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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ tray arrangement is recommended for distillation column having diameter upto 4 ft.

Radial flow
Split flow
Cascade
Cross flow

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Process Equipment and Plant Design
Shell side heat transfer co-efficient in case of square pitch as compared to the triangular pitch under similar condition of fluid flow and tube size is

Less
More
Same
Twice

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Process Equipment and Plant Design
__________ strain is measured using a 'strain rosetter'.

Volumetric
Linear
Shear
None of these

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Process Equipment and Plant Design
The diameter of a propeller agitator used in agitation tank ranges from __________ percent of the tank diameter and its peripherial speed is normally 300 to 500 metres/minute.

40 to 50
5 to 10
55 to 75
15 to 30

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Process Equipment and Plant Design
Which of the following lengths of heat exchanger tubes are normally not used in practice?

6 metres
0.5 metre
10 metres
2.5 metres

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Process Equipment and Plant Design
__________ closure is the weakest enclosure for cylindrical vessels.

Conical or flat plate
Hemispherical
Elliptical
Torispherical

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