Water (pw= 997 kg/m³, Cp,w = 4179 J/kg·K, µw = 855×106 N•s/m², kw = 0.613 W/m•K, and Pr, = 5.83) enters a thin-walled (negligible thickness) tube of 10-mm diameter and 2-m length with mass flow rate m, =0.2 kg/s and inlet mean temperature Tm,i = 47°C. The tube is heated by passing air at T = 100°C and velocity V = 10 m/s in cross flow over the tube. The properties of the cross flowing air are evaluated as vair= 20.92×10-6 m2/s, kair=0.03 W/m•K, Prair=0.7. Determine the exit temperature of the water leaving the tube and the total heat loss from the water as it passes through the tube. Tm,0 = 46.62°C

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Water (p= 997 kg/m³, Cp,w = 4179 J/kg·K, µw= 855×106 N•s/m², kw = 0.613 W/m·K,
and Pr, = 5.83) enters a thin-walled (negligible thickness) tube of 10-mm diameter and
2-m length with mass flow rate m, = 0.2 kg/s and inlet mean temperature Tm,i= 47°C.
The tube is heated by passing air at T = 100°C and velocity V = 10 m/s in cross flow
over the tube. The properties of the cross flowing air are evaluated as vair= 20.92×10-6
m2/s, kair=0.03 W/m•K, Prair=0.7. Determine the exit temperature of the water leaving
the tube and the total heat loss from the water as it passes through the tube.
Tm,0 = 46.62°C
Transcribed Image Text:Water (p= 997 kg/m³, Cp,w = 4179 J/kg·K, µw= 855×106 N•s/m², kw = 0.613 W/m·K, and Pr, = 5.83) enters a thin-walled (negligible thickness) tube of 10-mm diameter and 2-m length with mass flow rate m, = 0.2 kg/s and inlet mean temperature Tm,i= 47°C. The tube is heated by passing air at T = 100°C and velocity V = 10 m/s in cross flow over the tube. The properties of the cross flowing air are evaluated as vair= 20.92×10-6 m2/s, kair=0.03 W/m•K, Prair=0.7. Determine the exit temperature of the water leaving the tube and the total heat loss from the water as it passes through the tube. Tm,0 = 46.62°C
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