Novel chromatographic purification of succinic acid from whey fermentation broth by anionic exchange resins

dc.contributor.authorOmwene, Philip Isaac
dc.contributor.authorOcal, Zehra Betul
dc.contributor.authorYagcioglu, Meltem
dc.contributor.authorKaragündüz, Ahmet
dc.contributor.authorKeskinler, Bülent
dc.date.accessioned2025-10-29T11:33:10Z
dc.date.issued2022
dc.departmentFakülteler, Mühendislik Fakültesi, Çevre Mühendisliği Bölümü
dc.description.abstractReplacement of the petroleum-based refineries with the biorefinery is regarded as an essential step towards a zero waste (circular) economy. Biobased succinic acid (SA) is listed by the United States Department of Energy among the top ten chemicals with the potential to replace chemicals from petroleum synthesis with renewable sources. Purification of bio-based succinic acid from fermentation by-products such as alcohols, formic acid, acetic acid and lactic is a major drawback of fermentative SA production. This study addresses this issue through a novel chromatographic separation using three distinct anionic resins: Amberlite IRA958 Cl (strong base anion exchange resin), Amberlite HPR 900 OH (strong base anion exchange resin) and Amberlyst A21 (week base anion exchange resin). The influence of process variables such as flow rate (0.18 BV/h, 0.42 BV/h and 0.84 BV/h), eluent concentration (1%, 5% and 10% HCl) and temperature (20, 30 and 40 degrees C) were investigated. The results indicated SA separation efficiency of 76.1%, 69.3% and 81.2% for Amberlyst A21, Amberlite HPR 900 OH and Amberlite IRA958 Cl, respectively. As the regenerant HCl concentration increased from 1 to 10%, calculated succinic acid separation efficiencies decreased from 80.3 to 70.7%. Notably, as the regenerant strength increased from 1 to 10%, the total amount of organic acids desorbed from the resin sharply increased. At operation temperatures of 20, 30 and 40 degrees C, SA separation efficacies were 81.2%, 73.9% and 76.4%, respectively. The insights from this study will be of great value in design of chromatographic separation systems for organic acids.
dc.description.sponsorshipScientific and Technological Research Council of Turkey (TuBITAK) [115Y824]
dc.description.sponsorshipWe wish to thank the Scientific and Technological Research Council of Turkey (TuBITAK) for providing the financial support under project No. 115Y824
dc.identifier.doi10.1007/s00449-022-02805-w
dc.identifier.endpage2017
dc.identifier.issn1615-7591
dc.identifier.issn1615-7605
dc.identifier.issue12
dc.identifier.orcid0000-0002-3617-5596
dc.identifier.orcid0000-0002-8513-677X
dc.identifier.pmid36352044
dc.identifier.scopus2-s2.0-85141573505
dc.identifier.scopusqualityQ1
dc.identifier.startpage2007
dc.identifier.urihttps://doi.org/10.1007/s00449-022-02805-w
dc.identifier.urihttps://hdl.handle.net/20.500.14854/12290
dc.identifier.volume45
dc.identifier.wosWOS:000880511400001
dc.identifier.wosqualityQ2
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.indekslendigikaynakPubMed
dc.language.isoen
dc.publisherSpringer
dc.relation.ispartofBioprocess and Biosystems Engineering
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzKA_WOS_20251020
dc.subjectSuccinic acid
dc.subjectWhey
dc.subjectResins
dc.subjectChromatography
dc.titleNovel chromatographic purification of succinic acid from whey fermentation broth by anionic exchange resins
dc.typeArticle

Dosyalar