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Pharmaceutical Manufacturing Handbook: Production and

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MILLING EQUIPMENT 1167<br />

whereas smaller diameter balls facilitate the formation of fi ne product by reducing<br />

void spaces between the balls.<br />

The most important factors governing the performance of the mill <strong>and</strong> the<br />

achievement of the desired particle size are as follows:<br />

1. Amount of material required for subsequent testing (sample volume)<br />

2. Speed of rotation of ball mill<br />

A high volume of powder feed produces a cushioning effect whereas small<br />

sample volumes cause a loss of effi ciency <strong>and</strong> abrasive wear of the mill parts. The<br />

amount of material to be milled in a ball mill may be expressed as a material - to - void<br />

ratio (ratio of the volume of material to that of the void in the ball charge). As the<br />

amount of material is increased, the effi ciency of a ball mill is increased until the<br />

void space in the bulk volume of ball charge is fi lled; then, the effi ciency of milling<br />

is decreased by further addition of material.<br />

Rotational speed is the most signifi cant factor controlling the particle size specifi<br />

cation. The optimum speed of rotation is dependent on mill diameter. At low<br />

angular velocities the balls move with the drum until the force due to gravity<br />

exceeds the frictional force of the bed on the drum, <strong>and</strong> the balls then slide back<br />

to the base of the drum. This sequence is repeated, producing very little relative<br />

movement of balls so that size reduction is minimal. At high angular velocities the<br />

balls are thrown out onto the mill wall by centrifugal force <strong>and</strong> no size reduction<br />

occurs. At about two - thirds of the critical angular velocity where centrifuging occurs,<br />

a cascading action is produced. Balls are lifted on the rising side of the drum until<br />

their dynamic angle of repose is exceeded. At this point they fall or roll back to the<br />

base of the drum in a cascade across the diameter of the mill. By this means, the<br />

maximum size reduction occurs by impact of the particles with the balls <strong>and</strong> by<br />

attrition.<br />

The critical speed of a ball mill is the speed at which the balls just begin to centrifuge<br />

with the mill. Thus, at the critical speed, the centrifugal force is equal to the<br />

weight of the ball. At <strong>and</strong> above the critical speed, no signifi cant size reduction<br />

occurs. The critical speed n c is given by the equation<br />

n<br />

c =<br />

76 6<br />

D<br />

.<br />

where D is the diameter of the mill.<br />

A larger mill reaches its critical speed at a slower revolution rate than a smaller<br />

mill. Ball mills are operated at from 60 to 85% of the critical speed. Over this range,<br />

the output increases with the speed; however, the lower speeds are for fi ner grinding.<br />

An empiric rule for the optimum speed of a ball mill is<br />

n= 57 −40log<br />

D<br />

where n is the speed in revolutions per minute <strong>and</strong> D is the inside diameter of the<br />

mill in feet.

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