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dc.contributor.authorGül, Abdulkadir
dc.contributor.authorTanyıldızı, Muhammet Şaban
dc.date.accessioned2025-03-17T12:21:52Z
dc.date.available2025-03-17T12:21:52Z
dc.date.issued15 May 2025en_US
dc.identifier.citationScopus EXPORT DATE: 17 March 2025 @ARTICLE{Gül2025, url = {https://www.scopus.com/inward/record.uri?eid=2-s2.0-85216252302&doi=10.1016%2fj.fuel.2025.134477&partnerID=40&md5=8c62e8076a9cb40b2112bf6981e57523}, affiliations = {Department of Genetics and Bioengineering, Faculty of Engineering and Natural Sciences, Gumushane University, Gumushane, Türkiye; Department of Bioengineering, Faculty of Engineering, Firat University, Elazig, Türkiye}, correspondence_address = {A. Gül; Department of Genetics and Bioengineering, Faculty of Engineering and Natural Sciences, Gumushane University, Gumushane, Türkiye; email: kadirgul@gumushane.edu.tr}, publisher = {Elsevier Ltd}, issn = {00162361}, coden = {FUELA}, language = {English}, abbrev_source_title = {Fuel} }en_US
dc.identifier.urihttps://hdl.handle.net/20.500.12440/6481
dc.description.abstract5-Hydroxymethylfurfural (HMF), which can be produced in high yields by acid-catalyzed dehydration of carbohydrates, is used as a feedstock in biofuel and biopolymer production. However, these acidic catalysts are usually added externally, which increases HMF production costs. Furthermore, other important parameters for high yields of HMF production are raw material selection, reaction medium, and separation-purification processes. The aim of this study is to produce HMF in one-pot without the addition of any exogenous catalyst by evaluating the fructose remaining in the production medium in which the glucose from sucrose hydrolysis is microbially fermented into gluconic acid (GA). HMF production from fructose in a biphasic system consisting of a fermentation liquid containing GA and fructose and 2-Methyltetrahydrofuran (2-MeTHF) was optimized using Central Composite Design (CCD). The variables examined included reaction time, reaction temperature, solvent type, salt type, and organic/aqueous phase ratio. In the study, by chelating GA and calcium ions, the low degree of ionization of GA was increased, and HMF was produced in high yields without the addition of a catalyst. Under optimum conditions, using 2-MeTHF/ fermentation liquid (6:1) and 7.56 wt% CaCl2, the yield of HMF produced in pressurized (hydrothermal) vessels at about 147 °C for 158 min reached 77.6 % of the theoretical yield. The amount of GA in the production medium was 92.64 % preserved from degradation. GA and HMF in different phases of the biphasic system were purified from the production medium in high yields. Furthermore, 2-MeTHF, which constitutes the organic phase of the biphasic system, was recovered at approximately 95 % by vacuum evaporation. As a result, HMF production from sucrose, which is a more economical and abundant raw material compared to glucose and fructose, was realized in one-pot without the addition of any catalyst. © 2025 Elsevier Ltden_US
dc.language.isoengen_US
dc.publisherElsevier Ltden_US
dc.relation.ispartofFuelen_US
dc.rightsinfo:eu-repo/semantics/openAccessen_US
dc.subject5-Hydroxymethylfurfural; Biphasic system; Central composite design; Gluconic acid; One-poten_US
dc.titleA strategy for the one-pot direct production of 5-hydroxymethylfurfural (HMF) from sucrose using organic weak acid in situ as a catalysten_US
dc.typearticleen_US
dc.relation.publicationcategoryMakale - Ulusal Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.departmentFakülteler, Mühendislik ve Doğa Bilimleri Fakültesi, Genetik ve Biyomühendislik Bölümüen_US
dc.authorid0000-0003-4879-6194en_US
dc.identifier.volume388en_US
dc.contributor.institutionauthorGül, Abdulkadir
dc.identifier.doi10.1016/j.fuel.2025.134477en_US
dc.authorscopusid58158413100en_US


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