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MNV
Overview Geology Mineral Resources & Ore Reserves Mining Mineral Processing
The Group owns 100% of the MNV joint-stock company, which has a licence for the extraction of gold ore valid until December 2018. Operations at MNV consist of both underground and open-pit mining of several high grade gold deposits. In addition, MNV has its own gold processing plant. MNV was initially brought into production by its previous owners in 1991 and operated until 1997, when the mine was closed due to poor technical and financial performance and a lack of funds for reconstruction and development. Following a change of ownership and the introduction of the current management team, gold mining and gold extraction recommenced in 1999 under the direction of the new management team. Subsequent capital investment in mining and metallurgical equipment, has meant that the technical performance of the mine has significantly improved over the last five years.
The ore bodies at Mnogovershinnoe are located within two zones, the Main Zone and the Intermediate Zone. The Main Zone is some 5.8 km long and contains the Central, Upper and Reindeer ore bodies. The Intermediate Zone is some 6.2 km long and is located 1.5 km north-west of the Main Zone and contains the Intermediate I and II ore bodies together with the South, Flank, North, Deep, Quiet and Boulder ore bodies. The overall width of the two zones is some 2.5 km. All the ore bodies strike north-east and dip to the north-west. Generally both ore body thickness and gold grade distribution is highly irregular. The Intermediate Zone is also confined to a steeply dipping fault with a north-east strike and consists of a thick quartz vein surrounded by a halo of quartz veinlets. The total zone thickness varies between 20 m and 80 m. The Intermediate Zone is subdivided into blocks by a number of north-west faults with vertical displacement. The Mnogovershinnoe ore bodies are characterised as gold-chalcedony-quartz, low sulphide, veins. Quartz constitutes more than 95% of the ore bodies. Gold is distributed irregularly in the form of fine disseminated impregnations, small individual pockets and thin veinlets. The majority (92-96%) of the gold and silver (80-90%) occurs in a free form amenable to standard cyanidation leaching. Some amounts also occur as fine inclusions in quartz, other rock-forming minerals and sulphides. Visible gold is uncommon and cyanide leaching test work confirms that the gold is non-refractory, with extraction levels of 95% being achievable at standard grind parameters. Mineral Resources & Ore Reserves
Open Pit Mining is standard open pit benching. Waste benches of 10 m and ore benches of 5 m are drilled using Russian-made drills with hole diameters of 125 mm to 250 mm. Holes are charged with Anfo(Ammonium Nitrate Fuel Oil) and the blasting ratio is 0.25 kg/t of rock (ore and waste). The overall pit slopes are between 45º and 55º. The mountainous topography enables the pits to be designed to minimise pumping and maximise the advantages of downhill haul gradients. Primary loading is done using small (4-5 m3) electric rope shovels. Belaz trucks of 27 t and 40 t capacity are used for ore and waste transport. Underground The mining method currently in use is long hole sub-level caving with an interval of 14 m between sub-levels. 100 mm diameter long holes are drilled up from each sub-level using a Russian drill rig. Development is undertaken using modern mobile drill rigs and LHDs. Ore is loaded from the draw points using modern diesel-powered 3.5m3 LHDs. The ore is tipped into a central ore pass system where it gravitates into a series of loading chutes on the No11 level. Ore and waste is loaded from the chutes into 2.6 m3 wagons which are hauled to the tip at the mouth of the adit by a locomotive powered by electricity from an overhead power line. Ore and waste is loaded at the tip by a conventional front end loader into 40 t off-road trucks and transported 3.6 km to the mill or the waste dump.
The milling circuit comprises two 7.0 m x 2.3 m SAG mills each fitted with 1,600 kw motors and two 3.6 m x 4.0 m ball mills each fitted with 1,000 kw motors. The normal running format is to operate one SAG mill with both ball mills.
Loaded resin is periodically removed from the leaching circuit and treated through the desorption and electro winning system to generate plated cathode gold. This gold is then smelted to produce bullion bars, which are shipped off site for final refining. Leached pulp containing approximately 300 to 400 ppm residual cyanide is neutralised using the calcium hypochlorite technique, prior to being deposited in a tailings facility approximately 4 km from the plant. All decanted water is recycled from the dam and returned to the plant; any additional make up water requirements are drawn from a nearby stream. |
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