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Process Equipment and Plant Design

Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

√d
√(2πd)
D
√(2d)

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

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

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Process Equipment and Plant Design
In perforated plate towers, the

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

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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.

1/2
4
2
8

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Process Equipment and Plant Design
For high pressure process equipments/vessels, the connected nozzle should be

Welded
Screwed
Brazed
Flanged

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Process Equipment and Plant Design
In seive plate column, holes are drilled or punched in sizes ranging from 2.5 to 12 mm (5 mm being widely used). The hole pitch is normally __________ times the hole diameter to give the required hole area.

0.5 to 1.5
10 to 15
5 to 10
2.5 to 4.0

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