Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation

World energy consumption is forecasted to grow significantly for the foreseeable future with fossil fuel remains the governing energy source. The demand in the need to explore alternative fuel source was further triggered by the overwhelmingly inconsistent cost of gasoline. Bio-oil is an alternative...

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Main Authors: Ahmad, Murni M, Nordin, M Fitrir R, Azizan, M Tazli
Format: Conference or Workshop Item
Published: 2009
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Online Access:http://eprints.utp.edu.my/3121/1/CUTSE2009.docx
http://eprints.utp.edu.my/3121/
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spelling my.utp.eprints.31212017-01-19T08:25:09Z Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation Ahmad, Murni M Nordin, M Fitrir R Azizan, M Tazli TP Chemical technology World energy consumption is forecasted to grow significantly for the foreseeable future with fossil fuel remains the governing energy source. The demand in the need to explore alternative fuel source was further triggered by the overwhelmingly inconsistent cost of gasoline. Bio-oil is an alternative energy source produced from pyrolysis of biomass. However it is undesirable as a ready alternative transportation fuel due to its unfavourable nature i.e. highly oxygenated and low octane number. To overcome these physicochemical issues, hydrodeoxygenation reaction is a possible upgrading method i.e. by partial or total elimination of oxygen and hydrogenation of chemical structures. Hence, this work aims to investigate feasible routes and to develop the process route to upgrade the pyrolytic bio-oil from biomass into value-added chemicals for the production of transportation fuel, i.e. benzene and cyclohexane, via hydrodeoxygenation process using simulation approach. This study also promotes the prospect of co-processing bio-oil in standard refinery units to produce chemicals and fuels. In this work, hydrodeoxygenation of phenols and substituted phenols is used to represent the hydrodeoxygenation of the major oxygen compound in bio-oil due to their low reactivity in HDO. By assuming the feedstock used is 1% of the total palm shell available in Malaysia, i.e. 2,587 kg/hr bio-oil, the simulation predicts the production of 226 kg/hr benzene, 236 kg/hr cyclohexane and 7 kg/hr cyclohexene, with the yield of 34%, 81% and 3% respectively. The preliminary economic potential is calculated to be positive. It is also observed that hydrogen is the limiting reactant in the hydrogenation reaction. 2009-11-24 Conference or Workshop Item PeerReviewed application/pdf http://eprints.utp.edu.my/3121/1/CUTSE2009.docx Ahmad, Murni M and Nordin, M Fitrir R and Azizan, M Tazli (2009) Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation. In: Curtin University of Technology Science and Engineering (CUTSE) International Conference, 24-25 November 2009, Miri, Malaysia . http://eprints.utp.edu.my/3121/
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Institutional Repository
url_provider http://eprints.utp.edu.my/
topic TP Chemical technology
spellingShingle TP Chemical technology
Ahmad, Murni M
Nordin, M Fitrir R
Azizan, M Tazli
Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation
description World energy consumption is forecasted to grow significantly for the foreseeable future with fossil fuel remains the governing energy source. The demand in the need to explore alternative fuel source was further triggered by the overwhelmingly inconsistent cost of gasoline. Bio-oil is an alternative energy source produced from pyrolysis of biomass. However it is undesirable as a ready alternative transportation fuel due to its unfavourable nature i.e. highly oxygenated and low octane number. To overcome these physicochemical issues, hydrodeoxygenation reaction is a possible upgrading method i.e. by partial or total elimination of oxygen and hydrogenation of chemical structures. Hence, this work aims to investigate feasible routes and to develop the process route to upgrade the pyrolytic bio-oil from biomass into value-added chemicals for the production of transportation fuel, i.e. benzene and cyclohexane, via hydrodeoxygenation process using simulation approach. This study also promotes the prospect of co-processing bio-oil in standard refinery units to produce chemicals and fuels. In this work, hydrodeoxygenation of phenols and substituted phenols is used to represent the hydrodeoxygenation of the major oxygen compound in bio-oil due to their low reactivity in HDO. By assuming the feedstock used is 1% of the total palm shell available in Malaysia, i.e. 2,587 kg/hr bio-oil, the simulation predicts the production of 226 kg/hr benzene, 236 kg/hr cyclohexane and 7 kg/hr cyclohexene, with the yield of 34%, 81% and 3% respectively. The preliminary economic potential is calculated to be positive. It is also observed that hydrogen is the limiting reactant in the hydrogenation reaction.
format Conference or Workshop Item
author Ahmad, Murni M
Nordin, M Fitrir R
Azizan, M Tazli
author_facet Ahmad, Murni M
Nordin, M Fitrir R
Azizan, M Tazli
author_sort Ahmad, Murni M
title Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation
title_short Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation
title_full Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation
title_fullStr Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation
title_full_unstemmed Upgrading of Bio-Oil into High-Value Hydrocarbons via Hydrodeoxygenation
title_sort upgrading of bio-oil into high-value hydrocarbons via hydrodeoxygenation
publishDate 2009
url http://eprints.utp.edu.my/3121/1/CUTSE2009.docx
http://eprints.utp.edu.my/3121/
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