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Neutralization of Industrial Water by Electrodialysis

机译:电渗析中和工业用水

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摘要

The process of non-reagent adjustment of the pH of a NaCl solution (0.5 g/L) of different acidity was investigated by the method of bipolar electrodialysis on a device operating according to the K-system (concentration). The experiments were carried out in the range pH = 2.0–12.0 with monopolar cation-exchange MK-40 (for alkaline solutions) or anion-exchange MA-40 (for acidic solutions) and bipolar MB-2 membranes. The regularities of the change in the pH of the solution on the current density, process productivity and energy consumption for the neutralization process have been investigated. Revealed: with different productivity of the apparatus (Q = 0.5–1.5 m3/h), in the range of pH 3.0–11.0, with an increase in the current density, a neutral pH value is achieved. It has been shown that at pH above 11.0 and below 3.0, even at high current densities (i > 20 A/m2), its value cannot be changed. This is due to the neutralization of the H+ or OH− ions generated by the bipolar membrane by water ions, which are formed as a result of the dissociation of water molecules at the border of the monopolar membrane and the solution under conditions when the value of current exceeds the limiting value.
机译:通过在根据K-System(浓度)操作的装置上的双极电渗析的方法研究了不试剂调节的不同酸度的NaCl溶液(0.5g / L)的pH值。实验在pH = 2.0-12.0的范围内进行,具有单极阳离子交换MK-40(用于碱性溶液)或阴离子交换MA-40(用于酸性溶液)和双极MB-2膜。研究了对电流密度的溶液pH的变化的规律,研究了中和过程的过程生产力和能量消耗。揭示:具有不同生产率的装置(Q = 0.5-1.5m 3 / h),在pH 3.0-11.0的范围内,随着电流密度的增加,实现中性pH值。已经表明,在11.0至3.0以下,即使在高电流密度(i> 20a / m2),它的值也不能改变。这是由于通过水离子中和由双极膜产生的H +或OH-离子,其在单极膜边界处的水分子和溶液在值下的溶液的结果中形成电流超过限制值。

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