A method for producing potassium sulfate from magnesium sulfate-metachloride type potassium-containing brine
A technology of chloride and magnesium sulfate, applied in the field of salt chemical industry, can solve the problems of low flotation yield, unsatisfactory process conditions, and low grade of magnesite.
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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, and 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 r...
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, and 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 ...
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, and 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 b...
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