Difference between revisions of "Benchmarking: Ball Mill Power Draw Models"

Revision as of 19:01, 26 January 2014

Nelson, M; Valery, W; Morrell, S, Performance Characteristics and Optimisation of the Fimiston (KCGM) SAG Mill Circuit, Page 233 - 248, SAG 1996 Conference, Vancouver, Canada.

Survey	Survey Power, kW at input	Mill speed, %critical	Total load, %v/v	Pulp %solids, w/w	Morrell BM Model, kW at input / shell	Nordberg Model, kW at input / shell
Survey 1	3,864	68.3	38.7	72.0	3,933 / 3,776	3,592 / 3,345

Muteb, P. & Allaire, J., Meadowbank Mine Process Plant Throughput Increase, Proceedings of the Canadian Mineral Processors Annual General Meeting, Ottawa, Canada, January 2013.

	DCS Power, kW	Mill filling	Morrell Model, kW	Nordberg model, kW no density correction	Nordberg model, kW density correction
May 2012	4,341	30.6% v/v	4,765 (+9.3%)	4,426 (+1.9%)	4,753 (+9.5%)

Latchireddi, S. & Faria, E., Achievement of High Energy Efficiency in Grinding Mills at Santa Rita, Proceedings of the Canadian Mineral Processors Annual General Meeting, Ottawa, Canada, January 2013.
Faria, E. & Latchireddi, S., Commissioning and Operation of Milling Circuit at Santa Rita Nickel Operation, Paper #137: Proceedings of the International Autogenous Grinding, Semiautogenous Grinding and High Pressure Grinding Roll Technology Conference, Vancouver, Canada, September 2011.

	DCS Power, kW	Mill filling	Morrell Model, kW	Nordberg model, kW (no density correction)	Nordberg model, kW (density correction)
July 2010	5085	27.5% v/v	4979 (-2.1%)	4706 (-8.1%)	5083 (0.0%)

@@ Line 38: / Line 38: @@
 ! Mill filling
 ! Morrell Model, kW
-! Nordberg model, kW
-density correction
 ! Nordberg model, kW
 no density correction
+! Nordberg model, kW
+density correction
 |-
 | May 2012
@@ Line 47: / Line 47: @@
 | 30.6% v/v
 | 4,765 (+9.3%)
-| 4,753 (+9.5%)
 | 4,426 (+1.9%)
+| 4,753 (+9.5%)
 |}