Method for preparing magnesium sulphate heptahydrate by laterite-nickel ore acid leaching nickel immersing waste water
A technology of magnesium sulfate heptahydrate and laterite nickel ore, applied in directions such as magnesium sulfate, can solve the problems such as no reports on the recovery of magnesium sulfate from nickel precipitation wastewater, large amount of lime, not meeting the requirements for direct discharge of industrial wastewater, etc., and achieves mild operating conditions. , Simple operation, the effect of increasing the concentration
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Embodiment 1
[0036] Embodiment 1: The method for preparing magnesium sulfate heptahydrate by acid leaching nickel wastewater of laterite nickel ore in this embodiment is as follows:
[0037] (1) Take 1000 mL of sulfurized nickel precipitation wastewater from the acid leaching solution of laterite nickel ore. After testing, its pH value is 2.3, its magnesium ion concentration is 20528.35mg / L, sodium ion concentration is 1731.20mg / L, and ferrous ion concentration is 1121.12 mg / L, the concentration of aluminum ion is 977.57 mg / L, and the concentration of other metal ions is less than 20 mg / L. Air was introduced under stirring conditions, and magnesite was added. When the pH value of the solution reached 5.6, the feeding was stopped and the reaction was continued for 2 hours. After testing, the end pH value was 6.0. After filtration and separation, 967 mL of magnesium-rich liquid was obtained. After analysis, the magnesium ion concentration was 25467.37 mg / L and the aluminum ion concentration was...
Embodiment 2
[0039] Embodiment 2: The method for preparing magnesium sulfate heptahydrate by acid leaching nickel wastewater of laterite nickel ore in this embodiment is as follows:
[0040] (1) Take 1000mL of sulfurized nickel precipitation wastewater from the acid leaching solution of laterite nickel ore. After testing, its pH value is 2.5, its magnesium ion concentration is 21437.20mg / L, sodium ion concentration is 1943.12mg / L, and ferrous ion concentration is 1023.32 mg / L, the concentration of aluminum ion is 737.42mg / L, and the concentration of other metal ions is less than 15mg / L. Air was introduced under stirring conditions, the air volume was 70 mL / min, and magnesite was added intermittently. When the pH value of the solution reached 6.12, the feeding was stopped and the reaction was continued for 2 hours. After testing, the end pH value was 6.5. After filtration and separation, 962 mL of magnesium-rich liquid was obtained. After analysis, the magnesium ion concentration was 23234.20 ...
Embodiment 3
[0042] Embodiment 3: The method for preparing magnesium sulfate heptahydrate by acid leaching nickel wastewater of laterite nickel ore in this embodiment is as follows:
[0043] (1) Take 1000mL of sulfurized nickel precipitation wastewater from the acid leaching solution of laterite nickel ore. After testing, its pH value is 2.32, its magnesium ion concentration is 20975.32mg / L, sodium ion concentration is 1877.42mg / L, and ferrous ion concentration is 1043.25 mg / L, the concentration of aluminum ion is 645.39mg / L, and the concentration of other metal ions is less than 20mg / L. Air was passed through under stirring conditions, the air volume was 60 mL / min, and magnesite was added intermittently. When the pH value of the solution reached 5.9, the feeding was stopped and the reaction was continued for 2 hours. After testing, the end pH was 6.27. After filtration and separation, 972 mL of magnesium-rich liquid was obtained. After analysis, the magnesium ion concentration was 24123.20 m...
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