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Process Equipment and Plant Design

Process Equipment and Plant Design
Value of Peclet number = 0, is the representative of

Eddy diffusivity = 0
Plug flow
Laminar flow
Complete back mixing

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Process Equipment and Plant Design
Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

Containing suspended solids flows at low velocity
Containing suspended solids flows at high velocity
Is highly viscous
Is of high specific gravity

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

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

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Process Equipment and Plant Design
With increase in temperature drop (in a shell and tube heat exchanger), the LMTD correction factor, FT

Increases linearly
Decreases very rapidly
Remains constant
Increases very rapidly

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Process Equipment and Plant Design
In case of a 'thin' pressure vessel, the ratio of its diameter to wall thickness is

> 10
> 20
< 10
30

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Process Equipment and Plant Design
The ratio of lateral strain to linear strain is termed as the

Shear modulus
Poisson's ratio
Bulk modulus
Modulus of elasticity

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