Method applied to acid-base combined extraction of aluminum, potassium and sodium from water-insoluble potassium ore
A water-insoluble, acid-base combined technology, applied in the field of extraction of aluminum, potassium and sodium by acid-base combined process, can solve the problems of reduced production economic benefits, large slag volume, and high energy consumption for high-temperature sintering
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Embodiment 1
[0072] Mix 90% nepheline with a particle size of less than 200 mesh and concentrated sulfuric acid. The amount of 90% concentrated sulfuric acid added is 1.6 times the mass of the water-insoluble potassium ore. Obtain sulfuric acid slaking material. The sulfuric acid slaking material is mixed evenly according to the coal ratio of 8%, and the rapid reduction roasting is carried out at a temperature of 750 ° C for 5 minutes.
[0073] The reduced calcined sand is soaked in water at a temperature of 90°C for 60 minutes and a liquid-solid ratio of 2:1 so that potassium and sodium enter the water soaking solution and aluminum is enriched in the slag. Potassium sulfate and sodium sulfate products are prepared by fractional evaporation and crystallization of water immersion liquid. The crystallization mother liquor can be returned to add water to leach the new calcined sand.
[0074] Alkali dissolution is carried out on the water leaching residue, the dissolution temperature is 100°...
Embodiment 2
[0076] Mix 90% nepheline with a particle size of less than 200 mesh and concentrated sulfuric acid. The amount of 93% concentrated sulfuric acid added is 2.2 times the mass of the water-insoluble potassium ore. Obtain sulfuric acid slaking material. The sulfuric acid slaking material is uniformly mixed with coal powder at a coal ratio of 15%, and is subjected to rapid reduction roasting at a temperature of 800°C, and the roasting time is 10 minutes.
[0077] The reduced calcined sand is immersed in water at a temperature of 70°C for 30 minutes and a liquid-to-solid ratio of 3:1 so that potassium and sodium enter the water immersion solution and aluminum is enriched in the slag. Potassium sulfate and sodium sulfate products are prepared by fractional evaporation and crystallization of water immersion liquid. The crystallization mother liquor can be returned to add water to leach the new calcined sand.
[0078] Alkali dissolution is carried out on the water leaching residue, t...
Embodiment 3
[0080] Mix 80% nepheline with a particle size of less than 200 mesh and concentrated sulfuric acid. The amount of 95% concentrated sulfuric acid added is 1.8 times the mass of the water-insoluble potassium ore. Obtain sulfuric acid slaking material. The sulfuric acid slaking material is passed into the gas in the fluidized roasting furnace, and the rapid reduction roasting is carried out at a temperature of 750 ° C, and the roasting time is 1 min.
[0081] The reduced calcined sand is immersed in water at a temperature of 70°C for 30 minutes and a liquid-to-solid ratio of 3:1 so that potassium and sodium enter the water immersion solution and aluminum is enriched in the slag. Potassium sulfate and sodium sulfate products are prepared by fractional evaporation and crystallization of water immersion liquid. The crystallization mother liquor can be returned to add water to leach the new calcined sand.
[0082] Alkali dissolution is carried out on the water leaching residue, the...
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