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A preparation method and application of hydrometallurgy zinc purification and cobalt removal agent

A technology of hydrometallurgy and cobalt removal agent, applied in the direction of improving process efficiency, etc., can solve the problems of low cobalt content in purification slag, high cost, high temperature requirements, etc., and achieve high purification and impurity removal efficiency, fast reaction speed, and process simple effect

Active Publication Date: 2021-09-21
济源市华信科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Using antimony salt or arsenic salt zinc powder replacement method to remove cobalt is the most popular and conventional method at present: the purification ability is strong, although it is easy to produce highly toxic substance SbH in the replacement process 3 or AsH 3 , but as long as the purification tank is well-ventilated, it is also safe and reliable, but there are defects such as large zinc powder consumption, high temperature requirements in the purification process, large steam consumption, low cobalt content in the purification slag, and difficult recycling, resulting in high costs.

Method used

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  • A preparation method and application of hydrometallurgy zinc purification and cobalt removal agent
  • A preparation method and application of hydrometallurgy zinc purification and cobalt removal agent
  • A preparation method and application of hydrometallurgy zinc purification and cobalt removal agent

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preparation example Construction

[0021] A preparation method of a zinc hydrometallurgy purification cobalt removal agent, comprising the following steps:

[0022] (1) Prepare 40% sodium formex aqueous solution;

[0023] (2) Take the aqueous solution of Sodium Dimethicone in step (1) and place it in a 10-liter enamel reaction kettle with a stirring intensity of 60-85r / min, start the refrigerator, and feed frozen 0 ℃ salt water, keep the temperature of the kettle at 10-25 ℃, slowly add caustic soda according to 0.5-1% of the mass of sodium formex aqueous solution, and stir evenly;

[0024] (3) Use a pipette to pipette 2-4% carbon disulfide in the aqueous solution of formamic acid, the specific gravity of carbon disulfide is 1.26g / mL, slowly add carbon disulfide to the mixed solution obtained in step (2), and keep the temperature in the kettle at 10- 25 ℃, and stirring, after adding carbon disulfide, continue to react for 30-60 minutes;

[0025] (4) Take 3-4% sodium nitrite in the aqueous solution of thiram, s...

Embodiment 1

[0034] (1) Measure 5L of 40% sodium formazate aqueous solution, and the specific gravity of the sodium formazate aqueous solution is 1.17g / mL;

[0035] (2) Put the aqueous sodium formamate solution in step 1 in a 10-liter enamel reaction kettle, start the freezer, and feed frozen 0°C brine into the jacket of the reaction kettle or the cooling coil, and keep the temperature of the kettle at 10- 25°C, and start stirring, slowly add caustic soda 29.3 ~ 58.5g, and stir evenly;

[0036] (3) Use a pipette to pipette 92.8-185.7 mL of 1.26 g / mL carbon disulfide, slowly add carbon disulfide dropwise to the mixed solution obtained in step (2), keep the temperature in the kettle at 10-25 ° C, and stir, add carbon disulfide After completion, continue to react for 30 to 60 minutes;

[0037] (4) Weigh 175.5-234g of sodium nitrite, slowly add it into the solution obtained in step (3), and stir evenly to obtain the finished cobalt removal agent for purification.

[0038] Prepare 2000mL of p...

Embodiment 2

[0041] (1) Measure 5L of 40% sodium formazate aqueous solution, and the specific gravity of the sodium formazate aqueous solution is 1.17g / mL;

[0042] (2) Put the aqueous sodium formamate solution in step 1 in a 10-liter enamel reaction kettle, start the freezer, and feed frozen 0°C brine into the jacket of the reaction kettle or the cooling coil, and keep the temperature of the kettle at 10- 25°C, and start stirring, slowly add 29.3g of caustic soda, and stir evenly;

[0043] (3) Use a pipette to pipette 92.8mL of 1.26g / mL carbon disulfide, slowly add carbon disulfide dropwise to the mixed solution obtained in step (2), keep the temperature in the kettle at 10-25°C, and stir, after adding carbon disulfide , continue to react for 30 minutes;

[0044] (4) Weigh 175.5g of sodium nitrite, slowly add it to the solution obtained in step (3), and stir evenly to obtain the finished cobalt removal agent for purification.

[0045]Take 5.0L of the pre-cobalt removal solution of an el...

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Abstract

A kind of preparation method of hydrometallurgy zinc purifying cobalt removal agent, comprises the following steps: 1. prepare sodium formex aqueous solution, 2. place in reaction kettle, pass into cooling medium to reaction kettle jacket or internal cooling coil, keep kettle Temperature 10-25°C, slowly add caustic soda according to 0.5-1% of the quality of the sodium formazate aqueous solution, and stir evenly; 3. Use a pipette to pipette 2-4% carbon disulfide in the quality of the sodium formazate aqueous solution, and add it to the mixed solution obtained in step 2 Slowly add carbon disulfide to the mixture, keep the temperature in the kettle at 10-25°C, and stir. After adding carbon disulfide, continue to react for 30-60 minutes; 3. In the obtained solution, stir evenly to obtain the finished product purification cobalt removal agent. The invention has high purification and impurity removal efficiency, simple process, small consumption, fast reaction speed, and can obtain purification slag with higher cobalt valence state. It can remove nickel, copper, cadmium and other metal impurities at the same time, without affecting the zinc electrodeposition.

Description

technical field [0001] The invention belongs to the technical field of zinc solution purification in zinc hydrometallurgy process, and in particular relates to a preparation method and application of a hydrometallurgy zinc purification and cobalt removal agent. Background technique [0002] The main process of zinc hydrometallurgy is divided into five processes: roasting, leaching, cleaning liquid, electrowinning and melting and casting. In order to meet the requirements of zinc electrowinning, harmful impurities such as cobalt, copper, cadmium, nickel, arsenic, antimony, and germanium in the zinc sulfate leaching solution must be purified to below the specified standard, and copper, cadmium, cobalt, and Valuable metals such as nickel are well enriched for easy recycling. Therefore, purification is one of the most important processes in zinc hydrometallurgy. The purification methods used at home and abroad mainly include arsenic salt or antimony salt zinc powder replacemen...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/46C22B19/20
CPCC22B3/46C22B19/26Y02P10/20
Inventor 张欣
Owner 济源市华信科技有限公司
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