A company owns a refrigeration system whose refrigeration capacity is 200 tons
( 1 ton of refrigeration = \(211 \mathrm{~kJ} / \mathrm{min}\) ), and you are to
design a forced-air cooling system for fruits whose diameters do not exceed \(7
\mathrm{~cm}\) under the following conditions:
The fruits are to be cooled from \(28^{\circ} \mathrm{C}\) to an average
temperature of \(8^{\circ} \mathrm{C}\). The air temperature is to remain above
\(-2^{\circ} \mathrm{C}\) and below \(10^{\circ} \mathrm{C}\) at all times, and
the velocity of air approaching the fruits must remain under \(2 \mathrm{~m} /
\mathrm{s}\). The cooling section can be as wide as \(3.5 \mathrm{~m}\) and as
high as \(2 \mathrm{~m}\).
Assuming reasonable values for the average fruit density, specific heat, and
porosity (the fraction of air volume in a box), recommend reasonable values
for the quantities related to the thermal aspects of the forced-air cooling,
including (a) how long the fruits need to remain in the cooling section, \((b)\)
the length of the cooling section, \((c)\) the air velocity approaching the
cooling section, \((d)\) the product cooling capacity of the system, in
\(\mathrm{kg}\) fruit/h, \((e)\) the volume flow rate of air, and \((f)\) the type
of heat exchanger for the evaporator and the surface area on the air side.