Processes for recovering metals from aqueous solutions

Patent metadata

Field	Value
Publication number	US-9822425-B2
Application number	US-201514607578-A
Country	US
Kind code	B2
Filing date	Jan 28, 2015
Priority date	Jul 7, 2009
Publication date	Nov 21, 2017
Grant date	Nov 21, 2017

Abstract

Provided herein are processes for recovering metal present at low concentration from an acidic aqueous solution, including contacting the acidic aqueous solution with an organic phase solution including one or more 5-(C 8 to C 14 alkyl)-2-hydroxyaryloxime, thereby extracting at least part of the metal from the acidic aqueous phase; increasing or maintaining the concentration of metal in the organic phase solution by recycling a portion of the organic phase solution containing the metal and contacting the organic phase with an acidic aqueous solution containing the metal; contacting the organic phase solution containing metal with an aqueous phase strip solution comprising an inorganic compound that back-extracts the metal, thereby stripping at least part of the metal from the organic phase solution to the aqueous phase strip solution; and separating the metal from the aqueous phase strip solution, thereby recovering the metal.

First claim

What is claimed is:

1. A solvent extraction process for recovering a metal present at low concentration from an acidic aqueous solution, the process comprising:
a) contacting in a mixer the acidic aqueous solution with an organic phase solution comprising 5-nonylsalicylaldoxime, thereby extracting at least part of the metal from the acidic aqueous solution into the organic phase solution; increasing or maintaining the concentration of metal in the organic phase solution by recycling from 50-100% by volume of the organic phase solution containing the metal and contacting the organic phase solution with the acidic aqueous solution containing the metal until the concentration ranges from 0.3 g/L to 25 g/L;
b) contacting the organic phase solution containing metal with an aqueous phase strip solution comprising an inorganic compound that back-extracts the metal, thereby stripping at least part of the metal from the organic phase solution to the aqueous phase strip solution; and
c) separating the metal from the aqueous phase strip solution, thereby recovering the metal.

2. A process according to claim 1 , wherein the recycling step comprises flowing an aqueous phase solution in contact with an organic phase solution wherein a metallurgical organic phase to aqueous phase ratio is from 0.001 to 0.20, and setting an internal organic phase to aqueous phase ratio of 0.5 to 2.0 in the mixer.

3. A process according to claim 1 , wherein the recycling step is continuous.

4. A process according to claim 1 further comprising one or more scrubbing steps performed by contacting at least part of the organic phase solution loaded with metal with a mineral acid solution, thereby removing any impurities from the organic phase solution.

5. A process according to claim 1 further comprising a second recycling step comprising recycling from 5-100% by volume of the aqueous phase strip solution containing the metal and contacting the aqueous phase strip solution with an organic phase solution containing the metal, thereby increasing or maintaining the concentration of the metal in the aqueous phase strip solution.

6. A process according to claim 5 , wherein the second recycling step is performed until the concentration of metal in the aqueous phase strip solution is at least from 5.0 g/L to 200 g/L.

7. A process according to claim 5 , wherein the second recycling step comprises flowing an aqueous phase strip solution in contact with an organic phase solution containing the metal wherein the organic phase to aqueous phase ratio is 1 to 1000, and setting an internal organic phase to aqueous phase ratio of 0.5 to 10 in the mixer.

8. A process according to claim 1 , wherein the combined concentration factor from steps (a) and (b) is from 20 to 10,000.

9. A process according to claim 1 , wherein the process is performed following a major metal extraction.

10. A process according to claim 1 , wherein the metal is chosen from one or more members selected from the group consisting of transition metals, alkali metals, alkaline earth metals, rare earth metals, lanthanides, and actinides.

11. A process according to claim 1 further comprising stripping a second metal from the organic phase solution with a second aqueous phase strip solution comprising a compound that is specific for stripping the second metal.

12. A process according to claim 10 , wherein the metal is a transition metal.

13. A process according to claim 12 , wherein the transition metal is molybdenum.

14. A process according to claim 12 , wherein the transition metal is copper.

15. A process according to claim 10 , wherein the metal is a rare earth metal or actinide metal.

16. A solvent extraction process for recovering a metal present at low concentration from an acidic aqueous solution, the process comprising:
contacting in a mixer the acidic aqueous solution with an organic phase solution comprising:
(a) a phosphinic acid compound represented by:

wherein each of R 1 and R 2 is independently chosen from an optionally substituted radical selected from the group consisting of C 1 -C 30 alkyl, C 3 -C 30 cycloalkyl, C 3 -C 30 alkoxyalkyl, C 4 -C 30 alkylcyclo, C 7 -C 30 alkylaryl, C 7 -C 30 aralkyl, and C 8 -C 30 cycloalkylaryl; and
(b) a modifier compound comprising a functional group selected from the group consisting of phenols, aromatic esters, aliphatic esters, organophosphorus compounds, phosphates, phosphine oxides, aromatic aliphatic alcohols, aliphatic alcohols, nitriles, ketones, amides, carbamates, sulfoxides, ureas, carbonates, oximes, ethers, polyethers, ester-ethers, phosphonium salts, ammonium salts, and combinations thereof,

thereby extracting at least part of the metal from the acidic aqueous solution into the organic phase solution;
increasing or maintaining the concentration of metal in the organic phase solution by recycling from 50-100% by volume of the organic phase solution containing the metal and contacting the organic phase solution with the acidic aqueous solution containing the metal until the concentration ranges from 0.3 g/L to 25 g/L;
contacting the organic phase solution containing metal with an aqueous phase strip solution comprising an inorganic compound that back-extracts the metal, thereby stripping at least part of the metal from the organic phase solution to the aqueous phase strip solution; and
separating the metal from the aqueous phase strip solution, thereby recovering the metal.

17. A process according to claim 16 , wherein the metal is chosen from one or more members selected from the group consisting of transition metals, alkali metals, alkaline earth metals, rare earth metals, lanthanides, and actinides.

18. A process according to claim 17 , wherein the metal is a transition metal.

19. A process according to claim 18 , wherein the transition metal is molybdenum.

20. A process according to claim 18 , wherein the transition metal is copper.

Assignees

• Cytec Tech Corp

Inventors

• Bednarski Troy Allan
• Cocalia Violina Antoneta
• Soderstrom Matthew Dean
• Kamenetzky Eduardo Alberto
• Cameron Andrew Michael
• Harris Douglas

Classifications

• C22B60/0226

  using acidic solutions or liquors · CPC title

• C22B3/0005

  Chemistry & Metallurgy · mapped topic

• C22B3/1683 Primary

  Leaching with organo-metallic compounds · CPC title

• Y02P10/234

  Cross-Sectional Technologies · mapped topic

• C22B34/34

  Obtaining molybdenum {(treatment or purification of solutions by adsorption on solids C22B3/24, by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42; preparation of molybdenum involving liquid-liquid extraction, adsorption or ion-exchange C01G39/003)} · CPC title