Two-feeding-opening fully-loaded rare earth fractional extraction separation process method

A technology of two feed inlets and a process method is applied in the field of hydrochloric acid extractant to achieve the effects of improving the degree of greening, reducing the separation cost and increasing the concentration

Inactive Publication Date: 2015-04-29
NANCHANG HANGKONG UNIVERSITY
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] The purpose of the present invention is to propose a kind of process method of separating rare earths by fractional distillation extraction with full load of two feed ports for the side effects of hydrogen ion washing in the existing two-feed inlet rare earth fractionation extraction, so as to eliminate the side effects of hydrogen ion washing and reduce the rare earth Separation of acid and alkali consumption, improve the efficiency of fractionation and extraction stage at the second feed port, and reduce the cost of rare earth separation

Method used

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  • Two-feeding-opening fully-loaded rare earth fractional extraction separation process method

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Effect test

Embodiment 1

[0027] Fractional distillation extraction with full load at the second feed port ~ Nd / Sm ~ group separation of monazite rare earth ore and medium yttrium and europium rich ore

[0028] 1) Rare earth liquid

[0029] The first rare earth feed solution is an aqueous chloride solution of monazite rare earth ore, the rare earth concentration is 1.2 M, the pH value is 3, the molar fraction of light rare earth La to Nd is 0.95, and the molar fraction of medium and heavy rare earth Sm to Lu and Y is 0.05.

[0030] The second rare earth feed solution is a rare earth chloride aqueous solution of medium yttrium and europium-rich ore. The mole fraction is 0.45.

[0031] The molar ratio of feed amount of medium yttrium and europium-rich ore liquid to monazite rare earth ore liquid is 1:1.

[0032] 2) Rare earth extraction organic phase

[0033] The rare earth extraction organic phase is a kerosene solution of P507, and the volume percentage concentration of P507 is 36%; it is added to ...

Embodiment 2

[0048] Fractional distillation extraction with full load at the second feed port~Nd / Sm~Group separation of bastnaesite and medium yttrium-europium-enriched ore

[0049] 1) Rare earth liquid

[0050] The first rare earth feed solution is bastnaesite chloride aqueous solution, its rare earth concentration is 1.5 M, pH value is 4, the mole fraction of light rare earth La~Nd is 0.98, and the mole fraction of medium and heavy rare earth Sm~Lu and Y is 0.02.

[0051] The second rare earth feed solution is a rare earth chloride aqueous solution of medium yttrium and europium-rich ore. The mole fraction is 0.45.

[0052] The molar ratio of feed amount of middle yttrium and europium-rich ore liquid to bastnaesite feed liquid is 1:2.

[0053] 2) Rare earth extraction organic phase

[0054] The rare earth extraction organic phase is a kerosene solution of P507, and the volume percentage concentration of P507 is 35%; it is added to the fractionation extraction system in the form of li...

Embodiment 3

[0069] Separation of Terbium and Dysprosium by Fractional Distillation Extraction of Tb / Dy with Two Feed Inlets

[0070] 1) Rare earth liquid

[0071] The first rare earth feed liquid is an aqueous solution of terbium-dysprosium chloride, the rare earth concentration is 1.0 M, the pH value is 5, the mole fraction of terbium (Tb) is 0.60, and the mole fraction of dysprosium (Dy) is 0.40.

[0072] The second rare earth feed liquid is an aqueous solution of terbium-dysprosium chloride, the rare earth concentration is 1.0 M, the pH value is 3, the mole fraction of terbium (Tb) is 0.40, and the mole fraction of dysprosium (Dy) is 0.60.

[0073] The molar ratio of the feed amount of the second rare earth feed liquid to the first rare earth feed liquid is 1:1.

[0074] 2) Rare earth extraction organic phase

[0075] The organic phase of rare earth extraction is sulfonated kerosene solution of P507, and the concentration of P507 is 30% by volume; it is added to the fractionation ext...

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Abstract

The invention discloses a two-feeding-opening fully-loaded rare earth fractional extraction separation process method. According to the method, P507 serves as a rare earth extracting agent; in a two-feeding-opening fractional extraction separation process, an acid extraction section which takes N235 as an acid extracting agent and takes trioctyl phosphate as an N235 organic phase demulsifying agent is arranged, and the side effect of hydrogen ions can be eliminated through the acid extracting effect of the N235, so that not only is the rare earth separation coefficient not reduced, but also the extracting amount of rare earth in a two-feeding-opening fractional extraction system is not lower than the saponification amount of the rare earth. Compared with the existing two-feeding-opening fractional extraction process, the consumption of acid and alkali in a rare earth separation process can be greatly reduced, wherein the consumption amount of an alkaline reagent is reduced by 39 to 51 percent, and the consumption amount of hydrochloric acid can be reduced by 17 to 26 percent; the waste water discharging amount in the rare earth extraction separation process is greatly reduced; the green degree of rare earth separation is greatly improved; the stage number of extracting tanks can be reduced by 32 to 38 percent; the total investment of the rare earth extraction separation process is reduced. Therefore, the separation cost is remarkably reduced.

Description

technical field [0001] The invention relates to a process method for separating rare earths through full-load fractionation extraction at two feed ports, in particular to using 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (usually abbreviated as P507) as rare earth extractant and tertiary amine N235 as hydrochloric acid extraction A fractional distillation extraction system is used to process two kinds of chlorinated mixed rare earth feed liquids, and the rare earth extraction amount of the fractional distillation extraction system is not lower than the saponification amount of the rare earth. The invention belongs to the field of solvent extraction in hydrometallurgy. Background technique [0002] Because rare earth elements have unique physical and chemical properties, they have become the cradle of modern new materials; however, rare earth elements are a group of symbiotic and difficult to separate elements, so the separation of rare earth elements has always been ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/38C22B3/40C22B59/00
CPCY02P10/20
Inventor 钟学明
Owner NANCHANG HANGKONG UNIVERSITY
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