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Process Equipment and Plant Design

Process Equipment and Plant Design
The stress developed in a material without any permanent set is called the

Ultimate stress
Yield stress
Elastic limit
Breaking stress

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Process Equipment and Plant Design
Baffles may be eliminated for

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

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Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

Low cost
Non-corrosive condensate
High latent heat
High film co-efficient

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Process Equipment and Plant Design
In case of a continuous distillation column, increase in reflux ratio may result in the

Lower fixed charges for the column
Greater cost for the reboiler heat supply
All of these
Greater cost for the condenser coolant

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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

0.95
0.99
0.8
0.55

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

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

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