dc.contributor.author | Rodríguez, Elena | |
dc.contributor.author | Palos Urrutia, Roberto | |
dc.contributor.author | Gutiérrez Lorenzo, Alazne | |
dc.contributor.author | Trueba Fraile, Juan David | |
dc.contributor.author | Arandes Esteban, José María | |
dc.contributor.author | Bilbao Elorriaga, Javier | |
dc.date.accessioned | 2024-02-08T10:25:30Z | |
dc.date.available | 2024-02-08T10:25:30Z | |
dc.date.issued | 2020-01-28 | |
dc.identifier.citation | Energy Conversion and Management 207 : (2020) // Article ID 112554 | es_ES |
dc.identifier.issn | 0196-8904 | |
dc.identifier.uri | http://hdl.handle.net/10810/65300 | |
dc.description.abstract | The co-feeding of high-density polyethylene pyrolysis waxes (HDPE waxes) with vacuum gasoil (VGO) on the catalytic cracking has been investigated. Runs have been conducted by feeding a blend of HDPE waxes/VGO (1/4 in mass) to a laboratory-scale reactor that mimics the behavior of the riser reactor of the industrial FCC unit. Tested operating conditions have been the following: 500–560 °C; catalyst to oil mass ratio (C/O), 3–7 gcat gfeed−1; and, contact time, 6 s. The comparison of obtained results, i.e., yield and composition of the fractions, in the cracking of the blend with those obtained in the cracking of the VGO and HDPE waxes separately, has exposed the existence of synergetic mechanisms. This way, the cracking of the blend produces a more olefinic gaseous fraction and a naphtha with higher content of iso-paraffins and olefins and lower of aromatics, together with a comparable yield of coke. | es_ES |
dc.description.sponsorship | 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 European Union’s ERDF funds and the European Commission (HORIZON H2020- MSCA RISE-2018. Contract No. 823745) and the Basque Government (grant IT1218-19). Dr. Roberto Palos thanks the University of the Basque Country UPV/ EHU for his postdoctoral grant (UPV/EHU 2019). David Trueba is also grateful for his PhD grant awarded by the University of the Basque Country UPV/EHU (PIF 2018). The authors also acknowledge Petronor Refinery for providing the VGO and the catalyst used in this work. | es_ES |
dc.language.iso | eng | es_ES |
dc.publisher | Elsevier Ltd. | es_ES |
dc.relation | info:eu-repo/grantAgreement/EC/H2020/823745 | |
dc.relation | info:eu-repo/grantAgreement/MICIU/RTI2018-096981-B-I00 | |
dc.rights | info:eu-repo/semantics/openAccess | es_ES |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/3.0/es/ | * |
dc.subject | cracking | es_ES |
dc.subject | FCC unit | es_ES |
dc.subject | waste plastic | es_ES |
dc.subject | non-conventional fuels | es_ES |
dc.subject | waste refinery | es_ES |
dc.title | Towards waste refinery: Co-feeding HDPE pyrolysis waxes with VGO into the catalytic cracking unit | es_ES |
dc.type | info:eu-repo/semantics/article | es_ES |
dc.rights.holder | © 2020 Elsevier. This manuscript version is made available under the CC-BY-NC-ND 4.0 license https://creativecommons.org/licenses/by-nc-nd/4.0/ | * |
dc.relation.publisherversion | https://www.sciencedirect.com/science/article/pii/S019689042030090X | |
dc.identifier.doi | 10.1016/j.enconman.2020.112554 | |
dc.contributor.funder | European Commission | |
dc.departamentoes | Ingeniería química | es_ES |
dc.departamentoeu | Ingeniaritza kimikoa | es_ES |