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Process Equipment and Plant Design

Process Equipment and Plant Design
Hoop (circumferential) stress induced in a thin walled 'Horton Sphere' used for the storage of liquid ammonia under pressure is

pD/3t
pD/6t
pD/2t
pD/4t

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Be supported very easily
Be fabricated very easily
Withstand higher pressure for a given metallic shell thickness
Be designed without wind load considerations

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Process Equipment and Plant Design
The clearance between two tubes in a shell and tube heat exchanger is known as 'ligament', whose minimum value is __________ the outside diameter of the tube, but in no case it should be less than 4.5 mm.

Equal to
Three fourth
Half
One fourth

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Process Equipment and Plant Design
The slope of operating line in the rectifying section of a distillation column is unity, if the reflux ratio is

Minimum
∞
0
1

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Lower limit of vapour velocity
Height of the plate spacing
Upper limit of the vapour velocity
Hole diameter of the seive tray

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Process Equipment and Plant Design
Optimum reflux ratio in a continuous distillation column is determined by the

Maximum permissible vapour velocity
Flooding limit of the column
Total cost consideration (fixed cost of the column plus the cooling water & steam cost)
None of these

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