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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

3 to 5
4 to 8
6 to 12
2 to 3

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large reflux ratio
Resistance offered to flow of liquids by caps & risers and the flow of gas
Large plate spacing
Low gas velocity

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Process Equipment and Plant Design
Where does the maximum tensile strength occur in a thick cylindrical vessel subjected to internal pressure?

At the outer surface
None of these
At the mid thickness of the cylindrical wall
At the inner surface

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Process Equipment and Plant Design
Tubes are fixed to the tube sheet (a thick circular metallic plate) by the method of tube rolling and brazing (non-removable) or ferrule connection (removable). Thickness of the tube, sheet is normally __________ the outside diameter of the tube but in no case it should be less than 22 mm (7/8").

Equal to
Three fourth
Half
1.5 times

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Process Equipment and Plant Design
Normally, the ratio of the total riser area to the tower cross sectional area (for bubble cap towers of diameter more than 3 ft) is around

0.35-0.75
0.4-0.6
0.1-0.2
0.55-0.85

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Process Equipment and Plant Design
Brass valves are usually made for pipe sizes __________ inches.

>3.5
?1
?2
>2.5

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