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Energy, exergy, exergoeconomic, and environmental assessment of different technologies in the production of bio-jet fuel by palm oil biorefineries
•Production of biofuels using HEFA and ATJ routes.•Biorefinery configurations to evaluate biofuel production from palm oil.•Evaluation of biorefineries using thermodynamics and exergoeconomics tools.•Integral methodology to guide decision making in the use of biomass for biorefineries.•Life Cycle As...
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Published in: | Energy conversion and management 2021-09, Vol.243, p.114393, Article 114393 |
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description | •Production of biofuels using HEFA and ATJ routes.•Biorefinery configurations to evaluate biofuel production from palm oil.•Evaluation of biorefineries using thermodynamics and exergoeconomics tools.•Integral methodology to guide decision making in the use of biomass for biorefineries.•Life Cycle Assessment of the main products was carried out.
This work explores palm oil and the residual biomass from oil palm extraction to obtain valuable products via sustainable routes in integrated biorefineries, which were separated into three scenarios: Baseline Scenario is the current Brazilian application of palm in the energy sector using a biodiesel plant with a cogeneration system; Scenario 1 integrates a Hydrotreatment of Esters and Fatty Acids unit to produce bio-jet fuel into the previous case; and Scenario 2, integrates a second-generation ethanol plant and an Alcohol-to-Jet process in order to obtain bio-jet fuel from the second generation. Taking into account that the selection and integration of processes carried out in a biorefinery would impact the overall efficiency of the system, the production costs and the impacts on the environment of the plant make it is necessary to carry out a comprehensive evaluation of the system that allows characterizing and quantify the energy, economic and environmental aspects related to the biomass energy conversion. A methodology of analysis was proposed to address all of these aspects and to provide results that allow for a decision-making guide in technology selection. It was identified that the main need for improvement in the biorefineries relies on cogeneration, which exergy destruction rate ranged from 167.99 to 213.63 MW. The unit exergoeconomic costs founded for glycerol, biodiesel, and electricity were all lower than the market costs, the bio-jet fuel costs, from hydrotreatment, were nearly the same as those from the Brazilian market 0.49 and 0.46 USD/L, respectively. However, the costs of upgrading ethanol were the highest found and way higher than the market rate at 5.15 USD/L. Environmentally, the selected configuration of biorefineries provides all produced biofuel environmental gains compared to conventional non-renewable fuels. Biodiesel and bio-jet fuels would avoid emission of 324.65 kgCO2eq/t and 3092.45 kgCO2eq/t, respectively. |
doi_str_mv | 10.1016/j.enconman.2021.114393 |
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This work explores palm oil and the residual biomass from oil palm extraction to obtain valuable products via sustainable routes in integrated biorefineries, which were separated into three scenarios: Baseline Scenario is the current Brazilian application of palm in the energy sector using a biodiesel plant with a cogeneration system; Scenario 1 integrates a Hydrotreatment of Esters and Fatty Acids unit to produce bio-jet fuel into the previous case; and Scenario 2, integrates a second-generation ethanol plant and an Alcohol-to-Jet process in order to obtain bio-jet fuel from the second generation. Taking into account that the selection and integration of processes carried out in a biorefinery would impact the overall efficiency of the system, the production costs and the impacts on the environment of the plant make it is necessary to carry out a comprehensive evaluation of the system that allows characterizing and quantify the energy, economic and environmental aspects related to the biomass energy conversion. A methodology of analysis was proposed to address all of these aspects and to provide results that allow for a decision-making guide in technology selection. It was identified that the main need for improvement in the biorefineries relies on cogeneration, which exergy destruction rate ranged from 167.99 to 213.63 MW. The unit exergoeconomic costs founded for glycerol, biodiesel, and electricity were all lower than the market costs, the bio-jet fuel costs, from hydrotreatment, were nearly the same as those from the Brazilian market 0.49 and 0.46 USD/L, respectively. However, the costs of upgrading ethanol were the highest found and way higher than the market rate at 5.15 USD/L. Environmentally, the selected configuration of biorefineries provides all produced biofuel environmental gains compared to conventional non-renewable fuels. Biodiesel and bio-jet fuels would avoid emission of 324.65 kgCO2eq/t and 3092.45 kgCO2eq/t, respectively.</description><identifier>ISSN: 0196-8904</identifier><identifier>EISSN: 1879-2227</identifier><identifier>DOI: 10.1016/j.enconman.2021.114393</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Bio-jet fuel ; Biodiesel fuels ; Biofuels ; Biomass ; Biomass energy ; Biomass energy production ; Biorefineries ; Cogeneration ; Decision making ; Diesel ; Energy ; Energy conversion ; Energy industry ; Environmental aspects ; Environmental assessment ; Environmental impact ; Esters ; Ethanol ; Exergoeconomics ; Exergy ; Fatty acids ; Fuels ; Glycerol ; Jet engine fuels ; Life cycle assessment ; Palm oil ; Production costs ; Refining ; Thermodynamics</subject><ispartof>Energy conversion and management, 2021-09, Vol.243, p.114393, Article 114393</ispartof><rights>2021 Elsevier Ltd</rights><rights>Copyright Elsevier Science Ltd. Sep 1, 2021</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c340t-66988f2c2cda85477341d3489f3d3f19b357fa51574ea5ecbbbb931d61a4971c3</citedby><cites>FETCH-LOGICAL-c340t-66988f2c2cda85477341d3489f3d3f19b357fa51574ea5ecbbbb931d61a4971c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids></links><search><creatorcontrib>Julio, Alisson Aparecido Vitoriano</creatorcontrib><creatorcontrib>Batlle, Eric Alberto Ocampo</creatorcontrib><creatorcontrib>Trindade, Aline Bhering</creatorcontrib><creatorcontrib>Nebra, Silvia Azucena</creatorcontrib><creatorcontrib>Reyes, Arnaldo Martín Martinez</creatorcontrib><creatorcontrib>Palacio, José Carlos Escobar</creatorcontrib><title>Energy, exergy, exergoeconomic, and environmental assessment of different technologies in the production of bio-jet fuel by palm oil biorefineries</title><title>Energy conversion and management</title><description>•Production of biofuels using HEFA and ATJ routes.•Biorefinery configurations to evaluate biofuel production from palm oil.•Evaluation of biorefineries using thermodynamics and exergoeconomics tools.•Integral methodology to guide decision making in the use of biomass for biorefineries.•Life Cycle Assessment of the main products was carried out.
This work explores palm oil and the residual biomass from oil palm extraction to obtain valuable products via sustainable routes in integrated biorefineries, which were separated into three scenarios: Baseline Scenario is the current Brazilian application of palm in the energy sector using a biodiesel plant with a cogeneration system; Scenario 1 integrates a Hydrotreatment of Esters and Fatty Acids unit to produce bio-jet fuel into the previous case; and Scenario 2, integrates a second-generation ethanol plant and an Alcohol-to-Jet process in order to obtain bio-jet fuel from the second generation. Taking into account that the selection and integration of processes carried out in a biorefinery would impact the overall efficiency of the system, the production costs and the impacts on the environment of the plant make it is necessary to carry out a comprehensive evaluation of the system that allows characterizing and quantify the energy, economic and environmental aspects related to the biomass energy conversion. A methodology of analysis was proposed to address all of these aspects and to provide results that allow for a decision-making guide in technology selection. It was identified that the main need for improvement in the biorefineries relies on cogeneration, which exergy destruction rate ranged from 167.99 to 213.63 MW. The unit exergoeconomic costs founded for glycerol, biodiesel, and electricity were all lower than the market costs, the bio-jet fuel costs, from hydrotreatment, were nearly the same as those from the Brazilian market 0.49 and 0.46 USD/L, respectively. However, the costs of upgrading ethanol were the highest found and way higher than the market rate at 5.15 USD/L. Environmentally, the selected configuration of biorefineries provides all produced biofuel environmental gains compared to conventional non-renewable fuels. Biodiesel and bio-jet fuels would avoid emission of 324.65 kgCO2eq/t and 3092.45 kgCO2eq/t, respectively.</description><subject>Bio-jet fuel</subject><subject>Biodiesel fuels</subject><subject>Biofuels</subject><subject>Biomass</subject><subject>Biomass energy</subject><subject>Biomass energy production</subject><subject>Biorefineries</subject><subject>Cogeneration</subject><subject>Decision making</subject><subject>Diesel</subject><subject>Energy</subject><subject>Energy conversion</subject><subject>Energy industry</subject><subject>Environmental aspects</subject><subject>Environmental assessment</subject><subject>Environmental impact</subject><subject>Esters</subject><subject>Ethanol</subject><subject>Exergoeconomics</subject><subject>Exergy</subject><subject>Fatty acids</subject><subject>Fuels</subject><subject>Glycerol</subject><subject>Jet engine fuels</subject><subject>Life cycle assessment</subject><subject>Palm oil</subject><subject>Production costs</subject><subject>Refining</subject><subject>Thermodynamics</subject><issn>0196-8904</issn><issn>1879-2227</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNqFUE1LAzEQDaJgrf4FCXjt1mSzm93cFPELCl70HNJk0mbZJjXZiv0b_mKzVMGbcxmGee_Nm4fQJSVzSii_7ubgdfAb5eclKemc0ooJdoQmtG1EUZZlc4wmhApetIJUp-gspY4QwmrCJ-jr3kNc7WcYPv_0AFkwbJyeYeUNBv_hYr4AflA9VilBSuOAg8XGWQtxHAbQax_6sHKQsPN4WAPexmB2enDBj9ilC0UHA7Y76PFyj7eq3-Dg-nERwbpsJXPP0YlVfYKLnz5Fbw_3r3dPxeLl8fnudlFoVpGh4Fy0rS11qY1q66ppWEUNq1phmWGWiiWrG6tqWjcVqBr0Mpdg1HCqKtFQzabo6qCbTb7vIA2yC7vo80lZ1rxlhNO2zih-QOkYUsou5Ta6jYp7SYkc85ed_M1fjvnLQ_6ZeHMgQv7hw0GUSbuMBOMi6EGa4P6T-AZjmZTb</recordid><startdate>20210901</startdate><enddate>20210901</enddate><creator>Julio, Alisson Aparecido Vitoriano</creator><creator>Batlle, Eric Alberto Ocampo</creator><creator>Trindade, Aline Bhering</creator><creator>Nebra, Silvia Azucena</creator><creator>Reyes, Arnaldo Martín Martinez</creator><creator>Palacio, José Carlos Escobar</creator><general>Elsevier Ltd</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>H8D</scope><scope>KR7</scope><scope>L7M</scope><scope>SOI</scope></search><sort><creationdate>20210901</creationdate><title>Energy, exergy, exergoeconomic, and environmental assessment of different technologies in the production of bio-jet fuel by palm oil biorefineries</title><author>Julio, Alisson Aparecido Vitoriano ; Batlle, Eric Alberto Ocampo ; Trindade, Aline Bhering ; Nebra, Silvia Azucena ; Reyes, Arnaldo Martín Martinez ; Palacio, José Carlos Escobar</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c340t-66988f2c2cda85477341d3489f3d3f19b357fa51574ea5ecbbbb931d61a4971c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Bio-jet fuel</topic><topic>Biodiesel fuels</topic><topic>Biofuels</topic><topic>Biomass</topic><topic>Biomass energy</topic><topic>Biomass energy production</topic><topic>Biorefineries</topic><topic>Cogeneration</topic><topic>Decision making</topic><topic>Diesel</topic><topic>Energy</topic><topic>Energy conversion</topic><topic>Energy industry</topic><topic>Environmental aspects</topic><topic>Environmental assessment</topic><topic>Environmental impact</topic><topic>Esters</topic><topic>Ethanol</topic><topic>Exergoeconomics</topic><topic>Exergy</topic><topic>Fatty acids</topic><topic>Fuels</topic><topic>Glycerol</topic><topic>Jet engine fuels</topic><topic>Life cycle assessment</topic><topic>Palm oil</topic><topic>Production costs</topic><topic>Refining</topic><topic>Thermodynamics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Julio, Alisson Aparecido Vitoriano</creatorcontrib><creatorcontrib>Batlle, Eric Alberto Ocampo</creatorcontrib><creatorcontrib>Trindade, Aline Bhering</creatorcontrib><creatorcontrib>Nebra, Silvia Azucena</creatorcontrib><creatorcontrib>Reyes, Arnaldo Martín Martinez</creatorcontrib><creatorcontrib>Palacio, José Carlos Escobar</creatorcontrib><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>Energy conversion and management</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Julio, Alisson Aparecido Vitoriano</au><au>Batlle, Eric Alberto Ocampo</au><au>Trindade, Aline Bhering</au><au>Nebra, Silvia Azucena</au><au>Reyes, Arnaldo Martín Martinez</au><au>Palacio, José Carlos Escobar</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Energy, exergy, exergoeconomic, and environmental assessment of different technologies in the production of bio-jet fuel by palm oil biorefineries</atitle><jtitle>Energy conversion and management</jtitle><date>2021-09-01</date><risdate>2021</risdate><volume>243</volume><spage>114393</spage><pages>114393-</pages><artnum>114393</artnum><issn>0196-8904</issn><eissn>1879-2227</eissn><abstract>•Production of biofuels using HEFA and ATJ routes.•Biorefinery configurations to evaluate biofuel production from palm oil.•Evaluation of biorefineries using thermodynamics and exergoeconomics tools.•Integral methodology to guide decision making in the use of biomass for biorefineries.•Life Cycle Assessment of the main products was carried out.
This work explores palm oil and the residual biomass from oil palm extraction to obtain valuable products via sustainable routes in integrated biorefineries, which were separated into three scenarios: Baseline Scenario is the current Brazilian application of palm in the energy sector using a biodiesel plant with a cogeneration system; Scenario 1 integrates a Hydrotreatment of Esters and Fatty Acids unit to produce bio-jet fuel into the previous case; and Scenario 2, integrates a second-generation ethanol plant and an Alcohol-to-Jet process in order to obtain bio-jet fuel from the second generation. Taking into account that the selection and integration of processes carried out in a biorefinery would impact the overall efficiency of the system, the production costs and the impacts on the environment of the plant make it is necessary to carry out a comprehensive evaluation of the system that allows characterizing and quantify the energy, economic and environmental aspects related to the biomass energy conversion. A methodology of analysis was proposed to address all of these aspects and to provide results that allow for a decision-making guide in technology selection. It was identified that the main need for improvement in the biorefineries relies on cogeneration, which exergy destruction rate ranged from 167.99 to 213.63 MW. The unit exergoeconomic costs founded for glycerol, biodiesel, and electricity were all lower than the market costs, the bio-jet fuel costs, from hydrotreatment, were nearly the same as those from the Brazilian market 0.49 and 0.46 USD/L, respectively. However, the costs of upgrading ethanol were the highest found and way higher than the market rate at 5.15 USD/L. Environmentally, the selected configuration of biorefineries provides all produced biofuel environmental gains compared to conventional non-renewable fuels. Biodiesel and bio-jet fuels would avoid emission of 324.65 kgCO2eq/t and 3092.45 kgCO2eq/t, respectively.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.enconman.2021.114393</doi></addata></record> |
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subjects | Bio-jet fuel Biodiesel fuels Biofuels Biomass Biomass energy Biomass energy production Biorefineries Cogeneration Decision making Diesel Energy Energy conversion Energy industry Environmental aspects Environmental assessment Environmental impact Esters Ethanol Exergoeconomics Exergy Fatty acids Fuels Glycerol Jet engine fuels Life cycle assessment Palm oil Production costs Refining Thermodynamics |
title | Energy, exergy, exergoeconomic, and environmental assessment of different technologies in the production of bio-jet fuel by palm oil biorefineries |
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