Electro-deionization of Cr (VI)-Containing Solution. Part II: Chromium Transport through Inorganic Ion-Exchanger and Composite Ceramic Membrane

被引:25
作者
Dzyazko, Yuliya S. [1 ]
Vasilyuk, Sergey L. [1 ]
Rozhdestvenskaya, Ludmila M. [1 ]
Belyakov, Vladimirn. [1 ]
Stefanyak, Nikolayv. [1 ]
Kabay, Nalan [2 ]
Yueksel, Mithat [2 ]
Arar, Oezguer [3 ]
Yueksel, Uemran [3 ]
机构
[1] VI Vernadskii Inst Gen & Inorgan Chem, UA-03142 Kiev, Ukraine
[2] Ege Univ, Dept Chem Engn, Izmir, Turkey
[3] Ege Univ, Dept Chem, Izmir, Turkey
关键词
Ceramic membrane; Chromate; Desalination; Electro-deionization; Electrodialysis; Hydrated zirconium dioxide; HEXAVALENT CHROMIUM; NICKEL IONS; CHROMATE; ELECTRODEIONIZATION; ELECTRODIALYSIS; RESINS; WATER; SORPTION; REMOVAL; FLUXES;
D O I
10.1080/00986440802303715
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
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.
引用
收藏
页码:22 / 38
页数:17
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