APV Dryer Handbook - Umbc
APV Dryer Handbook - Umbc
APV Dryer Handbook - Umbc
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52<br />
Figure 24 illustrates the very rapid reduction in air temperature that occurs due<br />
to the high heat transfer rate obtained in the fluid bed.<br />
OPERATING PARAMETERS<br />
Inlet temperature of the drying air introduced into the chamber is dependent on the<br />
particular characteristics of the product being dried but generally would be similar<br />
to that used on a spray dryer for the same product.<br />
Outlet temperature is selected by test work to provide the desired powder moisture<br />
and is controlled by the speed of the feed screw. Since the Spin Flash dryer<br />
produces a finer particle size than does a spray dryer, it has been found that a<br />
slightly lower outlet temperature may be used to obtain the same powder moisture.<br />
This provides an increase in thermal efficiency.<br />
95°<br />
105°<br />
110°<br />
125°<br />
85°<br />
Figure 24. Fluid bed provides rapid air<br />
temperature reduction<br />
Air velocity through the cross<br />
section of the drying chamber<br />
is an important design factor<br />
and is determined, in part, by<br />
the final particle size required.<br />
A lower velocity will tend to<br />
reduce the final dried particle<br />
size carried out of the<br />
chamber. The major factor,<br />
however, is the stability of<br />
the very complex bed which<br />
must neither settle back into<br />
the air distributor nor blow<br />
out of the top of chamber.<br />
Once the maximum velocity<br />
has been determined by<br />
test work for a given product,<br />
the diameter of a drying<br />
chamber can be selected<br />
to provide the desired water<br />
evaporation rate.