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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 P/A
A/P
4 A/P
√A

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Process Equipment and Plant Design
Lap joints are preferred for plates having thickness __________ mm.

43961
< 12.5
> 3
> 5

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Process Equipment and Plant Design
Shortest distance between two tubes is

None of these
Called tube clearance
More in case of triangular pitch as compared to square pitch of tube layout
Called tube pitch

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.5
G0.2
G0.8
G1.5

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Process Equipment and Plant Design
Speed of industrial paddle agitator ranges from __________ rpm.

500 to 750
20 to 100
1000 to 2000
1 to 5

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

5.5
2
3.5
1

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