FEED TECHNOLOGY UPDATE - AquaFeed.com
FEED TECHNOLOGY UPDATE - AquaFeed.com
FEED TECHNOLOGY UPDATE - AquaFeed.com
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DENSITY CONTROL<br />
500<br />
Extruder Discharge Density (g/l)<br />
450<br />
400<br />
350<br />
300<br />
4% Added Steam<br />
250<br />
0 1 2 3 4 5 6 7 8<br />
DDC Retention Time (min)<br />
Figure 3: Effect of Preconditioner Retention Time on Bulk Density<br />
RETENTION TIME CONSIDERATIONS<br />
Another method of altering product density<br />
is to alter the process retention time. This<br />
can be done in either the extruder or preconditioner.<br />
Figure 3 illustrates the<br />
impact of preconditioner<br />
retention time on final bulk<br />
density. As the retention<br />
time increases it creates<br />
addition cook and thus a<br />
much lighter final product<br />
density.<br />
The retention time of the<br />
entire system can be<br />
altered by changing the<br />
feed rate or capacity.<br />
This assumes that the up<br />
and downstream production<br />
equipment can handle<br />
the added loads due to the<br />
increased capacity.<br />
As the extrusion feed rate<br />
increases (at constant die<br />
open area), there is a reduction<br />
of retention time<br />
Final Piece Density, Coated (g / ml)<br />
1.4<br />
1.2<br />
1<br />
0.8<br />
0.6<br />
0.4<br />
0.2<br />
0<br />
and thus an increase in product density (see<br />
Figure 4).<br />
The density shown is actually piece density<br />
not bulk density as often used in many of<br />
the other figures and tables. Piece density<br />
Note: Die Open Area is Constant<br />
0 1000 2000 3000 4000 5000 6000<br />
Dry Feed Rate (kg / hr)<br />
Figure 4: Feed Rate vs. Piece Density<br />
• <strong>FEED</strong> <strong>TECHNOLOGY</strong> <strong>UPDATE</strong> — June/July 2006 •