Simulated acid mine drainage treatment in iron oxidizing ceramic membrane bioreactor with subsequent co-precipitation of iron and arsenic

dc.authorid0000-0001-9675-0348
dc.authorid0000-0003-2576-1300
dc.authorid0000-0002-9447-1668
dc.authorid0000-0002-9898-9173
dc.authorid0000-0001-9423-6556
dc.contributor.authorDemir, Emir Kasim
dc.contributor.authorYaman, Belma Nural
dc.contributor.authorCelik, Pinar Aytar
dc.contributor.authorPuhakka, Jaakko A.
dc.contributor.authorŞahinkaya, Erkan
dc.date.accessioned2025-05-10T19:43:52Z
dc.date.issued2021
dc.departmentİMÜ, Fakülteler, Mühendislik ve Doğa Bilimleri Fakültesi, Biyomühendislik Bölümü
dc.description.abstractAcid mine drainage (AMD), generated in the active and abandoned mine sites, is characterized by low pH and high metal concentrations. One AMD treatment possibility is biologically oxidizing Fe2+ followed by precipitation through pH control. As compared to autotrophic iron oxidizing microbial community, a microbial community enriched in the presence of organic nutrients was hypothesized to yield higher biomass during commissioning the bioreactor. In this study, the treatment of Fe, Cu, Co, Mn, Zn, Ni, and As containing simulated AMD was studied using an iron-oxidizing ceramic membrane bioreactor (CMBR) at varying hydraulic retention times (HRTs) (6-24 h) and two different feed Fe2+ concentrations (250 and 750 mg/L). The impact of tryptone soya broth (TSB) on the CMBR performance was also investigated. Almost complete Fe2+ oxidation and sustainable flux at around 5.0 L/(m2.h) were obtained in the CMBR with the Alicyclobacillus tolerans and Acidiphilium cryptum dominated enrichment culture. The Fe2+ oxidation rate, as assessed in batch operation cycles of CMBR, increased significantly with increasing Fe2+ loading to the bioreactor. The iron oxidation rate decreased by the elimination of organic matter from the feed. The increase of the CMBR permeate pH to 3.5-4.0 resulted in selective co-precipitation of As and Fe (over 99%) with the generation of biogenic schwertmannite.
dc.description.sponsorshipResearch Fund of Istanbul Medeniyet University [F-GAP-2019-1487]
dc.description.sponsorshipThis work was supported by the Research Fund of Istanbul Medeniyet University. Project Number: F-GAP-2019-1487.
dc.identifier.doi10.1016/j.watres.2021.117297
dc.identifier.issn0043-1354
dc.identifier.issn1879-2448
dc.identifier.pmid34118649
dc.identifier.scopus2-s2.0-85108699843
dc.identifier.scopusqualityQ1
dc.identifier.urihttps://doi.org/10.1016/j.watres.2021.117297
dc.identifier.urihttps://hdl.handle.net/20.500.14730/10762
dc.identifier.volume201
dc.identifier.wosWOS:000681713800013
dc.identifier.wosqualityQ1
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.indekslendigikaynakPubMed
dc.language.isoen
dc.publisherPergamon-Elsevier Science Ltd
dc.relation.ispartofWater Research
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzKA_WOS_20250302
dc.subjectIron oxidation
dc.subjectAcid mine drainage
dc.subjectArsenic removal
dc.subjectSchwertmannite
dc.subjectCeramic membrane bioreactor
dc.subjectAlicyclobacillus tolerans
dc.titleSimulated acid mine drainage treatment in iron oxidizing ceramic membrane bioreactor with subsequent co-precipitation of iron and arsenic
dc.typeArticle

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