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Solar drying of fruits, vegetables, spices, medicinal plants and fish ...

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International <strong>Solar</strong> Food Processing Conference 2009<br />

Fig. 8. Ro<strong>of</strong> integrated solar dryer<br />

3. Mathematical Modeling<br />

Mathematical models are useful for predicting performance <strong>and</strong> optimal designs <strong>of</strong> solar <strong>drying</strong><br />

systems. The fundamentals <strong>of</strong> heat <strong>and</strong> mass transfer during <strong>drying</strong> are given in Bala (1997a).<br />

The details <strong>of</strong> heat <strong>and</strong> mass transfer during <strong>drying</strong> <strong>of</strong> chilli in a solar tunnel dryer <strong>and</strong> ro<strong>of</strong><br />

integrated solar dryer are given in Hossain (2004) <strong>and</strong> Hossain et al (2005), <strong>and</strong> Janjai et al.<br />

(2006) respectively. Mathematical models to simulate the heat <strong>and</strong> mass transfer in a solar<br />

tunnel drier are discussed below:<br />

Analysis <strong>of</strong> Collector Performance<br />

Considering an element, dx <strong>of</strong> collector at a distance, x from the inlet (Fig. 9.), the energy<br />

balances on the collector components give the following equations (Bala <strong>and</strong> Woods, 1994).<br />

Energy Balances on the Plastic Cover<br />

Energy balance on the cover gives the following equations:<br />

h<br />

( T − T ) + h ( T − T ) + h ( T − T ) − h ( T − T ) = α (1 +τ ρ E (1)<br />

cam c am ca c a rcs c s rpc p c cS cS pS<br />

)<br />

9

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