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Method for removing calcium and magnesium in zinc hydrometallurgy process

A hydrometallurgical zinc smelting and process technology, applied in the field of metallurgy, can solve the problems of decreased current efficiency, increased energy consumption, crystallization blockage, etc., and achieves the effects of reducing blockage, reducing crystallization, and improving water swelling

Active Publication Date: 2020-04-07
南丹县南方有色金属有限责任公司
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  • Abstract
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  • Application Information

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Problems solved by technology

[0003] The zinc hydrometallurgy process is: roasting → leaching → purification → electrolysis → melting and casting. After roasting and leaching, Ca and Mg mainly enter the leaching supernatant solution in the form of sulfate, which is difficult to remove in the traditional purification process. As a result, calcium and magnesium are continuously cyclically enriched in the wet system, which brings problems such as crystallization blockage, decrease in current efficiency, and increase in energy consumption to normal production, which is regarded as a major common problem in the industry

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  • Method for removing calcium and magnesium in zinc hydrometallurgy process

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Embodiment 1

[0033] A method for removing calcium and magnesium in a zinc hydrometallurgy process, comprising the following steps:

[0034] 1) Calcium removal: the new solution obtained from the purification process, the waste electrolyte obtained from the electrolysis process, and the 4 2H 2 O The underflow of the thickener of the seed crystal is added to the seed crystal mixing tank for mixing, the internal temperature of the seed crystal mixing tank is controlled to be 65-75°C, the material residence time is more than 10min, the flow rate of the new liquid is 6.7 times of the underflow flow of the thickener, and the stirring speed 34r / min; adjust the pH to 2-3 and then enter the cooling tower for cooling, control the inlet temperature of the cooling tower to 65-75°C, and the outlet temperature to 40-50°C; the cooled material enters the aging tank, and controls the internal temperature of the aging tank to 35~45℃, material residence time: more than 60min, stirring speed is 34r / min; then...

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Abstract

The invention belongs to the technical field of metallurgy, and particularly relates to a method for removing calcium and magnesium in a zinc hydrometallurgy process. The method comprises the following steps: 1) calcium removal: adding a fresh solution, a waste electrolyte and thickener underflow containing CaSO4.2H2O crystal seeds into a crystal seed mixing tank, carrying out cooling, then feeding the above materials into a ripening tank and a thickener, allowing one half of the thickener underflow to return to the seed crystal mixing tank and the other half of the thickener underflow to enter a reaction tank No. 1, slurrying CaCO3, adding the slurried CaCO3 into the reaction tank No. 1, adjusting a pH value to 2.5-3, adding the waste electrolyte into the reaction tank No. 1, conveying the materials in the reaction tank No. 1 to a reaction tank No. 2, carrying out a reaction, conveying a reaction product to a centrifuge, and performing centrifuging to obtain a centrifuge calcium-removed filtrate and centrifuge calcium-containing filter residues; and 2) magnesium removal: adding the centrifuge filtrate into a neutralizing tank, slurrying Ca(OH)2, adding the slurried Ca(OH)2 into the neutralizing tank, adjusting a pH value to 8-9, then conveying the treated filtrate to a filter press, and conveying the obtained magnesium-containing filtrate to a sewage station for treatment. With the method, calcium and magnesium ions in a zinc hydrometallurgy system can be effectively removed and maintained at a reasonable concentration level, the power consumption of zinc electrolysis is greatly reduced, and production cost is saved.

Description

【Technical field】 [0001] The invention relates to the technical field of metallurgy, in particular to a method for removing calcium and magnesium in a zinc hydrometallurgy process. 【Background technique】 [0002] Wet zinc smelting is to use dilute sulfuric acid (ie waste electrolyte) to leach zinc roasted ore to obtain zinc sulfate solution. After purification, zinc is electrolytically separated from the solution by electrolysis. [0003] The zinc hydrometallurgy process is: roasting → leaching → purification → electrolysis → melting and casting. After roasting and leaching, Ca and Mg mainly enter the leaching supernatant solution in the form of sulfate, which is difficult to remove in the traditional purification process. As a result, calcium and magnesium are continuously cyclically enriched in the wet system, causing problems such as crystallization blockage, decreased current efficiency, and increased energy consumption to normal production, which is regarded as a major ...

Claims

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Application Information

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IPC IPC(8): C22B7/00C22B19/20
CPCC22B7/006C22B19/20Y02P10/20
Inventor 周南方马宝军周裕高汤浅一郎杨明学韦勇王智侯荣昌吴少华
Owner 南丹县南方有色金属有限责任公司