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Process Equipment and Plant Design

Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Small diameter tall tanks
Small diameter tanks
All of these
Large diameter tanks

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

0.55
0.8
0.95
0.99

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Process Equipment and Plant Design
In the design of a paddle agitator, the ratio (paddle dia/tank dia) is normally taken as

0.1
0.8
0.25
0.5

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Process Equipment and Plant Design
The ratio of lateral strain to linear strain is termed as the

Poisson's ratio
Shear modulus
Bulk modulus
Modulus of elasticity

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

2.5
3.5
1.25
1.75

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Process Equipment and Plant Design
__________ liquor is best handled in a long tube vertical evaporator.

Viscous
Foamy
Scaling
Salting

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