A. 2
B. 1/2
C. 4
D. 1/4
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.
A. Providing a higher skirt clearance or a higher weir
B. Decreasing the number of rows of caps through which the liquid flows or by decreasing the
velocity of liquid flow past the caps or by reducing the distance along the tray through which
the liquid must flow
C. Using split flow, radial flow or cascade flow for column diameter large than 4 ft
D. All A., B. and C.
A. 0 to 0.08
B. 0 to 0.8
C. 0 to 1.5
D. 0 to 2.2
A. nth
B. (1/n)th
C. 0.5 nth
D. 1.5 nth
A. Half
B. Three fourth
C. Equal to
D. 1.5 times
A. Split
B. Cross
C. Cascade
D. Reverse
A. 25 and 60
B. 3 and 5
C. 100 and 250
D. 250 and 600