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Process Equipment and Plant Design

Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Large horizontal
Thick walled
Tall vertical
Small horizontal

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Process Equipment and Plant Design
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

4(0.86p² - πd²)/πd
(p² - πd²/4)/πd
(4p² - πd²/4)/πd
4(0.86p² - πd²/4)/πd

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Process Equipment and Plant Design
The dust collection efficiency of a cyclone separator

None of these
Is directly proportional to the radius of the dust particle path
Is inversely proportional to the mass of the dust particle
Decreases with increase in gas flow rate

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

2.5
1.25
3.5
1.75

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Process Equipment and Plant Design
In inclined long tube vertical evaporators, the tubes are inclined at an angle of

15°
90°
60°
45°

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Process Equipment and Plant Design
Maximum acceptable total liquid gradient over a tray is about __________ mm.

12.5
30.5
5.5
45.5

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