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首页> 外文期刊>Journal of Hazardous Materials >A new approach to increasing the efficiency of low-pH Fe-electrocoagulation applications
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A new approach to increasing the efficiency of low-pH Fe-electrocoagulation applications

机译:一种提高低pH Fe电凝应用效率的新方法

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Incomplete oxidation of Fe(Ⅱ) species released from the anode to Fe(Ⅲ) may impede iron electrocoag-ulation processes conducted under low dissolved oxygen and/or pH < 7 conditions, accompanied by the typically high buffering capacity of wastewater. This paper introduces a new approach to overcome this drawback by applying a second electrochemical cell (Ti/RuCb anode and Ti cathode) to be operated in parallel to the electrocoagulation cell. The second unit oxidizes Ch ions invariably present in the water to HOCI, which is capable of oxidizing Fe(II) species at a high rate, irrespective of pH or C_(2(eq)) concentration. An electrolytic cell with a Ti/RuO_2 anode and Ti cathode was shown to successively oaqperate in parallel to a sacrificial electrocoagulation cell (Fe anode and Ti cathode) to attain complete Fe(Ⅱ) conversion to Fe(III) under low-pH conditions, in which, in the absence of the 2nd cell, unwanted Fe(Ⅱ) species would have dominated the dissolved iron species. Current efficiency for Cl2 production was 12.4% and 45.7% at 200 and 1000mg Cl/l, respectively. Under three practical conditions (pH 6,[Cl~-]-200mg/l; pH 6, @@[Cl~-]-400mg/l; pH 5, [Cl~-]-600mg/l) the power demand of the combined system was 25.29, 12.7 and 8.1 kWh/kg Fe(Ⅲ)~(produced), respectively, suggesting that the presented approach is competitive at [Cl~-]>~600mg/l.
机译:从阳极释放出来的Fe(Ⅱ)物种不完全氧化为Fe(Ⅲ)可能会阻碍在低溶解氧和/或pH <7的条件下进行的铁电凝过程,同时通常具有较高的废水缓冲能力。本文介绍了通过应用第二个电化学电池(Ti / RuCb阳极和Ti阴极)与电凝电池并联运行来克服这一缺陷的新方法。第二单元将水中始终存在的Ch离子氧化为HOCI,无论pH或C_(2(eq))浓度如何,它都能以高速率氧化Fe(II)物种。示出了具有Ti / RuO_2阳极和Ti阴极的电解池与牺牲电凝池(Fe阳极和Ti阴极)平行连续连续渗入,以在低pH条件下实现从Fe(Ⅱ)到Fe(III)的完全转化,其中,在没有第二个单元的情况下,不需要的Fe(Ⅱ)物种将主导溶解的铁物种。在200和1000mg Cl / l下,生产Cl2的当前效率分别为12.4%和45.7%。在三种实际条件下(pH 6,[Cl〜-]-200mg / l; pH 6,@@ [Cl〜-]-400mg / l; pH 5,[Cl〜-]-600mg / l),功率需求为组合系统的Fe(Ⅲ)〜(产生)分别为25.29、12.7和8.1 kWh / kg Fe(Ⅲ)〜,表明该方法在[Cl〜-]>〜600mg / l时具有竞争力。

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