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The removal of chromium ions from water in Donnan dialysis process

机译:Donnan透析过程中水中铬离子的去除

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The paper presents results of the studies on the removal of chromium ions (Cr2O72-) from multicomponent water solutions in the process of Donnan dialysis with anion-exchange membrane. The feeding solution contained the following salts: NaNO3, NaHCO3, NaCl (with a concentration of 3 mM for each component), and Na2Cr2O7 (with concentrations of 100, 300, or 500 mu g Cr(VI)/L). The Donnan dialysis process was conducted using a laboratory dialytic set-up equipped with 10 cell pairs with anion-exchange membranes, Selemion AMV (Asahi Glass, Japan) or Neosepta ACS (ASTOM Corp., Japan). The total working area of the membranes was 0.0756 m(2). NaCl solutions with concentrations of 100, 200, or 300 mM were used as receivers. The best effects of the anion exchange were obtained in the process with Selemion AMV membrane. Dichromate ions were efficiently removed from solutions with initial concentrations of 100 and 300 mu g Cr(VI)/L, at a relatively low salt concentration in the receiver equal to 100 mM NaCl. As a result of the anion exchange, chromium(VI) concentration was reduced to the value of 14 and 45 mu g Cr(VI)/L, respectively, that is, below the admissible value for potable water (50 mu g Cr(VI)/L). Mono-anion-selective membrane Neosepta ACS allowed to achieve satisfactory results of dichromate ion removal from the solution with a concentration of 100 mu g Cr(VI)/L - chromium(VI) concentration was reduced to the value of 13 mu g Cr(VI)/L (at the salt concentration of 100 mM NaCl). It should be underlined that for Neosepta ACS dichromate ions flux was three times lower than it was for Selemion AMV (0.030 x 10(-3) and 0.089 x 10(-3) mol/m(2) h, respectively). It standed for an adequately longer time of the anion exchange process with Neosepta ACS membrane.
机译:本文介绍了用阴离子交换膜在Donnan透析过程中从多组分水溶液中去除铬离子(Cr2O72-)的研究结果。进料溶液包含以下盐:NaNO3,NaHCO3,NaCl(每种成分的浓度为3 mM)和Na2Cr2O7(浓度为100、300或500μgCr(VI)/ L)。 Donnan透析过程使用配备10个带有阴离子交换膜的细胞对的实验室透析装置,Selemion AMV(日本Asahi Glass)或Neosepta ACS(日本ASTOM Corp.)进行。膜的总工作面积为0.0756 m(2)。浓度为100、200或300 mM的NaCl溶液用作接收器。用Selemion AMV膜在此过程中获得了最佳的阴离子交换效果。在接收器中相对较低的盐浓度等于100 mM NaCl的情况下,可以从初始浓度分别为100和300μg Cr(VI)/ L的溶液中有效地除去重铬酸根离子。由于阴离子交换的结果,铬(VI)的浓度分别降低到14和45μg Cr(VI)/ L的值,即低于饮用水的允许值(50μg Cr(VI)/ L )/ L)。单阴离子选择性膜Neosepta ACS允许以100μg Cr(VI)/ L的浓度从溶液中去除重铬酸根离子获得令人满意的结果-铬(VI)的浓度降低至13μg Cr( VI)/ L(在100 mM NaCl的盐浓度下)。应该强调的是,对于Neosepta ACS,重铬酸盐离子通量比Selemion AMV低三倍(分别为0.030 x 10(-3)和0.089 x 10(-3)mol / m(2)h)。它与Neosepta ACS膜相比具有更长的阴离子交换过程时间。

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