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dc.contributor.authorBarredo, Asier
dc.contributor.authorAsueta, Asier
dc.contributor.authorAmundarain, Izotz
dc.contributor.authorLeivar, Jon
dc.contributor.authorMiguel-Fernández, Rafael
dc.contributor.authorArnaiz, Sixto
dc.contributor.authorEpelde Bejerano, Eva
dc.contributor.authorLópez Fonseca, Rubén ORCID
dc.contributor.authorGutiérrez Ortiz, José Ignacio ORCID
dc.date.accessioned2024-01-15T08:17:26Z
dc.date.available2024-01-15T08:17:26Z
dc.date.issued2023-03-31
dc.identifier.citationJournal of Environmental Chemical Engineering 11(3) : (2023) // Art. Id. 109823es_ES
dc.identifier.issn2213-3437
dc.identifier.urihttp://hdl.handle.net/10810/63965
dc.description.abstractThe high demand for recycled polyethylene terephthalate (rPET) driven by an increase in environmental awareness, the application of more restrictive environmental legislations, together with the large increase in the generation of post-consumer PET plastic waste, has resulted in an urgent need for efficient recycling processes. In this work, alkaline hydrolysis is presented as a promising chemical recycling alternative for PET tray waste. PET depolymerization reactions were carried out under mild conditions (80–100 ºC and atmospheric pressure) using tributylhexadecylphosphonium bromide quaternary salt (TBHDPB) as catalyst. Several operating variables were studied based on PET conversion and terephthalic acid (TPA) yield criteria: (i) catalyst mass ratio of TBHDPB to PET (0–0.2); (ii) particle size (0.5–10 mm); (iii) stirring rate (350–700 rpm); and, (iv) temperature (80–100 ◦C). A good compromise between PET conversion (99.9%) and TPA yield (93.5%) was established after 4 h of reaction, under the following operating conditions: TBHDPB:PET catalyst ratio, 0.2; 100 ◦C; particle size, 1–1.4 mm; and, stirring rate, 525 rpm. In addition, the experimental kinetic data correctly fits to the proposed shrinking core model. Activation energy values of 60 and 57.4 kJ mol-1 were established for the non-catalyzed and catalyzed reactions, respectively, which implies that TBHDPB catalyst does not apparently modify the reaction mechanism.es_ES
dc.description.sponsorshipBasque Government by its ELKARTEK 2020 Program (NEOPLAST Project, Reference KK-2020/00107), CDTI (Centro para el Desarrollo Tecnológico Industrial) (OSIRIS Project, CER-20211009).es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rightsinfo:eu-repo/semantics/openAccesses_ES
dc.subjectpolyethylene terephthalate wastees_ES
dc.subjectchemical recyclinges_ES
dc.subjectalkaline hydrolysises_ES
dc.subjectphase transfer catalystes_ES
dc.subjectterephthalic acides_ES
dc.subjectkinetic modelinges_ES
dc.titleChemical recycling of monolayer PET tray waste by alkaline hydrolysises_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.rights.holder© 2023 The Author(s). Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/)es_ES
dc.relation.publisherversionhttps://doi.org/10.1016/j.jece.2023.109823es_ES
dc.identifier.doi10.1016/j.jece.2023.109823
dc.departamentoesIngeniería químicaes_ES
dc.departamentoeuIngeniaritza kimikoaes_ES


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