Difference between revisions of "Benchmarking: Bond - Cadia"
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==Benchmarking: Bond/Barratt - Cadia== |
==Benchmarking: Bond/Barratt - Cadia== |
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''Dunne, R., Morrell, S., Lane, G., Valery, W. and Hart, S.'', '''Design of the 40 foot diameter SAG mill installed at the Cadia gold copper mine'''. Proceedings of SAG 2001, pages I-43 to I-58. |
''Dunne, R., Morrell, S., Lane, G., Valery, W. and Hart, S.'', '''Design of the 40 foot diameter SAG mill installed at the Cadia gold copper mine'''. Proceedings of SAG 2001, pages I-43 to I-58. |
Revision as of 18:50, 31 January 2015
Contents
Benchmarking: Bond/Barratt - Cadia
Dunne, R., Morrell, S., Lane, G., Valery, W. and Hart, S., Design of the 40 foot diameter SAG mill installed at the Cadia gold copper mine. Proceedings of SAG 2001, pages I-43 to I-58.
Lane, G., Foggiatto, B. and Bueno, M, Power-based comminution calculations using Ausgrind. Proceedings of Procemin 2013, Chapter 2, paper 2.
Papers describe a survey conducted shortly after start-up.
Ore characterization
- Monzonite ore type,
- WiC = 16.5 (metric)
- WiRM = 19.0 (metric)
- WiBM = 17.1 (metric)
- A×b = 36
- DWI = 7.5
- density = 2.7 t/m³
SAG mill characteristics
- Diameter inside shell = 12.2 m (40 ft)
- EGL = 6.1 m (20 ft)
- Ball filling = 12% v/v
- Total filling = 25% v/v
- Mill speed = 78% of critical (Lane et al, 2013 appears to have a typo. They claim 72% which actually looks like the BM speed)
- Pulp density = 70% w/w
- SAG feed is primary crushed to F80 = 98 mm
Ball mill characteristics
- Diameter inside shell = 6.7 m (22 ft)
- EGL = 11.3 m (36.5 ft)
- Ball filling = 30% v/v
- Mill speed = 72% of critical
- Pulp density = 70% w/w
- Ball mill circuit product P80 = 170 µm
Modelling
Results
Result for default model conditions:
Esag | Epeb | Ebm | Etotal | t/h | T80, mm | |
---|---|---|---|---|---|---|
Predicted | 8.6 | 0.3 | 8.5 | 17.4 | 2000 | 2.06 |
Survey | 8.6 | - | 8 | 16.6 | 2065 | 1.34 |
Difference | 0 | 0.3 | 0.5 | 0.8 | -65 | 0.72 |
Difference | 0% | - | 6% | 5% | -3% | 54% |