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dc.contributor.authorGül, Abdulkadir
dc.contributor.authorTanyıldızı, Muhammet Şaban
dc.date.accessioned2024-05-16T06:00:23Z
dc.date.available2024-05-16T06:00:23Z
dc.date.issued2024 May 9en_US
dc.identifier.urihttps://pubmed.ncbi.nlm.nih.gov/38720060/
dc.identifier.urihttps://link.springer.com/article/10.1007/s12010-024-04937-z
dc.identifier.urihttps://hdl.handle.net/20.500.12440/6243
dc.description.abstractGluconic acid (GA) is widely used in the pharmaceutical, food, detergent, textile, leather, and concrete industries. However, cost-effective and high-yield production of GA remains a challenge. Due to currently high raw material inputs of GA, various alternative carbohydrate sources are being investigated. Sucrose is one of the cost-effective biomass sources that can be used as feedstock. The most common industrial production of GA is based on wild-type bacteria and fungi, but there are many problems with this production. This study aimed to optimize the production of GA from glucose produced by hydrolysis of sucrose using recombinant E. coli Waksman (W) pqq+ strain. After sucrose was enzymatically hydrolyzed, significant medium components for GA production were determined as glucose, calcium carbonate (CaCO3), peptone, and ammonium phosphate ((NH4)3PO4) using Placket-Burman Design (PBD). Detailed optimization of the medium components that are significant in GA production was carried out using central composite design (CCD), and optimum values of the independent variables examined in maximum GA production (93.5 ± 2.95 g/L) were determined as glucose 95, CaCO3 25, peptone 2, and (NH4)3PO4 1.13 (g/L). Using results obtained in the Erlenmeyer experiments, GA production in the bioreactor was investigated by CCD. The maximum GA efficiency (3.20 ± 0.15 g/L. h) was obtained under conditions where the air supply rate was 10.82 L/min, stirring speed was 656.87 rpm, and CaCO3 concentration was 16.90 g/L. In conclusion, it has been shown that GA can be produced with a high yield with this novel approach using a recombinant strain for GA production from sucrose.en_US
dc.language.isoengen_US
dc.publisherPubMed Disclaimeren_US
dc.relation.ispartofPubMed Disclaimeren_US
dc.rightsinfo:eu-repo/semantics/openAccessen_US
dc.subjectE. coli Waksman pqq+en_US
dc.subjectBiomass sourcesen_US
dc.subjectCentral composite designen_US
dc.subjectGluconic aciden_US
dc.titleGluconic Acid Production by Using Recombinant Escherichia coli Waksman pqq+ Cells with a Novel Approach from Biomass Sourcesen_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.contributor.institutionauthorGül, Abdulkadir
dc.identifier.doi10.1007/s12010-024-04937-zen_US
dc.authorscopusid58158413100en_US
dc.description.pubmedpublicationid38720060en_US


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