Systems for recovering rare earth elements

Patent metadata

Field	Value
Publication number	US-10196709-B2
Application number	US-201615147985-A
Country	US
Kind code	B2
Filing date	May 6, 2016
Priority date	Mar 15, 2013
Publication date	Feb 5, 2019
Grant date	Feb 5, 2019

Abstract

Methods and systems for recovering or extracting rare earth elements under mild conditions include subjecting a material including rare earth element to a rare earth element crystallization medium under solvothermal conditions sufficient to form rare earth element crystals capable of gravity separation and purification.

First claim

We claim:

1. A system for recovering rare earth elements comprising:
a temperature and pressure controlled reaction vessel containing:
a raw material including rare earth metals and non-rare earth metals, and
a crystallization medium comprising at least one amide selected from the group consisting of formamide, N-carbylformamides, N,N-dicarbylformamides, or mixtures or combinations thereof, wherein the carbyl groups are the same or different and are selected from the group consisting of linear or branched alkyl groups having between 1 and 6 carbon atoms, aryl groups, araalkyl groups, alkaaryl group, or mixture thereof,
wherein the reaction vessel is maintained under solvothermal conditions sufficient to dissolve the rare earth metals and the non-rare earth metals from the raw material and to selectively crystallize the rare earth metals from the medium to form rare earth metal crystals capable of being gravity separated; and

a gravity separator connected to the vessel and containing:
the medium including the rare earth metal crystals from the reaction vessel, and a density separation medium,
wherein the rare earth metal crystals are separated from the medium to form a rare earth metal crystalline composition.

2. The system of claim 1 , further comprising:
a purifying vessel connected to the gravity separator and containing:
the rare earth metal crystalline composition, and
water,
wherein the rare earth metal crystalline composition is washed with the water to remove non-rare earth metal crystals to form a purified rare earth metal crystalline composition, and

a post-calcining vessel connected to the purifying vessel and containing:
the purified rare earth crystalline composition,
wherein the purified rare earth crystalline composition is calcined at a controlled temperature and pressure to form a purified rare earth metal oxide composition.

3. The system of claim 1 , wherein the crystallization medium further comprises:
at least one organic acid selected from the group consisting of formic acid, acetic acid, propanoic acid and mixtures or combinations thereof, and/or
water.

4. The system of claim 3 , wherein the at least one amide is formamide and the at least one organic acid is formic acid.

5. The system of claim 1 , wherein the crystallization medium comprises:
80 vol. % to 100 vol. % of the at least one amide,
0 vol. % to 10 vol. % of at least one organic acid selected from the group consisting of formic acid, acetic acid, propanoic acid and mixtures or combinations thereof, and
0 vol. % to 10 vol. % water.

6. The system of claim 5 , wherein the crystallization medium comprises:
80 vol. % of the at least one amide,
10 vol. % of the at least one organic acid, and
10 vol. % water.

7. The system of claim 6 , wherein the crystallization medium comprises:
95 vol. % of the at least one amide,
2.5 vol. % of the at least one organic acid, and
2.5 vol. % water.

8. A system for recovering rare earth elements comprising:
a pre-calcining vessel containing:
a raw material including rare earth metals and non-rare earth,
wherein the raw material is calcined at a controlled temperature and pressure to form a calcined raw material,

a temperature and pressure controlled reaction vessel connected to the pre-calcining vessel and containing:
the calcined raw material, and
a crystallization medium comprising at least one amide selected from the group consisting of formamide, N-carbylformamides, N,N-dicarbylformamides, or mixtures or combinations thereof, where the carbyl group are the same or different and are selected from the group consisting of linear or branched alkyl groups having between 1 and 6carbon atoms, aryl groups, araalkyl groups, alkaaryl group, or mixture thereof,
wherein the vessel is maintained under solvothermal conditions sufficient to dissolve the rare earth metals from the calcined raw material and the non-rare earth metals and to selectively crystallize the rare earth metals from the medium to form rare earth metal crystals capable of being gravity separated; and

a gravity separator connected to the vessel and containing:
the reaction medium including the rare earth metal crystals, and
a density separation medium,
wherein the rare earth metal crystals are separated from the medium to form a rare earth metal crystalline composition.

9. The system of claim 8 , further comprising:
a purifying vessel connected to the gravity separator and containing:
the rare earth metal crystalline composition and
water,
wherein the rare earth metal crystalline composition is washed with the water to remove non-rare earth metal crystals to form a purified rare earth metal crystalline composition, and

a post-calcining vessel connected to the purifying vessel and containing:
the purified rare earth crystalline composition,
wherein the purified rare earth crystalline composition is calcined at a controlled temperature and pressure to form a purified rare earth oxide composition.

10. The system of claim 8 , wherein the crystallization medium further comprises:
at least one organic acid selected from the group consisting of formic acid, acetic acid, propanoic acid and mixtures or combinations thereof, and/or
water.

11. The system of claim 10 , wherein the at least one amide is formamide and the at least one organic acid is formic acid.

12. The system of claim 8 , wherein the crystallization medium comprises:
80 vol. % to 100 vol. % of the at least one amide,
0 vol. % to 10 vol. % of at least one organic acid selected from the group consisting of formic acid, acetic acid, propanoic acid and mixtures or combinations thereof, and
0 vol. % to 10 vol. % water.

13. The system of claim 12 , wherein the crystallization medium comprises:
80 vol. % of the at least one amide,
10 vol. % of the at least one organic acid, and
10 vol. % water.

14. The system of claim 13 , wherein the crystallization medium comprises:
95 vol. % of the at least one amide,
2.5 vol. % of the at least one organic acid, and
2.5 vol. % water.

15. A system for recovering rare earth elements comprising:
a comminuting unit containing:
a raw material including rare earth metals and non-rare earth metals,
wherein the raw material is comminuted to form a comminuted raw material,

a pre-calcining vessel connected to the comminuting unit and containing:
the comminuted raw material,
wherein the comminuted raw material is calcined at a controlled temperature and pressure to form a calcined comminuted raw material,

a temperature and pressure controlled reaction vessel connected to the pre-calcining vessel and containing:
the calcined comminuted raw material, and
a crystallization medium comprising at least one amide,
where the vessel is maintained under solvothermal conditions sufficient to dissolve the rare earth metals and the non-rare earth metals and to selectively crystallize the rare earth metals to form rare earth metal crystals capable of being gravity separated;

a gravity separator connected to the vessel and containing:
the rare earth metal crystals to form a rare earth metal crystalline composition,

a purifying vessel connected to the vessel and containing:
the rare earth metal crystalline composition,
wherein the rare earth metal crystalline composition is washed with water to remove non-rare earth metal crystals to form a purified rare earth metal crystalline composition, and

a post-calcining vessel connected to the vessel and containing:
the purified rare earth crystalline composition,
wherein the purified rare earth crystalline composition

Assignees

• Univ Houston System
• Univ Houston System

Inventors

• Jacobson Allan J
• Samarasekere Pradeep

Classifications

• C01F17/206

  oxide or hydroxide being the only anion · CPC title

• C22B3/22

  by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title

• C22B3/02

  Apparatus therefor · CPC title

• C22B7/006

  Wet processes · CPC title

• C22B7/007

  by acid leaching · CPC title