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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
0.8
0.99

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Process Equipment and Plant Design
Heat transfer co-efficient for a horizontal condenser as compared to a vertical condenser operating under similar conditions is

Same
About 3 times
Less
About 0.33 times

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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

Decreases
None of these
Increases
Remain unaffected

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Process Equipment and Plant Design
Pressure drop (Δp) and the superficial gas mass velocity (G) in case of packed absorption tower operating in the preloading range are related as

Δp = G2
Δp = G
Δp = 1/G0.6
Δp = G0.5

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Process Equipment and Plant Design
In a __________ rivetted joint, the number of rivets decreases from the innermost row to the outermost row.

Zig-zag
None of these
Chain
Diamond

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Process Equipment and Plant Design
The ratio of shear stress to shear strain is called

Modulus of rigidity
Modulus of elasticity
Bulk modulus
Shear modulus

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