Oxidation energy-saving method for recycling aluminium ions and sulphuric acid of oxidation tank and improving current density
A technology of current density and oxidation tank, which is applied in the field of aluminum product processing to achieve the effect of reducing the amount of dissolution, shortening the oxidation time, and reducing the energy consumption of oxidation
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Embodiment 1
[0141] Embodiment 1 (continuous production of aluminum alloy anodic oxidation)
[0142] Close No. 3 valve 03, No. 9 valve 09, open No. 1 valve 01, No. 2 valve 02, No. 4 valve 04, frequency conversion pump 4 and refrigerator, cool down the oxidation tank, and start production of the oxidation line;
Embodiment 2
[0143] Embodiment 2 (on-line recovery aluminum ammonium sulfate)
[0144] 1. Open No. 3 valve 03, close No. 2 valve 02, No. 9 valve 09, and turn 30M 3 After the oxidizing solution is pumped into the reaction tank, open the No. 2 valve 02 and close the No. 3 valve 03; open the gas stirring No. 8 valve 08 and start stirring; add ammonium sulfate according to 2.5 times the weight of the aluminum ion concentration, and stir while adding; After the ammonium has been added, continue stirring for 30 minutes and then close No. 8 valve 08 and leave it for 2 hours;
[0145] 2. Open No. 5 valve 05, and the crystalline solid enters the centrifuge. Turn on the centrifuge for solid-liquid separation; open No. 10 valve 010 to repeatedly spray the solids in the centrifuge. When the pH value of the recovered liquid at the outlet of the centrifuge is greater than 4.5, close No. 10 valve 010 to stop spraying and centrifugation machine, recycling ammonium aluminum sulfate by-product;
Embodiment 3
[0146] Embodiment 3 (on-line recovery oxidation solution)
[0147] Open No. 6 valve 06, No. 7 valve 07 and No. 2 pump 8, and send the recovered and regenerated oxidation solution back to the oxidation tank to complete the recovery of sulfuric acid;
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