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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understand<strong>in</strong>g of the various mechanisms <strong>in</strong>volved <strong>in</strong> the fragmentati<strong>on</strong> of the particles<br />
such as <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> chamber pressure, amount of holdup <strong>in</strong> the <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> chamber, particle<br />
shape, air flow <strong>in</strong> the <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> and classificati<strong>on</strong> chamber besides the operati<strong>on</strong>al<br />
parameters and design parameters such as, classifier speed, nozzle distance, feed<br />
rate and <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> pressure (Kolacz, 2004).<br />
Figure 2.1 shows the schematic diagram of opposed fluidized bed <strong>jet</strong> <strong>mill</strong>. The<br />
fluidized-bed <strong>jet</strong> <strong>mill</strong> c<strong>on</strong>sists of a vertical <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> chamber with oppos<strong>in</strong>g gas <strong>jet</strong>s near<br />
its lower end. Particles c<strong>on</strong>ta<strong>in</strong>ed <strong>in</strong> the hopper is c<strong>on</strong>t<strong>in</strong>uously fed by screw feeder <strong>in</strong>to<br />
the <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> chamber where they are ground at the meet<strong>in</strong>g po<strong>in</strong>t of the three<br />
c<strong>on</strong>current air <strong>jet</strong>s formed by ceramic nozzles supplied with compressed air. The<br />
breakage mechanism <strong>in</strong> the <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> chamber is primarily due to impact and abrasi<strong>on</strong><br />
with other particles and very much dependent <strong>on</strong> the operat<strong>in</strong>g c<strong>on</strong>diti<strong>on</strong> of the <strong>jet</strong> <strong>mill</strong>.<br />
After <strong>gr<strong>in</strong>d<strong>in</strong>g</strong>, the particles are carried out by air flow up to the wheel classifier, which<br />
removes the <strong>f<strong>in</strong>e</strong> particles and return the coarser <strong>on</strong>es to the <strong>gr<strong>in</strong>d<strong>in</strong>g</strong> z<strong>on</strong>e result<strong>in</strong>g <strong>in</strong><br />
relatively tight particle-size distributi<strong>on</strong>s (Godet-Morand, 2002). Figure 2.2 shows the<br />
flow of the particles <strong>in</strong> the <strong>gr<strong>in</strong>d<strong>in</strong>g</strong>-classify<strong>in</strong>g chamber. The <strong>f<strong>in</strong>e</strong> particles are collected<br />
<strong>in</strong> a c<strong>on</strong>ta<strong>in</strong>er below an air cycl<strong>on</strong>e (Berthiaux and Dodds, 1999).<br />
Hopper<br />
Screw feeder<br />
Gr<strong>in</strong>d<strong>in</strong>g<br />
air<br />
Ground<br />
product<br />
Figure 2.1: Schematic diagram of opposed fluidized bed <strong>jet</strong> <strong>mill</strong> (Berthiaux and<br />
Dodds,1999)<br />
Classifier<br />
Cycl<strong>on</strong>e<br />
16<br />
Filter bag house<br />
Air outlet<br />
Blower