Method for producing potassium sulfate from magnesium sulfate-metachloride potassium-containing brine
A chloride, magnesium sulfate technology, applied in the field of salt chemical industry, can solve the problems of not reaching ideal process conditions, affecting the output and quality of potassium sulfate, and low grade of strontium
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Embodiment 1
[0032] In this embodiment, the magnesium sulfate-partial chloride type potassium-containing salt lake brine is selected from a certain salt lake brine in Qinghai in China, and the original brine composition is as follows: K + 0.415%, Mg 2+ 2.92%, Cl - 14.96%, SO 4 2- 2.80%, Na + 5.18%, H 2 O73.725%.
[0033] (1) Inject the magnesium sulfate-metachloride type potassium-containing brine into the sodium chloride salt field, let it dry naturally until the epsom salt begins to precipitate, then inject the brine into the epsom salt field, and part of the sodium chloride and epsom After salting, the brine is injected into the first-grade carnallite salt field, and the first-grade carnallite ore is precipitated, which is naturally sun-dried into the brine that meets the second-grade carnallite stage salt field, and then the first-grade carnallite salt field is discharged into the second-grade carnallite salt field Stone salt fields continue to evaporate, and when the brine reach...
Embodiment 2
[0047] In this embodiment, the magnesium sulfate-partial chloride type potassium-containing salt lake brine is selected from a certain domestic salt lake brine, and the original brine composition is as follows: K + 0.502%, Mg 2+ 4.32%, Cl - 17.42%, SO 4 2- 3.41%, Na + 4.29%, H 2 O70.058%.
[0048](1) Inject the magnesium sulfate-metachloride type potassium-containing brine into the sodium chloride salt field, let it dry naturally until the epsom salt begins to precipitate, then inject the brine into the epsom salt field, and part of the sodium chloride and epsom After salting, the brine is injected into the first-grade carnallite salt field, and the first-grade carnallite ore is precipitated, which is naturally sun-dried into the brine that meets the second-grade carnallite stage salt field, and then the first-grade carnallite salt field is discharged into the second-grade carnallite salt field Stone salt fields continue to evaporate, and when the brine reaches the brine...
Embodiment 3
[0059] In this embodiment, the magnesium sulfate-partial chloride type potassium-containing salt lake brine is selected from a certain domestic salt lake brine, and the original brine composition is as follows: K + 0.530%, Mg 2+ 2.62%, Cl - 16.29%, SO 4 2- 2.02%, Na + 6.18%, H 2 O72.36%.
[0060] (1) Inject the magnesium sulfate-metachloride type potassium-containing brine into the sodium chloride salt field, let it dry naturally until the epsom salt begins to precipitate, then inject the brine into the epsom salt field, and part of the sodium chloride and epsom After salting, the brine is injected into the first-grade carnallite salt field, and the first-grade carnallite ore is precipitated, which is naturally sun-dried into the brine that meets the second-grade carnallite stage salt field, and then the first-grade carnallite salt field is discharged into the second-grade carnallite salt field Stone salt fields continue to evaporate, and when the brine reaches the brine...
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