Method for recycling tungsten and ammonia in one step from ammonium paratungstate crystallization mother solution smelt through tungsten

A technology of ammonium paratungstate and crystallization mother liquor, applied in the field of tungsten hydrometallurgy, can solve the problems of high cost, incomplete tungsten precipitation, long process, etc., and achieve the effects of solving environmental protection problems, high precipitation recovery rate and mature technology

Inactive Publication Date: 2013-02-06
ZHONGXIANG TUNGSTEN IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] ① Precipitation method, calcium chloride artificial scheelite precipitation - acid decomposition of scheelite - crude tungstic acid - return to the main process; this process usually uses calcium chloride as a precipitant, and supplemented with sodium hydroxide to adjust the pH value, in practical applications It is generally reflected that the tungsten precipitation is not complete, and the tungsten content in the liquid is still in the range of 100-200mg/L. This is because a large amount of ammonia is released when adding alkali to adjust the pH value. The working environment is harsh and not environmentally friendly. At the same time, most companies consider Considering the cost and environmental...

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  • Method for recycling tungsten and ammonia in one step from ammonium paratungstate crystallization mother solution smelt through tungsten
  • Method for recycling tungsten and ammonia in one step from ammonium paratungstate crystallization mother solution smelt through tungsten

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Embodiment 1

[0021] After the evaporation and crystallization of APT is completed, the ammonium paratungstate solution pumped from the mother liquor to the blow-off reactor contains 20 g / L tungsten trioxide, 20 g / L ammonium ion, and the volume of the solution is 500 mL. 17.2 grams, the excess coefficient of its theoretical molar stoichiometric ratio is 1.11, blow off ammonia and sink tungsten in the stripping reactor, the ammonia gas that blows off is separated by condensing gas-liquid, and is made into ammonium chloride with hydrochloric acid spraying, The ammonium chloride is returned to the configuration analysis solution, and the scheelite slag is returned to the pressure cooking process; the content of tungsten trioxide in the solution after analysis and stripping is 1 mg / L, and the ammonium ion is 30 mg / L; the content of tungsten trioxide in the filter residue is 63.32%.

Embodiment 2

[0023] After the evaporation and crystallization of APT is completed, the ammonium paratungstate solution pumped from the mother liquor to the blow-off reactor contains 21.5 g / L tungsten trioxide, 22.5 g / L ammonium ion, the volume of the solution is 2000 mL, and 84 g of calcium oxide with a main component of more than 90% is added , the excess coefficient of its theoretical molar stoichiometric ratio is 1.2, and the stripping of ammonia and precipitation of tungsten is carried out in the stripping reactor. The ammonia gas blown out is separated by condensing gas and liquid, sprayed with hydrochloric acid to make ammonium chloride, ammonium chloride is returned to configure the analysis solution, and the scheelite slag is returned to the pressure cooking process; the content of tungsten trioxide in the solution after analysis is 5 mg / L, ammonium ion 25.8 mg / L; the filter residue contains 65.72% tungsten trioxide.

Embodiment 3

[0025] After the evaporation and crystallization of APT is completed, the ammonium paratungstate solution pumped from the mother liquor to the blow-off reactor contains 18g / L tungsten trioxide, 21 g / L ammonium ion, and the volume of the solution is 2000mL. By adding 85g of calcium oxide with a main component of more than 90% , the excess coefficient of its theoretical molar stoichiometric ratio is 1.3, and the stripping of ammonia and precipitation of tungsten is carried out in the stripping reactor. The blown out ammonia gas is separated by condensing gas and liquid, sprayed with hydrochloric acid to make ammonium chloride, ammonium chloride is returned to configure the analysis solution, and scheelite slag is returned to the pressure cooking process. The content of tungsten trioxide in the stripped liquid was analyzed to be 1 mg / L, and the ammonium ion was 29 mg / L. The filter residue contains 64.53% tungsten trioxide.

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Abstract

The invention discloses a method for recycling tungsten and ammonia in one step from an ammonium paratungstate crystallization mother solution smelt through tungsten. After the ammonium paratungstate (APT) is subjected to evaporative crystallization, a mother solution is pumped into a reaction kettle for stripping treatment, calcium oxide with content above 90% or calcium hydroxide with content above 95% are added into the mother solution, a stripping process which is commonly used in the crystallization mother solution in the APT preparation process is utilized to recycle the ammonia, the reaction temperature is in a range from 25 DEG C to 90 DEG C, when the ammonia is subjected to gas-liquid separation through condensation concentration, the ammonia is sprayed with a hydrochloric acid to prepare ammonium chloride to return to a main process to prepare an analytical solution, white tungsten slag returns to a pressure boiling process, when a potential of hydrogen (pH) value of a reaction system is maintained in a range from 9 to 11 and concentration of ammonia nitrogen in water is reduced to about 30mg/L, the reaction is finished, and a waste liquid free of the ammonia nitrogen is subjected to a mixing treatment with an ion exchange post-liquid which is generated in the main process working procedure. The method has the advantages that the process procedures are greatly simplified, the tungsten deposition rate is high, the process is simple, the operation is easy, and the treating cost is slightly low.

Description

technical field [0001] The invention belongs to tungsten hydrometallurgy, in particular to a method for recovering tungsten and ammonia in one step from ammonium paratungstate crystallization mother liquor produced by tungsten smelting. Background technique [0002] my country is a country with large tungsten resources. Tungsten resources mainly exist in the form of wolframite and scheelite. With the decreasing amount of wolframite resources, mining scheelite resources has become the main mineral variety of tungsten resources. The smelting technology of scheelite It has also been greatly improved, and the technology has been further matured. The ion exchange process has become the main process of tungsten smelting in my country. With the advancement of technology and the improvement of environmental protection awareness, most tungsten smelting enterprises have paid attention to the treatment of effluent wastewater and the improvement of the total recovery rate of tungsten, es...

Claims

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Application Information

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IPC IPC(8): C01C1/02C01G41/02
Inventor 王小军李义兵刘开忠邓波王战斌
Owner ZHONGXIANG TUNGSTEN IND
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