grinding cycles. The Bond Work Index is calculated using the formula: 𝑖=1,1 44,5 𝑃𝑐 0,23𝐺,82(10 √𝑃80 −10 √𝐹80) (1) where W i – Bond work index (kWh/t) P c – test sieve mesh size (µm) G – weight of the test sieve fresh undersize per mill revolution (g/rev) F 80 – sieve mesh size passing 80% of the feed before grinding(µm) P 80
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comminution circuit will be predicted plus the individual specific energies of the primary crusher, pebble crusher and combined SAG/Ball mill stages. The model was originally developed using 3 data bases of operating comminution circuits to validate and benchmark its accuracy. These 3 data bases cover crushers, HPGRs and AG/SAG/ball mill circuits.
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W is the work index measured in a laboratory ball mill (kilowatthours per metric or short ton) P 80 is the mill circuit product size in micrometers; F 80 is the mill circuit feed size in micrometers. Rod mill. A rotating drum causes friction and attrition between steel rods and ore particles.
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Each crusher is designed to work with a certain maximum size of raw material, and often delivers its output to a screening machine which sorts and directs the product for further processing. Typically, crushing stages are followed by milling stages if the materials need to be further reduced.
Enter the width, length, thickness, and product density and hit the "Calculate" button to calculate your estimate. If you do not know the product density, use the optional density estimator* or contact a local sales representative.
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Capacity is primarily a function of: crusher design characteristics such as width and depth of crushing chamber. open and closed side settings. options on feeding method, intermittent or continuous. operating characteristics like the length of stroke, the number of strokes per minute, and the nip angle.
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Metallurgical Overview for Ore Reserves Estimation Operating Cost Estimate. Work index (Crusher, BM, RM, SAG), abrasion index. Flow sheet with material balances for .
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