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Process Equipment and Plant Design

Process Equipment and Plant Design
Normally, the ratio of the total riser area to the tower cross sectional area (for bubble cap towers of diameter more than 3 ft) is around

0.1-0.2
0.4-0.6
0.35-0.75
0.55-0.85

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

75
300
10
25

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Process Equipment and Plant Design
Le/D for a Tee (used as elbow, entering run) would be around

5
200
350
60

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets
Skirts
Saddles
Columns

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

Elliptical
Torispherical
Hemispherical
None of these

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Process Equipment and Plant Design
In the design of a paddle agitator, the ratio (paddle dia/tank dia) is normally taken as

0.8
0.1
0.5
0.25

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