Method for producing potassium chloride by adopting carnallite hot-melt brine
A technology of carnallite and potassium chloride, applied in the direction of alkali metal chloride, etc., can solve the problems of increasing energy consumption, difficulty in meeting market demand, high energy consumption, etc., and achieve the effect of reducing energy consumption
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Embodiment 1
[0016] This embodiment includes the following steps:
[0017] (1) Evaporation and crystallization of carnallite: send the filtrate of the fine crystal slurry and the original halogen from step (5) into the evaporator according to the mass ratio of filtrate:original halogen=1:0.5, and send the raw material into the evaporator for the initial production The brine obtained by directly dissolving the carnallite ore extracted from the mine with fresh water is preheated to 137°C for evaporation and concentration. When the boiling point of the liquid in the evaporation chamber rises to 25°C, the material is discharged, and the evaporated mother liquid is discharged to the carnallite for cooling and crystallization. The end temperature of the cooling crystallization is 40°C. The slurry in the cooling crystallizer is sent to the thickener A. The overflow part of the thickener A is the old brine. The bottom flow of the thickener A is filtered and separated, and the obtained filter cake i...
Embodiment 2
[0023] This embodiment includes the following steps:
[0024] (1) Evaporation and crystallization of carnallite: send the filtrate of the fine crystal slurry and the original halogen from step (5) into the evaporator according to the mass ratio of filtrate:original halogen=1:0.55, and send the raw material into the evaporator for the initial production The brine obtained by directly dissolving the carnallite ore extracted from the mine with fresh water is preheated to 140°C for evaporation and concentration, when the boiling point of the material liquid in the evaporation chamber rises to 26°C, the material is discharged, and the evaporated mother liquid is discharged to the carnallite for cooling and crystallization The end temperature of the cooling crystallization is 36°C. The slurry in the cooling crystallizer is sent to the thickener A. The overflow part of the thickener A is the old brine. The bottom flow of the thickener A is filtered and separated, and the obtained filt...
Embodiment 3
[0030] This embodiment includes the following steps:
[0031] (1) Evaporation and crystallization of carnallite: send the filtrate of the fine crystal slurry and the original halogen from step (5) into the evaporator according to the mass ratio of filtrate:original halogen=1:0.56, and send the raw material into the evaporator for the initial production The brine obtained by directly dissolving the carnallite ore extracted from the mine with fresh water is preheated to 142°C for evaporation and concentration, when the boiling point of the material liquid in the evaporation chamber rises to 25°C, the material is discharged, and the evaporated mother liquid is discharged to the carnallite for cooling and crystallization The end temperature of the cooling crystallization is 41°C. The slurry in the cooling crystallizer is sent to the thickener A. The overflow part of the thickener A is the old brine. The bottom flow of the thickener A is filtered and separated, and the obtained filt...
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