A method for in-situ electrolytic regeneration of acidic copper chloride etching solution and copper recovery
A technology of electrolytic regeneration and recovery method, applied in electrolysis components, electrolysis process, electrodes and other directions, can solve the problems of chlorine and hydrogen evolution operation, complicated technical process and operation, and need for centrifugal deliquoring, etc., so as to avoid chlorine evolution and increase reaction Area, simple operation effect
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Embodiment 1
[0052] The composition of the initial cathodic solution is: CuCl 2 0.34mol / L, CuCl 0.16mol / L, NaCl 2mol / L, HCl 2mol / L. When the electrolytic regeneration and copper recovery system is in operation, the etching liquid stream 4 with a flow rate of 16.9 (Q) L / h and the catholyte branch stream 11 with a flow rate of 0.53 L / h (0.03 Q) are combined and used as the anode liquid stream 5 into the anode chamber 1 for regeneration. The anode outlet liquid stream 6 is divided into a regenerated etching liquid stream 7 and a regenerated etching liquid branch stream 8 with a flow rate of 0.53L / h (0.03Q). The regenerated etching liquid branch stream 8 and the cathodic discharge stream 9 merge to form the cathode outdoor circulation stream 12, and the cathode outdoor circulation stream is divided into the catholyte branch stream 11 and the flow rate of 0.53L / h (0.03Q). The cathode inflow stream 10 of 3.96 L / h (0.23Q), the cathode inflow stream 10 enters the cathode chamber for copper depo...
Embodiment 2
[0055] The composition of the initial cathodic solution is: CuCl 2 0.50mol / L, CuCl 0.14mol / L, NaCl 2mol / L, HCl 2mol / L. When the electrolytic regeneration and copper recovery system is in operation, the etching liquid stream 4 with a flow rate of 17.0 (Q) L / h and the catholyte branch stream 11 with a flow rate of 0.60 L / h (0.035 Q) are merged and then used as the anode inflow stream 5 into the anode chamber 1 for regeneration. The anode outlet liquid stream 6 is divided into a regenerated etching liquid stream 7 and a regenerated etching liquid branch stream 8 with a flow rate of 0.60 L / h (0.035 Q). The regenerated etching liquid branch stream 8 and the cathodic discharge stream 9 merge to form the cathode outdoor circulation stream 12, and the cathode outdoor circulation stream is divided into the catholyte branch stream 11 and the flow rate of 0.60L / h (0.035Q). 6.48L / h (0.38Q) of the cathode inflow stream 10, the cathode inflow stream 10 enters the cathode chamber for copp...
Embodiment 3
[0058] The composition of the initial cathodic solution is: CuCl 2 0.40mol / L, CuCl 0.15mol / L, NaCl 2mol / L, HCl 2mol / L. When the electrolytic regeneration and copper recovery system is in operation, the etching liquid stream 4 with a flow rate of 20.1 (Q) L / h and the catholyte branch stream 11 with a flow rate of 0.67 L / h (0.033 Q) are combined and used as the anode liquid stream 5 into the anode chamber 1 for regeneration. The anode outlet liquid stream 6 is divided into a regenerated etching liquid stream 7 and a regenerated etching liquid branch stream 8 with a flow rate of 0.67L / h (0.033Q). The regenerated etching liquid branch stream 8 and the cathodic discharge stream 9 merge to form the cathode outdoor circulation stream 12, and the cathode outdoor circulation stream is divided into the catholyte branch stream 11 and the flow rate of 0.67L / h (0.033Q). The cathode inflow stream 10 of 9.36L / h (0.47Q), the cathode inflow stream 10 enters the cathode chamber for copper de...
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