Method for removing chlorine in process of zinc electrolysis by ammonia method
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An electrolytic zinc and process technology, which is applied to the field of chlorine removal in the ammonia electrolytic zinc process, can solve the problems of high chlorine removal cost of high-chlorine zinc-containing materials, blockage of electrolyte pipelines, large hardware investment, etc., and is conducive to popularization and application. , The operation process is stable, and the effect of each index reaching the standard
Inactive Publication Date: 2018-11-06
宁夏鼎辉科技有限公司
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[0002] Since the chlorine content of the acid electrolyte in the electrolytic zinc process needs to be less than 0.2g / L, the chlorine element becomes a harmful element in the traditional acid electrolytic zinc process, resulting in that high-chlorine zinc-containing materials cannot be preferentially selected and used; at the same time, high-chlorine The cost of chlorine removal for zinc-containing materials is also high, mainly due to: low efficiency of chlorine removal by heating and roasting in the furnace or rotary kiln; lengthy process of alkali washing method, large loss of zinc, high treatment cost, and difficulty in sewage treatment; hardware investment in ion exchange method Large size and high cost of consumables; therefore, the ammonia-based electrolytic zinc with obvious advantages has been widely concerned and scrambled to be developed by electrolytic zinc companies. The advantages of low environmental pressure and low price
[0003] Although ammonia-based electrolytic zinc has the above-mentioned advantages, there are very few manufacturers that have actually put into industrialized and mass-produced production, and the enterprises that have already put into production also have many problems such as temperature control, additive selection, chlorine crystallization pipe plugging, etc., and cannot realize continuous production.
Among them, chlorine crystal plugging is the main problem affecting production, mainly because during long-term use, the concentration of chloride ions will gradually increase and reach saturation, and after supersaturation, it will be crystallized in the form of ammonium chloride, resulting in Difficulty in leaching hydraulic filtration, blockage of electrolyte pipelines, reduction of electrolysis current efficiency, etc.; at the same time, many ammonia process literatures only mention that high-chlorine zinc-containing materials can be used, but the limit and exceeding the concentration of chloride ions in the electrolyte How to remove chlorine after the limit is not detailed, which seriously affects the continuous process of ammonia electrolytic zinc process
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[0017] Such as figure 1 Shown, the method for removing chlorine in a kind of ammonia method electrolytic zinc process comprises following operation:
[0018] (1) Leaching: Alkaline leaching of high-chloride zinc-containing materials with liquid ammonia, the reaction temperature is 45°C-50°C, and the pH at the end of the reaction is controlled to be 8.0-8.5;
[0019] (2) Solid-liquid separation: The leached product is subjected to solid-liquid separation to obtain leaching liquid and leaching slag, which can be recycled and reused;
[0020] (3) Purification: Transport the leaching solution to a purification tank, add hydrogen peroxide for oxidative deferrification, then add zinc powder for replacement and removal of impurities, and control the temperature at the end of the reaction to 40°C to 45°C to obtain a purified electrolytic solution and purification slag, the purification slag can be recycled and reused;
[0021] (4) Electrolysis: The electrolytic net liquid is transpo...
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Abstract
The invention belongs to the technical field of chemical treatment and relates to a method for removing chlorine in the process of zinc electrolysis by an ammonia method. The method includes: firstly,leaching is performed, wherein alkaline leaching is performed on a high-chlorine zinc-containing material with liquid ammonia; secondly, solid liquid separation is performed, wherein leachate is obtained; thirdly, purification is performed, wherein the leachate is subjected to oxidization iron removing and zinc powder replacement, and electrolytic clean liquid is obtained; fourthly, electrolysisis performed, wherein electrolytic residual liquid is obtained; and fifthly, chlorine removal is performed, wherein when the concentration of chlorine ions in the electrolytic residual liquid is between 180g / L and 280g / L, the electrolytic residual liquid is used for the leaching work procedure; and when the concentration exceeds 280g / L, part of the electrolytic residual liquid is used for the leaching work procedure, and the other part is subjected to standing cooling in a cooling pond, and clean liquid flows back to an electrolysis work procedure to be used. By using the method, the concentration of chlorine ions in electrolyte is effectively reduced, the current efficiency in the electrolysis process is improved, and it is guaranteed that production is continuously performed; and meanwhile, the precipitation speed of ammonium chloride is increased through the cooling pond, and the method is safe, capable of saving energy, easy to operate, small in investment, environment-friendly andfree of emission.
Description
technical field [0001] The invention belongs to the technical field of chemical treatment, and relates to a method for removing chlorine in an ammonia-based electrolytic zinc process. Background technique [0002] Since the chlorine content of the acid electrolyte in the electrolytic zinc process needs to be less than 0.2g / L, the chlorine element becomes a harmful element in the traditional acid electrolytic zinc process, resulting in that high-chlorine zinc-containing materials cannot be preferentially selected and used; at the same time, high-chlorine The cost of chlorine removal for zinc-containing materials is also high, mainly due to: low efficiency of chlorine removal by heating and roasting in the furnace or rotary kiln; lengthy process of alkali washing method, large loss of zinc, high treatment cost, and difficulty in sewage treatment; hardware investment in ion exchange method Large size and high cost of consumables; therefore, the ammonia-based electrolytic zinc w...
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