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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

None of these
Tall (say 30 metres), but is full of liquid
Short (< 2 m) and housed indoor
Tall but empty

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Density of the fluid
Total cost considerations (pumping cost plus fixed cost of the pipe)
Viscosity of the fluid
None of these

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Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

2.5 times
One-fourth of
Less than
1.25-1.50 times

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Process Equipment and Plant Design
Thin spherical shells subjected to internal pressure, develop __________ stresses.

Both A & B
Neither A nor B
Radial
Circumferential

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

All of these
Back trapping
Maldistribution of gas
Gas blowing beneath cap skit

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