Electro-deionization of Cr (VI)-Containing Solution. Part II: Chromium Transport through Inorganic Ion-Exchanger and Composite Ceramic Membrane
dc.contributor.author | Dzyazko, Yuliya S. | |
dc.contributor.author | Vasilyuk, Sergey L. | |
dc.contributor.author | Rozhdestvenskaya, Ludmila M. | |
dc.contributor.author | Belyakov, Vladimirn. | |
dc.contributor.author | Stefanyak, Nikolayv. | |
dc.contributor.author | Kabay, Nalan | |
dc.contributor.author | Yueksel, Mithat | |
dc.contributor.author | Arar, Oezguer | |
dc.contributor.author | Yueksel, Uemran | |
dc.date.accessioned | 2019-10-27T20:20:01Z | |
dc.date.available | 2019-10-27T20:20:01Z | |
dc.date.issued | 2009 | |
dc.department | Ege Üniversitesi | en_US |
dc.description | Somer Symposium 2007 -- MAY 14-15, 2007 -- Middle East Tech Univ, Ankara, TURKEY | en_US |
dc.description.abstract | Cr (VI) transport through a composite ceramic membrane containing an ion-exchange component, namely xerogel of hydrated zirconium dioxide, was investigated. The diffusion coefficient of Cr (VI) species through the membrane, which has been determined under open circuit conditions, is 1.80 x 10(-10) m(2) s(-1). The transport number of Cr (VI) species through the ceramic membrane was found to rise with increasing voltage and reached 0.17 under over-limiting current conditions. On the other hand, the transport of chromate ions through hydrogel of hydrated zirconium dioxide becomes more intensive with a decrease in potential drop through the system involving ion-exchanger bed and ceramic membrane due to decrease in the membrane resistance. The diffusion coefficient of Cr (VI) ions in hydrogel of the inorganic ion exchanger was estimated as 4.36 x 10(-12) m(2) s(-1). A possibility of Cr (VI) removal from a weakly acidic diluted solution using an electro-deionization method was shown: the degree of solution purification was found to reach 50%. The transport of species is realized through both the solution and the ion exchanger. | en_US |
dc.identifier.doi | 10.1080/00986440802303715 | |
dc.identifier.endpage | 38 | en_US |
dc.identifier.issn | 0098-6445 | |
dc.identifier.issn | 0098-6445 | en_US |
dc.identifier.issue | 01.Feb | en_US |
dc.identifier.startpage | 22 | en_US |
dc.identifier.uri | https://doi.org/10.1080/00986440802303715 | |
dc.identifier.uri | https://hdl.handle.net/11454/41555 | |
dc.identifier.volume | 196 | en_US |
dc.identifier.wos | WOS:000260209200003 | en_US |
dc.identifier.wosquality | Q3 | en_US |
dc.indekslendigikaynak | Web of Science | en_US |
dc.language.iso | en | en_US |
dc.publisher | Taylor & Francis Inc | en_US |
dc.relation.ispartof | Chemical Engineering Communications | en_US |
dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | en_US |
dc.rights | info:eu-repo/semantics/closedAccess | en_US |
dc.subject | Ceramic membrane | en_US |
dc.subject | Chromate | en_US |
dc.subject | Desalination | en_US |
dc.subject | Electro-deionization | en_US |
dc.subject | Electrodialysis | en_US |
dc.subject | Hydrated zirconium dioxide | en_US |
dc.title | Electro-deionization of Cr (VI)-Containing Solution. Part II: Chromium Transport through Inorganic Ion-Exchanger and Composite Ceramic Membrane | en_US |
dc.type | Article | en_US |