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Process Equipment and Plant Design

Process Equipment and Plant Design
The ratio of tube length to shell diameter in case of liquid shell and tube heat exchanger ranges from

4 to 8
3 to 5
2 to 3
6 to 12

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Height of the plate spacing
Lower limit of vapour velocity
Hole diameter of the seive tray
Upper limit of the vapour velocity

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Process Equipment and Plant Design
In case of saddle packing (e.g., berl and intralox saddles), the maximum size of the packing should not exceed __________ of the column diameter.

l/50th
l/5th
l/15th
l/30th

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Process Equipment and Plant Design
The minimum tray spacing in distillation column of diameter less than 3 ft is normally __________ inches.

24
6
34
18

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Process Equipment and Plant Design
Large process vessels operating under extreme temperature and pressure conditions are normally clad/ lined with materials like stainless steel, aluminium, nickel & its alloys, copper & its alloys and titanium. The cladding thickness is generally about __________ percent of the total thickness.

1 to 5
10 to 20
40 to 50
30 to 40

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Process Equipment and Plant Design
Safety valves are provided in chemical equipments to guard against excessive

Temperature
Turbulence
Noise
Pressure/pressure fluctuation

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