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Process Equipment and Plant Design

Process Equipment and Plant Design
Le/D for fully open globe value may be around

25
300
10
75

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

Either A or B
Neither A nor B
U-bend
Floating head tube sheet

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Process Equipment and Plant Design
In case of saddle packing (e.g., berl and intralox saddles), the maximum size of the packing should not exceed __________ of the column diameter.

l/50th
l/30th
l/5th
l/15th

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Process Equipment and Plant Design
Removable connection of tubes to tube sheet is called

Socket
Saddle
Nipple
Ferrule

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Withstand higher pressure for a given metallic shell thickness
Be supported very easily
Be fabricated very easily
Be designed without wind load considerations

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Process Equipment and Plant Design
Correct use of 'factor of safety' is very important in equipment design. It is defined as the ratio of the

Ultimate stress to breaking stress
Working stress to ultimate stress
Ultimate stress to working stress
None of these

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