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Process Equipment and Plant Design

Process Equipment and Plant Design
Width and depth of grooves in the tube sheet holes normally are __________ inch respectively.

1/64 and 1/8
1/8 and 1/64
1/2 and 8
1/2 and 5

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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
180 and 300
5 and 10
45 and 75

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Process Equipment and Plant Design
Filtration rate is affected by the

Area of filtering surface & the viscosity of filtrate
Pressure drop across the cake & filter medium
Cake & filter medium resistance
All of these

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Process Equipment and Plant Design
Hole diameter of the seive trays in the distillation column ranges from __________ mm.

4 to 8
3 to 12.5
12.5 to 18.5
L to 3

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Process Equipment and Plant Design
Steam economy is defined as the amount of evaporation per unit amount of steam used, while the capacity is the total evaporation obtained per hour. Use of multiple effect in evaporation

Increases economy
Does not affect the capacity
Both B & C
Increases capacity

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Process Equipment and Plant Design
An underdesigned steam trap will

None of these
Destroy itself of acceleration wear due to rapid recycling
Waste steam
Back up condensate and cause water hammer in steam line

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