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离子交换法生产碳酸钾的工艺探讨
引用本文:王秀巩固 唐明林 等. 离子交换法生产碳酸钾的工艺探讨[J]. 矿物岩石, 1990, 10(1): 166-169
作者姓名:王秀巩固 唐明林 等
作者单位:成都地质学院,成都地质学院,成都地质学院应用化学系工业分析专业 89届毕业生
摘    要:本文讨论以工业KCI和NH4HCO3为原料、采用离子交换法(国产732钠型树脂)生产K2CO3的工艺。小试验的结果:以20%KCI溶液上柱,以分段交换率在50%以前为穿漏点、流速为0.033(ml/min.ml树脂)时,总交换率达83.3%,工作交换容量达2.24(毫摩尔钾/ml树脂);当以饱和NH4HCO3溶液进行解脱、流速在0.033(ml/min.ml树脂)时,解脱率达91.8%,产品的含量为98.2%。

关 键 词:氯化钾 碳酸氢铵 离子交换法 碳酸钾 工艺流程

TECHNIQUE OF PRODUCING POTASSIUM CARBONATE BY ION EXCHANGE
Wang Xiuying Tang Minglin Zhu Ming. TECHNIQUE OF PRODUCING POTASSIUM CARBONATE BY ION EXCHANGE[J]. Journal of Mineralogy and Petrology, 1990, 10(1): 166-169
Authors:Wang Xiuying Tang Minglin Zhu Ming
Abstract:In order to produce potassium carbonate, the method presented here uses a strongly acidic cation exchange resin,applying industrial potassium chlorate and ammonium hydrogen carbonate as raw materials. The exchange rate of the potassium chlorate can reach 83.3%. When ammonium hydrogen carbonate is used as washing agent,the washing rate can reach 91.8% ,and the potassium carbonate concentration of the product is 98. 2%.
Keywords:potassium chlorate  ammonium hydrogen carbonate  potassium carbonate  ion exchange  technical process
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