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Method for extracting silver from silver slag

A silver slag separation and solid-liquid separation technology, which is applied in the field of silver recovery, can solve the problems of high processing cost, loss of precious metals, and difficulty in recycling and processing, and achieve reliable process, simple equipment, and environmental friendliness

Active Publication Date: 2008-06-11
JINCHUAN GROUP LIMITED
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the complex composition of the silver slag, low precious metal content, and difficulty in recycling, some smelters return the silver slag to the fire method for smelting and blowing, resulting in the loss of precious metals and high processing costs; while some smelters return the silver slag Return directly to the anode slime treatment process. This treatment method not only cannot effectively recover the precious metals and valuable metals, but also increases the burden on the anode slime treatment process.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0011] Accurately weigh 400g of silver slag, put it into a 5000ml beaker, add H 2 O1200ml, after slurrying for 45 minutes, added H 2 O 1200ml to make the solid-liquid mass ratio of the system reach 1:6, then slowly stir and add industrial H 2 SO 4 until the slurry contains H 2 SO 4 0.55mol / L, heated to 50°C and slowly added NaClO 3 8g, the oxidation-reduction potential of the solution is about 400mv-480mv, keep the system temperature in the range of 50°C-60°C for 4.5 hours. After oxidation pretreatment, liquid-solid separation is carried out. The pretreatment liquid can recover metal Cu and Ni, and the pretreatment slag uses Na 2 SO 3 Cent Silver, CH 2 The process of reducing silver by O can obtain coarse silver powder with a grade greater than 93%. (The conditions of the silver separation stage are: slurry solid-liquid mass ratio 1:3, normal temperature slurry time 1 hour, silver separation solid-liquid mass ratio 1:5, silver separation temperature 33°C-38°C, adjust s...

Embodiment 2

[0013] Accurately weigh 1200g of silver slag, put it into a 10L enamel kettle, add H at a solid-liquid mass ratio of 1:2 2 O 2.4 L after slurrying for 30 minutes, supplemented with H 2 O4.8L, make the solid-liquid mass ratio of the system reach 1:6, then slowly stir and add industrial H 2 SO 4 to slurry H 2 SO 4 The concentration is 0.38mol / L, heating to 55°C and slowly adding NaClO 3 28g, the redox potential of the solution is 420mv-460mv, and the temperature of the system is kept within the range of 50°C-60°C for 5 hours. After oxidation pretreatment, liquid-solid separation is carried out. The pretreatment liquid can recover metal Cu and Ni, and the pretreatment slag uses Na 2 SO 3 Cent Silver, CH 2 The process of reducing silver by O can obtain coarse silver powder with a grade greater than 93%. (The conditions of the silver separation stage are: slurry solid-liquid mass ratio 1:3, normal temperature slurry time 1 hour, silver separation solid-liquid mass ratio 1:5...

Embodiment 3

[0015] Accurately weigh 15Kg of silver slag, put it into a 100L enamel kettle, and add H 2 After O37.5L was slurried for 50 minutes, add H 2 O 37.5L, make the solid-liquid mass ratio of the system reach 1:5, then slowly stir and add industrial H 2 SO 4 to slurry H 2 SO 4 The concentration is 0.4mol / L, heating to 60°C and slowly adding NaClO 3 About 370g, the redox potential of the solution is 440mv-480mv, keep the system temperature in the range of 50°C-60°C for 3.5 hours. After oxidation pretreatment, liquid-solid separation is carried out. The pretreatment liquid can recover metal Cu and Ni, and the pretreatment slag uses Na 2 SO 3 Cent Silver, CH 2 The process of reducing silver by O can obtain coarse silver powder with a grade greater than 93%. (The conditions of the silver separation stage are: slurry solid-liquid mass ratio 1:3, normal temperature slurry time 1 hour, silver separation solid-liquid mass ratio 1:5, silver separation temperature 33°C-38°C, adjust so...

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PUM

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Abstract

The invention discloses a method for extracting silver from silver separated residue, which relates to a method for recycling silver from the solid residue of copper anode sludge after the metal such as Se, Cu, Te, Au, and Ag is separated and extracted. The invention is characterized in that the invention comprises the steps that firstly, the silver separated residue is pulped, industrial H2SO4 is adopted to adjust the acidity of the solution, the oxidizing agent NaClO3 is added to control oxidation reduction potential of the solution to perform oxidizing pretreatment, Ag2O, Ag2SO4, Ag2S, and simple substance Ag in the silver separated residue which can be hardly leached are changed into AgCl which can be easily leached by Na2SO3, and the AgCl is reduced into coarse Ag powder through CH2O under the alkalinity condition. The method of the invention has the advantages that the equipment is simple, the process flow is simple, the silver recovery ratio is high, the loss of the noble metal such as Pt and Pd, etc. in the silver separated residue can not be caused, and the invention is suitable for large-scale industrial production.

Description

technical field [0001] A method for extracting silver from silver-separating slag relates to a method for recovering silver from the solid residue after separating and extracting Se, Cu, Te, Au, Ag and other metals from copper anode slime. Background technique [0002] Silver separation slag is the solid residue left after extracting main components such as Se, Cu, Te and precious metals Au, Ag, Pt, Pd from copper anode slime. Generally, the output rate of anode slime is 50%-55%, while the output rate of silver-separating slag is 28%-33% of that of copper anode slime. At present, many copper smelting plants in China produce a large amount of silver slag every year. Due to the complex composition of the silver slag, low precious metal content, and difficulty in recycling, some smelters return the silver slag to the fire method for smelting and blowing, resulting in the loss of precious metals and high processing costs; while some smelters return the silver slag Directly ret...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B11/00C22B7/00
CPCY02P10/20
Inventor 郭锋陈彩霞马晶
Owner JINCHUAN GROUP LIMITED
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