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The chemistry of the Olympic Dam concentrate leaching process and viability of reductive leaching Lung, Felix
Abstract
The WMC Olympic Dam currently mines ore containing chalcocite, bornite, and hematite. The ore is expected to downgrade from chalcocite/bornite to chalcopyrite in the future. The result is increased strain on the direct smelter to blister process currently in operation and a necessary change to a two-step smelter-converter process. The chemistry of the concentrate leaching process was studied with the purpose of applying a reductive leach to enrich the concentrate. Enrichment increases the Cu:S ratio and would allow the current smelting process to continue in the future. Reductive leaching was conducted in acid sulfate media with iron reductant and WMC concentrate over a range of acidity (0.15 M - 0.60 M), reductant to chalcopyrite ratio (0.5 - 2.1), temperature range (25°C - 70°C), and % solids (4 % - 20 %). Select tests were repeated on chalcopyrite and a mixture of chalcopyrite and hematite for comparison. When hematite was present, reduction was modestly successful and most of the iron was consumed by side reactions within the first 10 minutes. Leaching with just chalcopyrite produced much better results. Copper reductant was used but produced minimal results unless high acidity and temperature were applied. Copper was consumed in hematite reduction as well. 77% of the hematite in WMC concentrate was removed by treating the concentrate in 200 g/L sulfuric acid at 90°C over 24 hours. Reductive leaching after this treatment should be investigated as a two-stage process.
Item Metadata
Title |
The chemistry of the Olympic Dam concentrate leaching process and viability of reductive leaching
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Creator | |
Publisher |
University of British Columbia
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Date Issued |
2003
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Description |
The WMC Olympic Dam currently mines ore containing chalcocite, bornite, and
hematite. The ore is expected to downgrade from chalcocite/bornite to chalcopyrite in
the future. The result is increased strain on the direct smelter to blister process currently in operation and a necessary change to a two-step smelter-converter process. The chemistry of the concentrate leaching process was studied with the purpose of applying a reductive leach to enrich the concentrate. Enrichment increases the Cu:S ratio and would allow the current smelting process to continue in the future.
Reductive leaching was conducted in acid sulfate media with iron reductant and WMC
concentrate over a range of acidity (0.15 M - 0.60 M), reductant to chalcopyrite ratio
(0.5 - 2.1), temperature range (25°C - 70°C), and % solids (4 % - 20 %). Select tests
were repeated on chalcopyrite and a mixture of chalcopyrite and hematite for comparison.
When hematite was present, reduction was modestly successful and most of the iron was
consumed by side reactions within the first 10 minutes. Leaching with just chalcopyrite
produced much better results. Copper reductant was used but produced minimal results unless high acidity and temperature were applied. Copper was consumed in hematite
reduction as well. 77% of the hematite in WMC concentrate was removed by treating the
concentrate in 200 g/L sulfuric acid at 90°C over 24 hours. Reductive leaching after this
treatment should be investigated as a two-stage process.
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Extent |
10764280 bytes
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Genre | |
Type | |
File Format |
application/pdf
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Language |
eng
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Date Available |
2009-11-20
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Provider |
Vancouver : University of British Columbia Library
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Rights |
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.
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DOI |
10.14288/1.0079048
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URI | |
Degree | |
Program | |
Affiliation | |
Degree Grantor |
University of British Columbia
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Graduation Date |
2004-05
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Campus | |
Scholarly Level |
Graduate
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Aggregated Source Repository |
DSpace
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Item Media
Item Citations and Data
Rights
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.