Heat Transfer
The thickness of condensate layer in filmwise condensation depends on the

Surface configuration
All of these
Condensation rate
Liquid flow rate from the surface

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Heat Transfer
Nusselt number is the ratio of the

Heat flux at the wall to that across the entire pipe
Temperature difference to the temperature gradient at the wall
None of these
Temperature gradient of the wall to that across the entire pipe

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Heat Transfer
1000 Kg of liquid at 30°C in a well stirred vessel has to be heated to 120°C, using immersed coils carrying condensing steam at 150°C. The area of the steam coils is 1.2 m² and the overall heat transfer co-efficient to the liquid is 1500 W/m².°C. Assuming negligible heat loss to the surrounding and specific heat capacity of the liquid to be 4 kJ/kg.°C, the time taken for the liquid to reach desired temperature will be

44 min
15 min
51 min
22 min

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Heat Transfer
Air is to be heated by condensing steam. Two heat exchangers are available (i) a shell and tube heat exchanger and (ii) a finned tube heat exchanger. Tube side heat transfer area are equal in both the cases. The recommended arrangement is

Shell and tube heat exchanger with air on shell side and steam inside tubes
Finned tube heat exchanger with air outside and steam inside
Shell and tube heat exchanger with air inside tubes and steam on shell side
Finned tube heat exchanger with air inside and steam outside

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