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Process Equipment and Plant Design

Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

Less than
One-fourth of
2.5 times
1.25-1.50 times

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Viscosity of the fluid
Total cost considerations (pumping cost plus fixed cost of the pipe)
None of these
Density of the fluid

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Process Equipment and Plant Design
The force due to wind load acting on a tall vessel depends upon its

Outside diameter
Height
Shape
All of these

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for

Creating turbulence
Fixing the tubes
Reducing scale deposition
Increasing pressure drop

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Process Equipment and Plant Design
With increase in pressure drop (for a given particle size), the dust collection efficiency of a cyclone separator will

Decrease
Increase
Increase or decrease depending on the nature of the dust
Remain unaffected

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Process Equipment and Plant Design
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

Increase by 1.8
Decrease by 22
None of these
Increase by 21.6

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