A fluid of density 978 kg/m3 is heated in pipe, enters a 20 mm diameter tube with a velocity of 2 m/s at 10 ∘C. Convective heat transfer coefficient at outside surface of tube is equal to 10 kW/m2. The length of tube is 5 meter and properties of water at mean temperature is approximated as following,
k=0.332 WmK, μ=4×10−4 kg/m-s, Pr=2.54
the value of overall heat transfer coefficient is