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Process Equipment and Plant Design

Process Equipment and Plant Design
The difficulty of liquid distribution in packed towers is accentuated, when the ratio of tower diameter to packing diameter is

> 20 < 50
< 7
> 7 < 15
< 30

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Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

Less
More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein
Same
More

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Process Equipment and Plant Design
Needle valves are generally not used for

High pressure throttling service
Smaller sizes of pipe
Very accurate flow control
Very large diameter pipes

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Process Equipment and Plant Design
What is the minimum recommended ligament for square pitch arrangement in case of heat exchangers?

6.5 mm
6.5 cms
Equal to tube I.D
Equal to tube O.D

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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.

8
1/2
4
2

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Process Equipment and Plant Design
The maximum liquid gradient over a tray must not exceed

2"-3.5"
5"
0.5" -1.25"
Half the tray spacing

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