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Process Equipment and Plant Design

Process Equipment and Plant Design
Hazards associated with the relief valve leakage for extremely hazardous material storage can be taken care of by providing

None of these
Rupture diaphragm
Dikes
Surge chamber

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Process Equipment and Plant Design
Log mean temperature difference in case of multi-pass shell and tube heat exchanger is always

More than arithmetic mean value
Both B & C
Less than arithmetic mean value
More than geometric mean value

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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 = 1.6 √t
D = 1.5 t
D = 3√t
D = 1.1 t

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Horizontal cylinderical
Thick spherical
Thick walled vertical
Tall vertical

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

4
2
1/2
8

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Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

0.75 d
0.5 d
2 d
D

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