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A kind of rare earth saponification method of acidic phosphorus extractant p204

A saponification and rare earth technology, applied in the field of rare earth solvent extraction, can solve the problems of increasing the production cost of rare earth separation, increasing the complexity of the separation process, prolonging the length of the rare earth separation production process, etc., and achieving the effects of saving energy, reducing production costs, and improving purity

Inactive Publication Date: 2017-08-04
NANCHANG HANGKONG UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The result is to extend the length of the rare earth separation production process, increase the complexity of the separation process, and increase the production cost of rare earth separation

Method used

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  • A kind of rare earth saponification method of acidic phosphorus extractant p204

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] Control the molar ratio of rare earth chloride to P204 to be 0.12:1, the ratio of the total exchange moles of chloride ions (i.e. the total exchange capacity) of hydroxide type weakly basic styrene-based anion exchange resin to the moles of rare earth chloride 6:1; in a 1000L saponification reactor, add 500L of P204 sulfonated kerosene solution with a concentration of 1.0M, 60L of a rare earth chloride aqueous solution with a pH of 3 and a rare earth concentration of 1.0M, and the effective exchange capacity for chloride ions is 4mol / kg and average particle diameter are 90kg (dry weight) of hydroxide type weakly basic styrene-based anion exchange resin of 0.5mm. After fully stirring at room temperature for 30 min, the layers were separated. The upper layer is the rare earth saponified P204 organic phase, the middle layer is the water phase, and the lower layer is the solid weakly basic styrene anion exchange resin phase; the water phase and the weakly basic styrene ani...

Embodiment 2

[0018] Control the molar ratio of rare earth chloride to P204 to be 0.15:1, and the ratio of the total exchange moles of chloride ions (that is, the total exchange capacity) of the hydroxide-type weakly basic styrene-based anion exchange resin to the moles of rare earth chloride 7.5:1; in the 1000L saponification reactor, add 500L of P204 kerosene solution with a concentration of 0.5M, 75L of rare earth chloride aqueous solution with a pH of 4 and a rare earth concentration of 0.5M, and the effective exchange capacity for chloride ions is 3mol / kg and 93.75 kg (dry weight) of hydroxide-type weakly basic styrene-based anion exchange resin with an average particle diameter of 0.6 mm; after fully stirring at room temperature for 40 min, leave to stand and separate. The upper layer is the rare earth saponified P204 organic phase, the middle layer is the water phase, and the lower layer is the solid weakly basic styrene anion exchange resin phase; the water phase and the weakly basic...

Embodiment 3

[0020] Control the molar ratio of rare earth chloride to P204 to be 0.1:1, and the ratio of the total exchange moles of chloride ions (that is, the total exchange capacity) of the hydroxide-type weakly basic styrene-based anion exchange resin to the moles of rare earth chloride 4.5:1; in a 1000L saponification reactor, sequentially add 500L of P204 kerosene solution with a concentration of 1.5M, 50L of a rare earth chloride aqueous solution with a pH of 2 and a rare earth concentration of 1.5M, and the effective exchange capacity for chloride ions is 5mol / kg and 67.5 kg (dry weight) of hydroxide-type weakly basic styrene-based anion exchange resin with an average particle size of 0.4 mm; after fully stirring at room temperature for 20 min, stand to separate into layers. The upper layer is the rare earth saponified P204 organic phase, the middle layer is the water phase, and the lower layer is the solid weakly basic styrene anion exchange resin phase; the water phase and the we...

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Abstract

The invention discloses a rare earth saponification method of an acidic phosphorus extractant P204, which uses a hydroxide type weakly basic styrene anion exchange resin as an auxiliary agent to realize the metal saponification of the acidic phosphorus extractant P204. In the saponification reactor, P204 kerosene or sulfonated kerosene solution, rare earth chloride aqueous solution and hydroxide type weakly basic styrene anion exchange resin were sequentially added; after fully stirring at room temperature, the reaction was completed and left to stand for stratification. The upper layer is a rare earth saponified P204 organic phase of an acidic extractant, the middle layer is an aqueous phase, and the lower layer is a solid weakly basic styrene-based anion exchange resin phase. The water phase and the styrene-based anion exchange resin phase are released to obtain a rare earth saponified P204 organic phase with a saponification rate of 30% to 45%. The invention has the advantages of improving product purity, reducing production cost, saving energy and the like.

Description

technical field [0001] The invention relates to a preparation method for saponifying an organic phase with an acidic extractant, in particular to a rare earth saponification method for an acidic phosphorus extractant P204 with a hydroxide-type weakly basic styrene-based anion exchange resin as an auxiliary agent. The invention specifically belongs to the technical field of rare earth solvent extraction. Background technique [0002] Solvent extraction is one of the important methods for separating non-ferrous metal elements such as rare earths. Di(2-ethylhexyl)phosphoric acid (commonly referred to as P204 in industry) is one of the commonly used extractants and is widely used in the separation of non-ferrous metal elements such as rare earth elements. [0003] In the specific extraction and separation process, in order to obtain higher extraction efficiency, it is usually necessary to use alkaline reagents to saponify P204. At present, the saponification agents used in rar...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/38C22B59/00
CPCC22B59/00C22B3/37Y02P10/20
Inventor 钟学明
Owner NANCHANG HANGKONG UNIVERSITY