Publication:
Pilot-scale test results of electrodialysis bipolar membrane for reverse-osmosis concentrate recovery

dc.contributor.authorKestioğlu, O. Erdem
dc.contributor.buuauthorGazigil, Leyla
dc.contributor.buuauthorGAZİGİL, LEYLA
dc.contributor.buuauthorEr, Eren
dc.contributor.buuauthorYonar, Taner
dc.contributor.buuauthorYONAR, TANER
dc.contributor.departmentBursa Uludağ Üniversitesi/Mühendislik Fakültesi/Çevre Mühendisliği Bölümü.
dc.contributor.orcid0000-0001-8139-1338
dc.contributor.researcheridAAX-9798-2021
dc.contributor.researcheridAEA-5887-2022
dc.contributor.researcheridAAY-9420-2020
dc.date.accessioned2024-09-17T12:00:24Z
dc.date.available2024-09-17T12:00:24Z
dc.date.issued2022-01-01
dc.description.abstractIn this study, it is aimed to investigate the potential of electrodialysis bipolar membrane (EDBM) systems for the recovery of the concentrate originating from an organized industrial estate (OIE) wastewater treatment system with reverse osmosis (RO). Acids and bases were obtained from a pilot-scale treatment plant as a result of the research. Furthermore, the sustainability and affordability of acids and bases obtained by EDBM systems were investigated. Six cycles were carried out in continuous-flow mode with the EDBM system as batch cycles in the disposal of the concentrate and the production of acids and bases with the EDBM system. For each cycle, the EDBM system was operated for 66, 48, 66, and 80 min, respectively, and the last two cycles were operated for a total of 165 min (70 + 90) with 5 min of waiting. In the EDBM system, a working method was determined such that the cycle flow rate was 180 L/hour, energy to be given to the system was 25 V, and the working pressure was in the range of 0.8-2.5 bar. In the six cycles with the EDBM system, the concentrate, acid and base, conductivity, pH, and pressure increase values were investigated depending on time. Throughout all these studies, the cycles were continued over the products formed in the acid and base chamber. As a result of all the cycles, acid (HCl) production at a level of 1.44% and base (NaOH) production at a level of 2% were obtained.
dc.identifier.doi10.3390/membranes12010083
dc.identifier.issue1
dc.identifier.urihttps://doi.org/10.3390/membranes12010083
dc.identifier.urihttps://hdl.handle.net/11452/44833
dc.identifier.volume12
dc.identifier.wos000757055600001
dc.indexed.wosWOS.SCI
dc.language.isoen
dc.publisherMdpi
dc.relation.journalMembranes
dc.relation.publicationcategoryMakale - Ulusal Hakemli Dergi
dc.relation.tubitak7130586
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.subjectDesalination brines production
dc.subjectInnovative beneficial reuse
dc.subjectWaste-water treatment
dc.subjectAcid
dc.subjectIntegration
dc.subjectSeparation
dc.subjectNanofiltration
dc.subjectValorization
dc.subjectBroth
dc.subjectNf
dc.subjectElectrodialysis bipolar membrane
dc.subjectConcentrate
dc.subjectAcid recovery
dc.subjectBase recovery
dc.subjectMembrane
dc.subjectScience & technology
dc.subjectLife sciences & biomedicine
dc.subjectPhysical sciences
dc.subjectTechnology
dc.subjectBiochemistry & molecular biology
dc.subjectChemistry, physical
dc.subjectEngineering, chemical
dc.subjectMaterials science, multidisciplinary
dc.subjectPolymer science
dc.subjectBiochemistry & molecular biology
dc.subjectChemistry
dc.subjectEngineering
dc.subjectMaterials science
dc.subjectPolymer science
dc.titlePilot-scale test results of electrodialysis bipolar membrane for reverse-osmosis concentrate recovery
dc.typeArticle
dspace.entity.typePublication
relation.isAuthorOfPublication79cc1fe5-3be2-4b00-a3c2-3947a76505ab
relation.isAuthorOfPublication6f17179c-9535-4414-982e-bd78630bbedf
relation.isAuthorOfPublication.latestForDiscovery79cc1fe5-3be2-4b00-a3c2-3947a76505ab

Files

Collections