The original ball load in the mill was 6614 lb. (3000 kg.) and the load at the end of the 694 hr. was 6338 lb. ( kg.). During this time, 590 lb. ( kg.) of balls less than 3 in. ( mm.) in diameter were discarded from the mill. The screen analysis of the ball charge at the end of the operation is shown in Table 20.
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WhatsApp: +86 18203695377One obvious reason is that impact energies in laboratory mills are negligible compared to those in industrial mills. For example, Dodd et al. (1985) have estimated that an increase in ball kinetic energy from J for a m ball in a m ball mill to 350 J for a m ball in an m ball mill.
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WhatsApp: +86 18203695377A simulation started with the formation of a packed bed of the balls and powders in a still mill (Fig. 1 a).The mill then rotated at a given speed to lift the ballparticle mixtures (Fig. 1 b).After the flow reached the steady state as shown in Fig. 1 c (by monitoring flow velocity), the flow dynamics information was then collected and analysed. It should be noted the change of particle size ...
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