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Method for recycling copper from basic waste etching liquid

A technology for recovering copper from waste etching solution, applied in the field of copper recovery, can solve the problems of low copper extraction rate, high copper content in mother liquor, low copper powder efficiency, etc., and achieves good separation effect, low oxygen content, and copper extraction rate. high effect

Active Publication Date: 2013-11-20
广东柏宇新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The grade of sponge copper obtained by the replacement method is not high, and the copper content in the tail liquid after copper recovery is high. Although the copper powder produced by the electrolysis method has high purity and is better than the copper powder produced by other methods, the efficiency of the copper powder produced by the electrolysis method is higher than that of copper powder produced by other methods. Relatively low, high power consumption, and the concentration of heavy metal ions in the waste liquid cannot be reduced very low, strict treatment must be carried out before discharge, and the electrolysis method is easy to produce chlorine gas; neutralization precipitation method to treat copper-containing waste liquid, the process Simple, low investment, but the copper content of the mother liquor after copper sulfate crystallization is high, which needs further treatment, and the inorganic and organic substances such as ammonium salt in the wastewater cannot be recycled, causing serious environmental pollution
Although the extraction method currently used in the industry can extract copper, the copper extraction rate is low, only about 50%; the copper content in the wastewater is still about 60g / L, and the etching speed is slow when returning to etching.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] A certain alkaline waste etching solution, wherein pH is 7.7, copper ion 6g / L and a large amount of chloride ion; 10%Lix84-I: 5%N235 extractant and: the organic phase of 85% kerosene and alkaline waste etching solution by volume The ratio is 2:1 three-stage extraction. After extraction, the concentration of copper in the waste water is 0.10mg / L, and the extraction rate of copper is calculated to be 99%. : 1 three-stage washing, after washing, compare the loaded organic phase with the copper sulfate solution containing 140g / L of sulfuric acid and 8g / L of copper ions in a volume ratio of 8:1 for secondary stripping, after stripping, the organic phase returns Repeated use, the water phase is copper sulfate solution, the current density is 105A / m 2 Electrolytic copper was obtained by electrodeposition on stainless steel 316 cathode, the purity of electrolytic copper was 99.95%, and the copper sulfate solution containing 140g / L sulfuric acid and 8g / L copper ions after electr...

Embodiment 2

[0015] A certain alkaline waste etching solution, wherein the pH is 8.7, copper ions 140g / L and a large amount of chloride ions; 5% Lix973: 15% N235 extractant and: 80% 200 # The organic phase of the solvent oil and the alkaline waste etching solution are first-stage extracted at a volume ratio of 25:1. After the extraction, the analysis shows that the copper concentration in the waste water is 3.50mg / L, and the copper extraction rate is calculated to reach 99%. Then the loaded organic Phase and [H + ]=1.5mol / L dilute sulfuric acid solution by volume ratio is 5:1 secondary washing, after washing, the load organic phase and copper sulfate solution containing sulfuric acid 235g / L, copper ion 20g / L are by volume ratio 6:1 Compared with secondary stripping, after stripping, the organic phase is returned for reuse, and the aqueous phase is copper sulfate solution, at a current density of 200A / m 2 Under the conditions, stainless steel 304 cathodic electrodeposition obtains electrol...

Embodiment 3

[0018] A certain alkaline waste etching solution, wherein pH is 9, copper ion 160g / L and a large amount of chloride ion; 5%Lix984 extractant: 5%N235 extractant and: the organic phase of 90% kerosene and alkaline waste etchant by volume Ratio is 25: 1 first stage extraction, after extraction analysis records the copper concentration in the waste water is 5.50mg / L, and copper extraction rate reaches 99% through calculation; Then load organic phase and [H + ]=0.3mol / L dilute sulfuric acid solution by volume ratio is 0.2:1 first stage washing, after washing, the load organic phase and copper sulfate solution containing sulfuric acid 200g / L, copper ion 30g / L by volume ratio are 4:1 Compared with secondary stripping, after stripping, the organic phase is returned for reuse, and the aqueous phase is a copper sulfate solution, at a current density of 300A / m 2 Under the following conditions, electrolytic copper is obtained by cathodic electrodeposition of metal titanium plates, and the...

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PUM

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Abstract

The invention provides a method for recycling copper from a basic waste etching liquid. The method is characterized by comprising the following steps of: (1) extracting copper by adopting an organic phase of Lix<R> series extractant:N235 extractant: kerosene or 200#solvent oil and a basic waste etching liquid; (2) washing the loaded organic phase obtained in the step (1) by using a diluted sulfuric acid solution; (3) performing back-extracting on the loaded organic phase washed in the step (2) and a copper sulfate solution, and returning the back-extracted organic phase to the step (1) for recycling, wherein the water phase is a copper sulfate solution; and (4) electrically depositing the copper sulfate solution in the step (3) by adopting a metal cathode to obtain acid copper, and returning the copper sulfate solution after the step of electrically deposited the copper to the step (3) for recycling. The method for recycling copper from an acid waste etching liquid can be used for selectively separating copper from a basic waste etching liquid, and is simple in process and good in separation effect.

Description

technical field [0001] The invention relates to a method for recovering copper from alkaline waste etching solution. Background technique [0002] The production process of printed circuit board (PCB) is long, and the etching process is the largest part of the PCB production process. In the etching process, when the etching index, including speed, side erosion coefficient, surface cleanliness, etc., is lower than the process requirements due to too many substances dissolved in the etching solution, it becomes a waste etching solution. Etching liquids include acidic etching liquids, alkaline etching liquids and micro etching liquids. Alkaline etching generally speaking, every 1m produced 2 The circuit board needs to consume 2~2.5L of etching solution, and correspondingly produce 2~2.5L of waste etching solution. The concentration of copper ions is very high, reaching 160g / L or higher. The main components of these waste etching solutions are: heavy metal copper , ammonium s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C25C1/12
CPCY02P10/20
Inventor 陈飙
Owner 广东柏宇新材料科技有限公司
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