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Process Equipment and Plant Design

Process Equipment and Plant Design
Equivalent diameter for heat transfer calculation for a duct of square cross-section having each side as 'd' will be

D
√(2πd)
√(2d)
√d

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Process Equipment and Plant Design
__________ head is the most economical for cylindrical vessels designed for operating at high pressure (> 15 atm.).

Ellipsoidal
Hemispherical
Dished
Conical

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Process Equipment and Plant Design
Vertical storage vessels are never supported by __________ support.

Skirt
Lug
Saddle
Bracket

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Process Equipment and Plant Design
Which tube arrangement in a heat exchanger would facilitate highest heat transfer rate?

Square pitch
Triangular pitch
Heat transfer rate is independent of tube arrangement
Diagonal square pitch

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

Vapor load
Tray diameter
Liquid load
Permissible slot velocity

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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

75°
60°
45°
30°

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