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Process Equipment and Plant Design

Process Equipment and Plant Design
Liquid redistribution should be done in a packed tower packed with raschig rings every 6 metres or __________ times the column diameter, whichever is lower.

5-7.5
10-12.5
2.5-3.0
15-20

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Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A vapor phase reactor
A liquid phase reactor
A liquid phase catalytic reactor
Pot type reactor

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Process Equipment and Plant Design
Baffles may be eliminated for

None of these
High viscosity liquids (> 600 poise)
Large diameter tanks
Low viscosity liquids (< 200 poise)

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Process Equipment and Plant Design
For a 25 mm hole drilled in plates to be rivetted, the shank diameter of the rivet should be __________ mm.

27
23
26
25

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

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Process Equipment and Plant Design
__________ dished head is the strongest of all.

None of these
Elliptical
Hemispherical
Torispherical

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