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Process Equipment and Plant Design

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

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

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

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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
Increases very rapidly
Decreases very rapidly
Remains constant

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

10 to 20
1 to 2
20 to 30
4 to 10

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

2
8
4
1/2

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Process Equipment and Plant Design
25 per cent cut segmental baffle means that the baffle

Spacing is 75% of its height
Height is 25% of the I.D. of the shell
Height is 75% of the I.D. of the shell
Width is 25% of its height

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