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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 •

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