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Process Equipment and Plant Design

Process Equipment and Plant Design
for couplings and unions would be

200
60
350
Negligible

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Process Equipment and Plant Design
The normal range of velocity of steam in pipes is __________ m/sec.

0.1-0.5
10-20
1-5
80-100

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

D²
1/D⁵
1/D²
1/D

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Process Equipment and Plant Design
Floating head heat exchangers are used for the

Counter-current heat transfer systems
Heat transfer between corrosive fluids
Co-current heat transfer systems
Cases where temperature difference between the shell and the tubes is more (>50°C)

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Process Equipment and Plant Design
Wind load consideration in the design of a support can be neglected, when the vessel is

Short (< 2 m) and housed indoor
Tall (say 30 metres), but is full of liquid
None of these
Tall but empty

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Process Equipment and Plant Design
Circumferential (hoop) stress in a thin cylindrical vessel under internal pressure is __________ the longitudinal stress.

Equal to
Half
Eight times
Twice

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