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Heat and Mass Transfer

Heat and Mass Transfer
Thermal conductivity of water at 20°C is of the order of

0.1
0.23
0.42
0.51

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Heat and Mass Transfer
Two long parallel surfaces each of emissivity 0.7 are maintained at different temperatures and accordingly have radiation heat exchange between them. It is desired to reduce 75% of the radiant heat transfer by inserting thin parallel shields of emissivity 1 on both sides. The number of shields should be

Two
Three
One
Four

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Heat and Mass Transfer
The rate of energy transferred by convection to that by conduction is called

Stanton number
Nusselt number
Peclet number
Biot number

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Heat and Mass Transfer
40% of incident radiant energy on the surface of a thermally transparent body is reflected back. If the transmissivity of the body be 0.15, then the emissivity of surface is

0.55
0.4
0.75
0.45

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Heat and Mass Transfer
Unit of thermal conductivity in M.K.S. units is

K cal/kg m² °C
K cal m/hr m² °C
K calm/hr °C
K cal/hr m² °C

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Heat and Mass Transfer
According to Stefan's law, the total radiation from a black body per second per unit area is proportional to

T
T2
T5
Absolute temperature

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