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Method for removing sulfate radicals in rare earth precipitates and products obtained by the method

A sediment and sulfate technology, applied in the direction of improving process efficiency, etc., can solve the problems of restricting the effective utilization and development of rare earth materials, increasing the energy consumption of rare earth materials, etc., and achieve the effects of reducing energy consumption, improving purity, and simplifying the process flow

Active Publication Date: 2021-08-10
CHINA ENFI ENGINEERING CORPORATION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Firstly, the toxic and harmful substance barium chloride is introduced into the precipitation, and secondly, a large amount of secondary waste barium sulfate will be produced
At the same time, in order to improve the purity of rare earth precipitates, it is necessary to increase the roasting temperature, which leads to an increase in energy consumption for the preparation of rare earth materials, which seriously restricts the effective utilization and development of rare earth materials.

Method used

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  • Method for removing sulfate radicals in rare earth precipitates and products obtained by the method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031]The pretreated rare earth precipitate is prepared into a rare earth solution with a sulfate content of 0.75 mol / l. At 80°C, add a certain amount of ammonium sulfate dispersant, and under the stirring condition of 100r / min, continuously add oxalate precipitant to the reactor according to the molar ratio of rare earth ion to precipitant is 1:2, during the same time Constantly use ammonium salt to adjust the pH value of the system, so that the pH value of the reaction system is maintained at about 1.5. After adding the precipitant, ensure that the final pH value of the system is about 1.5, then continue to stir at a stirring speed of 100r / min for 30min, and age the reaction at 80°C for 60min after the reaction is completed. The obtained precipitated system was subjected to suction filtration, during which water and ethanol were used to wash 3 times and 5 times respectively. A certain amount of hydrochloric acid is used to dissolve the rare earth precipitate sample, the rar...

Embodiment 2

[0033] The pretreated rare earth precipitate is formulated into a rare earth-containing solution with a sulfate content of 1.5 mol / l. At 95°C, add a certain amount of ammonium sulfate dispersant, and under the stirring condition of 200r / min, continuously add oxalate precipitant to the reactor according to the molar ratio of rare earth ion and precipitant at 1:2, during the same time Constantly use ammonium salt to adjust the pH value of the system, so that the pH value of the reaction system is maintained at about 3. After adding the precipitating agent, ensure that the final pH value of the system is about 3, and then continue to stir at a stirring speed of 100r / min for 90min. After the reaction is completed, the reaction is aged at 95°C for 180min. The obtained precipitated system was subjected to suction filtration, during which water and ethanol were used to wash 3 times and 5 times respectively. A certain amount of hydrochloric acid is used to dissolve the rare earth pre...

Embodiment 3

[0035] The pretreated rare earth precipitate is formulated into a rare earth solution containing 1.0 mol / l of sulfate. At 75°C, add a certain amount of ammonium sulfate dispersant, and under the stirring condition of 200r / min, continuously add oxalate precipitant to the reactor according to the molar ratio of rare earth ion and precipitant at 1:2, during the same time Constantly use ammonium salt to adjust the pH value of the system to maintain the pH value of the reaction system at about 2. After adding the precipitating agent, ensure that the final pH value of the system is about 2, and then continue to stir at a stirring speed of 100r / min for 90min. After the reaction is completed, the reaction is aged at 75°C for 90min. The obtained precipitated system was subjected to suction filtration, during which water and ethanol were used to wash 3 times and 5 times respectively. A certain amount of hydrochloric acid is used to dissolve the rare earth precipitate sample, the rare e...

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Abstract

Disclosed is a method for removing sulfate radicals in rare earth precipitates, comprising: a solution forming step, preparing a pretreated rare earth precipitate into a solution containing sulfate ions and rare earth ions; a precipitation step, adding oxalate as a precipitant to A precipitation reaction is carried out in the solution to obtain a precipitate; and a purification step is to dissolve the precipitate with hydrochloric acid, and then carry out secondary precipitation with carbonate as a precipitating agent. The method of the invention effectively improves the purity of rare earth oxides; simplifies the process flow of rare earth precipitate purification; reduces energy consumption; and avoids the generation of waste residue and solid waste.

Description

technical field [0001] The invention relates to the field of hydrometallurgy, in particular to a method for removing sulfate radicals in rare earth precipitates and a product obtained by the method. Background technique [0002] Precipitation is an indispensable separation and purification method in the production of the metallurgical industry. In fact, almost all hydrometallurgical processes will have a precipitation process. It has the characteristics of simple operation, low cost, and low investment. Precipitation is a method of taking appropriate measures to supersaturate the solute in the solution and separate it after precipitation in solid form. With the continuous improvement of product quality requirements, the requirements for the impurity content in the sediment are also continuously improved. When extracting rare earth elements, it is of great significance to realize the effective separation of rare earth elements and impurity elements. The separation of rare e...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/44C22B1/02C22B59/00
CPCC22B1/02C22B3/44C22B59/00Y02P10/20
Inventor 付国燕李诺王玮玮李晓艳刘召波
Owner CHINA ENFI ENGINEERING CORPORATION