8. Saturated steam at 100°C condenses in a shell and tube heat exchanger with a surface area of 0.5m² and overall heat transfer coefficient of 2000 W/m²K. Water enters at 0.7 kg/s and 15°C. Determine the outlet temperature of the water and the rate of steam condensation. For logarithmic mean temperature difference calculation, the flow may be taken as counter flow.

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8. Saturated steam at 100°C condenses in a shell and tube heat exchanger with a surface
area of 0.5m² and overall heat transfer coefficient of 2000 W/m²K. Water enters at 0.7
kg/s and 15°C. Determine the outlet temperature of the water and the rate of steam
condensation. For logarithmic mean temperature difference calculation, the flow may be
taken as counter flow.
Transcribed Image Text:8. Saturated steam at 100°C condenses in a shell and tube heat exchanger with a surface area of 0.5m² and overall heat transfer coefficient of 2000 W/m²K. Water enters at 0.7 kg/s and 15°C. Determine the outlet temperature of the water and the rate of steam condensation. For logarithmic mean temperature difference calculation, the flow may be taken as counter flow.
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