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Process Equipment and Plant Design

Process Equipment and Plant Design
In case of 1.5" heat exchanger tubes, the inside flow area __________ with decrease in BWG.

Remains same
Decreases
None of these
Increases

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Process Equipment and Plant Design
Apex angle of conical heads used in the bottom heads of chemical process equipments is usually

45°
30°
75°
60°

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Process Equipment and Plant Design
__________ is the determining factor for the number of bubble caps to be used per tray.

Liquid load
Permissible slot velocity
Tray diameter
Vapor load

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

All of these
Operating pressure and column diameter
Type & size of packing
Fluid rates and fluid properties

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

5 to 10
10 to 20
1.5 to 2.5
0.01 to 1

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Process Equipment and Plant Design
Normally, the length to diameter ratio of rotary dryers varies form 4 to 10 and for its economic operation, the number of transfer units (NTU) for such dryers varies from

7.5-10.0
1.5-2.5
3.5-5.5
44119

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