Difference between revisions of "Morrell C-model"
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[[category:Models]] |
[[category:Models]] |
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[[category:Mill power draw models]] |
[[category:Mill power draw models]] |
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| + | Applies to both SAG and ball mills, with variants for grate-discharge and overflow mills. |
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This model was developed as part of the PhD thesis of Stephen Morrell at the University of Queensland and is the model used in the JK SimMet software for determining mill power draw. It is described as the "C-model" and should not be confused with the more empirical "D-model" that has a form similar to the Loveday equation. |
This model was developed as part of the PhD thesis of Stephen Morrell at the University of Queensland and is the model used in the JK SimMet software for determining mill power draw. It is described as the "C-model" and should not be confused with the more empirical "D-model" that has a form similar to the Loveday equation. |
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The same underlying model is used for SAG and ball milling, with minor differences for the way the charge density is calculated and whether the mill is a grate discharge (most of the SAG mills) or overflow discharge (typically a ball mill). |
The same underlying model is used for SAG and ball milling, with minor differences for the way the charge density is calculated and whether the mill is a grate discharge (most of the SAG mills) or overflow discharge (typically a ball mill). |
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| − | Within the classification, there are also two versions of the Morrell C-model |
+ | Within the classification, there are also two versions of the Morrell C-model: |
| + | <b>the "simplified" Morrell C-model </b>where only the major inputs are requested from the user |
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| − | * mill diameter |
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| + | * mill nominal diameter inside shell |
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* mill effective grinding length |
* mill effective grinding length |
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* ball load |
* ball load |
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| + | * [[Media density|ball density]] |
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| − | * ball density (only full model, 7.8 t/m<sup>3</sup> used for simplified) |
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* pulp percent solids |
* pulp percent solids |
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* mill speed |
* mill speed |
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| + | * liner effective thickness |
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| − | * sphere packing geometric factor J<sub>void</sub> |
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| − | * cone end angle (only full model, simplified: 30° for SAG and 15° used for ball mill) |
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| − | * trunnion diameter (only full model, fraction of mill diameter used for simplified) |
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| + | <b>the "full" Morrell C-model</b> where all possible inputs are available. |
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| − | * k-factor, conversion of "net power to gross power" (1.26) |
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| + | |||
| + | * mill nominal diameter inside shell |
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| + | * mill effective grinding length |
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| + | * ball load |
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| + | * [[Media density|ball density]] |
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| + | * pulp percent solids |
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| + | * mill speed |
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| + | * liner effective thickness |
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| + | * cone end angle |
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| + | * trunnion diameter |
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| + | * k-factor, empirical conversion of "net power to gross power" (1.26) |
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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). |
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| + | * Quantity of pinions (and motors) |
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==Model Outputs== |
==Model Outputs== |
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Latest revision as of 00:01, 18 June 2016
Applies to both SAG and ball mills, with variants for grate-discharge and overflow mills.
This model was developed as part of the PhD thesis of Stephen Morrell at the University of Queensland and is the model used in the JK SimMet software for determining mill power draw. It is described as the "C-model" and should not be confused with the more empirical "D-model" that has a form similar to the Loveday equation.
The simplest explanation of the model is that it is a friction balance between concentric layers within a moving mill charge which is used to calculate the torque experienced by the mill due to the charge geometry. The model contains several sub-equations that govern the charge geometry and is too complicated to explain here. People seeking more information should buy the book Mineral Comminution Circuits, Their Operation and Optimisation from JK Tech: http://www.jktech.com.au/mineral-comminution-circuits .
Model Inputs
The same underlying model is used for SAG and ball milling, with minor differences for the way the charge density is calculated and whether the mill is a grate discharge (most of the SAG mills) or overflow discharge (typically a ball mill).
Within the classification, there are also two versions of the Morrell C-model:
the "simplified" Morrell C-model where only the major inputs are requested from the user
- mill nominal diameter inside shell
- mill effective grinding length
- ball load
- ball density
- pulp percent solids
- mill speed
- liner effective thickness
the "full" Morrell C-model where all possible inputs are available.
- mill nominal diameter inside shell
- mill effective grinding length
- ball load
- ball density
- pulp percent solids
- mill speed
- liner effective thickness
- cone end angle
- trunnion diameter
- k-factor, empirical conversion of "net power to gross power" (1.26)
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).
- Quantity of pinions (and motors)
Model Outputs
The published version of this model provides power measured at the motor input of an induction motor driving a gearbox on a geared mill. This motor input is immediately converted to mill shell power for use in circuit model equations by multiplying the model result by 0.97 mechanical efficiency factor and by 0.96 typical induction motor efficiency factor.
The displayed Morrell C-model result in sagmilling.com is always corrected to mill shell power.
