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Process Equipment and Plant Design

Process Equipment and Plant Design
The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

A/P
4 A/P
4 P/A
√A

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Process Equipment and Plant Design
Le/D for 90° elbow (medium radius) and 90°square elbow would be respectively around

25 and 60
100 and 250
3 and 5
250 and 600

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Process Equipment and Plant Design
Le/D for fully open gate valves would be

Much more than that for fully open globe valves
Both B and C
Around 7
Much less (say 2% than that for fully open globe valves)

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Process Equipment and Plant Design
Height of the flights in the rotary drier is in the range of

0.2 to 0.5 d
0.5 to 0.6 d
0.08 to 0.12 d
0.02 to 0.05 d

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Process Equipment and Plant Design
If 'D' is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

D/5 or minimum 2" to 5D
None of these
D/2 or minimum 2" to 5D
D/5 or minimum 2" to D

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Process Equipment and Plant Design
Vertical vessels are not supported by

Saddles
Columns
Brackets
Skirts

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