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Process Equipment and Plant Design

Process Equipment and Plant Design
The force due to wind load acting on a tall vessel depends upon its

All of these
Shape
Outside diameter
Height

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Process Equipment and Plant Design
For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

(d1 + d2)/d2
D1/(d1 + d2)
(d1 + d2)/d1
D2/(d1 + d2)

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Process Equipment and Plant Design
In packed towers provided with pall rings liquid redistributors are positioned at heights of every 6 metres or 5-10 times the column diameter, whichever is less. Maximum size of the pall rings should not exceed __________ of the column diameter.

1/20-1/30th
1/5-1/10th
1/10-1/15th
1/2 to 1/4th

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Process Equipment and Plant Design
The clearance between two tubes in a shell and tube heat exchanger is known as 'ligament', whose minimum value is __________ the outside diameter of the tube, but in no case it should be less than 4.5 mm.

Three fourth
Equal to
One fourth
Half

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Process Equipment and Plant Design
__________ tower is the most suitable gas-liquid contacting device involving highly corrosive fluids.

Sieve plate
None of these
Bubble cap plate
Packed

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Process Equipment and Plant Design
Tube height in a calendria type evaporator is normally less than __________ metres.

2
1
3.5
5.5

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