(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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In addition to <strong>the</strong>se measures, Hatch Associates has estimated that a 10%<br />
reduction in emissions was feasible from <strong>the</strong> facilities not analyzed. This 10%<br />
reduction <strong>for</strong> <strong>the</strong> “Rest of <strong>Sector</strong>” is assumed to be <strong>for</strong> <strong>the</strong> total releases <strong>for</strong> all<br />
<strong>the</strong> facilities not specifically identified, not <strong>for</strong> each individual facility<br />
4.4.7. Summary of Capital Costs<br />
The capital costs of release reductions were estimated in Hatch Associates’<br />
report, Review of Environmental Releases <strong>for</strong> <strong>the</strong> <strong>Base</strong> <strong>Metals</strong> <strong>Smelting</strong><br />
<strong>Sector</strong> 164 . This report was reviewed by <strong>the</strong> <strong>Base</strong> <strong>Metals</strong> Environmental Technical<br />
Advisory Group (BETAG) and <strong>the</strong>re is general agreement on <strong>the</strong> overall<br />
correctness of <strong>the</strong> estimates.<br />
Table 79 presents a summary of <strong>the</strong> capital costs discussed above.<br />
Table 79: Capital 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 Sudbury<br />
Inco Copper Cliff<br />
Noranda Horne<br />
Incremental improvements to<br />
gas handling system<br />
Cost: $30 to 60 million<br />
Improvements to gas handling<br />
system<br />
Cost: $20 to 70 million<br />
Wet scrubbing technology or<br />
High Temperature Particulate<br />
Removal<br />
Cost: $6 to 20 million<br />
Wet scrubbing technology<br />
Cost: $50 to 80 million<br />
Wet scrubbing of Fluid Bed<br />
Roaster off-gas<br />
Cost: $60 to 80 million<br />
Increasing percentage of matte<br />
processed through <strong>the</strong> Noranda<br />
continuous converter, expansion<br />
of <strong>the</strong> acid plant and connection<br />
of Peirce-Smith converters to<br />
acid plant<br />
Cost: $20 to 50 million<br />
Installation of hydrometallurgical<br />
process*<br />
Cost: $500 to 800 million<br />
Smelter modernization and acid<br />
plant<br />
Cost: $500 to 700 million<br />
No major changes beyond 2008<br />
No major changes beyond 2008<br />
Continuous converting<br />
technology*<br />
Cost: $200 to 350 million<br />
No major changes beyond 2008<br />
164 Hatch Associates, Review of Environmental Releases <strong>for</strong> <strong>the</strong> <strong>Base</strong> <strong>Metals</strong> <strong>Smelting</strong> <strong>Sector</strong>,<br />
prepared <strong>for</strong> Environment Canada, dated November 2000<br />
184