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

Active Publication Date: 2015-03-04
BEIJING GENERAL RES INST OF MINING & METALLURGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, various methods are either of high temperature and high energy consumption, complicated process routes, and high equipment requirements, so there is no value for industrial production, so the technology is difficult to promote
After the 1970s, there were few foreign research reports on the production of potassium salt from potassium feldspar
[0006] 1. Too high alkalinity
Excessively high alkalinity (>1.1) is unnecessary for the reduction reaction, but it will increase the melting point and viscosity of the charge, which is not conducive to the diffusion of the reduction reaction
[0007] 2. Furnace charges fluctuate greatly
During the operation of the blast furnace, the charge fluctuates greatly, causing scarring in the furnace, and the furnace condition is not smooth. It must be maintained at a relatively high furnace temperature, which reduces the economic benefits of production.
[0008] 3. Too frequent slagging
Avoid the disadvantages of high temperature sintering in current industrial applications, such as high energy consumption and large amount of slag

Method used

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  • Method applied to acid-base combined extraction of aluminum, potassium and sodium from water-insoluble potassium ore

Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention discloses a method applied to acid-base combined extraction of aluminum, potassium and sodium from water-insoluble potassium ore resource such as nepheline, potassium feldspar and the like. The method comprises the following steps: uniformly mixing finely-ground water-insoluble potassium ore with a proper amount of concentrated sulfuric acid, curing, and carrying out rapid high-temperature reduction roasting desulfurization at a certain temperature by a reducing agent, wherein the sulfur-containing flue gas is used for acid preparation to achieve regeneration and cyclic utilization of sulfuric acid; extracting potassium and sodium by water from the reduced calcine, and preparing aluminum oxide by alkaline leaching. By virtue of the method, the decomposition of aluminosilicate-containing material phase in the water-insoluble potassium ore resource such as nepheline, potassium feldspar and the like is enhanced by high-temperature reaction of concentrated sulfuric acid; the cyclic utilization of sulfuric acid is realized. The method can be used for comprehensively recycling aluminum, potassium and sodium resources; the recycling rate of aluminum oxide is high; the energy consumption is low; the corrosion to equipment is small; the large-scale industrialization is easy to implement.

Description

technical field [0001] The invention belongs to the comprehensive utilization of non-water-soluble potassium ore resources such as nepheline, potassium feldspar, potassium-rich shale and illite, and specifically relates to a method for extracting aluminum, potassium and sodium from water-insoluble potassium ore, especially The acid-base combined process is used for extraction. Background technique [0002] my country is a large agricultural country, and potash is very important to our country, but our country is poor in potash, accounting for only 1.63% of the world's total reserves. Although my country's water-soluble potash resources are poor, my country's non-water-soluble potash resources are rich and diverse , such as potassium feldspar, alunite, illite, potassium-rich shale, etc., and the reserves are huge. It is conservatively estimated that the total amount of resources exceeds 20 billion tons. If such water-insoluble potash resources can be utilized on a large scale...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B1/06C22B3/04C22B3/12C22B26/10C22B21/00
CPCY02P10/20
Inventor 蒋开喜蒋训雄范艳青汪胜东张登高冯林永刘巍
Owner BEIJING GENERAL RES INST OF MINING & METALLURGY
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