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APV Dryer Handbook - Umbc

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30<br />

E F F I C I E N T<br />

E N E R G Y<br />

U T I L I Z A T I O N<br />

I N D R Y I N G<br />

It is generally necessary to employ thermal methods in order to achieve<br />

a product that is termed commercially dry. Thermal dryers, therefore, are<br />

an important unit operation in many industries. Products such as pigments,<br />

baby formula, kaolin and instant coffee usually have to be processed in dryers<br />

to obtain the final product.<br />

The commercial drying process can take place in a number of different types<br />

of dryers as described in the previous section. However, the thermodynamics<br />

of drying is the same regardless of the actual device. Water or another liquid<br />

such as a solvent has to be evaporated from a solid by the application of heat.<br />

Generally, the drying takes place in an air atmosphere, although some<br />

specialized dryers may use nitrogen or even superheated steam as<br />

the atmosphere.<br />

The most important parameter that governs the pretreatment and the dryer design<br />

is the “cost per unit weight of dried product.”<br />

While drying is an extremely energy intensive operation, there are techniques that<br />

can be used to minimize the energy costs per unit output of product, including:<br />

■ Minimizing the water content of the feed prior to feeding to the dryer.<br />

■ Maximizing the temperature drop of the drying gas. This implies maximum<br />

inlet and minimum outlet temperature.<br />

■ Employing the maximum possible recirculation of the drying gas.<br />

■ Considering the possibility of two stage counter flow drying.<br />

■ Utilizing the heat in the discharge air to preheat incoming air.

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