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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ dished head is the strongest of all.

None of these
Torispherical
Hemispherical
Elliptical

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Process Equipment and Plant Design
Width and depth of grooves in the tube sheet holes normally are __________ inch respectively.

1/2 and 8
1/64 and 1/8
1/8 and 1/64
1/2 and 5

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Process Equipment and Plant Design
1.2 to 3.8 cms is the value of the

Skirt clearance for bubble caps
Static submergence in case of a bubble cap tray for column operating under pressure (≥ 1 atm.)
All of these
Downcomer liquid seal in case of a balanced tray design

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Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

More
Less
More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein
Same

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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
Scale up problem in design based on the similarity concept takes into account __________ similarity.

Geometrical
All of these
Dynamic
Kinematic

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