Calculation of the overall heat transfer coefficient in
a radial system with fouling factors
David W. Schryer
July 9, 2003
Determine the overall heat transfer coefficient, Uo , based on the outer
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surface of a brass tube with Di = 2.5cm and Do = 3.34cm [k = 110 mK ] for
the following conditions: The inside and outside convective heat transfer co-
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efficients are, respectively, hi = 1200 m2 K and ho = 2000 m2 K , and the foul-
2
ing factors for the inside and outside surfaces are Fi = Fo = 0.00018 m K .
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1
