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Process Equipment and Plant Design

Process Equipment and Plant Design
Normally, the ratio of the total riser area to the tower cross sectional area (for bubble cap towers of diameter more than 3 ft) is around

0.1-0.2
0.35-0.75
0.4-0.6
0.55-0.85

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Process Equipment and Plant Design
The practical representative values of HETP for a number of commercial operations lies within a range of __________ metre.

0.4-0.9
1.2-1.5
0.2-0.5
0.1-0.2

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Process Equipment and Plant Design
Reflux ratio variation in a distillation column is between

Zero and infinity
Minimum and infinity
None of these
Zero and one

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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.

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

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Thick spherical
Horizontal cylinderical
Thick walled vertical
Tall vertical

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Process Equipment and Plant Design
For storing hazardous chemicals in large storage tanks, the minimum safe distance between the two tanks should range between __________ times the tank diameter.

4 to 5
6 to 8
2.5 to 3.5
1 to 1.5

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