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Treatment method of copper anode plate washing slag

A processing method and technology for copper anode plates, which are applied in chemical instruments and methods, process efficiency improvement, photographic technology and other directions, can solve the problems of low copper recycling and processing, increased processing costs, high energy consumption, etc., and meet the requirements of low equipment. , the effect of increasing added value and short process

Active Publication Date: 2021-04-09
YANGGU XIANGGUANG COPPER
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Minor problem with copper recovery and treatment: this process only carries out oxidative acid leaching for medium sand (containing 39% copper), while high-copper coarse sand (containing 79% copper, 9.6% barium sulfate) is still returned to the furnace for treatment, resulting in water washing slag Most of the copper and a small amount of barium sulfate (accounting for 78% of the total copper and 10% of barium sulfate in the washing slag) are not directly recovered, but enter the smelting system for treatment, which has a long process and high cost
High-temperature concentrated acid leaching of copper and barium sulfate on water-washed slag, the main problem of this process is high temperature 200-500 ℃, sulfuric acid concentration 18mol / L, high temperature and high acid working conditions require quite high equipment and consume a lot of energy
A large amount of dilute acid is produced after the acid leaching solution is diluted, and the dilute acid must be treated before it can be discharged, which will inevitably increase the treatment cost

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0070] (1) Weigh 200g of anode plate washing slag, add it to 240g / L sulfuric acid solution, the volume of sulfuric acid solution is 1.6L, stir the mixed slurry, raise the temperature to 70°C, and add hydrogen peroxide dropwise into the acid dipping solution. The mass ratio of the hydrogen peroxide to the copper element in the anode plate washing slag is 1.5:1. After the hydrogen peroxide is added dropwise, pickle (oxidize) for 1 hour. The copper leaching rate was 97%.

[0071] (2) Add 40mL of cationic polyacrylamide liquid with a concentration of 0.06wt% to the oxidized pickling solution, and the volume ratio of the cationic polyacrylamide solution to the pickling solution is 1:40. The silica gel was used for flocculation and precipitation, the flocculation time was 10min, and the filtration was very fast to obtain the acid leaching liquid and acid leaching residue. Filtrate (i.e. acid leaching liquid) composition: Cu 66g / L, Fe 0.06g / L, As 0.03g / L, Sb 0.005g / L, Bi 0.03g / L, H...

Embodiment 2

[0079] (1) Weigh 100g of anode plate washing slag, add it to 280g / L sulfuric acid solution, the volume of sulfuric acid solution is 1L, stir the mixed slurry, raise the temperature to 80°C, and add hydrogen peroxide dropwise into the acid dipping solution. The mass ratio of the hydrogen peroxide to the copper element in the anode plate washing slag is 1.5:1. After the hydrogen peroxide is added dropwise, pickle (oxidize) for 1 hour. The copper leaching rate was 96%.

[0080] (2) In the oxidized pickling solution, add 25 mL of cationic polyacrylamide liquid with a concentration of 0.0006 wt%, and the volume ratio of the cationic polyacrylamide solution to the pickling solution is 1:40. Carry out flocculation and precipitation, the flocculation time is 10min, and the filtration is very fast, and the acid leaching liquid and acid leaching residue are obtained. Filtrate composition (i.e. acid leaching liquid): Cu52g / L, Fe 0.08g / L, As 0.02g / L, Sb 0.005g / L, Bi 0.02g / L, H 2 SO 4 ...

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PUM

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Abstract

The invention relates to the technical field of anode plate washing slag treatment, in particular to a treatment method of copper anode plate washing slag. The treatment method comprises the following steps that (A) the copper anode plate washing slag, a sulfuric acid solution and an oxidizing agent are mixed, and acid leaching is carried out to obtain an acid leaching solution; (B) the acid leaching solution is mixed with a cationic polyacrylamide solution, and flocculent precipitation is carried out to obtain an acid leaching clear solution and acid leaching residues; and (C) the acid leaching residues are washed with water, size mixing and screening are carried out to obtain barium sulfate, the acid leaching clear solution is subjected to electrified electrodeposition, and the high-purity cathode copper is obtained. The problem of comprehensive recovery of valuable elements from the anode plate casting water washing slag is solved, a process scheme for oxidizing acid leaching treatment of the water washing slag is creatively provided, the problem of traditional water washing slag furnace returning treatment is solved, the process is different from other wet treatment processes, the process is simple, the flow is short, the equipment requirements are low, and the additional value of a product is enhanced.

Description

technical field [0001] The invention relates to the technical field of processing slag washing of anode plates, in particular to a method for treating slag washing of copper anode plates. Background technique [0002] In order to prevent the anode plate from being bonded to the copper mold and to avoid affecting the surface quality of the anode plate, a layer of release agent is usually applied to the casting mold before the copper smelting anode plate is cast. Barium sulfate has the characteristics of high melting point, stable properties, and no reaction with acid and alkali. In actual production, barium sulfate is usually used with a small amount of water glass as a release agent for copper anode plate casting. After the copper anode plate is cast and demoulded, it is usually cooled in a circulating water pool. Under the cooling effect of cold water, most of the release agent adhering to the anode plate entrains copper-containing materials and falls off from the anode p...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B15/00C22B26/20C22B7/00C25C1/12C01F11/46
CPCC22B15/0071C22B26/20C22B7/006C22B7/007C25C1/12C01F11/462Y02P10/20
Inventor 魏栋董广刚刘士祥李先和胥林朋李纪云
Owner YANGGU XIANGGUANG COPPER
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