IP Library Granted Patent US 12703894
Granted Patent B2
US 12703894 · App. 19/110,052 · Granted Aug 11, 2026

Carbonation and selective leaching for the recovery of metals

Inventors: Thomas Anthony Villalon, Jr. (Boston, MA); Rita Marie Silbernagel (Cambridge, MA); Henry Chase Hutcheson (Malden, MA)
Assignee: Phoenix Tailings, Inc.
C22B15/001C22B3/14C22B3/22C22B15/0078C22B15/0086
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Quick Facts
Patent No.
US 12703894
App. No.
19/110,052
Granted
Aug 11, 2026
Kind
B2
Abstract

The present disclosure is related to carbonation and selective ammonia leaching for the recovery of minor metals.

Claims (28)

1 . A method for extracting a target metal from a target metal-containing material, comprising:

exposing the target metal-containing material to carbon dioxide such that the carbon dioxide reacts with target metal associated with the target metal-containing material to form a target metal carbonate, wherein the target metal is a transition metal; and

leaching the target metal carbonate with a leaching agent to separate the target metal from the carbonate anion.

2 . The method of claim 1 , wherein the leaching agent comprises a Lewis base.

3 . The method of claim 1 , wherein leaching the target metal carbonate comprises forming a carbonato-ammine complex of the target metal.

4 . The method of claim 1 , wherein the target metal is a metal capable of coordinating with ammonia to form a metal ammine complex.

5 . The method of claim 1 , wherein the target metal comprises cobalt, nickel, copper, zinc, chromium, silver, gold, and/or platinum group metals.

6 . The method of claim 1 , wherein the target metal has an oxidation state of greater than or equal to +1.

7 . The method of claim 1 , wherein the target metal is a metallic metal having a zero oxidation state.

8 . The method of claim 1 , wherein the target metal-containing material comprises mafic rocks, ultramafic rocks, olivine minerals, pyroxene minerals, and/or serpentine minerals.

9 . The method of claim 1 , wherein the leaching agent is ammonia.

10 . The method of claim 1 , wherein the exposing step is performed at a temperature of greater than or equal to 20° C. and less than or equal to 350° C.

11 . The method of claim 1 , wherein the leaching step is performed at a temperature of greater than or equal to 80° C. and less than or equal to 330° C.

12 . The method of claim 1 , wherein the method is performed in a closed system.

13 . The method of claim 1 , wherein, during the exposing step, a pressure of carbon dioxide is greater than or equal to 100 psi and less than or equal to 5000 psi.

14 . The method of claim 1 , wherein, during the exposing step, the carbon dioxide is gaseous.

15 . The method of claim 1 , wherein the target metal is nickel, copper, cobalt, molybdenum, and/or zinc.

16 . The method of claim 1 , wherein the target metal-containing material further contains a second target metal, and wherein, during the exposing step, the second target metal also forms a carbonate.

17 . The method of claim 1 , wherein the leaching is performed in the presence of a liquid and/or solution comprising the leaching agent.

18 . The method of claim 1 , wherein the leaching is carried out under a pressure of greater than or equal to 0.1 atmospheres absolute and less than or equal to 2 atmospheres absolute.

19 . A method for extracting a target metal from a target metal-containing material, comprising:

exposing the target metal-containing material to carbon dioxide such that the carbon dioxide reacts with target metal associated with the target metal-containing material to form a target metal carbonate, wherein the target metal is a transition metal; and

leaching the target metal carbonate with a leaching agent to separate the target metal from the carbonate anion,

wherein the leaching results in less than 10 wt % of the carbonate material from the target metal carbonate forming carbon dioxide.

20 . A method for extracting a target metal from a target metal-containing material, comprising:

exposing the target metal-containing material to carbon dioxide such that the carbon dioxide reacts with target metal associated with target metal-containing material to form target metal carbonate; and

leaching the target metal carbonate with a leaching agent to separate the target metal from the carbonate anion,

wherein the leaching results in less than 10 wt % of the carbonate material from the target metal carbonate forming carbon dioxide.