Bio-based succinic acid recovery by ion exchange resins integrated with nanofiltration/reverse osmosis preceded crystallization

dc.contributor.authorOmwene, Philip Isaac
dc.contributor.authorSarihan, Zehra Betul Ocal
dc.contributor.authorKaragündüz, Ahmet
dc.contributor.authorKeskinler, Bülent
dc.date.accessioned2025-10-29T11:27:45Z
dc.date.issued2021
dc.departmentFakülteler, Mühendislik Fakültesi, Çevre Mühendisliği Bölümü
dc.description.abstractSuccinic acid is a key platform chemical for production of various products such as biodegradable polymers, pharmaceuticals, fine chemicals and foods. In the present study, bio-based succinic acid was recovered through two processes. Process I consisted of chro-matographic separation with anionic exchange resin followed by direct crystallization, whereas process II sequentially consisted of cationic exchanger, activated carbon, NF/RO membrane, vacuum distillation, and crystallization. The highest chromatographic separa-tion efficiency for succinic acid by Amberlite IRA900 Cl column was calculated as 69.3% at flow rate of 0.42 BV/h. Rejection of succinic aid (SA), lactic acid (LA), formic acid (FA) and acetic acid (AC) by NF90 membrane was 53.1, 51.8, 46.6 and 39.8%, respectively at pH less than 2. However, at pH 6.8 the respective rejections increased to 96.8, 90.6, 71.3 and 70.5%. Double pass with BW30 or HP reverse osmosis membranes achieved retention of SA, LA, FA and AC of 95.9%, 95.8%, 65.4% and 46.9%, respectively. Analysis of generated SA crystals by X-ray diffraction technique (XRD) and Fourier transform infrared (FTIR) showed the crys-tallinity of recovered SA as conformable to standard grade crytsals. The purity of generated succinic acid crystals was recorded as 98.5% and 96.7% for process I and process II, respec-tively. The calculated succinic acid yield was 78% for process I and 65% for process II. Herein, we demonstrated two alternative systems for bio-based succinic acid recovery, which will set a stage for research in efficient downstream purification of SA. (c) 2021 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
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 sup-port under project No. 115Y824.
dc.identifier.doi10.1016/j.fbp.2021.06.006
dc.identifier.endpage9
dc.identifier.issn0960-3085
dc.identifier.issn1744-3571
dc.identifier.orcid0000-0002-3617-5596
dc.identifier.orcid0000-0002-8406-0718
dc.identifier.scopus2-s2.0-85109549574
dc.identifier.scopusqualityQ1
dc.identifier.startpage1
dc.identifier.urihttps://doi.org/10.1016/j.fbp.2021.06.006
dc.identifier.urihttps://hdl.handle.net/20.500.14854/10883
dc.identifier.volume129
dc.identifier.wosWOS:000701724400001
dc.identifier.wosqualityQ2
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.language.isoen
dc.publisherElsevier
dc.relation.ispartofFood and Bioproducts Processing
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.subjectNanofiltration
dc.subjectReverse osmosis
dc.titleBio-based succinic acid recovery by ion exchange resins integrated with nanofiltration/reverse osmosis preceded crystallization
dc.typeArticle

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