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Process Equipment and Plant Design

Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

1/D²
D²
1/D⁵
1/D

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

8
4
1/2
2

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Process Equipment and Plant Design
Bracket supports are the most suitable for supporting __________ vessels.

Thick walled vertical
Thin shperical (e.g. Horton sphere)
Horizontal
None of these

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Process Equipment and Plant Design
The distance between the top of the slots and the liquid surface when the static liquid is just ready to flow over the overflow weir is called

Skirt clearance
Static submergence
Downcomer liquid seal
None of these

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

Socket
Nipple
Saddle
Ferrule

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Process Equipment and Plant Design
Nominal size of a pipe is an indication of its __________ diameter.

Inner
Approximate
Outer
None of these

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