Method for preparing high-purity peroxysulphate based on electrolytic oxidation through ion-exchange membrane electrolyzer for chlor-alkali production
A chlor-alkali ion membrane, persulfate technology, applied in the electrolysis process, electrolysis components, organic diaphragms, etc., can solve the problems of low current efficiency, caustic soda consumption, single product, etc., to achieve low power consumption, strong electrochemical corrosion resistance , the effect of high current efficiency
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Embodiment 1
[0066] A method for preparing high-purity persulfate by electrolysis, by using an electrolysis in which a perfluorinated ion exchange membrane 3 is arranged between electrodes and is mainly composed of an anode chamber 4, an anode 1, a perfluorinated ion exchange membrane 3, a cathode 2, and a cathode chamber 5. Slot, follow the steps below:
[0067] (1) In such figure 1 Electrochemical ion exchange is carried out in the ion-exchange membrane electrolyzer shown, the cathode electrode is a nickel-based mesh electrode with active coating, the anode electrode is a titanium-based mesh electrode, and the fluorine ion exchange membrane 3 is a DF988 type perfluorinated chlor-alkali Carboxylic acid-perfluorosulfonic acid composite membrane ion membrane, effective area 50cm 2 ;
[0068] (2) The anolyte raw material is a 30% mass concentration ammonium sulfate aqueous solution, and the catholyte raw material is a 28% mass concentration ammonium hydroxide solution; pump the anode and cathode ...
Embodiment 2
[0074] (1) In such figure 1 Electrochemical ion exchange is carried out in the ion-exchange membrane electrolyzer shown. The cathode electrode is a stainless steel-based mesh electrode with active coating, the anode electrode is a titanium-based mesh electrode, and the perfluorinated ion exchange membrane 3 is a DF2801 chlor-alkali full Fluorocarboxylic acid-perfluorosulfonic acid composite membrane ion membrane, effective area 50dm 2 ;
[0075] (2) The anolyte is an aqueous solution of sodium sulfate and the catholyte is a sodium hydroxide solution; the anolyte and catholyte raw materials are preheated to 35°C, and then the anolyte and catholyte are pumped into the anode compartment of the electrolytic cell. And in the cathode chamber;
[0076] (3) At 45℃, apply direct current to the electrolytic cell for constant current electrolysis, the current density is 3.5kA / m 2 , The anolyte entering the tank sulfate mass concentration is controlled at 40%, the flow rate is 9.66L / h; the cat...
Embodiment 3
[0080] Same as Example 1, the difference is that the current density in step (3) is 3.5kA / m 2 .
[0081] After data processing, the current efficiency of this process is 98.47%, the power consumption is 2210kWh / t, and the purity of the product ammonium persulfate is >99.72%.
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