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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum shell thickness for tank ≤ 15 metres diameter is limited to __________ mm, for reasons of elastic stability.

10
5
15
2

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Segmental
Independent of the type of
Orifice
Disk and ring

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Process Equipment and Plant Design
Which of the following material is seldom used for pressure vessel construction?

Killed steel
Mild steel
Semi-killed steel
Rimmed still

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Total cost considerations (pumping cost plus fixed cost of the pipe)
None of these
Viscosity of the fluid
Density of the fluid

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Process Equipment and Plant Design
Baffle spacing is generally __________ the I.D. of the shell.

More than
Not greater than
Both B and C
Not less than one fifth of

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

D1/(d1 + d2)
(d1 + d2)/d1
D2/(d1 + d2)
(d1 + d2)/d2

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