Molten salt electrolytic refining method and method for recovering and treating cathode deposition thereof
A molten salt electrolysis and recovery treatment technology, applied in the electrolysis process, electrolysis components, etc., can solve the problems of low solution concentration, lack of economy, pressure, etc., to reduce environmental pressure, improve process economy, and reduce recovery energy consumption effect
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example 1
[0022] In the process of molten salt electrolytic refining of titanium, 4kg of cathode precipitates in a single furnace, of which the electrolyte content is 25%, of which, TiCl 3 , FeCl 2 , AlCl 3 The content of other impurities is about 1.5%. Prepare 20kg of dilute hydrochloric acid aqueous solution with a concentration of 0.02mol / L, wrap the cathode precipitate with filter cloth and place it in dilute hydrochloric acid solution for leaching. After 30 minutes, the electrolyte is completely dissolved, remove the remaining titanium powder in the filter cloth, and mix it into the obtained solution. hydrochloric acid to maintain the acid concentration at 0.02mol / L. Get the cathode precipitate and continue leaching in the above-mentioned manner. After accumulatively leaching 20kg of the cathode precipitate, put the cathode precipitate into the solution and no longer dissolve, and NaCl crystals are precipitated in the obtained solution. At this point, a NaCl-KCl mixed salt satur...
example 2
[0025] In the process of molten salt electrolytic refining of titanium, 1kg of cathode precipitates in a single furnace, of which the electrolyte content is 80%, of which, TiCl 3 , FeCl 2 , AlCl 3The content of other impurities is about 0.5%. Prepare 7kg of dilute hydrochloric acid aqueous solution with a concentration of 1mol / L, wrap the cathode precipitate with filter cloth and place it in dilute hydrochloric acid solution for leaching. After 20 minutes, the electrolyte is completely dissolved, remove the remaining titanium powder in the filter cloth, and add hydrochloric acid to the resulting solution. , to maintain the acid concentration at 0.5wt%. Take the cathode precipitate and continue leaching in the above-mentioned manner. After accumulatively leaching 2.2 kg of the cathode precipitate, put the cathode precipitate into the solution and no longer dissolve, and NaCl crystals are precipitated in the obtained solution. At this point, a NaCl-KCl mixed salt saturated so...
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