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Process Equipment and Plant Design

Process Equipment and Plant Design
__________ tray arrangement is recommended for distillation column having diameter upto 4 ft.

Split flow
Cascade
Cross flow
Radial flow

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

4 to 10
10 to 20
1 to 2
20 to 30

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Process Equipment and Plant Design
Hoop (circumferential) stress induced in a thin walled 'Horton Sphere' used for the storage of liquid ammonia under pressure is

pD/4t
pD/6t
pD/2t
pD/3t

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Process Equipment and Plant Design
The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

2 d
0.5 d
0.75 d
D

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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

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

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Process Equipment and Plant Design
The value of fouling factor depends upon the

Suspended solids in the fluid
All of these
Characteristic of process fluid
Velocity of process fluid containing suspended solids

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