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....
| Authors: | , , , , , , , , |
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| 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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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 |
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info:eu-repo/semantics/openAccess http://creativecommons.org/licenses/by-nc-nd/4.0/ © 2019 Elsevier under CC BY-NC-ND license |
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openAccess |
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http://creativecommons.org/licenses/by-nc-nd/4.0/ © 2019 Elsevier under CC BY-NC-ND license |
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application/pdf |
| dc.publisher.none.fl_str_mv |
Elsevier |
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Elsevier |
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reponame:Addi. Archivo Digital para la Docencia y la Investigación instname:Universidad del País Vasco |
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Universidad del País Vasco |
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Addi. Archivo Digital para la Docencia y la Investigación |
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Addi. Archivo Digital para la Docencia y la Investigación |
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