A High Current Density Circulating Flow Anode Diaphragm Electrolyzer
A technology of high current density and diaphragm electrolysis, applied in electrolysis process, electrolysis components, etc., can solve the problems that catholyte cannot achieve high-speed flow, the quality of cathode products decreases, and the efficiency of cathode current decreases, so as to increase migration speed and reduce production Operating cost, effect of eliminating cathode concentration polarization
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Embodiment approach 1
[0014] Adjust the pH of the nickel sulfate solution to 3.0-3.5, heat to 70-75°C, add boric acid to 5-6g / L, the nickel sulfate solution flows from the high level tank to the electrolytic tank, and after the nickel sulfate solution is full of the electrolytic tank, Turn on the catholyte self-circulation pump to make the catholyte self-circulate in the tank and form a circulating flow on the surface of each cathode. When the catholyte self-circulation flow reaches 1500m 3 / Mt, to increase the cathode current density to 380A / m 2 , after 4 days of electrolysis, take out the cathode product, the cathode current efficiency reaches 96%, and the output ratio of single-cell cathode product is 230A / m 2 time increased by 66%.
Embodiment approach 2
[0016] Adjust the pH of the nickel sulfate solution to 3.0-3.5, heat to 70-75°C, add boric acid to 5-6g / L, the nickel sulfate solution flows from the high level tank to the electrolytic tank, and after the nickel sulfate solution is full of the electrolytic tank, Turn on the catholyte self-circulation pump to make the catholyte self-circulate in the tank and form a circulating flow on the surface of each cathode. When the catholyte self-circulation flow reaches 2000m 3 / Mt, increase the cathode current density to 420A / m 2 , after 4 days of electrolysis, the cathode product was taken out, the cathode current efficiency reached 95.8%, and the output ratio of the single-cell cathode product was 230A / m 2 time increased by 81.8%.
Embodiment approach 3
[0018] Adjust the pH of the nickel sulfate solution to 3.0-3.5, heat to 70-75°C, add boric acid to 5-6g / L, the nickel sulfate solution flows from the high level tank to the electrolytic tank, and after the nickel sulfate solution is full of the electrolytic tank, Turn on the catholyte self-circulation pump to make the catholyte self-circulate in the tank and form a circulating flow on the surface of each cathode. When the catholyte self-circulation flow reaches 2300m 3 / Mt, increase the cathode current density to 450A / m 2 , after 4 days of electrolysis, the cathode product was taken out, the cathode current efficiency reached 95.6%, and the output ratio of the single-cell cathode product was 230A / m 2 time increased by 95%.
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