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Process Equipment and Plant Design

Process Equipment and Plant Design
for couplings and unions would be

200
60
Negligible
350

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Process Equipment and Plant Design
Wall thickness of schedule 40 pipe as compared to that of schedule 80 pipe is

More
Less
Same
Cither A or B; depends upon the I.D. of the pipe

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Process Equipment and Plant Design
In case of 1.5" heat exchanger tubes, the inside flow area __________ with decrease in BWG.

None of these
Decreases
Increases
Remains same

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

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

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

20 to 30
4 to 10
10 to 20
1 to 2

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

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