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Process Equipment and Plant Design

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

0.55
0.95
0.8
0.99

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Process Equipment and Plant Design
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

Increase by 21.6
Decrease by 22
None of these
Increase by 1.8

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

Horizontal cylinderical
Tall vertical
Thick walled vertical
Thick spherical

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Process Equipment and Plant Design
A rivetted joint does not fail by __________ of rivets.

None of these
Tearing
Tearing of the plate across a row
Shearing

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Process Equipment and Plant Design
The buckling tendency of compression members is always in the direction of the

Least radius of gyration
Axis of the load
Perpendicular to the axis of the load
None of these

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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
Eight times
Twice
Half

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