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Process Equipment and Plant Design

Process Equipment and Plant Design
In packed towers provided with saddle packing, liquid redistributors are positioned at every __________ times column diameter or 6 metres whichever is less.

43959
20-25
43864
44119

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Process Equipment and Plant Design
An underdesigned steam trap will

Back up condensate and cause water hammer in steam line
None of these
Destroy itself of acceleration wear due to rapid recycling
Waste steam

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Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.8
0.95
0.55
0.99

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Process Equipment and Plant Design
Diameter of rivet hole (d, mm) and the plate thickness (t, mm) are related by Unwin's formula as

D = 1.1 t
D = 1.6 √t
D = 1.5 t
D = 3√t

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Process Equipment and Plant Design
Baffles may be eliminated for

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

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Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

0.1-0.12
0.2-0.45
0.4-0.5
0.45-0.6

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