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Heat Transfer

Heat Transfer
Boiling of milk in an open vessel is an example of __________ boiling.

Sub-cooled
Saturated nucleate
None of these
Film

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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

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

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

Independent of 't'
∝ √t
∝ t
∝ 1/t

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Heat Transfer
Controlling heat transfer film co-efficient is the one, which offers __________ resistance to heat transfer.

lower
the least
no
the largest

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Heat Transfer
The outlet temperature of cooling water in a heat exchanger is generally not allowed to exceed above 50°C in industrial practice mainly to avoid

Uneconomic LMTD
Its evaporation loss
Decrease in heat exchanger efficiency
Excessive corrosion

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Heat Transfer
Shell side pressure drop in a shell and tube heat exchanger does not depend upon the

Viscosity, density & mass velocity of shell side fluid
Tube diameter & pitch
None of these
Baffle spacing & shell diameter

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