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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

0.75
0.85
0.95
0.55

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

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

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Process Equipment and Plant Design
The necessary wall thickness for a metallic storage vessel is a function of the

All of these
Ultimate tensile strength (or yield point) of the material and operating temperature
Diameter of the vessel
Operating pressure and welding/joint efficiency

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

5.5
2
3.5
1

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Process Equipment and Plant Design
Which of the following is the most common type of baffle used in industrial shell and tube heat exchanger?

Orifice baffle
Disk and doughnut baffle
75% cut segmental baffle
25% cut segmental baffle

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Process Equipment and Plant Design
Typical static submergence for bubble cap plate column operating at atmospheric pressure may be around

0.5"
5"
2.5"
50% of the plate spacing

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