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Process Equipment and Plant Design

Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

7500
15000
1250
2500

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Process Equipment and Plant Design
The average velocity in the tubes of a 1-4 heat exchanger is __________ times that in 1-1 heat exchanger having the same size & number of tubes and operated at same liquid flow rate.

43832
4
2
43834

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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

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

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Process Equipment and Plant Design
The normal range of velocity of steam in pipes is __________ m/sec.

1-5
80-100
0.1-0.5
10-20

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Process Equipment and Plant Design
Skirt support is the most suitable for supporting __________ vessels.

Small horizontal
Thick walled
Large horizontal
Tall vertical

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Process Equipment and Plant Design
The dust collection efficiency of a cyclone separator

Is inversely proportional to the mass of the dust particle
Is directly proportional to the radius of the dust particle path
Decreases with increase in gas flow rate
None of these

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