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Process Equipment and Plant Design

Process Equipment and Plant Design
Diameter of rivet hole (d, mm) and the plate thickness (t, mm) are related by Unwin's formula as

D = 1.5 t
D = 3√t
D = 1.1 t
D = 1.6 √t

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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

0.8
0.99
0.55
0.95

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Process Equipment and Plant Design
For a 25 mm hole drilled in plates to be rivetted, the shank diameter of the rivet should be __________ mm.

27
23
26
25

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Hole diameter of the seive tray
Lower limit of vapour velocity
Height of the plate spacing
Upper limit of the vapour velocity

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Process Equipment and Plant Design
Le/D for fully open globe value may be around

25
300
10
75

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the problem of differential expansion between the shell and tube passes is taken care of by using a

U-bend
Neither A nor B
Either A or B
Floating head tube sheet

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