Modeling breakage rates of coarse particles in ball mills
This condition is approached by a mill that is fed with particles contained in a comparatively fine size range when compared to the ball size. In this case, Eq. (7) may be rewritten as (24) d w 1 ( t ) d t = ω N cap, 1 m ¯ p, 1 M 1 ∫ 0 ∞ p ( E ) b 11 ( E / N cap, 1 ) dE w 1 ( t )