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Process Equipment and Plant Design

Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.95
0.75
0.55
0.85

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Process Equipment and Plant Design
Floating head heat exchangers are used for the

Counter-current heat transfer systems
Cases where temperature difference between the shell and the tubes is more (>50°C)
Heat transfer between corrosive fluids
Co-current heat transfer systems

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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
__________ closure is the weakest enclosure for cylindrical vessels.

Elliptical
Torispherical
Conical or flat plate
Hemispherical

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Segmental
Independent of the type of
Disk and ring
Orifice

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

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

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