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Process Equipment and Plant Design

Process Equipment and Plant Design
Maximum size of the raschig rings used in a packed tower is about __________ of the coloumn diameter.

1/50th
1/30th
1/10th
1/20th

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Process Equipment and Plant Design
Vertical vessels are not supported by

Saddles
Skirts
Columns
Brackets

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Process Equipment and Plant Design
In a double pipe concentric heat exchanger, the equivalent diameter of annulus for heat transfer would be (where, D₁ and D₂ are I.D. of inner and outer pipes)

D₂ - D₁
None of these
(D₂² - D₁²)/D₂²
(D₂² - D₁²)/D₁²

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Process Equipment and Plant Design
Baffles may be eliminated for

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

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Process Equipment and Plant Design
Any shell opening greater than 5 cms for a storage tank must be reinforced for reason of

Making the joint leak proof
Reduction of discontinuity in shape at the junction
None of these
Preventing the local overstressing of the shell around the opening

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Square pitch
Triangular pitch
Heat transfer rate is independent of tube arrangement
Diagonal square pitch

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