Wet-method process for reclaiming zinc from zinc leaching residue

A technology of zinc leaching slag and wet process, which is applied in the field of zinc ore wet process, can solve the problems that the washing water cannot be directly returned to the process, the production cannot be carried out normally, and the water balance of the system is damaged, so as to achieve the benefit of extraction and organic Phase treatment, low loss, and the effect of reducing the amount of acid used

Inactive Publication Date: 2006-09-27
YUNNAN XIANGYUNFEILONG RESOURCES RECYCLING TECH CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

After the zinc leaching slag is filtered, the leach solution, which is generally more than 30% of the dry slag, is usually entrained in the filter residue, and the zinc concentration of this part of the solution is high, generally above 100g / L, so the slag entrains a considerable amount of zinc, which reduces the metal content. The recovery rate is high, causing metal loss and also polluting the environment
[0007] The zinc entrained in the slag is mainly water-soluble zinc. Although it can be washed out with water (or dilute acid), the washing water cannot be directly returned to the process, because the return process will destroy the water balance of the system and make the production impossible.
The zinc in the washing water is hydrolyzed and precipitated by neutralization, and the resulting precipitate is mainly zinc hydroxide, which also has a high water content. It will also bring water into the system as a raw material, so it cannot be directly returned to the process.
With the increase of oxidized ore processing capacity and the decrease of raw material metal grade, millions of tons of leaching slag will be discharged every year. If the zinc entrained in the slag is not recovered, tens of tons of metal loss will be caused. Not only waste of resources, but also cause serious pollution to the environment

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0020]

[0021] Since the cadmium content in the washing water is relatively high, and it will also be partially extracted into the organic phase during the extraction process, which will eventually affect the electrodeposition, therefore, cadmium removal must be carried out first. The removal of cadmium is replaced by zinc powder. When the amount of zinc powder is 1.5 to 4 times the theoretical replacement amount, the removal rate of cadmium replacement is above 98%.

[0022]

[0023] The back-extracted liquid is deoiled by 2g / L activated carbon adsorption and deoiled at a temperature of 10-80°C. After the concentration of organic matter in the water phase is reduced to below 1ppm, the water phase is used as a new liquid to prepare an electrolyte for zinc electrowinning. Under the current density of 500A / -, the electrolysis is carried out for 24 hours, the current efficiency is 91.3%, and the electrolytic zinc meets the requirements of No. 0 zinc containing...

example 2

[0025] The zinc oxide ore leaching slag containing 5% zinc is directly washed with dilute acid, and the Zn content in the washed solution is controlled to be about 10.8g / L, and the pH value is 2.0. with P 204 As an extractant, use 260# kerosene as a diluent, and the organic phase contains P 204 It is 30% extracted organic liquid, according to the extraction ratio of organic to aqueous phase is 1.2 / 1, three-stage countercurrent extraction is performed, mixed for 1 minute, the temperature is between 20 ° C and 30 ° C, and the mixed phase is clarified and separated for 2 minutes , to obtain a solution containing 15g / L of zinc in the loaded organic phase. There is no impurity removal and purification work before stripping, and the liquid after stripping is not directly used for electrowinning, but is incorporated into the liquid production section of zinc hydrometallurgy for neutral leaching, and a neutral leachate is produced, which is carried out together Purify and remove imp...

example 3

[0027] The zinc oxide ore leaching slag containing 6% zinc is directly washed with washing water, and the Zn content in the washed solution is controlled to be about 15.0 g / L, and the pH value is 3.5-5.2. with P 204As an extractant, use 260# kerosene as a diluent, and the organic phase contains P 204 It is 40% extracted organic liquid, according to the extraction ratio of organic to aqueous phase is 4 / 1, three-stage countercurrent extraction is carried out, mixed for 1 minute, the temperature is between 10°C and 40°C, and the mixed phase is clarified and separated for 2 minutes , to obtain a solution containing 15 g / L of zinc in the loaded organic phase. The loaded organic phase was washed in two stages (the washing solution contained 6g / L of zinc and 3g / L of sulfuric acid), and finally back-extracted, and the waste electrolyte was used for back-extraction, Zn=50g / L, and a certain amount of concentrated sulfuric acid was added to make the solution The concentration of sulfur...

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PUM

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Abstract

This invention relates to wet process of recovering zinc from leach slag containing zinc. It belongs to a wet process for zinc ore, in particular to a process for slag containing zinc produced from the systerm of wet zinc metallurgy. This method comprises the following steps: washing residue with water or diluted acid to get slag, selecting P204 as extractant and coal oil as thinner to extract them to water phase, configuring the solution containing zinc and sulfuric acid, eluting the impurity loaded in organic phase, back extracting the load organic phase with depleted electrolyte and sulfuric acid, transferring zinc in organic phase to water phase, deoiling all water phases which contact with organic phase, finally, taking the liquid which has been back extracted as fresh liquid, and adding it into zinc electrodeposition systerm. The invention has high metal recovery ratio, and can recovery zinc from leach slag containing zinc, save resource, avoid environmental contamination. And it perfectly joins with the process of wet processing of zinc oxide ore, decreases the consumption of acid in the leaching of zinc oxide, and reduces the cost.

Description

technical field [0001] The invention belongs to a zinc ore wet treatment process, in particular to a process for further recovering zinc from zinc-containing slag produced in a wet zinc smelting system. Background technique [0002] Zinc oxide ore is an important zinc-containing mineral resource. However, this kind of ore has a complex structure, a large amount of friable mud, low sorting index, many chemicals, and high cost. It is still a difficult problem in ore dressing. In the past, most rich ore was directly smelted. There are few enterprises dealing with zinc oxide ore in foreign countries, and the directly processed zinc oxide ore usually contains more than 35% zinc. Thailand's Badarien Zinc Smelter directly processes zinc oxide ore containing Zn>35%, and Iran processes zinc oxide ore containing about 40% Zn. [0003] Over the years, a lot of research has been done on the treatment of zinc oxide ore at home and abroad, including sulfuric acid method, sulfurous aci...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/04C22B3/26C22B3/20
CPCY02P10/20
Inventor 杨显万舒毓璋杨龙沈庆峰
Owner YUNNAN XIANGYUNFEILONG RESOURCES RECYCLING TECH CO LTD
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