Difference between revisions of "Template:EssbmEquation"

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(Created page with "category:Formula ==Single-stage Ball Mill Specific Energy Equation== This is a basic equation of the family of Bond/Barratt calculations. It describes specific energy req...")
 
 
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<noinclude>
 
[[category:Formula]]
 
[[category:Formula]]
 
==Single-stage Ball Mill Specific Energy Equation==
 
==Single-stage Ball Mill Specific Energy Equation==
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<math> E_{ssbm}=</noinclude>
 
<math> E_{ssbm}=</noinclude>
{{BondWiEquation|Wi=Wi_{C}|F80=F_{80}|P80=9400 }} + {{BondWiEquation|Wi=Wi_{RM}|F80=9400|P80=2100 }}\times EF_4^{RM} + {{BondWiEquation|Wi=Wi_{BM}|F80=2100|P80=P_{80} }} \times EF_4^{BM} \times EF_5</noinclude></math>
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{{BondWiEquation|Wi=Wi_{C}|F80=F_{80}|P80=9400 }} + {{BondWiEquation|Wi=Wi_{RM}|F80=9400|P80=2100 }}\times EF_4^{RM} + {{BondWiEquation|Wi=Wi_{BM}|F80=2100|P80=P_{80} }} \times EF_4^{BM} \times EF_5<noinclude></math>
   
 
See list of pages that use this formula: {{Special:WhatLinksHere/Template:EssbmEquation}}
 
See list of pages that use this formula: {{Special:WhatLinksHere/Template:EssbmEquation}}

Latest revision as of 22:40, 2 December 2012

Single-stage Ball Mill Specific Energy Equation

This is a basic equation of the family of Bond/Barratt calculations. It describes specific energy requirement of a most efficient comminution circuit consisting of a multi-stage crushing plant followed by single-stage ball milling. The conventional form of a single-stage ball mill equation requires Bond rod mill work index testing (see Rowland, 2006 for a detailed explanation) to account for the ore hardness in the size range of 10 mm down to about 2 mm.

Essbm as a function of feed size F80, transfer size T80 and the work index values at three different sizes:

  • WiC: the Bond low-energy impact crushing work index, covers 20 mm to 100 mm size range.
  • WiRM: the Bond rod mill work index, covers 2 mm to 10 mm size range.
  • WiBM: the Bond ball mill work index, less than 2 mm size range.

There are a series of calibration parameters that correspond to the size ranges listed above. It is useful to think of this model as a hypothetical 3-stage crushing — rod mill — ball mill circuit with a calibration adjustment (1.25) for SAG milling.

  • PC is the hypothetical tertiary crusher product size (default=9400 µm)
  • PR is the hypothetical rod mill product size (default=2100 µm)

Three Rowland Efficiency Factor adjustments are required:

  • EF4RM is the oversize feed factor for rod milling, and is a function of the hypothetical crusher product size or the larger of work index for crushing and work index for rod milling.
  • EF4BM is the oversize feed factor for ball milling, and is a function of the hypothetical rod mill product size and the work index for rod milling.


 E_{ssbm}=</noinclude>
{{BondWiEquation|Wi=Wi_{C}|F80=F_{80}|P80=9400 }} + {{BondWiEquation|Wi=Wi_{RM}|F80=9400|P80=2100 }}\times EF_4^{RM} + {{BondWiEquation|Wi=Wi_{BM}|F80=2100|P80=P_{80} }} \times EF_4^{BM} \times EF_5<noinclude>

See list of pages that use this formula: