Saturated steam at 1 atm is condensed on the external surface of a copper tube with an outside diameter 16 mm and tube wall of thickness 0.5 mm. The tube is cooled internally by water with a mass flow rate of 0.06 kg/s, which in turn is raised in temperature from 15 °C to 60 °C as it flows through the tube. Take the heat-transfer coefficient at the condensing side as 10.0 kW/m² K and the isobaric specific heat-capacity of water as 4180 J/kg K. i) Calculate the heat transfer rate to the cooling water. ii) Calculate the length of the tube. iii) Comment on how to enhance heat transfer in this case.

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Chapter7: Forced Convection Inside Tubes And Ducts
Section: Chapter Questions
Problem 7.4P
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How do i solve this question using Roger & Mayhew steam property tables:

Saturated steam at 1 atm is condensed on the external surface of a copper tube with
an outside diameter 16 mm and tube wall of thickness 0.5 mm. The tube is cooled
internally by water with a mass flow rate of 0.06 kg/s, which in turn is raised in
temperature from 15 °C to 60 °C as it flows through the tube.
Take the heat-transfer coefficient at the condensing side as 10.0 kW/m² K and the
isobaric specific heat-capacity of water as 4180 J/kg K.
i) Calculate the heat transfer rate to the cooling water.
ii)
Calculate the length of the tube.
iii) Comment on how to enhance heat transfer in this case.
Transcribed Image Text:Saturated steam at 1 atm is condensed on the external surface of a copper tube with an outside diameter 16 mm and tube wall of thickness 0.5 mm. The tube is cooled internally by water with a mass flow rate of 0.06 kg/s, which in turn is raised in temperature from 15 °C to 60 °C as it flows through the tube. Take the heat-transfer coefficient at the condensing side as 10.0 kW/m² K and the isobaric specific heat-capacity of water as 4180 J/kg K. i) Calculate the heat transfer rate to the cooling water. ii) Calculate the length of the tube. iii) Comment on how to enhance heat transfer in this case.
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