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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
Rivets are generally specified by the

Overall length
Shank diameter
Head diameter
None of these

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Process Equipment and Plant Design
Rate of filtrate delivery is inversely proportional to the

Viscosity of filtrate
Both A & B
Cake & filter medium resistance
Filtering area & the pressure difference driving force

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Process Equipment and Plant Design
Hoop (circumferential) stress induced in a thin walled 'Horton Sphere' used for the storage of liquid ammonia under pressure is

pD/2t
pD/4t
pD/3t
pD/6t

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Process Equipment and Plant Design
Heat transfer co-efficient for a horizontal condenser as compared to a vertical condenser operating under similar conditions is

Less
About 0.33 times
About 3 times
Same

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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
0.2-0.5
0.1-0.2
1.2-1.5

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