Method for carrying out precipitate impurity removal on copper electrolyte

A copper electrolyte and impurity removal technology, applied in the field of electrolyte purification, can solve the problems of long process flow, side effects of electrolyte, low impurity removal efficiency, etc., and achieve the effects of short process flow, simple operation and high removal rate.

Active Publication Date: 2017-09-15
JIANGXI UNIV OF SCI & TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the precipitation potential of arsenic, antimony, and bismuth is similar to that of copper, when the content of arsenic, antimony, and bismuth in the electrolyte reaches a certain concentration, it is easy to precipitate at the cathode together with copper. In addition, the arsenic, antimony, and Bismuth is easy to form "floating anode slime" to adhere or mechanically entrap on cathode copper, thus affecting the quality of cathode copper
[0003] In order to ensure the normal progress of the copper electrolysis process, the current copper electrolysis industry often uses the induction method to purify the electrolyte to remove impurities such as arsenic, antimony, and bismuth in the electrolyte. However, for copper electrolytes with high antimony and high bismuth, the The process has low impurity removal efficiency, large net liquid volume, high cost, and produces toxic gas and causes great environmental pollution.
In recent years, scholars at home and abroad have been seeking new copper electrolyte purification processes, and have developed many effective methods for

Method used

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  • Method for carrying out precipitate impurity removal on copper electrolyte

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] to 1 m 3 Add 15 kg of antimony trioxide to the copper electrolyte, react at a temperature of 85 °C for 1.0 hour, and filter to obtain a copper electrolyte of 0.99 m 3 and 24.46 kg of precipitation containing arsenic, antimony and bismuth, the removal rates of arsenic, antimony and bismuth in the copper electrolyte were 68.89%, 64.22% and 92.75%, respectively, and the precipitation reaction had a great influence on the copper and acid content in the copper electrolyte. The results of precipitation and impurity removal are as follows.

[0019] element

[0020] The precipitate containing arsenic, antimony and bismuth was decomposed under the protection of argon gas with a volume percentage of 99.99% at a temperature of 800 °C for 3 hours to obtain 17.58 kg of low-temperature decomposition slag and low-temperature decomposition gas. The low-temperature decomposition gas was condensed to obtain purity 98.59% As 2 o 3 6.88 kg; the low-temperature decomposition s...

Embodiment 2

[0022] to 1 m 3 Add 20 kg of antimony pentoxide to the copper electrolyte, react at a temperature of 65 °C for 1.5 hours, and filter to obtain a copper electrolyte of 0.99 m 3 and 33.21 kg of precipitation containing arsenic, antimony and bismuth, the removal rates of arsenic, antimony and bismuth in the copper electrolyte were 72.15%, 87.04% and 93.14%, respectively, and the precipitation reaction had a great influence on the copper and acid content in the copper electrolyte. The results of precipitation and impurity removal are as follows.

[0023] element

[0024] The precipitate containing arsenic, antimony and bismuth was decomposed at 700 °C for 2.5 h under the protection of argon gas with a volume percentage of 99.99%, and 23.26 kg of low-temperature decomposition slag and low-temperature decomposition gas were obtained. The low-temperature decomposition gas was condensed to obtain purity 99.04% As 2 o 3 9.95 kg; the low-temperature decomposition slag was ...

Embodiment 3

[0026] to 1 m 3 Add 32 kg of antimony pentoxide and 8 kg of antimony trioxide to the copper electrolyte, react at a temperature of 75 °C for 1.0 hour, and filter to obtain a copper electrolyte of 0.98 m 3 and 60.19 kg of precipitation containing arsenic, antimony and bismuth, the removal rates of arsenic, antimony and bismuth in the copper electrolyte were 71.65%, 79.53% and 94.18%, respectively, and the precipitation reaction had a great influence on the copper and acid content in the copper electrolyte. The results of precipitation and impurity removal are as follows.

[0027] element

[0028] The precipitate containing arsenic, antimony and bismuth was decomposed under the protection of argon gas with a volume percentage of 99.99% at a temperature of 550 °C for 3.0 h to obtain 42.90 kg of low-temperature decomposition slag and low-temperature decomposition gas. The low-temperature decomposition gas was condensed to obtain purity 99.48% As 2 o 3 17.29 kg; the l...

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Abstract

The invention discloses a method for carrying out precipitate impurity removal on a copper electrolyte. The method comprises the following steps: adding an antimony compound in the copper electrolyte to remove co-precipitates containing arsenic, antimony and bismuth in the copper electrolyte as a precipitant, then directly returning the copper electrolyte to an electrolysis system after the impurity removal, and comprehensively recovering the precipitates containing arsenic, antimony and bismuth through a gradient temperature-control firing method. Low-temperature decomposition is carried out on the precipitates to obtain a low-temperature decomposition gas and low-temperature decomposition residues under inert gas shied, the low-temperature decomposition gas is condensed to obtain an arsenic compound, high-temperature decomposition is carried out on the low-temperature decomposition residues under atmosphere control to obtain a bismuth compound and a high-temperature decomposition gas, the high-temperature decomposition gas is condensed to obtain an antimony compound, and the antimony compound is returned to a precipitate impurity removal procedure for the copper electrolyte as the precipitant. According to the method disclosed by the invention, arsenic, antimony and bismuth in the copper electrolyte are independently recovered in the form of high-purity compounds while being efficiently removed; and the method has the characteristics of being short in flow, simple to operate, high in removal rate, free from the emission of 'three wastes', capable of repeatedly using the precipitant, low in cost and the like, and is suitable for large-scale industrial production.

Description

technical field [0001] The invention relates to a method for purifying electrolyte in nonferrous metal hydrometallurgy process, in particular to a method for removing and comprehensively recovering arsenic, antimony and bismuth impurities in copper electrolyte. Background technique [0002] With the rapid development of the copper smelting industry, there are fewer and fewer high-quality copper concentrates, and the content of impurities such as arsenic, antimony, and bismuth in the anode copper of mines is on the rise, resulting in high content of arsenic, antimony, and bismuth in the copper electrolyte. Since the precipitation potential of arsenic, antimony, and bismuth is similar to that of copper, when the content of arsenic, antimony, and bismuth in the electrolyte reaches a certain concentration, it is easy to precipitate at the cathode together with copper. In addition, the arsenic, antimony, and Bismuth is easy to form "floating anode slime" to adhere to or be mech...

Claims

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Application Information

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IPC IPC(8): C25C7/06C25C1/12C22B15/00C22B30/00
CPCC22B15/0089C22B30/00C25C1/12C25C7/06Y02P10/20
Inventor 汪金良蔡兵胡华舟叶锋浦绍增
Owner JIANGXI UNIV OF SCI & TECH
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