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Process Equipment and Plant Design

Process Equipment and Plant Design
Safety valves are provided in chemical equipments to guard against excessive

Noise
Turbulence
Pressure/pressure fluctuation
Temperature

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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

0.99
0.8
0.55
0.95

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Process Equipment and Plant Design
Accidents in chemical plants are mostly due to

Faulty operating procedures
Inadequate equipment design
Failure of equipments
Improper layout of the equipments

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Process Equipment and Plant Design
Diameter of rivet hole (d, mm) and the plate thickness (t, mm) are related by Unwin's formula as

D = 3√t
D = 1.6 √t
D = 1.1 t
D = 1.5 t

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Process Equipment and Plant Design
A cylinderical pressure vessel of volume 6 πm³ has to be designed to withstand a maximum internal pressure of 10 atm. The allowable design stress of the material is 125N/mm² and corrosion allowance is 2 mm. The thickness of the vessel for a length/diameter ratio of 3 will be close to

6 mm
8 mm
10 mm
5 mm

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

Ultimate stress
Elastic limit
Yield stress
Breaking stress

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MORE MCQ ON Process Equipment and Plant Design

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