Method for producing coarse-grain special mirabilite
A manufacturing method and coarse particle technology, applied in chemical instruments and methods, alkali metal sulfite/sulfite, alkali metal compounds, etc., can solve the problems of particle unevenness, agglomeration, inconvenient use, etc., and achieve particle flow good sex effect
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Embodiment 1
[0028] Use a pump to pump hot water at 40-70°C to dissolve the Glauber's salt (sodium sulfate) in the ore to form a Glauber's salt (sodium sulfate) solution (abbreviation: salt water) containing various impurities and a sodium sulfate concentration of 28.4%. After refining to remove impurities, five-effect vacuum evaporation and concentration, crystallization, the nitric acid slurry is kept at 80°C for 0.5 hours in the thermal insulation crystallization tank, and after centrifugation, wet nitric acid with a water content of 3% is obtained, and the wet nitric acid is transported to the drying The device is dried, and the product is sent to the LLC-I special fluidized bed for treatment, to separate tiny particles of mirabilite, raw nitric water and various data of the purity of mirabilite obtained from production. figure 2 manifested in.
Embodiment 2
[0030] Use a pump to pump hot water at 40-70°C to dissolve sodium sulfate in the ore to form nitric water containing various impurities and a concentration of sodium sulfate of 28.1%. After refining to remove impurities, five-effect vacuum evaporation concentrates and crystallizes. Nitrate slurry is kept at 120°C for 0.5 hours in an insulated crystallization tank. After centrifugation, wet nitric acid with a water content of 6% is obtained. The wet nitric acid is transported to a drying device for drying, and the product is sent to LLC-I special fluidization Bed treatment, separation of tiny particles of thenardite, raw nitrate water and production of various data on the purity of thenardite figure 2 manifested in.
Embodiment 3
[0032] Use a pump to pump hot water at 40-70°C to dissolve sodium sulfate in the ore to form nitric water containing various impurities and a sodium sulfate concentration of 25.6%. After refining to remove impurities, five-effect vacuum evaporation concentrates and crystallizes. The nitric acid slurry is kept at 80°C for 3.0 hours in an insulated crystallization tank. After centrifugation, wet nitric acid with a water content of 6% is obtained. The wet nitric acid is transported to a drying device for drying, and the product is sent to LLC-I special fluidization Bed treatment, separation of tiny particles of thenardite, raw nitrate water and production of various data on the purity of thenardite figure 2 manifested in.
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