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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum baffle height should be

Twice the impeller diameter
Equal to the impeller diameter
3/4 of the tank height
Twice the tank diameter

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

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Process Equipment and Plant Design
Vertical vessels are not supported by

Columns
Saddles
Brackets
Skirts

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Process Equipment and Plant Design
In seive plate column, holes are drilled or punched in sizes ranging from 2.5 to 12 mm (5 mm being widely used). The hole pitch is normally __________ times the hole diameter to give the required hole area.

2.5 to 4.0
5 to 10
10 to 15
0.5 to 1.5

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Small
Tall but empty
Large horizontal cylindrical
Thick walled tall

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Remains constant
Increases very rapidly
Increases linearly
Decreases very rapidly

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