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Heat Transfer

Heat Transfer
For __________ Prandtl number values, the heat conduction will be negligible in the buffer zone.

Low
No
Extremely low
High

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Heat Transfer
In an extended surface heat exchanger, fluid having lower co-efficient

Flows through the tube
Can flow either inside or outside the tubes
Flows outside the tubes
Should not be used as it gives very high pressure drop

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Heat Transfer
The local surface conductance for laminar film condensation on vertical surface is (where, t = film thickness)

∝ √t
Independent of 't'
∝ 1/t
∝ t

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Heat Transfer
As per Kirchoffs law, the ratio of the total radiating power to the absorptivity of a body depends on the

temperature of the body only
nature of material of body
wavelength of monochromatic radiation
none of the listed here

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Heat Transfer
A metal ball of radius 0.1 m at a uniform temperature of 90°C is left in air at 30°C. The density and the specific heat of the metal are 3000 kg/m³ and 0.4 kJ/kg.K respectively. The heat transfer co-efficient is 50 W/m².K Neglecting the temperature gradients inside the ball, the time taken (in hours) for the ball to cool to 60°C is

555
0.55
0.15
55.5

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Heat Transfer
A cube, sphere & a thin circular plate (all having same mass and made of same material) are all heated to 300°C and allowed to cool in natural air. Which one will cool the slowest ?

Cube
Plate
Sphere
All of these

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