Recovery of precious and chalcophile metals
A process for recovery of one or more elements, selected from precious metals and chalcophile metals, as herein defined, from materials containing precious and/or chalcophile metal/s, said process including: (i) contacting the material with an alkaline solution containing a lixiviant comprising an amino acid, or derivative thereof, and an alkali stable transition metal complex in order to form a leachate containing the precious metal and/or chalcophile metal; and (ii) recovering the precious metal and/or chalcophile metal from the leachate.
1. A process for recovery of one or more elements, selected from precious metals and chalcophile metals, as herein defined, from materials containing precious and/or chalcophile metal/s, said process including:
contacting the material with an alkaline solution containing a lixiviant comprising an amino acid, or derivative thereof, and a rate enhancer comprising an alkali stable transition metal complex in order to form a leachate containing complexes of the precious metal with the amino acid and/or complexes of the chalcophile metal with the amino acid; and
(ii) recovering the precious metal and/or chalcophile metal from the leachate
wherein the amino acid concentration is greater than 0.05 g/L and the concentration of alkali stable transition metal complex is a minimum of 0.05 g/L and
wherein the amino acid is one or more of glycine, histidine, valine, alanine, phenylalanine, cysteine, aspartic acid, glutamic acid, lysine, methionine, serine, threonine, and tyrosine.
2. The process of claim 1 , wherein the amino acid concentration is less than 250 g/L.
3. The process of claim 1 , wherein the amino acid concentration is greater than 0.1 g/L.
4. The process of claim 1 , wherein the amino acid concentration is less than 30 g/L.
5. The process of claim 1 , wherein the alkali stable transition metal complex is an iron complex or a manganese complex.
6. The process of claim 1 , wherein the pH of the alkaline solution is at least 7.
7. The process of claim 1 , wherein the pH of the alkaline solution is at least 8.
8. The process of claim 1 , wherein the temperature of the process is between −5 and 90 degrees Celsius.
9. The process of claim 1 , wherein the temperature of the process is ambient temperature.
10. The process of claim 1 , wherein the alkali stable transition metal complex includes ligands selected from carboxylic and dicarboxylic acid salts, pH-stable cyanide complexes, hydroxy-carboxylic acids and their salts, and ethylene diamine tetra-acetic acid (EDTA) and its salts.
11. The process of claim 1 , wherein the alkali stable transition metal complex comprises one or more of chromate, permanganate, manganate, titanate, ferrate, and vanadate.
12. The process of claim 1 , wherein the alkali stable transition metal complex comprises one or more of ferrocyanide, ferricyanide, ferro gluconate, ferri gluconate, ferro citrate, ferri citrate, ferro/ferri tartrate, ferro/ferri ethylene diamine tetra-acetic acid (EDTA) salt.
13. The process of claim 1 , wherein the alkali stable transition metal complex comprises one or more of ferro/ferricyanide, ferric gluconate and ferric EDTA.
14. The process of claim 1 , wherein the transition metal in the alkali stable transition metal complex is partially substituted by one or more of ammonium ions, alkali metal ions and alkali earth metal ions.
15. The process of claim 1 , wherein the concentration of alkali stable transition metal complex is less than 50 g/L.
16. The process of claim 1 , wherein the concentration of alkali stable transition metal complex is a minimum of 0.1 g/L.
17. The process of claim 1 , wherein the concentration of alkali stable transition metal complex is less than 10 g/L.
18. The process of claim 1 , wherein the alkaline solution further includes an oxidant selected from the group comprising air, oxygen, hydrogen peroxide, calcium peroxide, sodium peroxide, ammonium peroxide manganese dioxide or permanganate.