The Veladero deposit is situated at the north end of the El Indio Gold Belt, a 120 km by 25 km north-trending corridor of Permian to late Miocene volcanic and intrusive rocks, which host a number of hydrothermal alteration zones and epithermal mineral deposits.

The Veladero deposit is a hypogene-oxidized, high sulphidation gold-silver deposit hosted by volcaniclastic sediments, tuffs, and volcanic breccias related to a Miocene diatreme-dome complex. Hydrothermal alteration is typical of high sulphidation gold deposits, with a silicified core grading outward into advanced argillic alteration, then into peripheral argillic and propylitic alteration haloes. Gold occurs as fine native grains, and is dominantly associated with silicification and with iron oxide or iron sulfate fracture coatings. Silver mineralization is distinct from gold, and occurs as a broader, more diffuse envelope, probably representing a separate mineralizing event.

Mine operations are exclusively by open pit method, with a fleet of primarily 218 tonne rigid frame haul trucks combined with a variety of diesel powered hydraulic shovels and front end loaders as the primary loading equipment. The haul trucks are also utilized to transport ore to the VLF for placement. Blasting is required other than for the occasional unconsolidated material at surface when starting a new pushback. A fleet of large diesel powered blast hole rigs are employed for the production drilling.

Gold is recovered from ore at Veladero using ROM and crushed ore cyanide heap leaching, and a Merrill-Crowe zinc cementation gold recovery plant. The lower gold grade ore, i.e., above the COG for ROM ore and below the COG for crushed ore, is mined and trucked to the VLF and co-mingled with crushed ore (in the past, ROM ore was stacked in a separate area from crushed ore). Final delivery to the pad for ROM and crushed ore is by haul truck and spreading is by track-mounted dozer.

Ore that has a gold grade above the cut-off grade for crushed ore is trucked from the mine or stockpiles and crushed in one of two two-stage crushing circuits to a nominal size of 80% passing (P80) 40 mm.

The crushing plant capacity is approximately 83,000 tonnes per operating day. The technical limit of the plant is 100,000 tonnes per operating day, which may be achievable through optimum operational and mechanical availability.

Haul trucks dump directly into the primary 1,270 mm by 1,650 mm gyratory crushers. After crushing, the ore from line one is discharged into a surge pocket and transferred to a 2,000 t live capacity covered stockpile via an apron feeder and a belt conveyor. The primary crushed ore from line two is reclaimed from the surge pocket and placed on a belt conveyor. From the belt conveyor the ore can either go directly to a secondary crusher surge bin or be transferred to the covered stockpile.

The primary crushed ore is reclaimed from the stockpile and conveyed to a splitter chute to feed two scalping screens that operate in parallel in line one to remove the material that meets the required size criteria. The oversize from the screens discharges to two MP800 standard cone crushers, after which lime is added to the recombined undersize and crusher product. Line two is similar to line one except it has only one scalping screen and one secondary cone crusher. The secondary crushers operate in open circuit so the crushed ore and the undersize from the scalping screens are fed to the crushed ore bin.

An overland conveyor that previously transported crushed ore from Ore Bin #1 to Ore Bin #2 has been out of service since February 2015, and subsequently decommissioned due to excessive maintenance and mechanical issues in this area. The crushed ore is hauled by a fleet of 11 trucks from the crushing plant to the VLF, a distance of approximately 4.2 km.

At the VLF, ore is stacked as cells in 13 m lifts. Cells are typically 200 m to 250 m by 80 m to 100 m in size, or approximately 20,000 m2, and contain approximately 450,000 t to 500,000 t of ore. The maximum height of the leach pad is constrained to an overall stack height of 150 m above the primary liner, but is typically 100 m or less stack height.

Approximately 230,000 m2 to 260,000 m2 of surface area in the VLF is actively under leach at any given time with dilute cyanide leach solution applied using drip emitters. The drip emitters are buried approximately 60 cm to 65 cm to maximize distribution of solution and minimize freezing risk and evaporation. The nominal capacity of the Barren Solution pumping system is 2,900 m3/h. Pregnant solution is collected by the dam, at the toe of the leach pad, and pumped to the Merrill- Crowe recovery plant. An additional 0-2,700 m3/h is provided by a PLS Recycle system which provides an ability to control the PSSA solution level and pursue solution enrichment with lower grade ore.

The pregnant solution is clarified in pressure leaf filters and stored in a clarified solution tank. From the tank, solution is pumped to a vacuum de-aeration tower which removes the dissolved oxygen from the precious metal bearing solution. Zinc dust is fed to the solution as it exits the de-aeration tower and the precious metals are removed from the solution as solid precipitate. Plate and frame filter presses are used to separate the precipitate from the solution. The barren solution is collected in a barren solution tank, cyanide and make-up water are added to the solution, and it is re-circulated to the VLF for reuse.

The zinc precipitate is collected from the filter presses and processed in retorts designed to recover mercury vapours from the precipitate as it is heated under vacuum. By-product mercury is collected and stored on site.

The dried precipitate is mixed with flux and smelted in electric induction furnaces. Gold doré that is produced by the refining process is shipped off site for further refining to produce fine gold and silver.