Method for gold recovery and extraction from electronic waste or gold containing minerals, ores and sands

Patent metadata

Field	Value
Publication number	US-11718893-B2
Application number	US-201816759751-A
Country	US
Kind code	B2
Filing date	Nov 1, 2018
Priority date	Nov 1, 2017
Publication date	Aug 8, 2023
Grant date	Aug 8, 2023

Abstract

A method for recovery of gold from gold-containing materials, such as electronic waste material, minerals and sands is described. The method includes crushing the gold containing material to obtain a particulate material. The particulate material is then preheated in an oxygen-containing gas environment in a preheating zone. The method also includes mixing the oxidized particulate material with a chlorine-containing material and treating the mixture in a reaction zone. The treatment is carried out by heating the mixture to provide thermal decomposition of the chlorine-containing material and produce a chlorine-containing gas mixture, and by applying an electromagnetic field to the chlorine-containing gas mixture to provide ionization of chlorine. A volatile gold-containing chloride product, produced in the reaction zone as a result of a chemical reaction between gold and chlorine ions, is then cooled to convert the volatile gold-containing chloride product into solid phase gold-containing materials.

First claim

The invention claimed is:

1. A method for recovery of gold from gold-containing material, the method comprising:
crushing said gold-containing material to obtain a gold-containing particulate material including particles having a predetermined grain size;
optionally subliming other metals from said material;
preheating said gold-containing particulate material in an oxygen-containing gas environment in a preheating zone to oxidize gold-containing particulate material;
mixing the oxidized gold-containing particulate material with a composition comprising chlorine-containing material and nano silica;
treating the mixture of the oxidized gold-containing particulate material with a chlorine-containing material in a reaction zone by (i) heating said mixture to provide thermal decomposition of the chlorine-containing material and produce a chlorine-containing gas mixture, (ii) applying an electromagnetic field to the chlorine-containing gas mixture to provide ionization of chlorine; thereby causing a chemical reaction between gold and chlorine ions and providing a volatile gold-containing chloride product in the reaction zone; and
cooling said volatile gold-containing chloride product to convert said volatile gold-containing chloride product into solid phase gold-containing materials.

2. The method of claim 1 , wherein the gold-containing material is selected from used gold-containing printed circuit boards, gold-containing parts of electronic devices, waste gold-containing electrical connectors and gold-containing minerals, ores and sands.

3. The method of claim 1 , wherein said predetermined grain size of said gold-containing particulate material is in the range of 0.07 mm to 40 mm.

4. The method of claim 1 , wherein the subliming step of other metals is at a temperature between 500 to 900 degrees Celsius.

5. The method of claim 1 , wherein an amount of the chlorine-containing material in the mixture of the oxidized gold-containing particulate material with a chlorine-containing material is in the range of 1 gram to 1 kilogram per kilogram of the gold-containing material.

6. The method of claim 1 , wherein said chlorine-containing material is a particulate material selected from potassium hypochlorite, sodium hypochlorite, calcium hypochlorite, magnesium hypochlorite, barium hypochlorite, potassium chloride-hypochlorite, sodium chloride-hypochlorite, calcium chloride-hypochlorite, magnesium chloride-hypochlorite, barium chloride-hypochlorite, potassium chloride, sodium chloride, ammonium chloride, calcium chloride, magnesium chloride, barium chloride, aluminum chloride, or any combination thereof.

7. The method of claim 1 , wherein said composition comprising chlorine- containing material and nano silica, consists of a mixture of calcium hypochlorite, calcium chloride and nano silica.

8. The method of claim 1 , wherein said composition comprising chlorine- containing material and nano silica, consists of calcium hypochlorite and nano silica.

9. The method of claim 1 , wherein said nano silica have particles size than between 10-200 nm.

10. The method of claim 1 , wherein said preheating of the gold-containing particulate material is carried out at a temperature in the range of 150 degrees Celsius to 750 degrees Celsius.

11. The method of claim 1 , wherein said preheating of the gold-containing particulate material is carried out for a time period in the range of 5 min to 60 min.

12. The method of claim 1 , wherein a content of oxygen in said oxygen-containing gas environment in the preheating zone is in the range of 20 volume percent to 98 volume percent.

13. The method of claim 1 , wherein said heating the mixture of the oxidized gold-containing particulate material with a chlorine-containing material to provide thermal decomposition of the chlorine-containing material and produce a chlorine-containing gas mixture is carried out at a temperature in the range of 150 degrees Celsius to 400 degrees Celsius.

14. The method of claim 1 , wherein said heating the mixture of the oxidized gold-containing particulate material with a chlorine-containing material to provide thermal decomposition of the chlorine-containing material and produce the chlorine-containing gas mixture is carried out for a time period in the range of 5 min to 120 min.

15. The method of claim 1 , further comprising passing a chlorine-containing gas from an external source through the reaction zone during the applying of an electromagnetic field.

16. The method of claim 1 , wherein a frequency of the electromagnetic field in the reaction zone is in the range of 50 kHz-12 GHz.

17. The method of claim 1 , wherein an irradiance of the electromagnetic field in the reaction zone is in the range of 0.1 kW/cm 2 to 10 kW/cm 2 .

18. The method of claim 1 , wherein said applying of the electromagnetic field to the chlorine-containing gas mixture to provide ionization of chlorine is carried out for a time period in the range of 5 min to 180 min.

19. The method of claim 1 , wherein said heating of the mixture of the oxidized gold-containing particulate material with the chlorine-containing material in the reaction zone is carried out simultaneously with said applying of electromagnetic field to the chlorine-containing gas mixture.

20. The method of claim 1 , wherein the other metals of said gold containing particulate material comprise arsenic and antimony and said arsenic and antimony are being sublimed by mixing with coal and reduced at temperatures of 500-900° C.

21. The method of claim 4 , wherein said other metals comprise arsenic, antimony or combination thereof.

22. The method of claim 8 , wherein said calcium hypochlorite is mixed with nano silica in solid or liquid form for better decomposition of said calcium hypochlorite to produce said chlorine-containing gas mixture.

23. The method of claim 7 wherein an amount of calcium hypochlorite in said composition of calcium hypochlorite and calcium chloride is in the range of 5 to 99 weight percent.

24. The method of claim 15 , wherein an amount of the chlorine-containing gas being passed from an external source through the reaction zone is in the range of 5 liters to 400 liters chlorine per a ton of said gold-containing material.

25. The method of claim 20 , wherein the coal consumption is 130-170% of the stoichiometric coal quantity required for the full reduction reaction of arsenic and antimony oxides with carbon.

Assignees

• Yeda Res & Dev

Inventors

• Lubomirsky Igor
• Kaplan Valery
• Dosmukhamedov Nurlan
• Zholdasbay Erzhan

Classifications

• Y02P10/20

  Recycling · CPC title

• C22B11/06 Primary

  Chloridising · CPC title

• C22B1/005 Primary

  Preliminary treatment of scrap (C22B1/02 - C22B1/26 take precedence) · CPC title

• C22B11/025

  from manufactured products, e.g. from printed circuit boards, from photographic films, paper, or baths · CPC title

• C22B1/02

  Roasting processes (C22B1/16 takes precedence) · CPC title