Difference between revisions of "Austin SAG model"
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=== Percent solids === |
=== Percent solids === |
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The model is run with a fixed 80% solids by weight <sup>[[Bibliography:_Mill_power_draw_models|Doll, 2013]]</sup>. This is because the form of the equation proposed by Austin appears to have the %solids term in the wrong place (denominator of the expression rather than the numerator where other models put it). The calibration presented at IMPC 2016 suggests the fixed %solids term is reasonably valid over the range of 60% to 80% solids. |
The model is run with a fixed 80% solids by weight <sup>[[Bibliography:_Mill_power_draw_models|Doll, 2013]]</sup>. This is because the form of the equation proposed by Austin appears to have the %solids term in the wrong place (denominator of the expression rather than the numerator where other models put it). The calibration presented at IMPC 2016 suggests the fixed %solids term is reasonably valid over the range of 60% to 80% solids. |
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+ | == Model Inputs== |
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+ | <b>Motor characteristics</b> are also requested: |
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+ | * Motor rated power (output shaft) |
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+ | * Mechanical efficiency of downstream drive (pinions, gearboxes) |
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+ | * Motor efficiency and any other efficiency factors to the DCS measurement position in the network. |
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+ | * Motor rated speed, in units of mill RPM (not motor RPM, must multiply by gear ratios). |
Revision as of 23:57, 17 June 2016
History
The SAG mill model by proposed by Leonard Austin (1990) was largely based on modifications of earlier tumbling mill models by Hogg & Fuerstenau and F. Bond. The model uses a kinetic-potential energy balance to describe the power draw of a mill charge. Many geometric components of the earlier models were fit to empirical relationships measured by Austin.
Model Form
The power draw model for a SAG mill cylinder of the following form:
Where:
- P is the power evolved at the mill shell, kW
- K and A are empirical fitting factors (use 10.6 and 1.03, respectively)
- D is the mill effective diameter (inside the effective liner thickness), m
- L is the mill effective grinding length (also referred to as the 'belly length), m
- Jtotal is the mill total volumetric filling as a fraction (eg. 0.30 for 30%)
- εB is the porosity of the rock and ball load (use 0.3)
- wC is the charge %solids, fraction by weight (use 0.80 Doll, 2013)
- Jballs is the mill volumetric filling of balls as a fraction (eg. 0.10 for 10%)
- ρX is the density of component X, t/m3
- φC is the mill speed as a fraction of critical (eg. 0.75 for 75% of critical)
Mill cone angles
The model supports flat-ended mills (cone angle of 0°) or a cone angle of 15°. Any other value entered for the cone angle will be treated as 15°.
To account for cone ends of mills, an allowance of 5% is used Doll, 2013 instead of the formula proposed by Austin.
Percent solids
The model is run with a fixed 80% solids by weight Doll, 2013. This is because the form of the equation proposed by Austin appears to have the %solids term in the wrong place (denominator of the expression rather than the numerator where other models put it). The calibration presented at IMPC 2016 suggests the fixed %solids term is reasonably valid over the range of 60% to 80% solids.
Model Inputs
Motor characteristics are also requested:
- Motor rated power (output shaft)
- Mechanical efficiency of downstream drive (pinions, gearboxes)
- Motor efficiency and any other efficiency factors to the DCS measurement position in the network.
- Motor rated speed, in units of mill RPM (not motor RPM, must multiply by gear ratios).