Process using polyhalite extraction mother liquor to produce potassium sulfate
A technology of polyhalite and potassium sulfate, applied in the field of potassium sulfate production technology, can solve the problems of low yield of potassium products, increase of potassium sulfate production, large amount of entrainment of mother liquor, etc., achieve high output and added value, and be easy for industrial production , The effect of simple process
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Embodiment 1
[0030] (1) Adjust the pH value: pass ammonia gas with a volume concentration of 92% into 2000g (volume 1750mL) of polyhalite leaching mother liquor (K + : 2.2wt%, Mg 2+ : 0.8wt%, Ca 2+ : 0.03wt%), until the pH value is 10.85, 1800mL Mg(OH) 2 slurry;
[0031] (2) CO 2 Carbonization: CO with a volume concentration of 95% 2 With the pressure of 0.3MPa and the speed of 4.8L / L solution h, pass through the 1800mLMg(OH) obtained in step (1) 2 Carry out carbonization reaction at room temperature at 20°C in the slurry, and stop the reaction when the pH value is 7.6 to obtain the carbonization mother liquor;
[0032] (3) Pyrolysis separation: heat and decompose the carbonized mother liquor obtained in step (2) at 45°C for 40 minutes, and separate solid and liquid to obtain MgCO 3 ·3H 2 O solid salt and pyrolysis separation mother liquor;
[0033] (4) Causticization separation: In the pyrolysis separation mother liquor obtained in step (3), calcium oxide and NH in the pyrolysis s...
Embodiment 2
[0038] (1) Adjust the pH value: pass ammonia gas with a volume concentration of 95% into 1000g (volume 850mL) of polyhalite leaching mother liquor (K + : 4.48wt%, Mg 2+ : 1.63wt%, Ca 2+ : 0.08wt%), to pH 11.3, 910mL Mg(OH) 2 slurry;
[0039] (2) CO 2 Carbonization: CO with a volume concentration of 88% 2 With the pressure of 0.2MPa and the speed of 0.8L / L solution h, pass through the 910mL Mg(OH) obtained in step (1) 2 In the slurry, carry out carbonization reaction at room temperature at 30°C, and terminate the reaction when the pH value is 7.8, to obtain the carbonization mother liquor;
[0040] (3) Pyrolysis separation: heat and decompose the carbonized mother liquor obtained in step (2) at 70°C for 30 minutes, and separate solid and liquid to obtain MgCO 3 ·3H 2 O solid salt and pyrolysis separation mother liquor;
[0041] (4) Causticization separation: In the pyrolysis separation mother liquor obtained in step (3), calcium oxide and NH in the pyrolysis separation ...
Embodiment 3
[0046] (1) Adjust the pH value: pass ammonia gas with a volume concentration of 99% into 1000g (volume 900mL) of polyhalite leaching mother liquor (K + : 3.29wt%, Mg 2+ : 1.50wt%, Ca 2+ : 0.05wt%), to pH 11.5, 940mL Mg(OH) 2 slurry;
[0047] (2) CO 2 Carbonization: CO with a volume concentration of 85% 2 With the pressure of 0.5MPa and the speed of 3.6L / L solution h, pass through the 940mLMg(OH) obtained in step (1) 2 In the slurry, carry out carbonization reaction at room temperature at 25°C, and terminate the reaction when the pH value is 7.9, to obtain the carbonization mother liquor;
[0048] (3) Pyrolysis separation: heat and decompose the carbonized mother liquor obtained in step (2) at 60°C for 40 minutes, and separate solid and liquid to obtain MgCO 3 ·3H 2 O solid salt and pyrolysis separation mother liquor;
[0049] (4) Causticization separation: In the pyrolysis separation mother liquor obtained in step (3), calcium hydroxide and NH in the pyrolysis separati...
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