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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

√(2d)
√(2πd)
D
√d

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Process Equipment and Plant Design
Corrosion allowance in the design of pressure vessel/chemical equipment is not necessary, if

Wall thickness is > 30 mm
Material of construction is high alloy steel
Both B & C
Plain carbon steel and cast iron parts are used

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Process Equipment and Plant Design
Power required for agitation depends upon the

Size of agitator & the tank
Agitator type & speed of agitation
Height & properties of the liquid
All of these

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Process Equipment and Plant Design
In a cylinderical vessel subjected to internal pressure, the longitudinal stress σL and the circumferential stress, σh are related by

σh = 2 σL
σh = σL/2
σh = σL
No relation exists

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Process Equipment and Plant Design
Value of Peclet number = ∞, is the representative of

Laminar flow
Eddy diffusivity = 0
Complete back mixing
Plug flow

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Process Equipment and Plant Design
At equal mass velocities, the values of film co-efficients for gases as compared to that for liquids are generally.

Lower
Higher
Unpredictable
Same

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