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Process Equipment and Plant Design

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

2
1
5.5
3.5

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Process Equipment and Plant Design
Commercial packed scrubbers are normally designed for a pressure drop range of __________ mm water coloumn per metre of packed height.

88-105
52-68
43929
17-34

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Process Equipment and Plant Design
Optimum economic pipe diameter for fluid flow is determined by the

Total cost considerations (pumping cost plus fixed cost of the pipe)
None of these
Density of the fluid
Viscosity of the fluid

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Process Equipment and Plant Design
Pressure drop due to pipe fittings can be estimated by the equation, ΔP/p = 4f.Le/D.V2/2gc, where, Le = equivalent length of straight pipeline which will incur the same frictional loss as the fitting and D = diameter of the fitting. The value of Le/D (dimensionless) for 45° elbow and 180° close return bends would be respectively around

300 and 500
5 and 10
45 and 75
180 and 300

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

Eddy diffusivity = 0
Laminar flow
Plug flow
Complete back mixing

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Process Equipment and Plant Design
The retention time of material in a rotary dryer depends upon its

Flights arrangement
All of these
Slope & length
Rpm

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