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Process Equipment and Plant Design

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

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

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Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Both A & B
Neither A nor B
Pitch
Layout

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Process Equipment and Plant Design
Generally, no corrosion allowance in wall thickness of a part is required, if the thickness is more than __________ mm.

5
20
30
10

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Process Equipment and Plant Design
Vertical storage vessels are never supported by __________ support.

Lug
Bracket
Skirt
Saddle

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Process Equipment and Plant Design
__________ closure is the weakest enclosure for cylindrical vessels.

Hemispherical
Elliptical
Torispherical
Conical or flat plate

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Process Equipment and Plant Design
Floating head heat exchangers are used for the

Cases where temperature difference between the shell and the tubes is more (>50°C)
Counter-current heat transfer systems
Heat transfer between corrosive fluids
Co-current heat transfer systems

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