Method for leaching tellurium from copper anode mud using pressurized acid leaching process

A copper anode slime and acid leaching technology, applied in the direction of improving process efficiency, element selenium/tellurium, etc., can solve the problems of poor working conditions, large loss of tellurium, low cost, etc. The effect of leaching

Inactive Publication Date: 2006-08-23
YUNNAN METALLURGICAL GROUP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are three ways to produce tellurium from tellurium dioxide. The first method is direct reduction with charcoal powder or flour; this method is simple and low in cost, but the loss of tellurium in the reduction process is large and the working conditions are not good
The second method is to dissolve tellurium dioxide in sulfuric acid and reduce it with sulfur dioxide; the tellurium recovered by this method is in the form of a sponge and has limited uses
Moreover, the anode slime is repeatedly carried out in alkaline and acidic environments during the treatment process, resulting in ineffective consumption of auxiliary materials; or causing the precious metals and other valuable metals in the anode slime to be converted into compounds that are difficult to process and extract, making the subsequent recovery of precious metals more difficult. difficult, affecting the recovery rate of precious metals; in addition, when the roasting process is used, the flue gas contains a large amount of SO2 gas, which increases the difficulty of flue gas treatment and easily causes environmental pollution; The process operation (low temperature process) is carried out alternately several times, which greatly increases the energy consumption of the process, and the energy utilization is unreasonable

Method used

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  • Method for leaching tellurium from copper anode mud using pressurized acid leaching process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Example 1: Copper anode slime contains 1.14% tellurium and 1% moisture.

[0031] Slurry the copper anode mud containing 1.14% tellurium and 1% moisture, and sieve out large grains of sand.

[0032] Slurry the sieved copper anode slime with sulfuric acid solution containing 70g / l of acid, add it into a titanium acid-resistant autoclave with a volume of 5L, and continuously feed compressed air to maintain the pressure in the autoclave at 0.5MPa and the temperature at 100°C. Pressure leaching, leaching time 60 minutes.

[0033] The tellurium leaching rate is 40.1%, the slag rate is 60.32%, and the leaching slag contains 1.10% tellurium.

Embodiment 2

[0034] Example 2: Copper anode slime contains 1.23% tellurium and 12% moisture.

[0035] Slurry the copper anode mud containing 1.23% tellurium and 12% moisture, and sieve out large grains of sand.

[0036] The sieved copper anode slime is slurried with sulfuric acid solution containing 100g / l of acid, and added to a titanium acid-resistant autoclave with a volume of 5L, and 33% oxygen-enriched air is continuously introduced to maintain the pressure in the autoclave at 0.7MPa. 120°C, pressurized leaching, leaching time 90 minutes.

[0037] The tellurium leaching rate is 41.3%, the slag rate is 55.46%, and the leaching slag contains 1.12% tellurium.

Embodiment 3

[0038] Embodiment 3: Copper anode slime contains 0.99% tellurium and 1% moisture.

[0039] Slurry the copper anode mud containing 0.99% tellurium and 1% water, and sieve out large grains of sand.

[0040] Mix the sieved copper anode slime with sulfuric acid solution containing 200g / l of acid, put it into a titanium acid-resistant autoclave with a volume of 5L, and continuously feed 99.5% industrial oxygen to maintain the pressure in the kettle at 1.6Mpa and the temperature at 180°C , carry out pressure leaching, leaching time 120 minutes.

[0041] The tellurium leaching rate is 45.3%, the slag rate is 53.46%, and the leaching slag contains 0.81% copper.

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Abstract

The present invention relates to pressurizing and acid leaching process for leaching out tellurium from copper anode mud, and belongs to the field of wet metallurgical technology of rare dispersion element. The process includes the following steps: mixing water and anode mud in 1-40 wt% to prepare slurry, filtering to eliminate large grain and sand, mixing with sulfuric acid solution of 70-300 g / L concentration, heating in a high pressure reactor at 100-180 deg.c, introducing gaseous oxidizing medium, regulating and maintaining the pressure at 0.5-1.6 MPa for direct acid leaching reaction for 60-120 min, solid-liquid separation to obtain the tellurium leachate. The present invention has simple technological process, less needed apparatus, reinforced process, short leaching period and high tellurium leaching rate.

Description

technical field [0001] The invention relates to a method for leaching tellurium from copper anode slime, which belongs to the technical field of wet extraction metallurgy of scattered elements. Background technique [0002] Scattered element tellurium is an alloy additive widely used in iron and steel and nonferrous metallurgy; a catalyst in chemical industries such as petroleum and rubber, and an important raw material for semiconductors and infrared optical devices. Because of its important position in the fields of modern high-tech industry, national defense and cutting-edge technology, tellurium has been paid more and more attention by people, and its application range has become wider and wider. Most of the world's recoverable tellurium is associated with copper deposits and telluride-type gold-silver deposits. [0003] The industrially produced tellurium element mainly comes from the anode slime in the copper electrolytic refining process. Due to the high price of te...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B19/02C22B3/08C22B3/22
CPCY02P10/20
Inventor 王吉坤冯桂林张博亚李皓阎江峰
Owner YUNNAN METALLURGICAL GROUP
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