- (A) Results in higher shell side pressure drop
- (B) Can accomodate less number of tubes for a given shell diameter
- (C) Facilitates easier shell side cleaning; hence is more suitable for handling high dirt factor shell side fluid
- (D) Creates relatively lower turbulence on the shell side resulting in lower shell side heat transfer co-efficient
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- (A) Double pipe
- (B) Finned
- (C) Plate type
- (D) Regenerative
- (A) 2
- (B) 1/2
- (C) 4
- (D) 1/4
- (A) Bending
- (B) Deformation
- (C) Shear
- (D) Elongation
- (A) U1 – U2
- (B) 1/U1 – 1/U2
- (C) 1/U2 – 1/U1
- (D) U2 – U1
- (A) 1.26 h1
- (B) 0.794 h1
- (C) 0.574 h1
- (D) 1.741 h1
- (A) (1/U) Vs. (1/v0.8)
- (B) (1/v0.8) Vs. U
- (C) v0.8 Vs . U
- (D) (1/U) Vs. (1/V)
- (A) 35.5
- (B) 43.75
- (C) 81.25
- (D) 48.25
- (A) Decreases the pressure drop
- (B) Decreases the outlet temperature of cooling medium
- (C) Increases the overall heat transfer coefficient
- (D) None of these
- (A) Facilitate draining out liquid from a tray when the unit is not in operation
- (B) Are normally located near the overflow weir so that any delivery of liquid during operation follows approximately the same path as the overflow fluid
- (C) Must be large enough (usually 1/4″ to 5/8″ dia) to prevent plugging but should not deliver excessive amount of fluid during operation
- (D) All

