Boric acid recovery from wastewater by chromatographic separation and mathematical modeling
| dc.authorid | OCAL, ZEHRA BETUL/0000-0002-3617-5596 | |
| dc.contributor.author | Kole, Zehra | |
| dc.contributor.author | Ocal, Zehra Betul | |
| dc.contributor.author | Omwene, Philip Isaac | |
| dc.contributor.author | Soydemir, Gulfem | |
| dc.contributor.author | Keskinler, Bulent | |
| dc.contributor.author | Karagunduz, Ahmet | |
| dc.date.accessioned | 2025-03-23T19:41:13Z | |
| dc.date.available | 2025-03-23T19:41:13Z | |
| dc.date.issued | 2024 | |
| dc.department | Sinop Üniversitesi | |
| dc.description.abstract | The new approaches in industrial wastewater management underscores the importance of reclaiming valuable materials. Within the boron industry, the generation of substantial wastewater containing preliminary boron species is a significant concern. This study focuses on recovering boric acid from boron production wastewater, addressing the challenge of separating impurities like sulfate, calcium, and magnesium. The methodology adopts chromatographic separation using a cation exchange resin in two forms: (1) Finex CS10GC cation exchanger in Na+ form and (2) Finex CS10GC cation exchanger in Ca2+/Mg2+ form. Notably, the Finex CS10GC ion exchanger in Na+ form achieves a separation efficiency of 95.5 % at a flow rate of 5 mL/min with a 0.20 bed volume (BV) loading. In contrast, the Ca2+/Mg2+ loaded resin achieves a separation efficiency of 23.3 % at the same flow rate. As the boron loading rate decreases to 10 %, the separation efficiency increases to 42.6 %. The flow rate also plays a crucial role, as an increase corresponds to a decrease in separation efficiency. Notably, the Finex CS10GC ion exchanger in Na+ form consistently exhibits superior separation efficiency and band resolution. A mathematical model is introduced to simulate the effective separation of boric acid from other impurities. The quality of the recovered boric acid conforms to the standard grade (Merck KGaA), exhibiting a purity level within the range of 99.5-100 %, suggesting substantial economic value. The proposed recovery process contributes significantly to environmental preservation by mitigating waste discharge, exemplifying a noteworthy commitment to resource conservation. | |
| dc.description.sponsorship | General Directorate of Eti Maden Enterprises | |
| dc.description.sponsorship | The authors would like to thank the General Directorate of Eti Maden Enterprises for their support and providing samples for this study. | |
| dc.identifier.doi | 10.1016/j.jclepro.2024.141633 | |
| dc.identifier.issn | 0959-6526 | |
| dc.identifier.issn | 1879-1786 | |
| dc.identifier.scopus | 2-s2.0-85187694243 | |
| dc.identifier.scopusquality | Q1 | |
| dc.identifier.uri | https://doi.org/10.1016/j.jclepro.2024.141633 | |
| dc.identifier.uri | https://hdl.handle.net/11486/6527 | |
| dc.identifier.volume | 448 | |
| dc.identifier.wos | WOS:001219073300001 | |
| dc.identifier.wosquality | Q1 | |
| dc.indekslendigikaynak | Web of Science | |
| dc.indekslendigikaynak | Scopus | |
| dc.language.iso | en | |
| dc.publisher | Elsevier Sci Ltd | |
| dc.relation.ispartof | Journal of Cleaner Production | |
| dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | |
| dc.rights | info:eu-repo/semantics/closedAccess | |
| dc.snmz | KA_WOS_20250323 | |
| dc.subject | Boron recovery | |
| dc.subject | Ion exchange | |
| dc.subject | Chromatographic separation | |
| dc.subject | Modeling | |
| dc.subject | Wastewater treatment | |
| dc.subject | Wastewater reuse | |
| dc.title | Boric acid recovery from wastewater by chromatographic separation and mathematical modeling | |
| dc.type | Article |












