The concentrated crystallization method of manganese sulfate monohydrate
A technology for concentrating crystallization and manganese sulfate, applied in manganese sulfate, crystallization separation, separation methods, etc., can solve the problems of wide product particle size distribution, harsh production environment, high cost, and achieve average product particle size, high product quality, and production cost. low effect
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Embodiment 1
[0034] Embodiment 1 adopts the method of the present invention to concentrate and crystallize to produce manganese sulfate monohydrate
[0035] a. Adding concentration to be concentrated in evaporator 1 and evaporator 2 respectively is a 30wt% manganese sulfate solution, and evaporator 1 is heated by steam at a temperature of 130° C. to crystallize the manganese sulfate solution;
[0036] b. Collect the steam escaping from evaporator 1 when heating evaporator 1, and use it to heat evaporator 2; wherein, the pressure maintained in evaporator 2 is -0.04~0.02MPa, and the manganese sulfate solution in evaporator 2 is Keep stirring at a speed of 25 rpm during heating; stop steam heating when the concentration of the manganese sulfate solution in evaporator 1 reaches 50%.
[0037] c. When the concentration of the manganese sulfate solution in the evaporator 2 reaches 50wt% synchronously in the evaporator 1 through the adjustment of the liquid replenishment amount, the temperature is...
Embodiment 2
[0038] Embodiment 2 Adopt the method of the present invention to concentrate and crystallize to produce manganese sulfate monohydrate
[0039] a. Add manganese sulfate solution with a concentration of 26wt% to evaporator 1 and evaporator 2 respectively. Evaporator 1 is heated with steam at a temperature of 120°C and stirred at a speed of 25 rpm to make the manganese sulfate solution Crystallization; the evaporator 1 and the evaporator 2 are a sealable evaporation crystallization tank with a stirrer inside;
[0040] b. Collect the steam that escapes from evaporator 1 when heating evaporator 1, and use it to heat evaporator 2; wherein, the pressure maintained in evaporator 2 is -0.04~0.02MPa, and the manganese sulfate solution in evaporator 2 is in Also stir at a speed of 27 rev / min during heating;
[0041] c. When the concentration of the manganese sulfate solution in the evaporator 2 reaches 45wt%, the temperature is raised to 100°C to crystallize the manganese sulfate soluti...
Embodiment 3
[0043] Embodiment 3 Adopt the method of the present invention to concentrate and crystallize to produce manganese sulfate monohydrate
[0044] a. Add manganese sulfate solution with a concentration of 25wt% to be concentrated in evaporator 1 and evaporator 2 respectively. Evaporator 1 is heated with steam at a temperature of 140°C and stirred at a speed of 35 rpm to make the manganese sulfate solution Crystallization; the evaporator 1 and the evaporator 2 are a sealable evaporation crystallization tank with a stirrer inside;
[0045] b. Collect the steam that escapes from evaporator 1 when heating evaporator 1, and use it to heat evaporator 2; wherein, the pressure maintained in evaporator 2 is -0.04~0.02MPa, and the manganese sulfate solution in evaporator 2 is in Stir at a speed of 35 rpm during heating; stop steam heating when the concentration of the manganese sulfate solution in the evaporator 1 reaches 50%.
[0046] c. When the concentration of the manganese sulfate sol...
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