Method for producing tribasic copper chloride

A production method and technology of copper chloride, applied in the direction of copper chloride, copper halide, etc., can solve the problems of high treatment cost, increased difficulty and cost of wastewater treatment, increased operation procedures, etc.

Inactive Publication Date: 2012-10-17
GUANGZHOU KECHENG ENVIRONMENTAL PROTECTION TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of this process route to produce basic copper chloride is that ammonia nitrogen is artificially added during production, which increases the difficulty and cost of subsequent wastewater treatment. At the same time, this process route has high production costs, increased operating procedures, and greater labor intensity. environmental pollution
However, the main evaporation recovery system (MVR) of ammonium chloride in the mother liquor is not mature enough, the corrosion problem of the compressor head has not been solved well, and the quality of recovered ammonium chloride is poor
[0005] Therefore, at present, the treatment of the etching waste liquid is completed, and the problems of ammonia nitrogen content are difficult to deal with and the treatment cost is high need to be solved.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] (1) Put 5m 3 The acidic etching waste liquid with 9% copper content is poured into the impurity removal reactor, 10L hydrogen peroxide is added, and the reaction is 10 minutes, and then sodium hydroxide is added to adjust the pH to 1.3. After the reaction is 20 minutes, pressure filter to remove lead and arsenic After impurities such as cadmium, mercury and iron, the filtrate enters the intermediate tank of the acid etching waste liquid.

[0029] (2) Toward 5.4 m 3 600kg of solid sodium hydroxide and 68.5kg of solid sodium carbonate are added to the water to prepare a sodium hydroxide mixed lye with a mass concentration of sodium hydroxide of about 10%.

[0030] (3) Preheat the mother liquor of basic copper chloride containing 600mg / L copper and 15g / L ammonia nitrogen to 70℃, and add the acid etching waste liquid and sodium hydroxide after removing impurities according to the volume flow ratio of 1:1.5. Solution, control the pH between 6.0 and 6.5, after 4 hours of reaction,...

Embodiment 2

[0033] (1) Put 5.5m 3 The acidic etching waste liquid with a copper content of 9.5% is injected into the impurity removal reactor. Under the condition of sufficient stirring, add 15L of sodium chlorate, react for 10 minutes, then add sodium hydroxide to adjust its pH to 1.5, and react for 20 After minutes, press filter to remove impurities such as lead, arsenic, cadmium, mercury, iron, etc., and the filtrate enters the intermediate tank of acid etching waste liquid.

[0034] (2) Towards 5.5 m 3 Add 786 kg of solid sodium hydroxide to the water to prepare a sodium hydroxide solution with a mass concentration of sodium hydroxide of 12.5%.

[0035] (3) Preheat the mother liquor of basic copper chloride containing 743mg / L copper and 11g / L ammonia nitrogen to 75℃, and add the acid etching waste liquid and sodium hydroxide solution after removing impurities according to the volume flow ratio of 1:2 , Control the pH between 6.5 and 7.0, after 4 hours of reaction, a total of 5.5t of acid e...

Embodiment 3

[0038] (1) Put 4.5m 3 The acid etching waste liquid with copper content of 8.5% is pumped into the impurity removal reactor, 8L hydrogen peroxide is added, and the reaction is for 10 minutes, and then sodium hydroxide is added to adjust the pH to 1.0. After 20 minutes of reaction, press filter to remove lead and arsenic. After impurities such as cadmium, mercury and iron, the filtrate enters the intermediate tank of the acid etching waste liquid.

[0039] (2) Toward 4.5 m 3 Add 500kg of solid sodium hydroxide and 55.6kg of solid sodium bicarbonate into the water to prepare a mixed lye of sodium hydroxide with a mass concentration of about 10%.

[0040] (3) Preheat the mother liquor of basic copper chloride containing 652mg / L copper and 8g / L ammonia nitrogen to 70℃, and add the acid etching waste liquid and sodium hydroxide after removing impurities according to the volume flow ratio of 1:1. The pH of the solution is controlled between 4.0 and 4.5. After 4 hours of reaction, a total...

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Abstract

The invention discloses a method for producing tribasic copper chloride. The method for producing the tribasic copper chloride includes the following steps of: (1) removing impurities from an acidic etching waste solution; (2) adding clean water or a tirbasic copper chloride production mother solution to a synthesis reactor, performing preheating, and then, preheating the acidic etching waste solution whose impurities have been removed and an alkaline solution of sodium hydroxide and mixing the two solutions for a reaction with the pH value and temperature of the reaction being controlled so as to gradually form the tribasic copper chloride, and discharging partial materials after a certain amount of reaction time; (3) filtering the materials discharged from the reaction system, and performing washing, suction filtration, centrifugation and drying on the filtrated residues to obtain the tribasic copper chloride; and (4) performing ammonia nitrogen removal treatment on filtrated liquid. By adopting the method for producing the tribasic copper chloride in the invention, continuous production can be achieved and the tribasic copper chloride with large particle size and high purity can be produced; further, production cost can be reduced and overall process can be integrated; and the method for producing the tribasic copper chloride is advantaged in simple ultimate steps of ammonia nitrogen removal, easiness in operation as well as reduced difficulty and cost of ammonia nitrogen treatment.

Description

technical field [0001] The invention belongs to the field of etching waste liquid treatment, and in particular relates to a production method of basic copper chloride. Background technique [0002] At present, copper sulfate is mostly used as a trace additive in domestic feed, but copper sulfate is easy to absorb moisture and agglomerate, has poor dispersibility, and strong oxidation during use, which destroys nutrients such as vitamins and fats in the feed, and is harmful to zinc and iron. There are disadvantages such as antagonistic effect which affects its absorption. Therefore, it is necessary to develop a new and efficient copper source additive to replace copper sulfate. [0003] Basic copper chloride has been used in the United States for more than ten years. Studies have shown that compared with copper sulfate, basic copper chloride has the following advantages: ①No moisture absorption, no agglomeration, uniform distribution, and rumen-passing function for ruminan...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01G3/05
Inventor 吴阳东王永成张素娟黄智源方健才韩福勇刘杨
Owner GUANGZHOU KECHENG ENVIRONMENTAL PROTECTION TECH
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