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Roasting-free evaporation-free method for producing cupric sulfate from zinc hydrometallurgy acid-wash copper dross

A technology for hydro-smelting zinc and copper sulfate, which is applied in the direction of copper sulfate and the improvement of process efficiency, can solve the problems of increased production cost, rising raw material cost, complicated operation, etc., and achieves water consumption saving, fast production speed, and utilization rate. high effect

Inactive Publication Date: 2012-08-15
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

From the perspective of solution evaporation, due to the high phase change heat of water, this process needs to absorb a large amount of energy; from the perspective of steam utilization, in order to ensure the evaporation speed of the solution, it is necessary to keep the solution in a boiling state, which is It will inevitably lead to the need to maintain a certain residual pressure of high-temperature and high-pressure steam, resulting in a large amount of lack of air, which eventually leads to a large consumption of steam. No matter whether it is the traditional methods and equipment to reduce steam consumption such as decompression evaporation or multi-effect evaporation, this core cannot be avoided. This is also the root cause of high energy consumption in the evaporation and concentration process
At the same time, in the process of evaporation and concentration, some impurities will reach supersaturation and precipitate out in the concentrated mother liquor, which will affect the quality of copper sulfate products. In order to ensure the quality of copper sulfate products, it is often necessary to use copper raw materials with less impurities, resulting in an increase in raw material costs and a decline in economic benefits. ; Although the method of purifying and removing impurities by solution has a certain effect, it also makes the operation complicated, increases the production cost, and introduces new impurities, and the purification slag produced will also reduce the copper recovery rate

Method used

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  • Roasting-free evaporation-free method for producing cupric sulfate from zinc hydrometallurgy acid-wash copper dross
  • Roasting-free evaporation-free method for producing cupric sulfate from zinc hydrometallurgy acid-wash copper dross

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] (1) Store 1.82t of pickling copper slag for 1 day, relying on the oxygen in the air to make it oxidize naturally; Among them, the pickling copper slag is the pickling copper slag produced by the purification of zinc hydrometallurgy solution, and the copper content The phase is elemental metal copper or copper metal compound, containing more than 38.71wt% copper (total copper);

[0027] (2) Using a sulfuric acid solution with a concentration of 250g / L as a leaching agent, the pickling copper slag oxidized in step (1) was leached for 2.5 hours at 100°C with a solid-to-liquid ratio of 1:6 to obtain a slurry;

[0028] (3) Filter the leached slurry obtained in step (2) at 100°C to obtain leaching liquid and leaching residue respectively; the obtained leaching residue is stored until natural oxidation and then returns to step (2) for repeated leaching 5 times until Copper (total copper) in leaching slag is less than 1wt%;

[0029] (4) The leaching solution obtained in step (...

Embodiment 2

[0032] (1) Store 2.75 tons of pickling copper slag for 3 days, relying on the oxygen in the air to make it oxidize naturally; Among them, the pickling copper slag is the pickling copper slag produced by the purification of the zinc hydrometallurgy solution, and the copper content The phase is simple metal copper or copper metal compound, containing 33.52wt% copper (total copper);

[0033] (2) Using a sulfuric acid solution with a concentration of 150g / L as a leaching agent, leaching the acid-washed copper slag oxidized in step (1) for 0.5 hours at 92°C with a solid-to-liquid ratio of 1:5 to obtain a slurry;

[0034] (3) Filter the leached slurry obtained in step (2) at 92°C to obtain leaching liquid and leaching residue respectively; the obtained leaching residue is stored until natural oxidation and then returns to step (2) for repeated leaching three times until leaching Copper (total copper) in slag is less than 1wt%;

[0035](4) The leaching solution obtained in step (3) ...

Embodiment 3

[0038] (1) Store 2.79 tons of pickling copper slag for 5 days, relying on the oxygen in the air to make it oxidize naturally; Among them, the pickling copper slag is the pickling copper slag produced by the purification of the zinc hydrometallurgy solution, and the copper content The phase is elemental metal copper or copper metal compound, containing more than 34.06wt% copper (total copper);

[0039] (2) Using a sulfuric acid solution with a concentration of 250g / L as a leaching agent, leaching the acid-washed copper slag oxidized in step (1) for 1 hour at 80°C with a solid-to-liquid ratio of 1:4 to obtain a slurry;

[0040] (3) Filter the leached slurry obtained in step (2) at 80°C to obtain leaching liquid and leaching residue respectively; the obtained leaching residue is stored until natural oxidation and then returns to step (2) for repeated leaching three times until leaching Copper (total copper) in slag is less than 1wt%;

[0041] (4) The leaching solution obtained i...

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Abstract

The invention provides a roasting-free evaporation-free method for producing cupric sulfate from zinc hydrometallurgy acid-wash copper dross, which comprises the following steps: stacking acid-wash copper dross for autoxidation; leaching the oxidated acid-wash copper dross at 75-100 DEG C according to a solid-to-liquid ratio of 1:(3-6) for 0.5-2.5 hours by using a 50-250g / L sulfuric acid solution as a leaching agent, thereby obtaining a slurry; filtering the leached slurry at 75-100 DEG C to respectively obtain a leach solution and a leached mud; and conventionally cooling to crystallize the leach solution, and carrying out centrifugal separation to obtain cupric sulfate and crystallization mother liquor. The oxidation of the acid-wash copper dross does not need roasting or addition of any oxidant, does not introduce any impurity, and is simple to operate. The invention does not have the process of concentration by evaporation, has the advantages of high production rate, obvious water-saving effect and obviously lower energy consumption (only about 10% of the traditional technique of concentration by evaporation). The invention also has the advantages of high resource comprehensive utilization ratio, no waste discharge and low environmental protection pressure.

Description

technical field [0001] The invention relates to a method for preparing copper sulfate crystals without roasting and evaporation from pickling copper slag produced in a zinc hydrometallurgy process, and belongs to the technical fields of hydrometallurgy and chemical industry. Background technique [0002] In the process of producing electric zinc by hydrometallurgy, the leaching solution containing zinc needs to be purified and removed. Usually, zinc powder is added to replace impurities such as copper and cadmium, and copper and cadmium slag is produced to recover zinc, copper, cadmium, and lead. Zinc, silver and other valuable elements are often leached out by pickling, soluble metals such as zinc, and zinc sulfate solution and pickling copper slag are produced. Copper in the pickling copper slag mainly exists in a metallic state. This type of copper slag contains more impurities, the direct selling price is lower, and the economic benefit is poor. It needs further treatmen...

Claims

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Application Information

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IPC IPC(8): C22B7/00C22B3/08C22B3/22C01G3/10C22B15/00
CPCY02P10/20
Inventor 张旭施哲沈庆峰
Owner KUNMING UNIV OF SCI & TECH