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The problem aSmall Gold Processing Plant can solve is for the need to to provide a small, relatively simple and inexpensive gold mill that will operate at a reasonable profit with a minimum of supervision. The limited availability of skilled operating personnel, availability of water and local power, high cost of transporting ore and expense of building, operating and maintaining such a mill have been taken into consideration in developing the flowsheet. A primary objective is to provide a mill having sufficiently low power and water requirements as to be supplied locally.
The flowsheet was developed for a siliceous ore with a high percentage of the gold present in a free milling state. In addition some gold bearing sulphides are present which require the inclusion of flotation in order to obtain maximum recovery. Most of the goldis, however, recoverable in bullion form for shipment to the mint. The gold tied up in the flotation concentrate is shipped to a smelter, although in remote areas a small batch cyanide plant may be used to extract the values and thereby eliminate the shipping and smelter charges.
Single stage crushing for the average small mill 100 tons or less is adequate. The crushed ore at approximately minus 1 inch is wet ground in a Ball Mill to free the gold and sulfide values. Grinding is in closed circuit with a classifier and in this case a 48 mesh grind was necessary.
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The Crushing plant is designed to crush the ore in one shift 8-10 hours. The Ball Mill and Classifier and the balance of the plant runs 24 hours per day.
To trap the heavy free gold in the grinding circuit a Mineral Jig is placed between the ball mill and classifier. This recovers the gold just as soon as released and avoids its accumulation in the bottom of the Classifier or Ball Mill scoop box. The high grade gold concentrate from the jig is ground in batches and amalgamated in a Amalgamation Unit. The residue from the unit is collected, dewatered, and saved as it usually contains sufficient value for retreatment or shipment to a smelter.
Flotation tailings are finally tabled for recovery of oxidized values. This product may be added to the flotation concentrates, or if some free gold is present, it may be amalgamated along with the Mineral Jig concentrate. The Table also serves as a pilot control of the mill circuit both as to grind and recovery.
In this example the concentrates from the Mineral Jig and Table were combined and amalgamated to give the above recovery in amalgam form. With amalgamation plates in the circuit as shown, the recovery of gold in bullion form should approach 80. The balance of the recoverable gold is in concentrate form for shipment to the smelter. In the example shown the combined shipping product residue plus flotation concentrate assays 6.45 oz. gold per ton. From 50 tons milled, 2.88 tons of concentratesare produced.
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