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Heat Transfer

Heat Transfer
According to Reynolds analogy, Stanton number is equal to (where, f = Fanning friction factor)

f/4
2f
f
f/2

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Heat Transfer
Calburn analogy is applicable for the value of Prandtl number from

120 to 400
0.6 to 120
0.001 to 1
0.5 to 5

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Heat Transfer
For a fluid flowing in an annulus space, the wetted perimeter for heat transfer and pressure drop are

Same
Never different
Linearly related
Different

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Heat Transfer
For an ideal black body

Transmissivity = 1
Emissivity = 0
Reflectivity = 1
Absorptivity = 1

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Heat Transfer
Minimum recommended baffle spacing in a shell and tube heat exchanger is about (where, D = shell diameter)

0.5 D
0.2 D
0.3 D
0.4 D

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Heat Transfer
The radiation heat flux from a heating element at a temperature of 800°C, in a furnace maintained at 300°C is 8 kW/m². The flux, when the element temperature is increased to 1000°C for the same furnace temperature is

14.6 kW/m²
16.5 kW/m²
12.0 kW/m²
11.2 kW/m²

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