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
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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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