(MERAF) for the Base Metals Smelting Sector - CCME
(MERAF) for the Base Metals Smelting Sector - CCME
(MERAF) for the Base Metals Smelting Sector - CCME
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converters when <strong>the</strong> continuous converter is not operating. According to<br />
Noranda, based on <strong>the</strong> current acid marketing dynamics, more sulphur dioxide<br />
captured means more sulphuric acid is produced, and <strong>the</strong> larger <strong>the</strong> losses on an<br />
operating and cash cost basis.<br />
A smelter modernization at Noranda Gaspé could result in lower manpower and<br />
energy costs estimated at $2 million per year. The modernization would result in<br />
more sulphuric acid being produced. According to Noranda, based on <strong>the</strong> current<br />
acid marketing dynamics, more sulphur dioxide captured means larger <strong>the</strong> losses<br />
on an operating and cash cost basis.<br />
Table 80 provides a summary of <strong>the</strong> estimates on <strong>the</strong> impact on <strong>the</strong> operating<br />
costs.<br />
Table 80: Operating Cost Estimates<br />
Site Option <strong>for</strong> Reduction By 2008 Option <strong>for</strong> Reduction By 2015<br />
Hudson Bay Mining<br />
and <strong>Smelting</strong><br />
Inco Thompson<br />
Falconbridge Kidd<br />
Falconbridge<br />
Sudbury<br />
Inco Copper Cliff<br />
Noranda Horne<br />
Incremental improvements to gas<br />
handling system<br />
Annual Cost: $3 to 6 million<br />
Improvements to gas handling<br />
system<br />
Annual Cost: $2 to 7 million<br />
Wet scrubbing technology<br />
Annual Cost: $1 to 2 million<br />
Wet scrubbing technology<br />
Annual Cost: $5 to 8 million<br />
Wet scrubbing of Fluid Bed<br />
Roaster off-gas<br />
Annual Cost: $6 to 8 million<br />
Increasing percentage of matte<br />
processed through <strong>the</strong> Noranda<br />
continuous converter, expansion of<br />
<strong>the</strong> acid plant and connection of<br />
Peirce-Smith converters to acid<br />
plant<br />
Installation of hydrometallurgical<br />
process*<br />
Annual Savings: $2 to 3 million<br />
Smelter modernization and acid<br />
plant<br />
Annual Cost: $35 to 45 million<br />
No major changes beyond 2008<br />
No major changes beyond 2008<br />
Continuous converting<br />
technology**<br />
Annual Savings: $2 million<br />
Potential costs due to additional<br />
acid production<br />
No major changes beyond 2008<br />
No operating savings identified as<br />
Peirce-Smith converters will<br />
continue to operate. Potential costs<br />
due to additional acid production<br />
Noranda Gaspé Incremental Improvements Smelter Modernization<br />
Annual Savings: $2 million<br />
186