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Heat Transfer

Heat Transfer
(NRe.NPr)(D/L) is called the __________ number

Stanton
None of these
Peclet
Graetz

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Heat Transfer
The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m².K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m².K. The overall heat transfer co-efficient at this time is

1200W/m².K
333W/m².K
894W/m².K
287 W/m².K

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Heat Transfer
Dropwise condensation of steam on cooling surface is promoted

None of these
Only in presence of air
An oily surface
When both the steam and the tube are clean

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Heat Transfer
The film thickness for laminar film condensation on vertical surface __________ from top to bottom.

Remains constant
Cummulatively decreases
And the surface conductance increase
Cummulatively increases

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Heat Transfer
Steam is routed through the tube in case of a __________ evaporator.

Horizontal tube
Long tube vertical
Short tube vertical
Basket type

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Heat Transfer
In an interphase heat transfer process, the equilibrium state corresponds to equality of temperature in the two phases, while the condition for equilibrium in an interphase mass transfer process is equality of

Chemical potentials
Activity co-efficients
Mass transfer co-efficients
Concentrations

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