111. Extremely large or small volumes of fluids are generally best routed through the shell side of a shell and tube heat exchanger, because of the
Less corrosion problems
Flexibility possible in the baffle arrangement
Low pressure drop
High heat transfer co-efficient
Correct answer: (B) Flexibility possible in the baffle arrangement
112. Film boiling is usually not desired in commercial equipments, because
The heat transfer rate is low in view of the large temperature drop
It is difficult to maintain
It is not economic
None of these
Correct answer: (A) The heat transfer rate is low in view of the large temperature drop
113. Film boiling occurs at _________ pressure.
Atmospheric
Sub-atmospheric
Negative
Very high
Correct answer: (D) Very high
114. Film condensation is promoted on a/an _________ surface.
Oily
Coated
Clean & smooth
Dirty
Correct answer: (C) Clean & smooth
115. Finned tube heat exchangers
Give larger area per tube
Use metal fins of low thermal conductivity
Facilitate very large temperature drop through tube wall
Are used for smaller heat load
Correct answer: (A) Give larger area per tube
116. Fluid motion in the natural convection heat transfer between a solid surface and a fluid in contact with it, results from the
Existence of thermal boundary layer
Temperature gradient produced due to density difference
Buoyancy of the bubbles produced at active nucleation site
None of these
Correct answer: (D) None of these
117. For _________ Prandtl number values, the heat conduction will be negligible in the buffer zone.
Extremely low
Low
High
No
Correct answer: (C) High
118. For a cold dilute feed to produce thick viscous liquor, backward feeding as compared to forward feeding results in
Increased economy
Decreased economy
Lower capacity
No effect on economy
Correct answer: (A) Increased economy
119. For a counter current heat exchanger with Ti h = 80°C, T°c = 60°C, T°h = 50°C and Ti c = 30°C, and the temperature difference between the two streams being the same everywhere along Z, the direction of flow of hot fluid. The temperature profile should satisfy
d2T/dZ2 > 0
d2T/dZ2 = 0
d2T/dZ2 < 0
dT/dZ = 0
Correct answer: (B)
d2T/dZ2 = 0
120. For a fluid flowing in an annulus space, the wetted perimeter for heat transfer and pressure drop are