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Process Equipment and Plant Design

Process Equipment and Plant Design
A shell may by termed as thin if its thickness to diameter ratio is less than 0.1. The factor which can be neglected in the calculation of membrane stresses is

Deformation
Elongation
Shear
Bending

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Process Equipment and Plant Design
Factor of safety (i.e., overdesign factor) in heat transfer equipments is about __________ percent more than the actual/theoretical design factor.

15-20
30-35
43961
35-40

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Increases
May increase or decrease depending upon the plate spacing
Remains same
Decreases

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

4 to 8
12.5 to 18.5
3 to 12.5
L to 3

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Thick walled tall
Large horizontal cylindrical
Tall but empty
Small

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Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

3.5
2
3
1

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