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Process Equipment and Plant Design

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

Small horizontal
Large horizontal
Tall vertical
Thick walled

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

(d1 + d2)/d1
(d1 + d2)/d2
D1/(d1 + d2)
D2/(d1 + d2)

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

Sieve plate
Packed
None of these
Bubble cap plate

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the shortest centre to centre distance between the adjacent tubes is

Called tube pitch
Always less than the diameter of the tube
Called tube clearance
None of these

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Process Equipment and Plant Design
In case of a shell and tube heat exchanger, the minimum shell thickness for carbon steel (inclusive of corrosion allowance) depends on shell diameter and is in the range of __________ mm.

44058
43962
44183
43895

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Process Equipment and Plant Design
Cylindrical storage tanks used for the storage of volatile liquids (e.g., naphtha) have __________ roofs.

Floating
Conical
Fixed
Flat

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