IP Library › Granted Patent US 8,177,881
Granted Patent B2
US 8,177,881 · App. 12/813,698 · Granted May 15, 2012

Method for extracting and separating rare earth elements

Assignees: Shin-Etsu Chemical Co., Ltd.; Japan Atomic Energy Agency
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,177,881
App. No.
12/813,698
Granted
May 15, 2012
Kind
B2
Abstract

Solvent extraction from an aqueous phase containing first and second rare earth elements is carried out by contacting an organic phase containing a diglycolamic acid as an extractant and a hydrocarbon or a low-polar alcohol as a solvent, with the aqueous phase below pH 3 for extracting the first rare earth element into the organic phase, back-extracting from the organic phase with an aqueous acid solution for recovering the first rare earth element, and recovering the second rare earth element which has not been extracted into the organic phase and has remained in the aqueous phase.

Claims (34)

1. A method for extracting and separating rare earth elements, comprising the steps of:

contacting an organic phase containing a diglycolamic acid having the general formula (1):

wherein R 1 and R 2 are alkyl groups independent of each other, at least one of R 1 and R 2 is a straight or branched alkyl group of at least 6 carbon atoms as an extractant and an organic solvent with an aqueous phase containing at least first and second rare earth elements under acidic conditions of pH 3 or below, for extracting the first rare earth element into the organic phase,

back-extracting from the organic phase with an aqueous acid solution for recovering the first rare earth element once extracted into the organic phase, and

recovering the second rare earth element which has not been extracted into the organic phase and has remained in the aqueous phase, wherein

provided that C 0 is a concentration of the diglycolamic acid extractant in the organic phase and C A is a concentration of rare earth elements in the aqueous phase, the extraction step is effected under the condition that a ratio of C 0 to C A is 2≦C 0 /C A ≦10 and C 0 is 0.1 mol/L≦C 0 ≦1.5 mol/L.

2. The method of claim 1 wherein C A is 0.01 mol/L≦C A ≦0.7 mol/L.

3. The method of claim 1 wherein the extraction and back-extraction steps are performed in a counter-current flow multistage mixer-settler.

4. The method of claim 1 wherein the step of contacting the organic phase with the aqueous phase is at a temperature lower than the flash point of a solvent used in the organic phase.

5. The method of claim 1 wherein the rare earth elements contained in the aqueous phase are at least two of light rare earth elements La, Ce, Pr, Nd, Sm, and Eu, or at least one of the light rare earth elements and at least one of other rare earth elements inclusive of Y.

6. The method of claim 1 wherein the rare earth elements contained in the aqueous phase are Nd and Pr, and in the extraction step, Nd is extracted into the organic phase while Pr remains in the aqueous phase, whereby Nd and Pr are separated.

7. A method for extracting and separating rare earth elements, comprising the steps of:

contacting an organic phase containing a diglycolamic acid having the general formula (1):

wherein R 1 and R 2 are alkyl groups independent of each other, at least one of R 1 and R 2 is a straight or branched alkyl group of at least 6 carbon atoms as an extractant and a low-polar alcohol having the general formula (2):

C n H 2n+1 OH  (2)

wherein n is an integer of 5 to 8 as a solvent, with an aqueous phase containing at least first and second rare earth elements under acidic conditions of pH 3 or below, for extracting the first rare earth element into the organic phase,

back-extracting from the organic phase with an aqueous acid solution for recovering the first rare earth element once extracted into the organic phase, and

recovering the second rare earth element which has not been extracted into the organic phase and has remained in the aqueous phase.

8. The method of claim 7 wherein the extraction and back-extraction steps are performed in a counter-current flow multistage mixer-settler.

9. The method of claim 7 wherein the step of contacting the organic phase with the aqueous phase is at a temperature lower than the flash point of the low-polar alcohol used in the organic phase.

10. The method of claim 7 wherein the rare earth elements contained in the aqueous phase are at least two of light rare earth elements La, Ce, Pr, Nd, Sm, and Eu, or at least one of the light rare earth elements and at least one of other rare earth elements inclusive of Y.

11. The method of claim 7 wherein the rare earth elements contained in the aqueous phase are Nd and Pr, and in the extraction step, Nd is extracted into the organic phase while Pr remains in the aqueous phase, whereby Nd and Pr are separated.

12. The method of claim 7 wherein a concentration of rare earth elements in the aqueous phase, C A is 0.01 mol/L≦C A ≦0.7 mol/L.

13. A method for extracting and separating rare earth elements, comprising the steps of:

contacting an organic phase containing a diglycolamic acid having the general formula (1):

wherein R 1 and R 2 are alkyl groups independent of each other, at least one of R 1 and R 2 is a straight or branched alkyl group of at least 6 carbon atoms as an extractant and an organic solvent with an aqueous phase containing at least first and second rare earth elements under acidic conditions of pH 3 or below, for extracting the first rare earth element into the organic phase,

back-extracting from the organic phase with an aqueous acid solution for recovering the first rare earth element once extracted into the organic phase, and

recovering the second rare earth element which has not been extracted into the organic phase and has remained in the aqueous phase, wherein

the organic phase resulting from the step of back-extracting from the organic phase with an aqueous acid solution for recovering the rare earth element once extracted into the organic phase is washed with water or an aqueous acid solution at pH 3 to 7 and reused in the extraction step.

14. The method of claim 13 wherein the extraction and back-extraction steps are performed in a counter-current flow multistage mixer-settler.

15. The method of claim 13 wherein the step of contacting the organic phase with the aqueous phase is at a temperature lower than the flash point of a solvent used in the organic phase.

16. The method of claim 13 wherein the rare earth elements contained in the aqueous phase are at least two of light rare earth elements La, Ce, Pr, Nd, Sm, and Eu, or at least one of the light rare earth elements and at least one of other rare earth elements inclusive of Y.

17. The method of claim 13 wherein the rare earth elements contained in the aqueous phase are Nd and Pr, and in the extraction step, Nd is extracted into the organic phase while Pr remains in the aqueous phase, whereby Nd and Pr are separated.

18. The method of claim 13 wherein a concentration of rare earth elements in the aqueous phase, C A is 0.01 mol/L≦C A ≦0.7 mol/L.

Assignments (3)
CHANGE OF ADDRESS Recorded Sep 11, 2023
From: SHIN-ETSU CHEMICAL CO., LTD.
To: SHIN-ETSU CHEMICAL CO., LTD.
Reel/Frame 064854/0128 →
NUNC PRO TUNC ASSIGNMENT Recorded Sep 11, 2023
From: JAPAN ATOMIC ENERGY AGENCY
To: SHIN-ETSU CHEMICAL CO., LTD.
Reel/Frame 064854/0706 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 15, 2010
From: SUGAHARA, HIROTO; SAKAKI, KAZUAKI; MINOWA, TAKEHISA; NAGANAWA, HIROCHIKA; SHIMOJO, KOJIRO
To: SHIN-ETSU CHEMICAL CO., LTD.; JAPAN ATOMIC ENERGY AGENCY
Reel/Frame 024537/0394 →
Priority Claims (3)
JP 2009-144426 · Jun 17, 2009 · national
JP 2009-144445 · Jun 17, 2009 · national
JP 2009-144457 · Jun 17, 2009 · national
Continuity (1)
Related Publication 20100319491A1 · Dec 23, 2010