Process Equipment and Plant Design

A. 0
B. ∞
C. > 1
D. <1

A. 300
B. 600
C. 1000
D. 1500

A. Overall plate efficiency
B. Murphree plate efficiency
C. Point efficiency
D. None of these

A. 1.25
B. 1.75
C. 2.5
D. 3.5

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

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. 60
B. 200
C. 350
D. Negligible

A. 8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers
B. 4 : 1 to 8 : 1 for liquid-liquid exchanger
C. < 4 : 1 for gas-gas exchangers
D. Both B. & C.