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Process Equipment and Plant Design

Process Equipment and Plant Design
The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

√A
4 A/P
4 P/A
A/P

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Process Equipment and Plant Design
The buckling tendency of compression members is always in the direction of the

Axis of the load
None of these
Perpendicular to the axis of the load
Least radius of gyration

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Process Equipment and Plant Design
In packed towers provided with saddle packing, liquid redistributors are positioned at every __________ times column diameter or 6 metres whichever is less.

43864
20-25
43959
44119

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Withstand higher pressure for a given metallic shell thickness
Be supported very easily
Be designed without wind load considerations
Be fabricated very easily

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

Thick walled vertical
Tall vertical
Thick spherical
Horizontal cylinderical

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Process Equipment and Plant Design
The distance between the top of the slots and the liquid surface when the static liquid is just ready to flow over the overflow weir is called

None of these
Static submergence
Downcomer liquid seal
Skirt clearance

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