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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.

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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