首页> 外文会议>9th International Symposium on Salt(第九届世界盐业大会)论文集 >STUDY ON THE SALTS CRYSTALLIZATION BEHAVIOURS DURING BITTERN BOILING EVAPORATION AT 70°C
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STUDY ON THE SALTS CRYSTALLIZATION BEHAVIOURS DURING BITTERN BOILING EVAPORATION AT 70°C

机译:70°C沸腾蒸发过程中盐的结晶行为研究

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Normally the production process to deal with the bittern includes three steps: KCl production with 2-effect vacuum evaporation of the mixture of bittern and mother liquor after KCl production; Br2 extraction through distillation process, and MgCl2·6H2O production by mono-effect evaporation. For the production of KCl, Most of the salt industry plants will mix the bittern and mother liquor after its production in the first evaporator, and separate the NaCl and MgSO4 solids from the mother liquor in the second evaporator. In the second evaporator, the operation temperature is 65~70°C, but the concentration is controlled by operation experience only, that may lead to the NaCl and MgSO4 solids can not be separated from the liquor completely, then the output is low, meanwhile big quantity of mother liquor is mixed in the solid, so the throughout of KCl product wiill be low also, and the further separation of the NaCl and MgSO4 solids will be not easy. Based on the analysis of Na+、K+、Mg2+//SO42- Cl--H2O phase diagram and the experimentation of the bittern evaporation in the laboratory, this paper studies the salt crystallization behaviours of the bittern evaporation under 70°C, which will supply reliable data for operation of the second evaporator in the production of KCl product.
机译:通常,用于处理卤水的生产过程包括三个步骤:氯化钾生产,在氯化钾生产后,对卤水和母液的混合物进行两效真空蒸发;蒸馏法提取Br2,单效蒸发法生产MgCl2·6H2O。对于氯化钾的生产,大多数制盐工厂将在第一个蒸发器中将卤水和母液混合后,在第二个蒸发器中从母液中分离出NaCl和MgSO4固体。在第二台蒸发器中,操作温度为65〜70℃,但浓度仅受操作经验的控制,这可能导致NaCl和MgSO4固体不能完全从液体中分离出来,因此产量低,同时固体中混有大量的母液,因此KCl产物的全部含量也较低,并且进一步分离NaCl和MgSO4固体也不容易。在分析Na +,K +,Mg2 + // SO42-Cl-H2O相图的基础上,结合实验室的卤水蒸发实验,研究了卤水在70℃下的盐析出行为,为盐雾的结晶提供了理论依据。用于生产KCl产品的第二个蒸发器的可靠数据。

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