Heap-leaching method for separating copper and tin from tin-plated copper wires

A technology of tinned copper wire and heap leaching method, applied in the direction of improving process efficiency, etc., can solve problems such as difficult large-scale production, difficult large-scale production, expensive copper sulfate, etc., to simplify the waste liquid treatment process, reduce The effect of waste liquid removal and simple process

Active Publication Date: 2010-02-10
UNIV OF SCI & TECH BEIJING +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this method is a conventional chemical method for separating copper and tin, in which the method of stirring must be adopted. Due to the high density of copper, it is difficult to realize large-scale production in industry using the method of stirring, and this method directly replaces tin with copper sulfate , recycle tin (oxide or salt) through follow-up process, there is no copper sulfate replacement liquid regeneration process, because the price of copper sulfate is relatively expensive, the recovery cost is too high, and it is difficult to produce on a large scale

Method used

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  • Heap-leaching method for separating copper and tin from tin-plated copper wires
  • Heap-leaching method for separating copper and tin from tin-plated copper wires
  • Heap-leaching method for separating copper and tin from tin-plated copper wires

Examples

Experimental program
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Effect test

Embodiment 1

[0020] Wash 10 kg of tin-plated copper wires with their skins removed, and stack them on an acid-proof and alkali-proof heap leaching table for heap leaching. The heap leaching solution is 100 kg, the concentration of copper sulfate in the heap leaching solution is 150g / L, and the concentration of sulfuric acid is 120mL , the heap leaching adopts the spray liquid distribution method, in which the temperature of the heap leaching liquid is 60°C, and the spraying intensity is 15L / (h·m 2 ), the heap leaching time is 4 hours; after the heap leaching, the heap leaching slag is pickled with the regenerated heap leaching liquid, and the solution after pickling is returned to the heap leaching process for the next heap leaching, and the heap leaching slag is washed with water to obtain detinned Copper wire, water washing solution is recycled; add hydrogen peroxide to the heap leaching solution until no white precipitate is produced, heat the above reaction solution to boil, then stop h...

Embodiment 2

[0022] Wash 10 kilograms of tinned copper wires with peeled wires in water, and pile them up on the anti-acid and anti-alkali heap leaching platform for heap leaching. The concentration of copper sulfate in the medium is 100g / L, the concentration of sulfuric acid is 250mL, and the heap leaching adopts the spray liquid distribution method, in which the temperature of the heap leaching solution is 55°C, and the spray intensity is 10L / (h·m 2 ), the heap leaching time is 2 hours; after the heap leaching, the heap leaching slag is pickled with the regenerated heap leaching liquid in Implementation Case 1, and the pickling solution is returned to the next heap leaching process for heap leaching. Wash with water to obtain detinned copper wire, and the washing solution is recycled; add hydrogen peroxide to the heap leaching solution until no white precipitate is produced, heat the above reaction solution to boil, then stop heating, and filter after standing for 24 hours; the filter res...

Embodiment 3

[0024] Wash 10 kilograms of tinned copper wires with peeled wires in water, and pile them up on an acid-proof and alkali-proof heap leaching platform for heap leaching. The concentration of copper sulfate in the medium is 75g / L, the concentration of sulfuric acid is 150mL, and the heap leaching adopts the spray liquid distribution method, in which the temperature of the heap leaching solution is 50°C, and the spray intensity is 20L / (h·m 2 ), the heap leaching time is 4 hours; after the heap leaching, the heap leaching slag is pickled with the regenerated heap leaching liquid in Implementation Case 2, and the pickling solution is returned to the next heap leaching process for heap leaching. After the pickling, the heap leaching slag is The detinned copper wire is obtained by washing with water, and the washing solution is recycled; hydrogen peroxide is added to the heap leaching solution until no white precipitate is produced, the above reaction solution is heated and boiled, th...

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Abstract

The invention provides a heap-leaching method for separating copper and tin from tin-plated copper wires, belonging to the recovery processing of waste tin-plated copper wires. The method adopting thecopper sulfate replacement/heap-leaching method comprises the following steps: washing and stacking peeled waste tin-plated copper wires on an acid-proof and alkali-proof heap-leaching platform for heap-leaching; pickling the heap-leaching residue with recycling heap-leaching solution, and further washing the pickled heap-leaching residue to obtain detinned copper wires; adding hydrogen peroxideto the heap-leaching solution until no white precipitation is generated, heating the reaction solution until the reaction solution is boiling, standing, filtering, and drying to obtain original stannic acid, and further calcining the original stannic acid to obtain stannic oxide; adding a proper amount of copper powder and blowing air to the filtrate, wherein the addition amount of the copper power is the copper amount required by copper sulfate in the recycling heap-leaching solution; and controlling the temperature and time of the reaction and adjusting the concentrations of copper sulfate and sulfuric acid of the solution by sulfuric acid and water. The method has the advantages that the process is simple and easy-to-operate, the materials and devices are common and cheap, the tin-plated copper wires dispense with stirring in the heap-leaching process, the heap-leaching solution is recyclable and pollution-free, the removal rate of tin is higher than 95%, and the recovery rate of hydrogen peroxide immersion tin is higher than 98%.

Description

technical field [0001] The invention belongs to the recycling treatment of tinned copper wires, in particular to a copper sulfate replacement-heap leaching method for separating copper and tin from tinned copper wires. Background technique [0002] The electronics and communication industries use a large number of tinned copper wires. During the production and use of tinned copper wires, a large amount of waste tinned wires will inevitably be produced. For the treatment of this part of tinned copper wires, except for a part used for production In addition to bronze alloys, for other applications, it is required to remove the tinned layer on the copper wire. The tin content in the tinned copper wire is about 1wt%, and the copper content is above 98%, which has a high recycling value. [0003] At present, fire method, fire electrolysis method, electrochemical method and chemical method are mainly used at home and abroad to recycle tinned copper wire. Chinese invention patent...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B3/08C22B25/06C22B15/00
CPCY02P10/20
Inventor 潘德安张深根田建军李彬
Owner UNIV OF SCI & TECH BEIJING
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