A method for electrowinning and regenerating copper-containing etching waste liquid in acidic chlorination system
A technology for etching waste liquid and copper etching, which is used in the improvement of process efficiency, photography process, instruments, etc., to avoid running costs, strong metal luster and brightness, and good flatness and compactness.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0028] A method for electrodeposition and regeneration of copper-containing etching waste liquid in an acidic chlorination system, comprising the following steps:
[0029] (1) Filter the copper-containing etching liquid waste liquid overflowing from the circuit board etching process, and pump the clarified copper-containing etching waste liquid without solid particles into the electrolyte circulation tank for subsequent use; the etching waste liquid copper The content is 80g / l, the concentration of hydrochloric acid is 1.5N;
[0030] (2) Pump the filtrate obtained in step (1) into the electrowinning tank for electrowinning and decoppering; the voltage of the electrowinning tank is 1.9V, and the current density is 500A / m 2 ; The temperature of the electrowinning waste liquid is 50°C;
[0031] (3) The cathode copper obtained in step (2) (when the weight of copper reaches 20kg) is dried with compressed air after scalding, and packed into the warehouse; the scalding condition is ...
Embodiment 2
[0037] A method for electrodeposition and regeneration of copper-containing etching waste liquid in an acidic chlorination system, comprising the following steps:
[0038] (1) Filter the copper-containing etching liquid waste liquid overflowing from the circuit board etching process, and pump the clarified copper-containing etching waste liquid without solid particles into the electrolyte circulation tank for subsequent use; the etching waste liquid copper The content is 130g / l, the concentration of hydrochloric acid is 2.2N;
[0039] (2) Pump the filtrate obtained in step (1) into the electrowinning tank for electrowinning and copper removal; the voltage of the electrowinning tank is 1.5V, and the current density is 100A / m 2 ; The temperature of the electrowinning waste liquid is 30°C;
[0040] (3) The cathode copper obtained in step (2) (when the weight of copper reaches 20kg) is dried with compressed air after scalding, and packed into the warehouse; the scalding condition...
Embodiment 3
[0046] A method for electrowinning and regenerating copper-containing etching waste liquid in an acidic chlorination system, comprising the following steps:
[0047](1) Filter the copper-containing etching liquid waste liquid overflowing from the circuit board etching process, and pump the clarified copper-containing etching waste liquid without solid particles into the electrolyte circulation tank for subsequent use; the etching waste liquid copper The content is 160g / l, the concentration of hydrochloric acid is 2.5N;
[0048] (2) Pump the filtrate obtained in step (1) into the electrowinning tank for electrowinning and decoppering; the voltage of the electrowinning tank is 2.0V, and the current density is 500A / m 2 ; The temperature of the electrowinning waste liquid is 20°C;
[0049] (3) The cathode copper obtained in step (2) (when the weight of copper reaches 20kg) is dried with compressed air after scalding, and packed into the warehouse; the scalding condition is that t...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
