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Process Equipment and Plant Design

Process Equipment and Plant Design
Most of the storage vessels/tanks are made cylindrical, because of the fact that a cylinder

Has greater structural strength
Both A & B
Is easy to fabricate
Neither A nor B

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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
2
4

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Process Equipment and Plant Design
Lug support is

The most suitable for thick vertical vessel
All of these
Same as bracket support
Provided usually for vessels of much smaller height than skirt supported vessels

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Process Equipment and Plant Design
In perforated plate towers, the

Hole sizes may be around 1/8" or 3/16"
Pressure drop is less compared is similar bubble cap towers
All of these
Total hole area may be around 6 to 15% of tower cross-sectional area

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Process Equipment and Plant Design
The force due to wind load acting on a tall vessel depends upon its

Shape
Outside diameter
Height
All of these

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

(d1 + d2)/d2
D2/(d1 + d2)
(d1 + d2)/d1
D1/(d1 + d2)

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