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Process Equipment and Plant Design

Process Equipment and Plant Design
Longitundinal stress induced in a thin walled cylindrical storage vessel is

PD/6t
PD/3t
PD/2t
PD/4t

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Process Equipment and Plant Design
Baffles may be eliminated for

High viscosity liquids (> 600 poise)
Low viscosity liquids (< 200 poise)
None of these
Large diameter tanks

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Process Equipment and Plant Design
A pressure vessel is said to be made of 'thick' shell, if the ratio of its diameter to wall thickness is

10
20
10
20

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Is highly viscous
Containing suspended solids flows at low velocity
Containing suspended solids flows at high velocity
Is of high specific gravity

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Process Equipment and Plant Design
In the agitators, the power required will be changed with the increase of diameter of agitator (D) as

D
D⁵
D⁹
D²

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Process Equipment and Plant Design
To avoid the tearing off the plate of an edge, the margin (i.e., the minimum distance from the centre of the rivet hole to the nearest edge of the plate) should be equal to

D
1.5 d
0.5 d
2.5 d

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