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Method for extracting gallium from fly ash on basis of resin method

A technology of fly ash and resin, which is applied to the improvement of process efficiency, photography technology, instruments, etc., can solve the problems of high alkali consumption, high cost, poor adsorption effect, etc., to reduce the absolute amount, realize extraction and recovery, The effect of reducing dosage

Active Publication Date: 2020-10-16
SHENHUA ZHUNNENG RESOURCE COMPREHENSIVE DEV COMPANY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

At present, some methods of extracting gallium have been disclosed. For example, Chinese patent CN 102191384A "A method for extracting gallium from fly ash" discloses a method for extracting gallium from fly ash in a circulating fluidized bed. Using cation exchange resin to directly recover gallium from the acid leaching solution, this method needs to precipitate all the iron ions in the solution, and the alkali consumption is high; another example, the patent CN 104018012A "a method for extracting gallium from aluminum chloride solution" A method for extracting gallium from an aluminum chloride solution is disclosed. In the method, an iron ion masking agent is first added to the pickling solution to reduce iron ions, and then gallium is recovered through an anion exchange resin. The iron ion masking agent can be sodium sulfite, ascorbic acid , iron powder, etc.; at room temperature, the amount of ascorbic acid used is large and the cost is high, and the ascorbic acid reduction solution is not stable enough when heated, the reduction is not complete when sodium sulfite is used, and the adsorption effect of gallium is poor. When iron powder is used for reduction, gallium is extracted while A large amount of ferrous chloride solution (twice the iron content in the original solution) is produced, which increases the difficulty of waste liquid treatment

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  • Method for extracting gallium from fly ash on basis of resin method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] (1) Separation and preparation of gallium extraction stock solution by resin method

[0053] Pass the crude semen into the strongly basic anion exchange resin (removing iron resin) of model LSC-Fe, the flow rate of the crude semen is 2BV / h, and the adsorption temperature is 70°C. Fe 3+ , Ga 3+ At the same time, it is adsorbed by the resin, and the concentration of ferric chloride and gallium chloride in the refined iron removal solution obtained after adsorption is 0.04g / L, and the concentration of gallium chloride is 0.01g / L, which is used in the subsequent alumina process. After the adsorption is completed, wash the iron-removing resin with 1% hydrochloric acid. The flow rate of the washing liquid is 1BV / h, and the temperature is normal temperature. / L. Evaporating and concentrating the eluent from the iron removal resin, the ferric chloride concentration in the obtained concentrated solution is 405g / L, and the gallium chloride concentration is 2.0g / L, which is the...

Embodiment 2

[0063] (1) Preparation of gallium extraction stock solution by resin method

[0064] According to the method of Example 1, the gallium extraction stock solution is obtained, the difference is that the strong basic anion exchange resin of 201×7 is used as the iron removal resin, and the ferric chloride concentration in the gallium extraction stock solution of the gained is 400g / L, gallium chloride concentration It is 1.60g / L.

[0065] (2) Separation and enrichment of gallium by resin method

[0066] Pass the gallium extraction stock solution into the gallium extraction resin of type 4-APR, the flow rate is 0.8BV / h, and the temperature is normal temperature. The ferric chloride concentration in the gallium-extracting solution obtained after adsorption is 378g / L, and the gallium chloride concentration is 0.007g / L. After the adsorption was completed, the gallium resin was washed with 0.7mol / L sulfuric acid, and the washing liquid flow rate was 1BV / h, and the temperature was norm...

Embodiment 3

[0074] (1) Preparation of gallium extraction stock solution by resin method

[0075] According to the method of Example 1, the gallium extraction stock solution is obtained, the difference is that the strong basic anion exchange resin of 201×4 is used as the iron removal resin, and the ferric chloride concentration in the obtained gallium extraction stock solution is 380g / L, and the concentration of gallium chloride is 380g / L. It is 1.3g / L.

[0076] (2) Separation and enrichment of gallium by resin method

[0077] Pass the gallium extraction stock solution into the gallium extraction resin of type 4-APR, the flow rate is 0.6BV / h, and the temperature is normal temperature. The ferric chloride concentration in the gallium-extracting solution obtained after adsorption is 360 g / L, and the gallium chloride concentration is 0.005 g / L. After the adsorption was completed, the gallium resin was washed with 0.5mol / L nitric acid, and the washing liquid flow rate was 1BV / h, and the temp...

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Abstract

The invention provides a method for extracting gallium from fly ash on the basis of a resin method. An acid leaching solution obtained after acid leaching treatment of the fly ash is used as a raw material, the method includes the steps of preparation of a gallium extracting stock solution with the resin method, separation and enrichment of the gallium with the resin method, neutralization for removal of iron, transformation for deposition of the gallium, solution making and purification, electrolytic deposition and the like, and thus the gallium is extracted from the fly ash. Compared with existing technologies, the method has the advantages that the method is based on the resin method, the use amount of reagents such as alkaline liquor and the like are obviously reduced, additional reagents such as an iron masking agent, a reducing agent and the like are not required to be used, production of a lot of waste water is avoided, the method is economical and environment-friendly, and theextraction efficiency of the gallium is substantially improved. The method is stable in technology, reliable in running and controllable in cost and is a novel gallium extracting technology having thegreat application prospect.

Description

technical field [0001] The invention relates to the field of hydrometallurgy, in particular to a method for extracting gallium from fly ash based on a resin method. Background technique [0002] Gallium is an important scattered metal. With the deepening of the international mining structure, the development and utilization of scattered metals is being raised to a strategic level by many countries. At present, the output of primary gallium in the world is about 300t / a, and the recycling level is extremely low. Due to the associated relationship, if the output is not increased, there will be a serious shortage in the next 20 to 30 years. [0003] Gallium is mainly dispersed in bauxite, lead-zinc ore, coal, copper, and iron ore, with an average content of about 50 μg / g. At present, about 90% of gallium in the world is recovered from the alumina production process. In recent years, the extraction of alumina from fly ash has become a research and development hotspot. The conten...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B58/00C22B7/00C25C1/22
CPCC22B58/00C22B7/007C25C1/22Y02P10/20
Inventor 王永旺徐靓赵宇航陈东张云峰李超赵飞燕郭志峰范培育
Owner SHENHUA ZHUNNENG RESOURCE COMPREHENSIVE DEV COMPANY
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