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Process Equipment and Plant Design

Process Equipment and Plant Design
To avoid the tearing off the plate of an edge, the margin (i.e., the minimum distance from the centre of the rivet hole to the nearest edge of the plate) should be equal to

2.5 d
D
0.5 d
1.5 d

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Containing suspended solids flows at high velocity
Is of high specific gravity
Containing suspended solids flows at low velocity
Is highly viscous

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Process Equipment and Plant Design
Welded joint efficiency in the design of chemical process equipment is taken as

0.55
0.95
0.75
0.85

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Process Equipment and Plant Design
In packed towers provided with pall rings liquid redistributors are positioned at heights of every 6 metres or 5-10 times the column diameter, whichever is less. Maximum size of the pall rings should not exceed __________ of the column diameter.

1/5-1/10th
1/10-1/15th
1/20-1/30th
1/2 to 1/4th

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Process Equipment and Plant Design
In case of a 'thin' pressure vessel, the ratio of its diameter to wall thickness is

> 10
< 10
30
> 20

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Fouling fluids
Double pipe heat exchanger
Multipass shell and tube heat exchanger
Counter flow of hot and cold fluids

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