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Process Equipment and Plant Design

Process Equipment and Plant Design
The circumferential (hoop) stress in a thin walled cylinderical vessel under internal pressure is

pd/2t
pd/t
pd/4t
pd/3t

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Process Equipment and Plant Design
Rivets are generally specified by the

Head diameter
Shank diameter
Overall length
None of these

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Process Equipment and Plant Design
Heat transfer co-efficient, hG(Kcal/hr.m² .°C) and mass velocity of air, G (kg/hr.m² ) for air flow parallel to the surface in case of constant drying rate in batch drying is related as hG = 0.0176G0.8. But when the flow of air perpendicular to the surface is encountered, this equation changes to

0.0176G1.37
1.004G0.8
HG = 1.004G0.37
HG = 0.0176G0.37

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Process Equipment and Plant Design
In common bubble cap distillation column design practice, riser area is approximately equal to (where, Aa = Annular passage area, and Sa = Slot area)

Aa = Sa
Sa = 1.5 Aa
Aa = 1.5 Sa
1.2 Aa = 1.2 Sa

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Process Equipment and Plant Design
Needle valves are generally not used for

Smaller sizes of pipe
Very accurate flow control
Very large diameter pipes
High pressure throttling service

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Process Equipment and Plant Design
The dust collection efficiency of electrostatic precipitator increases with increase in the

Both A & B
Gas flow rate
Electrode area
Neither A nor B

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