Method for carrying out precipitate impurity removal on copper electrolyte and carrying out chlorination regeneration on precipitant

A technology of copper electrolyte and precipitant, which is applied in the field of bismuth impurity removal and comprehensive recovery, arsenic and antimony in copper electrolyte, can solve the problems of long process flow, low impurity removal efficiency, side effects of electrolyte, etc. Short, high removal rate, simple operation effect

Active Publication Date: 2017-09-15
JIANGXI UNIV OF SCI & TECH +1
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  • 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 removing arsenic, antimony, and bismuth, including stannic acid and activated carbon adsorption purification, barium carbonate, strontium carbonate co-precipitation bismuth, Adsorption resin adsorption of antimony, bismuth, solvent extraction of arsenic, antimony, bismuth and other methods, but these methods have defects such as low impurity removal efficiency, large fixed investment, and certain side effects on the electrolyte to varying degrees
Patent applications 201410333413.1, 201510422489.6 and 201610775577.9 disclose methods for removing impurities by precipitation in copper electrolyte, using antimony or / and bismuth oxides and their hydrates as adsorbents or precipitants to remove arsenic, antimony and bismuth in the electrolyte , but the common point of these methods is to carry out alkali leaching to the obtained solid precipitate to regenerate the precipitant. Therefore, there are defects such as long process flow, acid-base alternation, and large reagent consumption. A variety of waste water will also be produced, which needs to be further recycled and treated

Method used

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  • Method for carrying out precipitate impurity removal on copper electrolyte and carrying out chlorination regeneration on precipitant

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] 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.

[0020] element

[0021] Mix the precipitate containing arsenic, antimony and bismuth with ammonium chloride and coke at a mass ratio of 10:20:1, and carry out carbothermal chlorination at a temperature of 800°C for 3.0 hours to obtain a mixture of chlorides containing arsenic, antimony and bismuth Gas 22.69 Nm 3 ; The mixed gas passed through a high-temperature condenser at 380°C and condensed for 2.0 hours to obtain 1.55 kg of...

Embodiment 2

[0023] to 1 m 3 Add 20 kg of antimony trioxide to the copper electrolyte, react at a temperature of 75 °C for 1.5 hours, and filter to obtain a copper electrolyte of 0.99 m 3 and 34.96 kg of precipitation containing arsenic, antimony and bismuth, the removal rates of arsenic, antimony and bismuth in the copper electrolyte were 72.56%, 85.71% and 94.25%, 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.

[0024] element

[0025] Mix the precipitate containing arsenic, antimony and bismuth with ammonium chloride, ferrous chloride and coke at a mass ratio of 10:15:5:2, and carry out carbothermal chlorination at a temperature of 900°C for 2.5 hours to obtain arsenic, Mixed gas of antimony and bismuth chloride 24.58 Nm 3 ; The mixed gas was condensed for 1.5 hours through a high-temperature condenser at 350°C to obtain 3.00 kg of b...

Embodiment 3

[0027] to 1 m 3 Add 35 kg of antimony trioxide to the copper electrolyte, react at a temperature of 70 °C for 2.5 hours, and filter to obtain a copper electrolyte of 0.98 m 3and 57.73 kg of precipitation containing arsenic, antimony and bismuth, the removal rates of arsenic, antimony and bismuth in the copper electrolyte were 70.69%, 80.52% and 93.54%, 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.

[0028] element

[0029] Mix the precipitate containing arsenic, antimony and bismuth with ammonium chloride, ferrous chloride, magnesium chloride and coke according to the mass ratio of 10:15:3:2:2, and carry out carbothermal chlorination at a temperature of 700°C for 4.0 hours, Obtain a mixed gas containing arsenic, antimony and bismuth chloride 39.75Nm 3 ; The mixed gas passed through a high-temperature condenser at 300°C and...

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Abstract

The invention discloses a method for carrying out precipitate impurity removal on a copper electrolyte and carrying out chlorination regeneration on a precipitant. The method comprises the following steps: adding an antimony compound in the copper electrolyte to remove co-precipitates containing arsenic, antimony and bismuth, then directly returning the copper electrolyte to an electrolysis system after the impurity removal, and comprehensively recovering the precipitates containing arsenic, antimony and bismuth by means of carbochlorination and gradient temperature-control condensation. The carbochlorination is carried out on the precipitates to obtain a mixed gas containing arsenic chlorides, antimony chlorides and bismuth chlorides under the action of coke and a chlorinating agent; high-temperature condensation is carried out on the mixed gas to obtain the bismuth chlorides and high-temperature condensation tail gas; medium-temperature condensation is carried out on the high-temperature condensation tail gas to obtain the antimony chlorides and medium-temperature condensation tail gas; low-temperature condensation is carried out on the medium-temperature condensation tail gas to obtain the arsenic chlorides and ammonia-containing tail gas; and the antimony chlorides and the ammonia-containing tail gas are slowly added in water, hydrolysis transformation is carried out on the antimony chlorides and the ammonia-containing tail gas to obtain the antimony compound, and the antimony compound is returned to a precipitate impurity removal procedure as the precipitant. The process method disclosed by the invention has the characteristics of being short in process 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 mechan...

Claims

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Application Information

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Patent Type & Authority Applications(China)
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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