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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

Low viscosity liquids (< 200 poise)
None of these
High viscosity liquids (> 600 poise)
Large diameter tanks

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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

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

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

Large horizontal cylindrical
Thick walled tall
Small
Tall but empty

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Process Equipment and Plant Design
Typical static submergence for bubble cap plate column operating at atmospheric pressure may be around

0.5"
5"
2.5"
50% of the plate spacing

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

Torispherical
Elliptical
Hemispherical
None of these

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Process Equipment and Plant Design
__________ shapedroof is the most commonly used roof for cylinderical storage tanks.

Conical
Umbrella
Dome
Flat

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