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首页> 外文期刊>Journal of the Chinese Institute of Chemical Engineers >CHROMIC ACID RECOVERY FROM CHROME PLATING RINSE WATER BY ION EXCHANGE
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CHROMIC ACID RECOVERY FROM CHROME PLATING RINSE WATER BY ION EXCHANGE

机译:通过离子交换从镀铬漂洗水中回收铬酸

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摘要

The regeneration of an anion bed saturated with dichromate ions by treatment with NaOH solution was studied in connection with the treatment of chrome plating rinse water by ion exchange. Column experiments were conducted to obtain an Cr(VI) elution curve and OH- breakthrough curve. The parametric effects of bed height, NaOH feed concentrations, and flow rate on the performance of regeneration were investigated. It was found that for a bed height of 70 cm and NaOH feed concentration of 1.5 to 2 mol/L with a flow rate of 100-150 mL/hr, up to a maximum concentration of 100 g/L of CrO3 could be obtained. Under the above operating conditions, the regenerant consumption is about 1.65 mole of OH- per mole of Cr(VI) recovered and the resin utilization is about 80%. An attempt is made to employ a simple analytic equation to correlate the OH- breakthrough and Cr(VI) elution data. The results of this work may be useful in the design and operation of systems for recovery and reuse of chromic acid by ion exchange in the chrome electroplating process. [References: 11]
机译:结合离子交换对镀铬漂洗水的处理,研究了用NaOH溶液处理重铬酸根离子饱和的阴离子床的再生。进行柱实验以获得Cr(VI)洗脱曲线和OH-穿透曲线。研究了床高,NaOH进料浓度和流速对再生性能的参数影响。已经发现,对于床高为70 cm和NaOH进料浓度为1.5至2 mol / L,流速为100-150 mL / hr的情况,可以获得最大浓度为100 g / L的CrO3。在上述操作条件下,每摩尔回收的Cr(VI)再生剂消耗量约为1.65摩尔OH-,树脂利用率约为80%。尝试采用一个简单的解析方程来关联OH突破和Cr(VI)洗脱数据。这项工作的结果对于在铬电镀工艺中通过离子交换回收和再利用铬酸的系统的设计和操作中可能有用。 [参考:11]

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