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Process Equipment and Plant Design

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.

8
1/2
4
2

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Process Equipment and Plant Design
In a distillation column, bubble caps are located on trays with a pitch of __________ times the outside diameter of the caps.

1.5 to 3
2.5
1.6 to 2
1.3 to 2

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Process Equipment and Plant Design
__________ heat exchanger is also known as 'hair pin type' exchanger,

Finned
Double pipe
Regenerative
Plate type

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Process Equipment and Plant Design
For pipe flows, head is proportional to __________ at constant capacity (where D = pipe diameter ).

D²
1/D⁵
1/D²
1/D

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Process Equipment and Plant Design
A cylinderical pressure vessel of volume 6 πm³ has to be designed to withstand a maximum internal pressure of 10 atm. The allowable design stress of the material is 125N/mm² and corrosion allowance is 2 mm. The thickness of the vessel for a length/diameter ratio of 3 will be close to

8 mm
5 mm
10 mm
6 mm

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Process Equipment and Plant Design
The main purpose of providing stepping on the trays is to

Improve the flow condition
Facilitate handling of large flow rate of liquid
Decrease the pressure drop
Increase the residence time

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