF pyrolysis. The results also show that the bed agglomeration yield and the formation of tar (and/or coke) are in broad linear correlations, indicating that the tar (and/or coke) formed during fast pyrolysis contributes to the bed agglomeration of bio-oil. The linear correlation from the data of bio-oil has a steeper gradient compared to that of WSF and WIF, clearly indicating the synergy taking place between the WSF and WIF during fast pyrolysis in enhancing bed agglomeration.
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institution Curtin University Malaysia
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publishDate 2018
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spelling curtin-20.500.11937-674172018-07-25T01:51:08Z Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor Gao, Wenran Zhang, Mingming Wu, Hongwei This study investigates bed agglomeration during fast pyrolysis of bio-oil in a fluidized-bed reactor at temperatures of 500-800 °C. The samples used include bio-oil, bio-oil water-soluble fraction (WSF), bio-oil water-insoluble fraction (WIF), and selected model compounds. Increasing pyrolysis temperature from 500 to 800 °C decreases the agglomeration yields of biooil, WSF, and WIF from 40% to 15%, 26.2% to 11.6%, and 15.0% to 5.2%, respectively. Investigation using model compounds suggests that the interactions between lignin-derived oligomers and sugar are mainly responsible for the high bed agglomeration yields of bio-oil and WSF, and such interactions weaken as pyrolysis temperature increases. Water has an insignificant effect on bed agglomeration during bio-oil or WSF pyrolysis. The results also show that the bed agglomeration yield and the formation of tar (and/or coke) are in broad linear correlations, indicating that the tar (and/or coke) formed during fast pyrolysis contributes to the bed agglomeration of bio-oil. The linear correlation from the data of bio-oil has a steeper gradient compared to that of WSF and WIF, clearly indicating the synergy taking place between the WSF and WIF during fast pyrolysis in enhancing bed agglomeration. 2018 Journal Article http://hdl.handle.net/20.500.11937/67417 10.1021/acs.energyfuels.8b00333 American Chemical Society restricted
spellingShingle Gao, Wenran
Zhang, Mingming
Wu, Hongwei
Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor
title Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor
title_full Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor
title_fullStr Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor
title_full_unstemmed Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor
title_short Bed Agglomeration during Bio-oil Fast Pyrolysis in a Fluidized-Bed Reactor
title_sort bed agglomeration during bio-oil fast pyrolysis in a fluidized-bed reactor
url http://hdl.handle.net/20.500.11937/67417