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Process Equipment and Plant Design

Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

1.75
2.5
3.5
1.25

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Process Equipment and Plant Design
The average velocity in the tubes of a 1-4 heat exchanger is __________ times that in 1-1 heat exchanger having the same size & number of tubes and operated at same liquid flow rate.

2
43832
43834
4

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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 < 15
< 7
< 30

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Process Equipment and Plant Design
In a __________ rivetted joint, the rivets in the various rows are opposite to each other.

Zig-zag
Diamond
None of these
Chain

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Process Equipment and Plant Design
The buckling tendency of compression members is always in the direction of the

Least radius of gyration
Axis of the load
Perpendicular to the axis of the load
None of these

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large plate spacing
Large reflux ratio
Low gas velocity
Resistance offered to flow of liquids by caps & risers and the flow of gas

ANSWER DOWNLOAD EXAMIANS APP
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