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Process Equipment and Plant Design

Process Equipment and Plant Design
Two iron pipes of the same nominal diameter but different schedule numbers will have the same

None of these
Outside diameter
Inside diameter
Wall thickness

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Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

Non-corrosive condensate
High film co-efficient
Low cost
High latent heat

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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

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

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Process Equipment and Plant Design
The thermal stress in a metallic bar does not depend upon the

Both A & B
Changes in temperature
Cross-sectional area
Neither A nor B

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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)

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

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Process Equipment and Plant Design
Longitundinal stress induced in a thin walled cylindrical storage vessel is

PD/2t
PD/3t
PD/4t
PD/6t

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