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Process Equipment and Plant Design

Process Equipment and Plant Design
The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

4 A/P
A/P
4 P/A
√A

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Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

0.1-0.12
0.45-0.6
0.2-0.45
0.4-0.5

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Process Equipment and Plant Design
Heat transfer co-efficient for a horizontal condenser as compared to a vertical condenser operating under similar conditions is

Less
About 0.33 times
About 3 times
Same

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Process Equipment and Plant Design
For given number of passes, pitch & tube diameter, the maximum number of tubes that can be accommodated in a shell of tripled inside diameter will be __________ times.

Considerably more than 9
About 3
About 9
Considerably less than 9

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Cross
Reverse
Split
Cascade

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Process Equipment and Plant Design
In a shell and tube heat exchanger, tube side __________ of the mass velocity.

Heat transfer co-efficient is proportional to 0.8th power
Neither A nor B
Pressure drop is proportional to the square
Both A & B

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