Method for extracting potassium chloride from carbonate type salt lake
A technology of carbonate type and potassium chloride, applied in the direction of alkali metal chloride, etc., can solve the problems of long production time, large equipment investment, unfriendly environment, etc., and achieve short production time, low quality requirements and simple process Effect
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Embodiment 1
[0013] Embodiment 1 A kind of method of extracting potassium chloride from carbonate type salt lake, this method is at first with salt field potash mixed salt ore as raw material, ore composition is K + : 5.54%, Cl - : 49.73%, SO 4 2- : 3.17%, CO 3 2- : 0.89%, HCO 3 - : 0.66%, B 2 o 3 : 0.89%, Na + : 27.95%, H 2 O: 6.92%; then take 2kg of raw ore, add 1.42kg of water, stir fully (stirring time is 45.0min) to make it completely dissolved, then heat to 60°C, and carry out solid-liquid separation at this temperature to obtain 1227.0g tailings (K + Content is 3.50%) and 2027.5g mother liquor (K + content is 8.00%); finally the mother liquor is cooled to 2.0 ℃ and solid-liquid separation is carried out to obtain 1826.5g recycled mother liquor (K + Content is 5.09%) and 163.0g KCl product (K + The content is 44.67%). The KCl product has a purity of 85.9%.
Embodiment 2
[0014] Embodiment 2 A kind of method of extracting potassium chloride from carbonate type salt lake, this method at first takes salt field potassium mixed salt ore as raw material, and former ore is composed of K + : 13.07%, Cl - : 49.65%, SO 4 2- : 5.24%, CO 3 2- : 1.87%, HCO 3 - : 0.11%, B 2 o 3 : 0.86%, Na + : 28.14%, H 2 O: 1.78%; then take 2kg of raw ore, add 1.43kg of water, stir fully (stirring time is 35.0min) to make it completely dissolved, then heat to 70°C, and carry out solid-liquid separation at this temperature to obtain 711.5g of tailings (K + Content is 3.53%) and 1586.6g mother liquor (K + content is 8.59%); finally the mother liquor is cooled to 14.5 ℃ and solid-liquid separation is carried out to obtain 1240.0g recycled mother liquor (K + Content is 5.09%) and 140.0g KCl product (K + The content is 45.38%). The KCl product has a purity of 87.3%.
[0015] Add 890g ore amount, 338.0g water yield in the mother liquor of recycling, repeat aforeme...
Embodiment 3
[0016] Embodiment 3 A kind of method of extracting potassium chloride from carbonate type salt lake, this method is at first with salt field potash mixed salt ore as raw material, ore composition is K + : 6.37%, Cl - : 49.73%, SO 4 2- : 3.22%, CO 3 2- : 0.90%, HCO 3 - : 0.12%, B 2 o 3 : 0.87%, Na + : 28.11%, H 2 O: 7.10%; then take 2kg of raw ore, add 1.44kg of water, stir fully (stirring time is 35.0min) to completely dissolve it, heat to 82°C, and carry out solid-liquid separation at this temperature to obtain 786.5g of tailings (K + Content is 3.57%) and 1943.0g mother liquor (K + Content is 8.35%); Carry out solid-liquid separation after the mother liquor is cooled to 0.0 ℃ at last, can obtain the mother liquor of 1300.0g recycling and 187.5g KCl product (K + Content is 46.92%), and this KCl product purity is 90.2%.
[0017] Add 1688.0g ore quantity, 452.0g water yield in the mother liquor of recycle, repeat aforesaid process, obtain 1717.0g secondary circulat...
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