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Wet method smelting process of high silicon zinc oxide crude ore

A technology of hydrometallurgy and zinc oxide, which is applied in the direct leaching of high-iron zinc oxide raw ore and high-silicon field, which can solve the problems of high iron content in the solution and easy formation of silica gel, etc., so as to simplify production, reduce production cost, and broaden process technology field effect

Inactive Publication Date: 2009-04-29
云南金鼎锌业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The technical problem to be solved by the present invention is to provide a high-silicon zinc oxide raw ore hydrometallurgy process, which can utilize zinc oxide raw ore with low zinc grade and high iron and high silicon content. The process is simple and can effectively solve the existing problems. During the leaching process, the solution contains high iron content, and it is easy to form silica gel and other problems.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0016] Take zinc oxide raw ore containing 20% ​​zinc, 20% iron, and 40% silicon, pulp it by ball milling, pulp it according to the liquid-solid ratio of zinc oxide raw ore and acid leaching solution 4:1, add acid leaching solution for leaching for 3 hours, The leaching temperature is 70°C, and 2.5% potassium permanganate and manganese dioxide by weight of the ore are added at the same time to extract the iron in the ore, and the leached pulp is neutrally concentrated by adding polyacrylamide flocculant. The supernatant is sent for purification; the concentrated underflow is used for the second-stage acid leaching operation, and the operating temperature is 60°C. The second-stage acid leaching pulp is added to the acidic pulp for acidic concentration, and the acidic supernatant is returned to the slurry. Slurry and filter residue are returned to the zinc recovery workshop. After the second-stage acid leaching pulp is filtered, there are still 3% to 6% water-soluble zinc in the ...

example 2

[0018] Take zinc oxide raw ore containing 20% ​​zinc, 25% iron, and 45% silicon, and make pulp by ball milling. According to the liquid-solid ratio of 3:1, add acid-soluble substances for leaching for 2.5 hours at a leaching temperature of 65°C. Potassium permanganate and manganese dioxide with 3% weight of the ore will remove the iron in the ore, and the leached pulp will be concentrated by adding a neutral polyacrylamide flocculant. The concentration time is 30 minutes, and the neutral supernatant is sent to the purification operation. Concentrated bottom stream is used for second-stage acid leaching operation, operating temperature is 65°C, acidic polyacrylamide flocculant is added to the second-stage acid leaching slurry for acid concentration, the acidic supernatant is returned to the ball mill for pulping, the acidic underflow whole pulp is press-filtered, and the filtrate is sent to the ball mill for milling Slurry and filter residue are returned to the zinc recovery wor...

example 3

[0020] Take zinc oxide raw ore containing 20% ​​zinc, 30% iron, and 50% silicon, and make pulp by ball milling. According to the liquid-solid ratio of 5:1, acid-soluble substances are added for leaching for 2 hours, and the leaching temperature is 60°C. Potassium permanganate and manganese dioxide with a weight of 3.5% of the ore will remove the iron in the ore, and the leached pulp will be concentrated by adding a neutral polyacrylamide flocculant. The concentration time is 25 minutes, and the neutral supernatant is sent to the purification operation. The concentrated underflow is carried out in the second-stage acid leaching operation. The operating temperature is 70°C. The second-stage acid leaching slurry is acid-concentrated by adding acidic polyacrylamide flocculant, and the resulting acidic supernatant is returned to the ball mill for pulping. Slurry and filter residue are returned to the zinc recovery workshop.

[0021] Below is the production contrast of high silicon ...

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PUM

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Abstract

The invention relates to a wet method smelting process for high silicon zinc oxide crude ore. The invention belongs to the field of wet method smelting, and provides a method for the direct leaching of high silicon, high-ferro zinc oxide crude ore. The method comprises the following steps: firstly the high silicon, high ferro zinc oxide crude ore is crushed and undergoes the wet mode ball milling and the acid leaching through the discarded electrolyte used in a zinc hydrometallurgy process; according to the content of ferrous iron ions during the acid leaching, potassium permanganate and / or manganese dioxide are / is added in an extracting stage; the dosage of the potassium permanganate and / or manganese dioxide is controlled 1 to 10 percent of the total weight of the ore; during the leaching, the temperature is controlled 40 to 90 DEG C, and the acidity pH value is 0.5 to 5.2; and a flocculant is added into the leached ore pulp for flocculation and concentration. According to the invention, the direct leaching of the high silicon zinc oxide ore can avoid the formation of silica sol, thereby effectively utilizing the high silicon zinc oxide ore resources. Compared with other high silicon ore treatment processes, the process has the advantages of low acid consumption, low production cost, simple technology, and the like.

Description

technical field [0001] The invention belongs to the field of hydrometallurgy, and is a method for directly leaching high-silicon and high-iron zinc oxide raw ore. Background technique [0002] With the expansion of the scope of zinc use, the consumption of zinc products in various countries in the world is increasing year by year, and the supply of zinc sulfide ore is becoming increasingly insufficient. The mining and utilization of zinc oxide ore has gradually attracted people's attention. my country's zinc oxide ore reserves are very rich and widely distributed, among which Yunnan and Guizhou rank first. However, the grade of this kind of ore is low, and its silicon content is also high, so it is difficult to separate it by beneficiation method. If the raw ore is directly processed by fire method, a large amount of gangue needs to be added, and the cost is high. The contradiction cannot be fundamentally resolved, so that the recovery rate is low, so high-silicon zinc oxid...

Claims

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Application Information

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IPC IPC(8): C22B19/34C01G9/02C01G3/06
CPCY02P10/20
Inventor 李树龙杨丽周杨晓冬杨再兴黄大雄
Owner 云南金鼎锌业有限公司
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