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Fluorine and chlorine removal process for zinc metallurgy industrialization ion exchange process with wet-process

An ion exchange method and a hydrometallurgical zinc smelting technology, which is applied in the field of purification of zinc sulfate liquid in hydrometallurgy zinc smelting, can solve the problems of high production cost, difficult process conditions, poor production management, etc. Loss, effect of large switching capacity

Inactive Publication Date: 2009-07-29
宋志红
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Problems solved by technology

[0009] 2. Copper slag removal of fluorine and chlorine: Its principle is based on the interaction between copper and copper ions and chloride ions in the electrolyte to form insoluble cuprous chloride precipitation, but the efficiency of this method is not high. The process conditions are difficult to master, the production cost is high, and it is rarely used in actual production
[0010] 3. Silver slag removal of fluorine and chlorine: Its principle is based on the interaction between silver ions and chloride ions in the electrolyte to form insoluble silver chloride precipitation, but the efficiency of this method is not high, and the process conditions are difficult to master , the production cost is high, the production is not easy to manage, and less used in actual production

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  • Fluorine and chlorine removal process for zinc metallurgy industrialization ion exchange process with wet-process

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Embodiment Construction

[0021] After the zinc sulfate leaching solution containing fluoride and chloride ions is purified by conventional three-stage zinc powder, it is placed in an ion exchange column equipped with anion resin D201 under acidic conditions with a pH value of 2.5 to 5.5, and the gate valve at the bottom of the exchange column is opened to adjust After 5 to 15 hours at a certain flow rate, take samples to analyze the remaining fluorine and chlorine content in the solution, control the remaining fluorine and chlorine content in the solution to 100 to 700 mg / liter and send the solution to the electrolytic workshop for electrolytic zinc deposition. The resin adsorbed with fluoride and chloride ions is put into a certain concentration of 5-10% sulfuric acid solution as the desorption solution according to a certain flow rate, so that the resin is regenerated from the fluorine and chlorine type to the sulfate radical type, so that the resin reaches the The effect of recycling.

[0022] The ...

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Abstract

Fluorine-chlorine removing technique by ion exchange technique in zinc metallurgy industrialization by the wet method belongs to a method for removing fluorine-chlorine in zinc sulphate solution in zinc metallurgy by the wet method. Under acidic condition that pH value is 2.5-5.5, the zinc sulfate flows through ion exchange resin which absorbs fluorine and chlorine ions to remove the fluorine and chlorine from the solution. The invention has short technological flow, and is easy to operate with high chlorine removing ratio, low zinc loss ratio and low operation cost.

Description

technical field [0001] The invention relates to a purification technology of zinc sulfate solution in zinc hydrometallurgy, in particular to a technology for removing fluorine and chlorine by an industrialized ion exchange method in zinc hydrometallurgy. Background technique [0002] Recently, more than 75% of zinc in my country is produced by hydrometallurgy. In the process of hydrometallurgy, the purification of zinc sulfate leaching solution is very important. Copper, cadmium, cobalt, nickel, Harmful impurities such as fluorine and chlorine must be purified to below the allowable content, so that the electrolytic zinc process can proceed smoothly, and the electrolytic zinc sheet can be qualified. [0003] If the chlorine content in the zinc sulfate leaching solution exceeds 250 mg / L and the fluorine content exceeds 150 mg / L, it will cause the "burning plate" phenomenon of anode plate dissolution during the electrolysis process, the current efficiency will decrease, and the...

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Application Information

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IPC IPC(8): C22B3/42C22B19/20
CPCY02P10/20
Inventor 宋志红
Owner 宋志红