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Process Equipment and Plant Design

Process Equipment and Plant Design
It is not desirable to design a heat exchanger for LMTD correction factor, FT, of less than

0.95
0.55
0.99
0.8

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Process Equipment and Plant Design
A rivetted joint does not fail by __________ of rivets.

None of these
Tearing
Tearing of the plate across a row
Shearing

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Process Equipment and Plant Design
For high pressure process equipments/vessels, the connected nozzle should be

Welded
Flanged
Screwed
Brazed

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Process Equipment and Plant Design
__________ shaped roof is most commonly used for cylindrical tanks.

Dome
Umbrella
Flat
Cone

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large plate spacing
Large reflux ratio
Resistance offered to flow of liquids by caps & risers and the flow of gas
Low gas velocity

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Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.60-0.90
0.15-030
0.5-0.65
0.75-0.85

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