Tumbling Mill (Power, Morrell Continuum): Difference between revisions
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== Model theory == | == Model theory == | ||
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Morrell's Continuum approach expresses power input to the motor of a tumbling mill as:{{Morrell (1996a)}} | Morrell's Continuum approach expresses power input to the motor of a tumbling mill as:{{Morrell (1996a)}} | ||
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The net power imparted to the charge in the cylindrical section of the mill was analytically derived as: | The net power imparted to the charge in the cylindrical section of the mill was analytically derived as: | ||
:<math>P_{\rm t} = \frac{\pi g L N_{\rm m} r_{\rm m}}{3 \left (r_{\rm m} - | :<math>P_{\rm t} = \frac{\pi g L N_{\rm m} r_{\rm m}}{3 \left (r_{\rm m} - zr_{\rm i} \right )} \left [ 2r_{\rm m}^3 - 3zr_{\rm m}^2 + r_{\rm i}^3 \left (3z - 2 \right ) \right ] \times \big [ \rho_{\rm c} \left ( \sin \theta_{\rm S} - \sin \theta_{\rm T} \right ) + \rho_{\rm p} \left ( \sin \theta_{\rm T} - \sin \theta_{\rm TO} \big ) \right ] + L \rho_{\rm c} \left ( \frac{N_{\rm m}r_{\rm m} \pi}{\left ( r_{\rm m} - zr_{\rm i} \right)} \right ) \left [ \left( r_{\rm m} - zr_{\rm i} \right )^4 - r_{\rm i}^4 \left (z - 1 \right )^4 \right ] </math> | ||
and for the cone end section: | and for the cone end section: | ||
:<math>P_{\rm c} = \frac{\pi L_{\rm d} g N_{\rm m}}{3(r_{\rm m} - r_{\rm t})} \bigg \{ \left ( r_{\rm m}^4 - 4r_{\rm m} | :<math>P_{\rm c} = \frac{\pi L_{\rm d} g N_{\rm m}}{3(r_{\rm m} - r_{\rm t})} \bigg \{ \left ( r_{\rm m}^4 - 4r_{\rm m}r_{\rm i}^3 + 3r_{\rm i}^4 \right ) \big[ \rho_{\rm c} \left ( \sin \theta_{\rm S} - \sin \theta_{\rm T} \right ) + \rho_{\rm p} \left ( \sin \theta_{\rm T} - \sin \theta_{\rm TO} \right ) \big] \bigg \} + \frac{2 \pi^3 N_{\rm m}^3 L_{\rm d} \rho_{\rm c}}{5(r_{\rm m} - r_{\rm t})} \big ( r_{\rm m}^5 - 5r_{\rm m}r_{\rm i}^4 + 4r_{\rm i}^5 \big )</math> | ||
where: | where: | ||
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* <math>r_{\rm m}</math> is the mill radius inside liners (m) | * <math>r_{\rm m}</math> is the mill radius inside liners (m) | ||
* <math>r_{\rm t}</math> is the trunnion radius inside liners (m) | * <math>r_{\rm t}</math> is the trunnion radius inside liners (m) | ||
* <math> | * <math>r_{\rm i}</math> is the inner charge surface radius (m) | ||
* <math>\theta_{\rm S}</math> is the angle of the charge shoulder (radians) | * <math>\theta_{\rm S}</math> is the angle of the charge shoulder (radians) | ||
* <math>\theta_{\rm T}</math> is the angle of the charge toe (radians) | * <math>\theta_{\rm T}</math> is the angle of the charge toe (radians) | ||
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=== Charge position === | === Charge position === | ||
The charge motion power equations require the position of the charge shoulder (<math>\theta_{\rm S}</math>), charge toe (<math>\theta_{\rm T}</math>), slurry pool level (<math>\theta_{\rm TO}</math>, for overflow discharge mills) and the inner charge surface radius (<math> | The charge motion power equations require the position of the charge shoulder (<math>\theta_{\rm S}</math>), charge toe (<math>\theta_{\rm T}</math>), slurry pool level (<math>\theta_{\rm TO}</math>, for overflow discharge mills) and the inner charge surface radius (<math>r_{\rm i}</math>), in addition to mill dimensions and charge composition. | ||
Morrell developed the following series of relations to estimate the charge geometry.{{Morrell (1996a)}} | Morrell developed the following series of relations to estimate the charge geometry.{{Morrell (1996a)}} | ||
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where <math>r_{\rm t}</math> (m) is the radius of the trunnion. | where <math>r_{\rm t}</math> (m) is the radius of the trunnion. | ||
The inner '''charge surface radius''', <math> | The inner '''charge surface radius''', <math>r_{\rm i}</math> (m), is: | ||
:<math> | :<math>r_{\rm i} = r_{\rm m} \left ( 1 - \frac{2 \pi \beta J_{\rm t}}{2 \pi + \theta_{\rm S} - \theta_{\rm T}} \right )^{0.5}</math> | ||
where the fraction of total charge in the active region, <math>\beta</math> (frac), is: | where the fraction of total charge in the active region, <math>\beta</math> (frac), is: | ||
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where <math>D</math> is mill diameter inside liners (m) | where <math>D</math> is mill diameter inside liners (m) | ||
== Additional notes== | === Additional notes === | ||
The Morrell C model is only applicable to grate discharge mills that do not exhibit a slurry pool, i.e. <math>U \leq 1</math>. | The Morrell C model is only applicable to grate discharge mills that do not exhibit a slurry pool, i.e. <math>U \leq 1</math>. | ||
For overflow discharge mills, the slurry pool component is accounted for by the <math>\theta_{\rm TO}</math> term, which assumes overflow at the exact height of the trunnion lip. | For overflow discharge mills, the slurry pool component is accounted for by the <math>\theta_{\rm TO}</math> term, which assumes overflow at the exact height of the trunnion lip. | ||
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== Excel == | == Excel == | ||
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\theta_{\rm T} \text{ (rad)}\\ | \theta_{\rm T} \text{ (rad)}\\ | ||
\theta_{\rm TO} \text{ (rad)}\\ | \theta_{\rm TO} \text{ (rad)}\\ | ||
r_{\rm i}\text{ (m)}\\ | |||
\end{bmatrix}\;\;\;\;\;\; | \end{bmatrix}\;\;\;\;\;\; | ||
</math> | </math> |
Latest revision as of 11:13, 4 December 2024
Description
This article describes the Morrell Continuum (Morrell C) method for estimating the power draw of a tumbling mill.[1]
The Morrell C model is a theoretical approach based on the dynamics of the grinding charge. By making simplifying assumptions about the charge shape, composition and position, Morrell developed analytical solutions to equations describing the the rate at which potential and kinetic energy is imparted to the charge during mill rotation.
Model theory
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Excel
The Morrell Continuum mill power model may be invoked from the Excel formula bar with the following function call:
=mdMillPower_MorrellC(Parameters as Range)
Invoking the function with no arguments will print Help text associated with the model, including a link to this page.
The Parameters array and model results are defined below in matrix notation, along with an example image showing the selection of the same arrays in the Excel interface:
|
SysCAD
The Morrell Continuum power model is an optional calculation for tumbling mill units. If selected, the input and display parameters below are shown.
See also
References
- ↑ Morrell, S., 1996. Power draw of wet tumbling mills and its relationship to charge dynamics. Pt. 1: a continuum approach to mathematical modelling of mill power draw. Transactions of the Institution of Mining and Metallurgy. Section C. Mineral Processing and Extractive Metallurgy, 105.