Process for producing magnesium sulfate heptahydrate by mother liquor obtained after mirabilite freezing
A technology of magnesium sulfate heptahydrate and mother liquor, applied in the direction of heating water/sewage treatment, etc., can solve the problems of underutilization of magnesium, waste of resources, etc., and achieve the effect of large-scale industrial production, saving consumption, and continuous and stable operation
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Embodiment 1
[0027] This embodiment includes the following steps:
[0028] (1) One-stage preheating: 4-stage series connection of 40°C brine clearing solution, and 11.5 tons / hour of mother liquor after frozen nitration at -3°C (mother liquor contains: 3.7wt% sodium sulfate, 18.1wt% sulfuric acid Magnesium, 0.3 wt% sodium chloride), preheated to 28 ° C;
[0029] (2) Second-stage preheating: use steam to condense water in 3 stages in series, and preheat the mother liquor after freezing and nitrating at 28°C obtained in step (1) to 55°C;
[0030] (3) Three-stage preheating: use the evaporated secondary steam to divide into three stages, and preheat the frozen mother liquor obtained in step (2) at 55°C to 110°C;
[0031](4) Multi-effect forced circulation evaporation: send the frozen mother liquor obtained in step (3) at 110°C to the first-effect evaporation tank of the four-effect forced circulation evaporation device, and carry out four-effect vacuum evaporation according to the downstream ...
Embodiment 2
[0036] This embodiment includes the following steps:
[0037] (1) One-stage preheating: use 38°C clear solution of bittern in series in 3 stages, and 4.6 tons / hour of mother liquor after freezing nitrate at -2°C (mother liquor contains: 3.5wt% sodium sulfate, 19.0wt% sulfuric acid Magnesium, 0.2wt% sodium chloride) preheating is heated up to 27 ℃;
[0038] (2) Two-stage preheating: use steam to condense water in two stages in series, and preheat the mother liquor after freezing and nitrating at 27°C obtained in step (1) to 52°C;
[0039] (3) Three-stage preheating: use the evaporated secondary steam to divide into three stages, and preheat the 52°C frozen mother liquor obtained in step (2) to 106°C;
[0040] (4) Multi-effect forced circulation evaporation: send the mother liquor obtained in step (3) after freezing nitrate at 106°C to the first-effect evaporation tank of the four-effect forced circulation evaporation device, and carry out four-effect vacuum evaporation accordi...
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