a study on fine grinding process in jet mill - ePrints@USM
a study on fine grinding process in jet mill - ePrints@USM
a study on fine grinding process in jet mill - ePrints@USM
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LIST OF FIGURES<br />
Figure 1.1 Loss of regularity <strong>in</strong> the crystall<strong>in</strong>e network<br />
Figure 2.1 Schematic diagram of opposed fluidized bed <strong>jet</strong> <strong>mill</strong><br />
Figure 2.2 Gr<strong>in</strong>d<strong>in</strong>g and classify<strong>in</strong>g chamber of opposed fluidized<br />
<strong>jet</strong> <strong>mill</strong><br />
Figure 2.3 Schematic representati<strong>on</strong> of breakage mechanism of<br />
hydrargillite particles <strong>in</strong> <strong>jet</strong> <strong>mill</strong><br />
Figure 2.4 Fragmentati<strong>on</strong> scheme for gibbsite ground <strong>in</strong> <strong>jet</strong> <strong>mill</strong><br />
Figure 2.5 Variati<strong>on</strong> of the circularity average values and the<br />
standard deviati<strong>on</strong><br />
Figure 2.6 Effect of separati<strong>on</strong> distance <strong>on</strong> the rate of <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> for<br />
target plate <strong>jet</strong> <strong>gr<strong>in</strong>d<strong>in</strong>g</strong><br />
Figure 2.7 Effect of separati<strong>on</strong> distance <strong>on</strong> the rate of <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> for<br />
two oppos<strong>in</strong>g nozzles <strong>jet</strong> <strong>gr<strong>in</strong>d<strong>in</strong>g</strong><br />
Figure 2.8 Types of nozzles: (a) abrupt nozzles (b) Laval shaped<br />
nozzles<br />
Figure 2.9 Median size of talc producti<strong>on</strong> as a functi<strong>on</strong> of feed rate<br />
for 7000 rpm (■), 9000 rpm (●), 11000 rpm (▲) and<br />
13000 rpm (▼)<br />
Figure 2.10 Influence of feed rate <strong>on</strong> product <strong>f<strong>in</strong>e</strong>ness <strong>in</strong> <strong>jet</strong> <strong>mill</strong><br />
<strong>gr<strong>in</strong>d<strong>in</strong>g</strong><br />
Figure 2.11 Difference specific surface area created as the functi<strong>on</strong><br />
of the factor P/N 2 for the fluidized bed <strong>jet</strong> <strong>mill</strong><br />
Page number<br />
4<br />
Figure 2.12 Pr<strong>in</strong>ciple of an impeller air classifier 34<br />
Figure 2.13 Mass held <strong>in</strong> the <strong>mill</strong> at different classifier speed: 7000<br />
rpm stable (■), 7000 rpm unsteady (□), 9000 rpm stable<br />
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