Method for processing and producing potassium chloride by using magnesium sulfate subtype or sulfate chloride transitional-type potassium-containing salt lake brine
A kind of magnesium sulfate isoform and chloride technology, applied in the direction of alkali metal chloride, etc., can solve the problems of poor potassium chloride product quality, low potassium yield and the like, and achieve the effects of good product quality and high potassium salt yield
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Embodiment 1
[0015] Embodiment 1, with reference to figure 1 , a method for processing and producing potassium chloride with magnesium sulfate subtype or sulfate chloride transition type potassium-containing salt lake brine, the specific steps are as follows:
[0016] (1) Raw material magnesium sulfate subtype potassium-containing salt lake brine or sulfate chloride transition type potassium-containing salt lake brine contains Na + 、K + , Mg 2+ , Cl - , SO 4 2- ions, and where SO 4 2- with K + The weight ratio is 0.5:1; the modifying agent is introduced in the halite stage of the brine evaporation process, that is, the modifying agent is introduced when it precipitates 0% sodium chloride, so that the SO in the brine 4 2- Pre-precipitation of ions; the amount of modifier added to control the modified brine SO 4 2- :K + The weight ratio is 0.1:1, after the crystalline gypsum and halite are precipitated, the modified brine is separated, and the modified brine continues to be sun-d...
Embodiment 2
[0018] Embodiment 2, with reference to figure 1 , a method for processing and producing potassium chloride with magnesium sulfate subtype or sulfate chloride transition type potassium-containing salt lake brine, the specific steps are as follows:
[0019] (1) Raw material magnesium sulfate subtype potassium-containing salt lake brine or sulfate chloride transition type potassium-containing salt lake brine contains Na + 、K + , Mg 2+ , Cl - , SO 4 2- ions, and where SO 4 2- with K + The weight ratio is 3.5:1; the modifier is introduced in the halite stage of the brine evaporation process, that is, the modifier is introduced when it precipitates 85% of sodium chloride, so that the SO in the brine 4 2- Pre-precipitation of ions; the amount of modifier added to control the modified brine SO 4 2- :K + The weight ratio is 2.0:1, after the crystalline gypsum and halite are precipitated, the modified brine is separated, and the modified brine continues to be sun-dried and e...
Embodiment 3
[0021] Embodiment 3, with reference to figure 1 , a method for processing and producing potassium chloride with magnesium sulfate subtype or sulfate chloride transition type potassium-containing salt lake brine, the specific steps are as follows:
[0022] (1) Raw material magnesium sulfate subtype potassium-containing salt lake brine or sulfate chloride transition type potassium-containing salt lake brine contains Na + 、K + , Mg 2+ , Cl - , SO 4 2- ions, and where SO 4 2- with K + The weight ratio of the brine is 2.0:1; the modifier is introduced in the halite stage of the brine evaporation process, that is, the modifier is introduced when 50% of the sodium chloride is precipitated, so that the SO in the brine 4 2- Pre-precipitation of ions; the amount of modifier added to control the modified brine SO 4 2- :K + The weight ratio is 1.5:1, after the crystalline gypsum and halite are precipitated, the modified brine is separated, and the modified brine continues to b...
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