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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.

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