Eureka AIR delivers breakthrough ideas for toughest innovation challenges, trusted by R&D personnel around the world.

Method for recovering copper from acid waste etching solution

A waste etching solution and copper recovery technology, which is applied in the field of copper recovery, can solve the problems of environmental pollution, high copper content in mother liquor, and easy generation of chlorine gas, etc., and achieve good separation effect, low oxygen content, and simple process

Inactive Publication Date: 2013-08-07
陈飙
View PDF4 Cites 10 Cited by
  • 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

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] An acidic waste etching solution, in which H + Concentration is 0.012mol / L, copper ion 120g / L and a large amount of chloride ion; The organic phase of 15%Lix84-I-85% kerosene and acid waste etchant are 10: 1 three-stage extraction by volume ratio, after extraction analysis measures The concentration of copper in the waste water is 0.50mg / L, and the copper extraction rate reaches 99% through calculation; then the loaded organic phase and pure water are washed in three stages of 10:1 by volume. After washing, the loaded organic phase is mixed with 130g of sulfuric acid. / L, copper sulfate solution with copper ion 5g / L is 10:1 by volume ratio compared with the secondary stripping, after stripping, the organic phase is returned for reuse, the water phase is copper sulfate solution, and the current density is 55A / m 2 Electrolytic copper was obtained by electrodeposition on stainless steel 316 cathode. The purity of electrolytic copper was 99.95%. After electrodeposited coppe...

Embodiment 2

[0015] An acidic waste etching solution, in which H + The concentration is 1.0mol / L, the copper ion is 140g / L and a large amount of chloride ion; 20% Lix973-80%200 # The organic phase of the solvent oil and the acidic waste etching solution are extracted in a volume ratio of 30:1. After the extraction, the copper concentration in the waste water is measured to be 3.50mg / L, and the copper extraction rate is calculated to reach 99%. Then the loaded organic phase Secondary washing with purified water at a volume ratio of 5:1. After washing, compare the loaded organic phase with a copper sulfate solution containing 245 g / L of sulfuric acid and 10 g / L of copper ions at a volume ratio of 5:1 for 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 200A / m 2 Under the following conditions, stainless steel 304 cathode electrodeposited to obtain electrolytic copper, the purity of elec...

Embodiment 3

[0017] An acidic waste etching solution, in which H + The concentration is 2.9mol / L, the copper ion is 100g / L and a large amount of chloride ion; the organic phase of 5% Lix984 extractant-95% kerosene and the acidic waste etching solution are extracted in a volume ratio of 20:1, and the analysis and measurement after extraction The concentration of copper in the waste water is 5.50mg / L, and the extraction rate of copper is calculated to be 99%; then the loaded organic phase and pure water are washed in the first stage at a volume ratio of 0.2:1. After washing, the loaded organic phase is mixed with 200g of sulfuric acid. / L, copper sulfate solution with copper ion 30g / L is 5:1 by volume ratio compared with secondary stripping. After stripping, the organic phase is returned for reuse, and the water phase is copper sulfate solution. 2 Under the following conditions, electrolytic copper is obtained by cathodic electrodeposition of metal titanium plates, and the purity of electrol...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
concentrationaaaaaaaaaa
Login to View More

Abstract

The invention relates to a method for recovering copper from an acid waste etching solution. The method is characterized by comprising the following steps of: (1) preparing an organic phase by adopting an Lix series extraction agent with the volume ratio of 5-20% and 80-90% of kerosene or No. 200 solvent oil; (2) performing copper extraction by using the organic phase and the acid waste etching solution according to the volume ratio of (1-30): 1; (3) washing the loaded organic phase obtained in the step (2) and pure water according to the volume ratio of (0.1-10): 1; (4) performing back extraction by using the loaded organic phase after washing in the step (3) and a copper sulfate solution according to the volume ratio of (1-10): 1, and returning the organic phase after back extraction to the step (2) for reuse, wherein a water phase is the copper sulfate solution; and (5) performing copper electrodeposition on the copper sulfate solution obtained in the step (4), and returning the copper sulfate solution after copper electrodeposition to the step (4) for reuse. According to the method for recovering the copper from the acid waste etching solution, disclosed by the invention, the copper can be selectively separated from the acid waste etching solution, the process is simple and the separation effect is good.

Description

technical field [0001] The invention relates to a method for recovering copper from acidic 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 etchant has too many dissolved substances and the etching index, including speed, side erosion coefficient, surface cleanliness, etc., is lower than the process requirements, it becomes a waste etchant. Etching liquids include acidic etching liquids, alkaline etching liquids and micro etching liquids. Acid etching is mainly used in the production of inner layer circuit patterns of multilayer circuit boards. 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 120g / L or higher. The main components o...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C23F1/46C22B3/26C25C1/12
CPCY02P10/20
Inventor 陈飙
Owner 陈飙
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Eureka Blog
Learn More
PatSnap group products