A kind of preparation method of food grade magnesium chloride
A magnesium chloride, food-grade technology, applied in the field of food chemistry, can solve the problems of high production cost and large process energy consumption.
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[0024] The embodiment of the present invention provides a kind of preparation method of food grade magnesium chloride, such as figure 1 Shown, described preparation method comprises steps:
[0025] S101. Evaporate the old brine from the salt lake in the salt pan to obtain the first brine with a specific gravity of 1.343-1.346.
[0026] In a preferred scheme, the old salt lake brine is the industrial tail liquid produced in the salt lake brine potassium extraction process, and the main chemical composition of the industrial tail liquid is: magnesium ions 105-110g / L, calcium ions 14-15g / L L. Chloride ion 350~360g / L, lithium ion 85~92mg / L, boron trioxide 650~700mg / L.
[0027] In a preferred solution, the old brine from the salt lake is evaporated in a salt pan to obtain the first brine with a specific gravity of 1.343-1.346.
[0028] It should be noted that after the specific gravity of the old brine in the salt lake evaporated to 1.345, magnesium chloride began to precipitate,...
Embodiment 1
[0039] (1) Obtain the industrial tail liquid produced in the salt lake brine potassium extraction process, that is, the old brine of the salt lake, and introduce the old brine into the salt pan for evaporation to form the first brine with a specific gravity of 1.343. The main chemical composition of the industrial tail liquid in this embodiment is: magnesium ion 105g / L, calcium ion 14g / L, chloride ion 350g / L, lithium ion 85mg / L, diboron trioxide 650mg / L.
[0040] (2) The first brine is introduced into the heat storage evaporation pool to continue to evaporate, and when the temperature of the brine in the heat storage evaporation pool reaches 45°C and there is bischofite solid phase deposition, the brine is drawn out to form the second brine. Wherein, the thermal storage evaporation pool in this embodiment is made of iron material, its outer wall is painted black, and a black geomembrane is laid inside the pool as a liner.
[0041] (3), the second brine is sent to the crystalli...
Embodiment 2
[0047] (1) Obtain the industrial tail liquid produced in the salt lake brine potassium extraction process, that is, the old brine of the salt lake, and introduce the old brine into the salt pan for evaporation to form the first brine with a specific gravity of 1.344. The main chemical composition of the industrial tail liquid in this embodiment is: magnesium ion 110g / L, calcium ion 15g / L, chloride ion 360g / L, lithium ion 92mg / L, diboron trioxide 700mg / L.
[0048](2) The first brine is introduced into the heat storage evaporation pool to continue to evaporate, and when the temperature of the brine in the heat storage evaporation pool reaches 55° C. and there is bischofite solid phase deposition, the bottom brine is drawn out to form the second brine. Wherein, the thermal storage evaporation pool in this embodiment is set as a deep-water salt pan with a depth of 4.5 meters, and a high-density polyethylene film is also laid in the pool of the deep-water salt pan as a liner.
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Abstract
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