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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

0.8
0.95
0.99
0.55

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Process Equipment and Plant Design
Normally, the length to diameter ratio of rotary dryers varies form 4 to 10 and for its economic operation, the number of transfer units (NTU) for such dryers varies from

1.5-2.5
44119
3.5-5.5
7.5-10.0

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Process Equipment and Plant Design
The units of Young's modulus of elasticity and __________ are the same.

Strain
Modular ratio
Stress
None of these

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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 = G
Δp = G2
Δp = G0.5
Δp = 1/G0.6

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Process Equipment and Plant Design
What is the minimum recommended ligament for square pitch arrangement in case of heat exchangers?

6.5 cms
Equal to tube I.D
6.5 mm
Equal to tube O.D

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Process Equipment and Plant Design
__________ strain is measured using a 'strain rosetter'.

Volumetric
None of these
Shear
Linear

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