Please use this identifier to cite or link to this item: https://hdl.handle.net/11147/13579
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dc.contributor.authorGüngörmüş, Elif-
dc.contributor.authorŞeker, Erol-
dc.contributor.authorAlsoy Altınkaya, Sacide-
dc.date.accessioned2023-07-27T19:49:54Z-
dc.date.available2023-07-27T19:49:54Z-
dc.date.issued2023-
dc.identifier.issn0016-2361-
dc.identifier.issn1873-7153-
dc.identifier.urihttps://doi.org/10.1016/j.fuel.2023.128685-
dc.identifier.urihttps://hdl.handle.net/11147/13579-
dc.description.abstractBiodiesel is an alternative biofuel that can be blended with conventional petroleum-derived diesel fuel to partly reduce the dependence on the imported oil. Catalytic membrane reactors are promising candidates for sustainable biodiesel production. Herein, we report a novel catalytically active polydopamine-modified poly (ether sulfone) (PES) membrane immobilized with an alumina-calcium oxide catalyst. The reaction temperature, butanol to canola oil ratio, and transmembrane pressure applied through the membrane were optimized with response surface methodology and Box-Behnken design. In contrast to all previous catalytic membrane studies for biodiesel production, we used butanol as a co-reactant to improve the winter problems of biodiesel made with methanol. FTIR and SEM-EDX analysis confirmed the successful immobilization of the catalyst. At the end of 30 days of storage in the reactant mixture, 95% of the catalyst loaded to the membrane was still on the surface, and biodiesel yield values and butanol flux of the membrane did not change. We compared the batch and flowthrough operation modes by measuring the catalytic activity of membranes under static and dynamic conditions within 24 h (8-cycle). The biodiesel yield under dynamic condition decreased in the first three cycles from 54.54 +/- 0.65% to 47.31 +/- 0.70% and then stayed constant, whereas a continuous decrease from 25.42 +/- 0.57% to 17.19 +/- 0.58% was observed under static condition. In each cycle, the equilibrium limitation for the yield was overcome only when the membrane was operated under pressure. The main reason for the decrease in catalytic activities was the fouling on the catalyst surface which was quickly removed by backwashing with butanol. It is concluded that catalytic membranes with antifouling properties and alcohol stability can make biodiesel production more cost-effective and environmentally friendly.en_US
dc.language.isoenen_US
dc.publisherElsevieren_US
dc.relation.ispartofFuelen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectCatalytic membraneen_US
dc.subjectSustainable biodiesel productionen_US
dc.subjectAluminaen_US
dc.subjectCalcium oxide catalysten_US
dc.subjectPolydopamine modified PES membraneen_US
dc.subjectAssisted immobilizationen_US
dc.subjectAcidified oilen_US
dc.subjectTransesterificationen_US
dc.titleAntifouling polydopamine-modified poly (ether sulfone) membrane immobilized with alumina-calcium oxide catalyst for continuous biodiesel productionen_US
dc.typeArticleen_US
dc.departmentİzmir Institute of Technology. Chemical Engineeringen_US
dc.identifier.volume349en_US
dc.identifier.wosWOS:001007338300001en_US
dc.identifier.scopus2-s2.0-85160032285en_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.identifier.doi10.1016/j.fuel.2023.128685-
dc.authorscopusid56278323000-
dc.authorscopusid6601967292-
dc.authorscopusid6603259612-
dc.identifier.scopusqualityQ1-
item.grantfulltextembargo_20250101-
item.openairetypeArticle-
item.fulltextWith Fulltext-
item.cerifentitytypePublications-
item.openairecristypehttp://purl.org/coar/resource_type/c_18cf-
item.languageiso639-1en-
crisitem.author.dept03.02. Department of Chemical Engineering-
crisitem.author.dept03.02. Department of Chemical Engineering-
Appears in Collections:Chemical Engineering / Kimya Mühendisliği
Scopus İndeksli Yayınlar Koleksiyonu / Scopus Indexed Publications Collection
WoS İndeksli Yayınlar Koleksiyonu / WoS Indexed Publications Collection
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