Review of 2005 |
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| FY2005 | FY2004 | % change | |||||
| Mining sales | (Rm) | 8,396.8 | 7,679.2 | 9.3 | |||
| Platinum | 5,745.0 | 5,667.6 | 1.4 | ||||
| Palladium | 661.9 | 711.5 | (7.0) | ||||
| Rhodium | 927.6 | 422.0 | 119.8 | ||||
| Nickel | 722.0 | 575.2 | 25.5 | ||||
| Other | 340.3 | 302.9 | 12.3 | ||||
| Mining cost of sales | (4,875.7) | (4,495.9) | (8.4) | ||||
| On-mine operations | (3,346.3) | (3,122.4) | (7.2) | ||||
| Concentrating and | |||||||
| smelting operations | (764.0) | (715.6) | (6.8) | ||||
| Refining operations | (376.8) | (337.3) | (11.7) | ||||
| Amortisation of mining | |||||||
| assets | (491.8) | (481.5) | (2.1) | ||||
| Increase/(decrease) | |||||||
| in metal inventories | 103.2 | 160.9 | (35.9) | ||||
| Mining gross profit | 3,521.1 | 3,183.3 | 10.6 | ||||
| (Loss)/profit from metal | |||||||
| purchase transactions | (Rm) | 11.7 | (1.7) | (788.2) | |||
| Sales of metals purchased | 3,643.8 | 3,419.5 | 6.6 | ||||
| IRS | 3,640.4 | 3,187.5 | 14.2 | ||||
| Other | 3.4 | 232.0 | (98.5) | ||||
| Cost of metals purchased | (3,632.1) | (3,421.2) | (6.2) | ||||
| IRS | (3,630.7) | (3,176.8) | (14.3) | ||||
| Other | (1.4) | (244.4) | 99.4 | ||||
| Gross profit | 3,532.8 | 3,181.6 | 11.0 | ||||
| Gross margin ex mine | % | 41.9 | 41.5 | 1.0 | |||
| Other operating costs | (Rm) | (251.5) | (224.8) | (11.9) | |||
| Royalty expense | (388.8) | (397.4) | 2.2 | ||||
| Sales volumes ex-mine | |||||||
| Platinum | (000 oz) | 1,103.1 | 1,070.5 | 3.0 | |||
| Palladium | (000 oz) | 512.2 | 471.9 | 8.5 | |||
| Rhodium | (000 oz) | 126.9 | 116.1 | 9.3 | |||
| Nickel | (000 t) | 7.9 | 7.1 | 11.3 | |||
| Sales volumes metals | |||||||
| purchased IRS | |||||||
| Platinum | (000 oz) | 434.0 | 383.2 | 13.3 | |||
| Palladium | (000 oz) | 304.7 | 257.6 | 18.3 | |||
| Rhodium | (000 oz) | 57.5 | 49.0 | 17.3 | |||
| Nickel | (000 t) | 4.1 | 5.4 | (24.1) | |||
| Prices achieved ex-mine | |||||||
| Platinum | ($/oz) | 841 | 767 | 9.6 | |||
| Palladium | ($/oz) | 208 | 219 | (5.0) | |||
| Rhodium | ($/oz) | 1,168 | 519 | 125.0 | |||
| Nickel | ($/t) | 14,598 | 11,758 | 24.2 | |||
| Exchange rate achieved | |||||||
| ex-mine | (R/$) | 6.21 | 6.92 | (10.3) | |||
| Production ex-mine | |||||||
| Tonnes milled | |||||||
| ex-mine | (000 t) | 15,778 | 15,639 | 0.9 | |||
| Platinum refined | (000 oz) | 1,114.6 | 1,090.3 | 2.2 | |||
| Palladium refined | (000 oz) | 515.2 | 501.2 | 2.8 | |||
| Rhodium refined | (000 oz) | 130.3 | 116.1 | 12.2 | |||
| Nickel refined | (000 t) | 7.9 | 6.9 | 14.5 | |||
| PGM refined | |||||||
| production | (000 oz) | 2,061.9 | 1,975.5 | 4.4 | |||
| Total cost 1 | 4,738.6 | 4,400.1 | (7.7) | ||||
| per tonne milled | (R/t) | 300 | 281 | (6.8) | |||
| ($/t) | 49 | 41 | (19.5) | ||||
| per PGM ounce | |||||||
| refined | (R/oz) | 2,298 | 2,227 | (3.2) | |||
| ($/oz) | 371 | 324 | (14.5) | ||||
| per platinum ounce | |||||||
| refined | (R/oz) | 4,251 | 4,036 | (5.3) | |||
| ($/oz) | 687 | 588 | (16.8) | ||||
| net of revenue received | |||||||
| for other metals | (R/oz) | 1,872 | 2,195 | 14.7 | |||
| ($/oz) | 302 | 320 | 5.6 | ||||
| Capital expenditure | (Rm) | 1,693 | 1,197 | 41.4 | |||
| ($m) | 274 | 174 | 57.5 | ||||
| 1 Restatement in FY2004 as a result of the adoption of IFRS2 (share-based payments). | |||||||
Impala Platinum platinum production (000oz)![]() |
Impala Platinum cost (R/platinum ounce)![]() |
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Impala Platinum capital expenditure (R million)
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| FY2005 | FY2004 | FY2003 | FY2002 | FY2001 | ||
| Tonnes milled ex-mine | (000 t) | 15,778 | 15,639 | 15,042 | 14,850 | 14,840 |
| UG2 milled | (%) | 45.5 | 46.1 | 45.7 | 53.6 | 49.6 |
| Headgrade | (g/t 5PGE+Au) | 4.82 | 4.91 | 5.06 | 5.05 | 4.90 |
| Platinum refined production | (000 oz) | 1,115 | 1,090 | 1,040 | 1,025 | 1,002 |
| PGM refined production | (000 oz) | 2,062 | 1,976 | 1,924 | 1,895 | 1,877 |
| Total cost/tonne milled | (R/t) | 300 | 281 | 266 | 239 | 213 |
| ($/t) | 48.5 | 40.9 | 29.5 | 23.6 | 28.0 | |
| Cost/PGM ounce refined | (R/oz) | 2,298 | 2,227 | 2,078 | 1,872 | 1,685 |
| ($/oz) | 371 | 324 | 230 | 185 | 221 | |
| Cost/platinum ounce refined | (R/oz) | 4,251 | 4,036 | 3,843 | 3,459 | 3,156 |
| ($/oz) | 687 | 588 | 426 | 341 | 415 | |
| Net of revenue received | (R/Pt oz) | 1,872 | 2,195 | 909 | (708) | (1,879) |
| for other metals | ($/Pt oz) | 302 | 320 | 101 | (70) | (247) |
| Capital expenditure | (Rm) | 1,693 | 1,197 | 1,079 | 1,009 | 978 |
| ($m) | 274 | 174 | 120 | 100 | 129 | |
| Labour complement* | (000) | 26.9 | 27.5 | 28.4 | 27.9 | 28.0 |
| Productivity | (m2/panel man) | 40.1 | 39.2 | 40.7 | 40.2 | 40.7 |
| (Pt oz/employee) | 41 | 40 | 37 | 37 | 36 | |
| * Average in service for the year (excluding capital projects). | ||||||
| Restatement of previous year's unit cost was as a result of the adoption of IFRS2 (share-based payments). | ||||||
| FY2005 | FY2004 | % change | |
| Conventional mining | 13,889 | 14,304 | (2.9) |
| Merensky | 6,711 | 7,087 | (5.3) |
| UG2 | 7,178 | 7,217 | (0.5) |
| Mechanized mining (Merensky) | 1,362 | 624 | 118.3 |
| Opencast mining (Merensky) | 527 | 711 | (25.9) |
| Total production | 15,778 | 15,639 | 0.9 |

Impala's strategy to develop and implement new technology aims to improve both safety and productivity and to reduce costs so as to give the operation a sustained competitive advantage. Impala is investing R45 million annually for three years (from FY2004 to FY2006) on new technology and mechanised mining. During FY2005, just over 1.4 million tonnes or 8.6% of total production from the Impala mining operation was from mechanised mining, primarily from 12 and 14 shafts. There is scope to increase the proportion of ore mined using mechanised methods to a maximum of 12%.
These technologies, which remove people from high-risk areas, are in line with global trends to create work environments that have a more skilled and less physically arduous profile. Two new technologies are currently being implemented, the drill jig, referred to as dynamic drilling technology, and extra low-profile trackless mining vehicles (mechanised mining).
The drill jigs have been designed to improve drilling accuracy and have the potential to increase the advance per blast by 10 15% to 1 metre. Drill jigs were implemented at 48 panels on the mine by the end of the 2005 financial year and a total of 300 Merensky panels by FY2007. Currently this technology is best suited to Merensky panels but steps are underway to adapt it for use on the narrower UG2 reef.
Low-profile trackless mining vehicles are used in stoping widths of 1.8 metres and trials are presently underway to test extra-low profile vehicles to operate in stoping widths of 1.2 metres. This mechanised equipment, which is suited for selected areas where the dips are flat and there is likely to be minimal dilution, enables a faster build-up to full production. The low-profile trackless equipment is being employed at 12 shaft. Currently, 57% of production at 12 shaft comes from mechanised mining, increasing to and stabilising at around 77% by FY2007. At 14 shaft, the current level of tonnage from mechanised mining is 21%. This is scheduled to rise to 24% in FY2006, after which it will decline and be maintained at 17% by FY2008.
Also under development and evaluation is a new cutting machine, the Alpine Reef Miner (ARM) 1,100 which cuts Merensky ore (as opposed to conventional drilling and blasting). In tandem, systems to clean the cutter's path and pick up ore are also being developed. Cutters generate copious amounts of dust and a scrubbing system has been devised and implemented to reduce this problem. Other technologies being tested at Impala include a locomotive drill-rig, a trackless sweeping machine, gas-based blasting systems, an invert drop raiser and an oil-less drill.
In line with the mining strategy, the capital programme is designed to ensure production of 1.1 million ounces of platinum annually from the Impala Platinum mining operation over the next 30 years. The first of these capital projects is the declines project which involves developing decline shafts below the current third generation shafts, thereby extending the lives of existing shaft systems and establishing access to deeper reserves. Production from the decline shafts will replace the mineral reserves from the first and second generation shafts which are nearing depletion. To date, three of the declines are at full production with most of the planned increase in tonnes milled to come from the 11, 12 and 14 shaft declines. The remaining two declines are still in the build-up phase.
The second major mining project is a greenfields one involving the construction of two new shafts. In September 2004, the Implats Board approved capital expenditure of R6.6 billion (in nominal terms) for the development of 16 and 20 shafts, the first of the new fourth generation shafts. At full production these two shafts will together produce 355,000 ounces of platinum annually; 20 shaft is scheduled to come into production in 2009 and 16 shaft in 2012. Construction work on the two shafts began in October 2004.
Work on the E & F Block (between 2 and 4 shafts) began in July 2004. Site establishment, earthworks, the office lay-out area and installation of a service winder have been completed. The equipping of the incline shaft and refurbishment of the headgear steel structure started during January 2005 and the winder will be installed by August 2005. Production is scheduled to begin in December 2006.
The 11 shaft decline project is nearing completion and a feasibility study exploring a further extension to this decline has been completed. This study will be presented to the Board for approval in August 2005.
14 shaft decline (which is a four-level decline) project is also nearing completion. Production from the first level has begun. A feasibility study is currently underway to extend this decline to access reserves below the fourth level.
With seven operational levels, 16 shaft will be 1,657 metres deep and will produce an estimated 226,500 tonnes of reef a month. The shaft will access both the Merensky and UG2 orebodies, although initially the focus will be on the former. There will be a down-cast shaft for the transport of rock, material and men, which will be the deepest, largest diameter, and highest tonnage shaft at Impala Platinum, as well as an up-cast ventilation shaft. As the virgin rock temperature will be 57°C at the deepest level, the refrigeration requirements will be extensive. The concrete headgear will be 108 metres high, the tallest in the world, and will house two winders, one to hoist men and material and the other rock. Conventional methods will be applied and all Merensky panels will be equipped with drill jigs.
Although it will be shallower than 16 shaft, 20 shaft will have a depth of 1,058 metres. 20 shaft, which is adjacent to 12 North shaft, will have a single large station below surface, with one decline system feeding upwards and another one feeding downwards. The focus initially will be on the mining of the Merensky Reef and once this has been depleted, the focus will shift to the UG2. Initial tonnage capacity forecasts are that 20 shaft will produce 185,000 tonnes per month of reef.
The development of the fourth generation shafts will be extended with investigations and the pre-feasibility study on 17 shaft due to begin shortly.

Impala Platinum's Mineral Processes incorporates the concentrating and smelting plants which process the ore mined at Impala's mining operations as well as concentrate sourced on behalf of IRS. Mineral Processes is currently running at peak performance with, for the second year in a row, tonnes milled, smelter throughputs and recoveries at record levels.
During the year, tonnes milled rose by 1% to 15.78 million tonnes. Overall concentrator recoveries rose again to a record level of 84.3% despite the increase in throughput. The increase in these recoveries, which was equivalent to 13,500 ounces of platinum for the year, was largely a result of the high-energy flotation technology implemented at the UG2 plant at a cost of R26 million. Recovery rates at the UG2 plant rose to 78% for the year. The tails scavenging plant, commissioned in December 2003, continued to deliver and contributed more than 1% to overall recoveries. The smelter was again in a position to benefit from the spot business arising from Lonplats.
Overall, operating costs at Mineral Processes remain below R50 per tonne milled.
Over the next 12 months, planned capital expenditure will be primarily on the implementation of high-energy flotation technology at the MF2 plant, which treats about 30% of the UG2 ore mined. This will help to increase recoveries to 79%, in line with those of the UG2 plant.
Impala Platinum's Refineries, which consists of the Base Metal Refinery (BMR) and the Precious Metals Refinery (PMR), continued to perform in line with expectations. Total output decreased by 6% to 1.848 million platinum ounces, a consequence of the once-off processing of material from Lonplats (232,000 ounces) in the previous financial year. If the once-off Lonplats material is excluded, then Impala Refineries reported record levels of production for all the platinum group metals produced, with the exception of ruthenium. Net of the Lonplats material, headline platinum production rose by 5% or 86,000 ounces.
The use of high-purity pipeline hydrogen from Sasol has been successfully incorporated into operations with better-than-expected efficiency gains (regarding the metallisation of nickel and cobalt), and an elimination of associated CO2 (greenhouse gas) emissions, of 3,000 tonnes per month, a by-product of the old, on-site reforming.
Metal recovery levels were maintained as were efficiencies and costs, and there was no deterioration in metal pipelines, despite the extensive expansion work undertaken during the course of the year.
Major capital projects at both the BMR and PMR have progressed successfully and will position Refineries well, both in terms of the broader Implats growth vision and in terms of current and future environmental legislation.
At the BMR, the major issue is the expansion project which is scheduled for completion in September 2005 and which will take the plant to a capacity of over 2 million ounces of platinum. Additional work in the 2006 financial year will progress plant capacity towards 2.3 million ounces. The ball mill, expanded second-stage (copper) leach, nickel sintering furnace (and associated nickel product handling circuit) and the ammonium sulphate crystalliser are all operational and providing relief to previously capacity-constrained areas.
The Ambatovy nickel project is an exciting development, which will involve a significant expansion to the BMR. The project has great potential to realise economies of scale and further improve base metal processing efficiencies.
At the PMR, the capital programme which is scheduled for completion at the end of FY2006 will increase the capacity to 2.3 million ounces of platinum. The processing expansion areas of base metal removal, ruthenium distillation and palladium ion exchange have all been successfully commissioned. Various pieces of gas scrubbing and liquid effluent handling equipment are well-advanced in construction, for commissioning early in the 2006 financial year. This will be followed by a full and detailed performance assessment to ensure that the requirements of the Environmental Impact Assessment (which incorporates the future anticipated permit conditions) are being, and will be met, on a continuous basis.
The research and development programme into ion-exchange technology has produced significant results in the further optimisation of existing, resin-based technology, leading to operational cost reductions in key processing areas. Investigations into alternate ion exchange methods have advanced to preliminary commercial-scale trials. New generation refining technology is being examined at bench scale with appreciable potential benefits in terms of both unit cost and pipeline performance anticipated.
The ability to recycle secondary materials within Refineries (as opposed to incurring significant external toll fees and exposing the operation to rand volatility) was further enhanced during the year with a dramatic improvement in the processing ability to purge certain minor metals and deleterious elements. This creates a far more robust process and allows for sustained, low-cost recycling.