Method for comprehensive recovery and utilization of fluorine-containing alkali waste water

A technology of waste alkaline water and alkalinity, which is applied in metallurgical wastewater treatment, chemical instruments and methods, aluminum fluoride, etc., can solve the problems of effective treatment of ions, pollution, and simple conditions, so as to save the treatment process and cost of three wastes, reduce Production cost, saponification cost reduction effect

Inactive Publication Date: 2011-06-15
PEKING UNIV FOUNDER GRP CO LTD +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The second method is first acid-dissolving and then alkali-transforming. For example, the method in the Chinese invention patent with the publication number CN1683569A is that bastnaesite is dissolved with hydrochloric acid after oxidation and roasting, and the insoluble part is transformed by alkali. Re-dissolving in acid, by controlling the dissolution conditions of hydrochloric acid, the cerium-rich lanthanum feed solution with less cerium and the cerium oxide product with a purity of more than 95% can be obtained respectively; the method in the Chinese invention patent with the publication number CN1240759 is also alkali conversion after hydrochloric acid dissolution, and fluorine removal by washing with water. But the conditions are simple, and only a primary product of mixed rare earth chloride is obtained in the end
Existing methods generally can only deal with OH alone - or F - , it is difficult to effectively control these two ions at the same time, resulting in serious pollution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Detect that the alkalinity in the waste alkaline water is 1.5mol / L, and the 1m 3 The waste alkaline water and 2.8m 3 The P507 organic phase (used after being diluted with kerosene, sulfonated kerosene, etc., this technology is a well-known technology in the art) was mixed and stirred in the reactor for 1 minute, and the reaction temperature was 25 ° C, and the saponification of the organic phase was completed, and the saponification value was 0.54mol / L. OH- enters the organic phase, and the aqueous phase is NaF solution. The organic phase is saponified for extraction, and the aqueous phase is concentrated to obtain a NaF product with a purity of 98%.

Embodiment 2

[0030] Detect that the alkalinity in the waste alkaline water is 0.8mol / L, control the water phase and the naphthenic acid / isomeric acid organic phase according to the volume ratio of 1:2, mix and stir in the reactor for 5 minutes, and the reaction temperature is 40°C. The saponification of the organic phase is completed, and the saponification value is 0.4mol / L. Oh - Enter the organic phase, and the aqueous phase is NaF solution. The organic phase is saponified for extraction, and the aqueous phase is concentrated to obtain a NaF product with a purity of 99.1%. In this example, the naphthenic acid organic phase and the isomeric acid are mixed at a volume ratio of 1:1 (thinners such as kerosene and octanol need to be added during use, which is also a well-known technology in the art).

Embodiment 3

[0032] Detect that the alkalinity in the waste alkaline water is 1.0mol / L, and the 1m 3 waste alkaline water with 2.5m 3 The organic phase (P204 and P507 are mixed in a volume ratio of 1:1) was mixed and stirred in the reactor for 6 minutes, and the reaction temperature was 30° C., and the saponification of the organic phase was completed, and the saponification value was 0.4mol / L. The organic phase is saponified for extraction, and the water phase is then added with inorganic salts of Al and Na to accurately control the molar ratio of the added ions to form cryolite (Na 3 AlF 6 ) crystallization to transfer and recover F.

[0033] By adopting the method of the invention, compared with the existing ammonia water and sodium hydroxide saponification method, the cost can be reduced by half, and the discharge of fluorine-containing waste water is only 10% of the existing method, and the economic benefit and environmental protection effect are remarkable.

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Abstract

The invention relates to a waste fluoride-containing alkaline water processing method during the rare earth hydrometallurgy production process. The processing method can also achieve the purpose of the extractant saponification. After mixed with the organic phase, the waste fluoride-containing alkaline water generated during the rare earth hydrometallurgy production process undergoes saponification; the saponified organic phase is mixed with the solution waiting for extraction, and then the extraction separation and reextraction are conducted; the saponified water phase is used for the NaF orcryolite preparation. The invention has the advantages that by using the available and cheap waste alkaline water as the raw material, the saponification cost is reduced during the extraction separation; the fluorine ion in the wastewater can be recycled so as to reduce the environment pollution and save a lot of the three wastes processing cost.

Description

technical field [0001] The invention belongs to the field of metallurgy and chemical industry, and in particular relates to a treatment method for fluorine-containing waste alkaline water in the rare earth hydrometallurgy process. In particular, it relates to a method for comprehensive recovery and utilization of fluorine-containing waste alkaline water. Background technique [0002] Bastnaesite is a rare earth resource dominated by light rare earths, and its development and application are crucial to the application of rare earths. [0003] For the smelting method of bastnaesite, the hydrochloric acid decomposition process is the most widely used at present, and the sulfuric acid method is rarely used. Many literature reports on the hydrochloric acid method can be roughly divided into the following two types. A kind of is first alkali transfer and then acid dissolution, as the method disclosed in the Chinese invention patent CN1205363A is to mix and roast with alkali meta...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F1/26C01D3/02C01F7/54C02F101/14C02F103/16
Inventor 王嵩龄贾江涛廖春生严纯华
Owner PEKING UNIV FOUNDER GRP CO LTD
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