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Wet Ball Mill = kg kWh = 0.16 A i-0.015 0.33; Dry Ball Mill = kg / kWh = 0.023A i 0.5; Replacement Ball Size. Rowland and Kjos proposed the use of their equation for the determination of the initial and replacement media size. Azzaroni 1981 and Dunn 1989 recommended the use of the following expression for the size of the makeup media:

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Wet Ball Mill = kg kWh = 0.16 A i-0.015 0.33; Dry Ball Mill = kg / kWh = 0.023A i 0.5; Replacement Ball Size. Rowland and Kjos proposed the use of their equation for the determination of the initial and replacement media size. Azzaroni 1981 and Dunn 1989 recommended the use of the following expression for the size of the makeup media:

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Wet Ball Mill = kg kWh = 0.16 A i-0.015 0.33; Dry Ball Mill = kg / kWh = 0.023A i 0.5; Replacement Ball Size. Rowland and Kjos proposed the use of their equation for the determination of the initial and replacement media size. Azzaroni 1981 and Dunn 1989 recommended the use of the following expression for the size of the makeup media:

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Ф1200×3000 ball mill: cylinder speed is 36r / min, ball loading is 3.5t, feed size ≤ 25mm, the finished size is 0.074-0.4mm, the motor power is 37kw, the weight is 12.8t, the per hour capacity is 1.6-5t;

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First, a Jar Mill grindability test requires a 5 lb. 2 kg sample and produces a direct measured specific energy net Hp-hr/t to grind from the design feed size to the required product size. The second test, a Bond Work Index determination, results in a specific energy value net Hp-hr/t from an empirical formula.

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