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

35-40
43961
15-20
30-35

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

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

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Process Equipment and Plant Design
Which of the following is not a graphical method (but is an analytical method) for the calculation of theoretical number of stages in case of continuous binary distillation?

None of these
Sorel-Lewis method
McCabe-Thiele's method
Ponchon-Savarit method

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Process Equipment and Plant Design
Hoop (circumferential) stress induced in a thin walled 'Horton Sphere' used for the storage of liquid ammonia under pressure is

pD/2t
pD/3t
pD/6t
pD/4t

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Process Equipment and Plant Design
In seive plate column, holes are drilled or punched in sizes ranging from 2.5 to 12 mm (5 mm being widely used). The hole pitch is normally __________ times the hole diameter to give the required hole area.

5 to 10
0.5 to 1.5
2.5 to 4.0
10 to 15

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