Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries

The slow pyrolysis of recycled high-density polyethylene (HDPE) has been investigated in a batch autoclave reactor at 430–490 °C and reaction times of 15–60 min, with the aim of obtaining the maximum yield of plastic oil (PO) with an adequate composition for its subsequent valorization in refinery....

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Authors: Palos Urrutia, Robert, Gutiérrez Lorenzo, Alazne, Vela Díaz, Francisco Javier, Maña Iglesias, Jon Ander, Hita del Olmo, Idoia, Asueta, Asier, Arnaiz, Sixto, Arandes Esteban, José María, Bilbao Elorriaga, Javier
Format: article
Publication Date:2019
Country:España
Institution:Universidad del País Vasco
Repository:Addi. Archivo Digital para la Docencia y la Investigación
OAI Identifier:oai:addi.ehu.eus:10810/65205
Online Access:http://hdl.handle.net/10810/65205
Access Level:Open access
Keyword:plastic waste
recycled HDPE
slow pyrolysis
liquid oil
waste-refinery
fuel
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spelling Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineriesPalos Urrutia, RobertGutiérrez Lorenzo, AlazneVela Díaz, Francisco JavierMaña Iglesias, Jon AnderHita del Olmo, IdoiaAsueta, AsierArnaiz, SixtoArandes Esteban, José MaríaBilbao Elorriaga, Javierplastic wasterecycled HDPEslow pyrolysisliquid oilwaste-refineryfuelThe slow pyrolysis of recycled high-density polyethylene (HDPE) has been investigated in a batch autoclave reactor at 430–490 °C and reaction times of 15–60 min, with the aim of obtaining the maximum yield of plastic oil (PO) with an adequate composition for its subsequent valorization in refinery. Specifically, PO yields up to 85–90 wt% have been achieved operating at 430 °C and 15–37.5 min, noting that the obtained yields strongly depend on temperature and, to a lesser extent, on reaction time. Simulated distillation and gas chromatography analyses of PO have shown its potential for its valorization in a waste refinery scheme targeting the production of alternative fuels. Thus, the PO obtained at 430 °C and 15 min is suitable to be cofed to the fluidized catalytic cracking (FCC) unit since it has a simulated distillation curve similar to that of vacuum gasoil (VGO). On the other hand, the PO obtained at 430 °C at the longest reaction time and those obtained at 460 °C are suitable to be fed together with light cycle oil (LCO) into a hydroprocessing unit. The composition of naphtha and middle distillates of PO reveals that these fractions are appropriate for their blending with commercial diesel and gasoline pools after a mild hydrotreating to reduce their olefin content.This work has been carried out with financial support of the Ministry of Science, Innovation and Universities (MICINN) of the Spanish Government (grant RTI2018-096981-B-I00), the Basque Government (grant IT2018-19), the European Union’s ERDF funds and the European Commission (HORIZON H2020-MSCA RISE-2018. Contract No. 823745).ElsevierEuropean Commission202420242019info:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/10810/65205reponame:Addi. Archivo Digital para la Docencia y la Investigacióninstname:Universidad del País VascoInglésinfo:eu-repo/grantAgreement/MICINN/RTI2018-096981-B-I00/info:eu-repo/grantAgreement/EC/H2020/823745https://www.sciencedirect.com/science/article/pii/S0165237019303456info:eu-repo/semantics/openAccesshttp://creativecommons.org/licenses/by-nc-nd/4.0/© 2019 Elsevier under CC BY-NC-ND licenseoai:addi.ehu.eus:10810/652052026-06-18T09:23:17Z
dc.title.none.fl_str_mv Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
title Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
spellingShingle Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
Palos Urrutia, Robert
plastic waste
recycled HDPE
slow pyrolysis
liquid oil
waste-refinery
fuel
title_short Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
title_full Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
title_fullStr Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
title_full_unstemmed Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
title_sort Assessing the potential of the recycled plastic slow pyrolysis for the production of streams attractive for refineries
dc.creator.none.fl_str_mv Palos Urrutia, Robert
Gutiérrez Lorenzo, Alazne
Vela Díaz, Francisco Javier
Maña Iglesias, Jon Ander
Hita del Olmo, Idoia
Asueta, Asier
Arnaiz, Sixto
Arandes Esteban, José María
Bilbao Elorriaga, Javier
author Palos Urrutia, Robert
author_facet Palos Urrutia, Robert
Gutiérrez Lorenzo, Alazne
Vela Díaz, Francisco Javier
Maña Iglesias, Jon Ander
Hita del Olmo, Idoia
Asueta, Asier
Arnaiz, Sixto
Arandes Esteban, José María
Bilbao Elorriaga, Javier
author_role author
author2 Gutiérrez Lorenzo, Alazne
Vela Díaz, Francisco Javier
Maña Iglesias, Jon Ander
Hita del Olmo, Idoia
Asueta, Asier
Arnaiz, Sixto
Arandes Esteban, José María
Bilbao Elorriaga, Javier
author2_role author
author
author
author
author
author
author
author
dc.contributor.none.fl_str_mv European Commission
dc.subject.none.fl_str_mv plastic waste
recycled HDPE
slow pyrolysis
liquid oil
waste-refinery
fuel
topic plastic waste
recycled HDPE
slow pyrolysis
liquid oil
waste-refinery
fuel
description The slow pyrolysis of recycled high-density polyethylene (HDPE) has been investigated in a batch autoclave reactor at 430–490 °C and reaction times of 15–60 min, with the aim of obtaining the maximum yield of plastic oil (PO) with an adequate composition for its subsequent valorization in refinery. Specifically, PO yields up to 85–90 wt% have been achieved operating at 430 °C and 15–37.5 min, noting that the obtained yields strongly depend on temperature and, to a lesser extent, on reaction time. Simulated distillation and gas chromatography analyses of PO have shown its potential for its valorization in a waste refinery scheme targeting the production of alternative fuels. Thus, the PO obtained at 430 °C and 15 min is suitable to be cofed to the fluidized catalytic cracking (FCC) unit since it has a simulated distillation curve similar to that of vacuum gasoil (VGO). On the other hand, the PO obtained at 430 °C at the longest reaction time and those obtained at 460 °C are suitable to be fed together with light cycle oil (LCO) into a hydroprocessing unit. The composition of naphtha and middle distillates of PO reveals that these fractions are appropriate for their blending with commercial diesel and gasoline pools after a mild hydrotreating to reduce their olefin content.
publishDate 2019
dc.date.none.fl_str_mv 2019
2024
2024
dc.type.none.fl_str_mv info:eu-repo/semantics/article
format article
dc.identifier.none.fl_str_mv http://hdl.handle.net/10810/65205
url http://hdl.handle.net/10810/65205
dc.language.none.fl_str_mv Inglés
language_invalid_str_mv Inglés
dc.relation.none.fl_str_mv info:eu-repo/grantAgreement/MICINN/RTI2018-096981-B-I00/
info:eu-repo/grantAgreement/EC/H2020/823745
https://www.sciencedirect.com/science/article/pii/S0165237019303456
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
http://creativecommons.org/licenses/by-nc-nd/4.0/
© 2019 Elsevier under CC BY-NC-ND license
eu_rights_str_mv openAccess
rights_invalid_str_mv http://creativecommons.org/licenses/by-nc-nd/4.0/
© 2019 Elsevier under CC BY-NC-ND license
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Elsevier
publisher.none.fl_str_mv Elsevier
dc.source.none.fl_str_mv reponame:Addi. Archivo Digital para la Docencia y la Investigación
instname:Universidad del País Vasco
instname_str Universidad del País Vasco
reponame_str Addi. Archivo Digital para la Docencia y la Investigación
collection Addi. Archivo Digital para la Docencia y la Investigación
repository.name.fl_str_mv
repository.mail.fl_str_mv
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