Determine the overall heat transfer coefficient based on outer area of a
3.81cm O.D and 3.175 cm I.D brass tube(k = 103.8 W/m K) if the heat
transfer coefficients for flow inside and outside the tubes are 2270 and
2840 W/m2
K respectively, and the unit fouling resistances at inside and
outside are Rfi = Rfo = 8.8 x 10-3 m2 K/W. full sum need no need answers
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