IP Library Granted Patent US 8,444,744
Granted Patent B2
US 8,444,744 · App. 12/878,488 · Granted May 21, 2013

Method for separating and recovering nickel and lithium

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 8,444,744
App. No.
12/878,488
Granted
May 21, 2013
Kind
B2
Abstract

A method for extracting nickel and lithium includes solvent extraction step of using three or more extraction stages to subject a solution containing lithium and nickel to solvent extraction with 2-Ethylhexyl phosphonic acid mono-2-ethylhexyl ester at a pH of 8.0 to 8.5, whereby the nickel and the lithium are co-extracted into a resultant organic phase.

Claims (32)

1. A method for extracting nickel and lithium comprising:

solvent extraction step of using three or more extraction stages to subject a solution containing lithium and nickel to solvent extraction with 2-Ethylhexyl phosphonic acid mono-2-ethylhexyl ester at a pH of 8.0 to 8.5, whereby the nickel and the lithium are co-extracted into a resultant organic phase.

2. The method according to claim 1 , wherein the solution containing lithium and nickel includes 5.0 to 15.0 g/L of nickel, 3.0 to 6.0 g/L of lithium, 0.01 to 0.03 g/L of cobalt, and less than 0.01 g/L of manganese.

3. A method for extracting nickel and lithium comprising:

a solvent extraction step comprising three or more extraction stages, wherein each stage subjects a solution containing lithium and nickel to solvent extraction with 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester at a pH of 8.0 to 8.5, whereby the nickel and the lithium are co-extracted into a resultant organic phase, then

the resultant organic phase undergoes a back extraction step wherein the resultant organic phase undergoes back extraction with a sulfuric acid solution, whereby the nickel and the lithium are concentrated into a back extraction liquid.

4. The method according to claim 3 , further comprising a nickel extraction and carbonation process which comprises:

adjusting pH of a water phase obtained by the back extraction step with sodium hydroxide;

subjecting the pH-adjusted liquid to extraction with neodecanoic acid to selectively extract nickel into a resultant oil phase; and

neutralizing the resultant oil phase by adding sodium carbonate to recover nickel in the form of nickel carbonate.

5. The method according to claim 4 , further comprising:

neutralizing a liquid which is not extracted by the nickel extraction and carbonation process with sodium carbonate to recover lithium in the form of lithium carbonate.

6. The method according to claim 5 , further comprising:

adjusting the liquid obtained by the nickel extraction and carbonation process to a pH of 9.5 to 10.5 before the neutralization.

7. The method according to claim 3 , further comprising:

adjusting pH of the back extraction liquid with sodium hydroxide;

subjecting the pH-adjusted liquid to extraction with neodecanoic acid to selectively extract nickel into a resultant oil phase;

adding potassium oxalate to the resultant oil phase to produce a compound of nickel oxalate; and

decomposing the compound thermally and recovering nickel powder.

8. The method according to claim 7 , further comprising:

adding an alkaline agent to keep the resultant oil phase at a pH of 1.5 or more to produce the compound of nickel oxalate.

9. The method according to claim 8 , wherein the decomposing step includes heating the compound at 330 to 370 degrees C.

10. A method for extracting nickel and lithium comprising:

a solvent extraction step comprising three or more extraction stages, wherein each stage subjects a solution containing lithium and nickel to solvent extraction with 2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester at a pH of 8.0 to 8.5, whereby the nickel and the lithium are co-extracted into a resultant organic phase, and then

the resultant organic phase undergoes a back extraction step wherein the resultant organic phase undergoes back extraction with a sulfuric acid solution, whereby the nickel and the lithium are concentrated into a back extraction liquid, and then

scavenging an oil phase obtained by the back extraction step with a solution having an acid concentration higher than the sulfuric acid solution used in the back extraction step, thereby effusing any nickel and the lithium remaining in the oil phase to a water phase, and then additionally subjecting the resulting oil phase to the solvent extraction step.

11. The method according to claim 10 , further comprising a nickel extraction and carbonation process which comprises:

adjusting pH of a water phase obtained by the back extraction step with sodium hydroxide;

subjecting the pH-adjusted liquid to extraction with neodecanoic acid to selectively extract nickel into a resultant oil phase; and

neutralizing the resultant oil phase by adding sodium carbonate to recover nickel in the form of nickel carbonate.

12. The method according to claim 11 , further comprising:

neutralizing a liquid which is not extracted by the nickel extraction and carbonation process with sodium carbonate to recover lithium in the form of lithium carbonate.

Assignments (1)
CHANGE OF ADDRESS Recorded Feb 7, 2017
From: JX NIPPON MINING & METALS CORPORATION
To: JX NIPPON MINING & METALS CORPORATION
Reel/Frame 041649/0733 →