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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.

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

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Process Equipment and Plant Design
Safety valves are provided in chemical equipments to guard against excessive

Temperature
Pressure/pressure fluctuation
Turbulence
Noise

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Process Equipment and Plant Design
The maximum liquid gradient over a tray must not exceed

Half the tray spacing
5"
2"-3.5"
0.5" -1.25"

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Process Equipment and Plant Design
The minimum shell thickness for tank ≤ 15 metres diameter is limited to __________ mm, for reasons of elastic stability.

15
5
10
2

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Maldistribution of gas
All of these
Gas blowing beneath cap skit
Back trapping

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Process Equipment and Plant Design
In shell and tube heat exchangers, straight tie rods are used to

Account for thermal strain
None of these
Fix the tubes in position
Hold baffle in space

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