Method for removing aluminum from rare-earth feed liquid

A rare earth feed liquid and rare earth element technology, applied in the direction of improving process efficiency, can solve the problems of large rare earth loss, low aluminum removal efficiency, and many process links, and achieve high rare earth recovery rate, low aluminum removal cost, and equipment investment. less effect

Active Publication Date: 2012-08-15
广东省富远稀土有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

(2) Acid method: also known as oxalic acid precipitation method, adding oxalic acid into the rare earth solution, because the solubility of aluminum oxalate in the acidic solution is relatively large, so that the aluminum remains in the solution, this method has a good effect on removing aluminum and is suitable for separating a large amount of rare earth This method is generally used for the final step of feed liquid treatment. For the intermediate feed liquid, due to the complex conversion process, many process steps, high cost of impurity removal, large oxalate dissolution loss, and difficult oxalic acid wastewater treatment, it is not practical. significance
Thanks Al 3+ with RE 3+ The pH value at the beginning of hydrolysis is quite close, resulting in the simultaneous hydrolysis and precipitation of aluminum and rare earth, and the subsequent treatment of the resulting colloidal precipitate is very difficult
This method has low aluminum removal efficiency and large loss of rare earth, so the hydrolysis method cannot effectively remove aluminum
(4) Extraction method: The traditional extraction method is to use a volume ratio of 25% naphthenic acid-20% isooctyl alcohol-kerosene to form an organic phase, first add ammonia water or sodium hydroxide for saponification, and the saponification value is 0.35M, and then use a single Stir and mix the rare earth liquid with a pH value of 3.0 in a one-stage stirring tank or a multi-stage extraction tank, about 30% of the aluminum is extracted, but the extraction loss of the rare earth is more than 10%. , otherwise it will easily cause emulsification of the system and make the extraction process impossible

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] 2500L of neodymium chloride feed liquid after extraction and separation of mixed rare earths, concentration of rare earths 1.26mol / L, Al 2 o 3 It is 8232.2mg / L, and the neodymium oxide contained in the neodymium chloride feed solution is calculated to be 525.63Kg. First prepare the organic phase, the composition of the organic phase is 25% naphthenic acid-25% mixed alcohol-kerosene by volume, and add 5000L organic phase to 10M 3 In the stirring tank; add 2500L of neodymium chloride feed solution to the stirring tank, start stirring, and mix well; under stirring conditions, add 358L of ammonia water with a concentration of 6mol / L; after the ammonia water is added, continue stirring for 30 minutes and then stop stirring After standing still for 30 minutes to separate the phases, release the water phase, which is the neodymium chloride feed liquid after removing aluminum; under stirring conditions, the organic phase is regenerated by back extraction with a hydrochloric a...

Embodiment 2

[0017] 1250L of praseodymium chloride feed liquid after extraction and separation of mixed rare earths, concentration of rare earths 1.22 mol / L, Al 2 o 3 It is 2453mg / L, and the calculated praseodymium chloride feed liquid contains 259.56Kg of praseodymium oxide. First prepare the organic phase, the composition of the organic phase is 15% naphthenic acid-15% mixed alcohol-kerosene by volume, and add 5000L organic phase to 10M 3 In the stirring tank; add 1250L of praseodymium chloride feed liquid to the stirring tank, start stirring, and mix well; under stirring conditions, add 280L of sodium hydroxide solution with a concentration of 3mol / L; after adding the sodium hydroxide solution, continue After stirring for 30 minutes, stop stirring, let stand for 20 minutes, and then release the water phase, which is the praseodymium chloride feed liquid after aluminum removal; The hydrochloric acid solution is stripped and regenerated, the organic phase is recycled, and the stripped s...

Embodiment 3

[0020] 2000L of samarium chloride feed liquid after mixed rare earth extraction group separation, rare earth concentration 1.18mol / L, Al 2 o 3 It is 6723mg / L, and the calculated samarium chloride feed liquid contains 411.58Kg of samarium oxide. First prepare the organic phase, the composition of the organic phase is 20% naphthenic acid-20% isooctyl alcohol-kerosene by volume, and add 5000L organic phase to 10M 3 In the stirring tank; add 2000L of samarium chloride feed liquid to the stirring tank, start stirring, and mix well; under stirring conditions, add 460L of ammonium bicarbonate aqueous solution with a concentration of 3mol / L; after the ammonium bicarbonate aqueous solution is added, continue After stirring for 20 minutes, stop stirring, and let stand for 20 minutes to separate the phases, then release the water phase, which is the samarium chloride feed liquid after aluminum removal; The hydrochloric acid solution is stripped and regenerated, the organic phase is re...

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Abstract

The invention discloses a method for removing aluminum from rare-earth feed liquid, belongs to rare-earth feed liquid treatment technology and aims to provide the method for removing the aluminum from the rare-earth feed liquid, of which the aluminum-removing effect is good, the aluminum-removing cost is low, the rare-earth recovery rate is high, the operation and control are convenient, the process is simple and the investment in equipment is small. The key point of the technical scheme mainly comprises the following steps of: (1) preparing an organic phase from 15 to 25 volume percent of naphthenic acid and 15 to 25 volume percent of alcohol-kerosene; (2) adding the prepared organic phase and the rare-earth feed liquid into a stirring tank in a volume ratio of 2-5:1, starting the tank, stirring and uniformly mixing; (3) adding alkaline solution into the mixed liquid obtained in the step (2) with stirring, wherein the total number of moles of the added alkali is 50 to 100 percent of that of rare-earth elements in the rare-earth feed liquid; and (4) after adding the alkaline solution, continuously stirring for a certain time, stopping stirring and standing for a certain time, wherein the solution is separated into an aqueous phase and an organic phase and the aqueous phase is the rare-earth feed liquid from which the aluminum is removed. The method is applied to aluminum removal for the rare-earth feed liquid.

Description

technical field [0001] The invention relates to a treatment technology of rare earth material liquid, more specifically, it relates to a method for removing aluminum from rare earth material liquid. Background technique [0002] In ion-adsorption rare earth ores, rare earth elements are adsorbed on the surface of clay minerals in an ion state. When leaching ionic rare earth ores, a large amount of aluminum ions in clay minerals enter the leaching solution along with rare earths. In the preparation of concentrates of early ion-adsorption rare earth ores, oxalic acid was used to precipitate rare earths in the leaching solution, and a large number of non-rare earth impurities including aluminum were removed. However, in recent years, the oxalic acid precipitation process of ion-adsorption rare earth ore leachate has been gradually replaced by ammonium bicarbonate precipitation. Although the cost of concentrate preparation has been greatly reduced, the non-rare earth impurities...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/40C22B59/00
CPCY02P10/20
Inventor 凌诚刘志强杨金华韩旗英陈怀杰
Owner 广东省富远稀土有限公司
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