Heat Transfer
The interchange factor for radiation heat transfer from surface 'x' to surface 'y' in case of an infinite parallel planes with emis-sivities εx & εy is given by

(εx + εy)/(εx + εy - εx . εy)
Εx . εy
1/εx + 1/εy
Εx + εy

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Heat Transfer
Condensing film co-efficient for steam on horizontal tubes ranges from 5000 to 15000 Kcal/hr.m² .°C. Condensation of vapor is carried out inside the tube in a shell and tube heat exchanger, when the

Temperature of the incoming vapor is very high
Condensate is corrosive in nature
Lower pressure drop through the exchanger is desired
Higher condensing film co-efficient is desired

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