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Process Equipment and Plant Design

Process Equipment and Plant Design
Minimum baffle spacing recommended in a shell and tube heat exchanger is equal to

40% of the I.D. of the shell
I.D. of the shell
5 cms
25 cms

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

Modulus of rigidity
Modulus of elasticity
None of these
Bulk modulus

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Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

D
√d
√(2d)
√(2πd)

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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

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

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Process Equipment and Plant Design
Floating head heat exchangers are used for the

Cases where temperature difference between the shell and the tubes is more (>50°C)
Heat transfer between corrosive fluids
Counter-current heat transfer systems
Co-current heat transfer systems

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Process Equipment and Plant Design
The dust collection efficiency of electrostatic precipitator increases with increase in the

Neither A nor B
Both A & B
Electrode area
Gas flow rate

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