Method for increasing extraction efficiency of copper in water solution

A technology for extracting efficiency and aqueous solution, which is applied in the field of improving the extraction efficiency of copper in aqueous solution, which can solve the problems of high investment, consumption of reagents, and increased liquid volume in the extraction system, and achieves high extraction efficiency and reduced equipment investment

A technology for extracting efficiency and aqueous solution, which is applied in the field of improving the extraction efficiency of copper in aqueous solution, which can solve the problems of high investment, consumption of reagents, and increased liquid volume in the extraction system, and achieves high extraction efficiency and reduced equipment investment

CN102864306BInactive Publication Date: 2014-02-05NORTHEASTERN UNIV LIAONING

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  • Method for increasing extraction efficiency of copper in water solution
  • Method for increasing extraction efficiency of copper in water solution
  • Method for increasing extraction efficiency of copper in water solution

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] The components and properties of the copper-containing solution in the hydrochloric acid system are as follows: 34.38g / L Cu, 1.26g / L Co, 79.30g / L Zn, 8.50 g / L Cd, 237.8g / L sodium citrate, pH=2.45 .

[0023] According to the effective loading rate of 30% LIX622N-kerosene extracting copper is 75% of the theoretical amount, compared to: in this example [Cu]a =34.38g / l, the maximum loading copper amount Lm of the LIX622N-kerosene organic phase with a concentration of 10% =5.9g / l, the volume percentage M=30 of the extractant in the organic phase, then use 30% of the LIX622N-kerosene organic phase to completely extract the copper in the aqueous solution compared to R={10×[Cu]a} / {Lm×M×0.75}={10×34.38} / {5.9×30×0.75}=2.59, therefore, the actual comparison is 2.6. Put 30% LIX622-kerosene organic phase and copper-containing solution into the separatory funnel according to the calculated ratio of 2.6, shake at room temperature for 5 minutes and let it stand still. After the organ...

Embodiment 2

[0027] The components and properties of the copper-containing solution in the sulfuric acid system are as follows: 22.72g / L Cu, 0.83g / L Co, 75.05g / L Zn, 2.50 g / L Cd, 142.67g / L ammonium citrate added, pH=1.55 .

[0028] For the copper-containing solution, when using 30% LIX984N-kerosene organic phase extraction, calculated according to the maximum load of the organic phase, the theoretical ratio is 1.3 when all the copper is to be extracted. Take 30mL of copper-containing solution each time, at room temperature, mix and shake 30% LIX984N3-kerosene organic phase and water phase according to different phases for 5 minutes, the oscillation frequency is 320r / min, after standing still, separate the water phase and organic phase, and detect the extraction The pH value of the remaining liquid, the experimental results are shown in Table 2, where O / A is the volume ratio of the organic phase to the aqueous phase.

[0029] Table 2

[0030] Test No. O / A Raffinate contains C...

Embodiment 3

[0032] The components and properties of the copper-containing nitric acid solution are as follows: 26.51g / L Cu, 0.78g / L Co, 47.59g / L Zn, 4.72 g / L Cd, 165.44g / L calcium citrate, pH=4.50 .

[0033] According to the effective load rate of 30% LIX973N-kerosene extracting copper is calculated as 75% of the theoretical amount, add 30% LIX973N-kerosene extractant and copper-containing leachate to the separatory funnel according to the calculated ratio, and shake at room temperature for 5 minutes After standing still, after the organic phase and the water phase are completely separated, the water phase is released, the copper content in the water phase is analyzed, and the extraction rate of copper is calculated. The results are shown in Table 3:

[0034] table 3

[0035]

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Abstract

The invention belongs to the technical field of extraction and separation and particularly relates to a method for increasing extraction efficiency of copper in a water solution. The method particularly comprises the steps of: adding a citrate with mole number equivalent to that of copper in a copper-containing solution of a strong acid system or adding a neutralizing reagent in a copper citrate solution system, regulating pH of the solution to 1.5-5; preparing an oxime extracting agent into a required organic phase by using kerosene according to the difference of concentrations of the copper in the water solution; and mixing the organic phase with the copper-containing solution, stirring and extracting for realizing efficient extraction of the copper. According to the invention, by using the citrate as a pH buffer agent, acid generated in a water phase in an extraction process is buffered by citrate radicals, the activity of hydrogen ions in the solution is reduced, therefore, the continuous extraction of the copper is facilitated; and because the copper extraction efficiency is high and the extraction stage number is reduced, the investment, the occupation area and the operation and maintenance cost of equipment are greatly lowered in practical use,.

Description

technical field [0001] The invention belongs to the technical field of extraction and separation, and in particular relates to a method for improving copper extraction efficiency in aqueous solution. Background technique [0002] Copper is a metal with a wide range of uses, and its production process is mainly divided into two technologies: pyrometallurgy and hydrometallurgy. So far, pyrometallurgy technology accounts for about 80% of total copper production, while hydrometallurgy accounts for about 20% of copper production. Pyrochemical copper smelting is a traditional process, which requires beneficiation and enrichment of the mined copper ore, and a huge sulfuric acid production system, which is a big constraint when the sulfuric acid market shrinks. Copper hydrometallurgy is a copper smelting technology that appeared in the late 1960s. It has the advantages of low investment and short process. At present, it is mainly used for the recovery and utilization of oxidize...

Claims

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Application Information

Patent Timeline
05 Feb 2014
Publication
CN102864306B
IPC
C22B3/30; C22B15/00
CPC
Y02P10/20
Inventors
路殿坤; 金哲男