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Heat and Mass Transfer

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

W/m °K
J/m² sec
J/m °K sec
Option (B) and (C) above

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Heat and Mass Transfer
In convection heat transfer from hot flue gases to water tube, even though flow may be turbulent, a laminar flow region (boundary layer of film) exists close to the tube. The heat transfer through this film takes place by

Convection
Both convection and conduction
Radiation
Conduction

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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

Four
One
Three
Two

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Heat and Mass Transfer
The unit of overall coefficient of heat transfer is

kcal/m² hr °C
kcal/m hr °C
kcal/hr °C
kcal/m²

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Heat and Mass Transfer
The value of the wave length for maximum emissive power is given by

Stefan’s law
Planck’s law
Wine’s law
Kirchhoff’s law

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Heat and Mass Transfer
Two plates spaced 150 mm apart are maintained at 1000°C and 70°C. The heat transfer will take place mainly by

Radiation
Convection
Forced convection
Free convection

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