Process for extracting precious metals

Details Process for extracting precious metals Process for extracting precious metals

1991-07-22

1993-05-25

Rosenberg, Peter D.

Specialized metallurgical processes, compositions for use therei

Processes

Free metal or alloy reductant contains magnesium

C22B 344

Patent

active

052136094

ABSTRACT:
The invention relates to a method of extracting gold from a gold-containing material. The invention provides a process of extracting precious metals from a precious metal-containing material comprising mixing the material in a finely-divided state with an alkaline cyanide solution to form a mixture and recovering the metal from solution by known methods characterized in that said process is carried out in the presence of peroxymonosulfuric acid or salt thereof and, where necessary, adding oxygen or a source thereof to said mixture to provide a dissolved oxygen level of at least about 6 ppm.
In a preferred embodiment the process is used in conjunction with a carbon-in-pulp plant. In the preferred process ore slurry 2 is passed through a valve means 3a to a wood screen 5 via line 4a. The slurry is separated from waste wood splinters 5a under gravity to a reservoir 6 where it is combined with an alkaline cyanide solution 7 introduced via line 4b and metering pump 8a. The slurry mixture is then introduced into a first leach tank 9a via line 4c, metering pump 8b and valve means 3b. The slurry is then agitated using an agitated drive 11a in the presence of a triple salt which has been introduced via line 4d, metering pump 8c and valve means 3c and also in the presence of activated carbon 12 which can be introduced into any of the tanks, typically 9f and returned into the previous leach tanks and ultimately tank 9a via lines 4e to 4i and pumps 8d to 8h. The mixture is then passed through self cleaning carbon screen 13a to remove loaded carbon 14 to a second leach leach tank 9b where it is agitated by agitated drive 11b. The mixture is then passed through a second carbon cleaning screen 13b to a third leach tank 9c and subsequently through tanks 9d to 9f. Slurry is also returned into the previous tanks via lines 4e to 4i and pumps 8d to 8h. Air or oxygen can also be introduced into any of the tanks typically tanks 9c or 9d. The triple salt may also be added to any one of tanks 9b to 9f via valve means 3d to 3h. After the slurry/carbon mixture has proceeded through all the tanks, carbon fines 15a are removed using a carbon fine screen 15 to give an end solution 16 which is separated from the tailings 17 by metering pump 8a and valve means 3i. The end solution 16 is then extracted for gold using known methods.

REFERENCES:
patent: 5034055 (1991-07-01), Rowson
patent: 5071477 (1991-12-01), Thomas

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