Method of preventing interphase impurity in vanadium-chromium extraction separation process

A technology for separation process and interface contamination, applied in the direction of improving process efficiency, etc., can solve the problems such as inability to circulate extraction-stripping, incomplete separation of vanadium and chromium, prolonging phase separation time, etc., and achieve good vanadium and chromium separation effect and extraction. Good separation effect and the effect of eliminating interface dirt

Active Publication Date: 2013-09-18
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The appearance of dirt at the interface during the extraction process will bring many adverse effects to the entire extraction process. It will seriously prolong the phase separation time, make the separation of vanadium and chromium incomplete, and cause the loss of extraction agent, increase production costs, and seriously Otherwise, the entire workshop will be shut down, making the extraction-stripping cycle impossible
However, dealing with interface fouling is a more challenging problem, because there are many influencing factors of interfacial fouling, such as aqueous phase composition, organic phase composition, external environment and the type of agitator will all promote the system to generate interfacial fouling, and interfacial fouling It is a stable heterogeneous emulsification system, its composition will be different with the change of the system, even in the same system, the composition of the interface dirt produced at different times is different, which is the interface dirt The elimination of the
[0005] Chinese patent CN1048889A discloses a preventive method involving interface emulsification in the separation and purification process of metal yttrium, which is characterized in that sulfide and chloride precipitants are used to remove impurities before extraction; The emulsified layer is settled and centrifuged, and then the different substances in the emulsified layer are separated; CN202671624U utility model patent discloses a device for efficiently separating the emulsified layer; CN101565776A discloses a method for eliminating emulsions in the extraction system of amines and phosphorus, Its feature is to add metal cleaning aids with brand names of CSP-925, CSQ-926 or GEA-746 in the extracted liquid in advance, and extract after stirring, settling, and filtering to remove impurities under certain conditions; US Patent US6500232 also The method of eliminating the interface dirt in the solvent extraction process has been reported, and the patent provides a special device to remove the interface dirt in the extraction process, although this method of separating the emulsified layer is suitable for the elimination of interface dirt in various systems , but it is necessary to add another equipment and an operation, which will increase the operating cost, and it cannot fundamentally eliminate the interface dirt, but only solve the problem to ensure the normal operation of the process
[0007] Based on the above mechanism research, the prevention method of the interface dirt of the system is put forward in a targeted manner. At present, there are no relevant literature reports at home and abroad.

Method used

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  • Method of preventing interphase impurity in vanadium-chromium extraction separation process
  • Method of preventing interphase impurity in vanadium-chromium extraction separation process
  • Method of preventing interphase impurity in vanadium-chromium extraction separation process

Examples

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Embodiment 1

[0020] Taking the material liquid after deep removal of impurities in the chromium-containing vanadium slag leachate as the extraction liquid, the organic phase was prepared with the primary amine N1923, the tertiary amine TOA, the demulsifier with the commodity number PAG, and the diluent cyclohexane, and the extraction and separation test was carried out. The pH values ​​of the feed liquid were adjusted to 3.20, 4.20, 5.20, and 6.00, the volume percentage concentration of the extraction agent primary amine was selected as 15%, the volume percentage concentration of the tertiary amine was 5%, the volume percentage concentration of the demulsifier was 1%, and the extraction temperature was room temperature 25 °C, mix the aqueous phase and the organic phase in a separatory funnel, then fix the separatory funnel on a Conrad shaker and shake for 15 minutes, remove the shaker and let the layers stand for 30 minutes, then take out the gap between the aqueous phase and the organic pha...

Embodiment 2

[0025]The material liquid after deep removal of impurities in the chromium-containing vanadium slag leaching liquid is used as the extraction liquid, and the organic phase is prepared with the primary amine N1923, the tertiary amine TOA, the demulsifier and the diluent cyclohexane, and the extraction and separation test is carried out. The volume percentage concentration of the demulsifier PAG 0.3%, 0.5%, 1%, and 1.5%, respectively, wherein the pH value of the feed liquid is adjusted to 5.20, the volume percentage concentration of the extraction agent primary amine is 15%, the volume percentage concentration of the tertiary amine is 5%, and the extraction temperature is room temperature 25°C. Mix the aqueous phase and the organic phase in a separatory funnel, then fix the separatory funnel on a Conrad shaker for 15 minutes, remove the shaker and let the layers stand for 30 minutes, then take out the interface between the aqueous phase and the organic phase Dirt, use a graduated...

Embodiment 3

[0030] Taking the material liquid after deep removal of impurities in the chromium-containing vanadium slag leachate as the extraction liquid, the organic phase was prepared with the primary amine N1923, the tertiary amine TOA, the demulsifier with the commodity number PAG, and the diluent cyclohexane, and the extraction and separation test was carried out. The diluents are kerosene, toluene, n-octanol, and cyclohexane respectively, the pH value of the feed liquid is adjusted to 5.20, the volume percentage concentration of the extractant is 15%, the volume percentage concentration of the tertiary amine is 5%, and the extraction temperature is room temperature 25°C. Mix the aqueous phase and the organic phase in a separatory funnel, then fix the separatory funnel on a Conrad shaker for 15 minutes, remove the shaker and let the layers stand for 30 minutes, then take out the interface between the aqueous phase and the organic phase Dirt, use a graduated cylinder of appropriate spe...

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Abstract

The invention discloses a method of preventing interphase impurity in a vanadium-chromium extraction separation process. The method is characterized by comprising the following steps of: deeply removing impurities in an extracted solution before extraction, such as phosphorus, silicon, calcium, iron, and the like; extracting the purified extracted solution through a mixed solution of an efficient composite amine extracting agent, a demulsifier and a thinner, regulating the pH of the extracted solution, controlling the extraction temperature, the extraction time, the concentration of the extracting agent and the concentration of the demulsifier in the extraction process. According to the method, solid particles possibly generating emulsification in the solution are deeply removed and the demulsifier is added to reduce the emulsification interphase stability when the extraction is finished so as to reduce the probability of inorganic salts in crystallizing on the interphase to form solid interphase membranes. The method can effectively eliminate the interphase impurity in the vanadium-chromium extraction separation process, improve the extraction equilibrium phase splitting speed, reduce the organic phase loss, save the operating cost and ensure the long-term circulation of the extraction system.

Description

technical field [0001] The invention belongs to the field of interface dirt prevention in metal extraction, and in particular relates to a method for preventing interface dirt from occurring in the extraction and separation process of vanadium and chromium. Background technique [0002] With the continuous deepening of environmental protection awareness, the recycling of toxic and harmful substances has become a research hotspot in current scientific research. Heavy metal resources, especially the mining of low-grade ores and the recovery and recycling of a large number of heavy metals have attracted more and more attention. Chromium-containing vanadium slag contains a large amount of rare metals vanadium and chromium. If it is not properly treated, it will pose a great threat to the ecological environment and people's health. Therefore, the vanadium and chromium in it are separated and recovered for recycling. deep meaning. [0003] The separation of vanadium and chromium...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/28C22B34/22C22B34/32
CPCY02P10/20
Inventor 宁朋歌曹宏斌张懿
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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