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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

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

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Process Equipment and Plant Design
In actual operation of a bubble cap distillation tower, the __________ at the bottom of the tower is more than that at the top of the tower.

Pressure and temperature
Vapour molecular weight
Molal flow rate of vapour
All of these

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Process Equipment and Plant Design
With increase in gas flow rate to fabric surface area ratio (Nm³/hr/m² fabric surface area), the size & the cost of a bag filter

Increases
Remain unaffected
Decreases
None of these

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Process Equipment and Plant Design
In shell and tube heat exchangers, straight tie rods are used to

Fix the tubes in position
Account for thermal strain
None of these
Hold baffle in space

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Process Equipment and Plant Design
Thin spherical shells subjected to internal pressure, develop __________ stresses.

Radial
Both A & B
Circumferential
Neither A nor B

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Process Equipment and Plant Design
Rivets are generally specified by the

Head diameter
None of these
Shank diameter
Overall length

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