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Process Equipment and Plant Design

Process Equipment and Plant Design
Larger depth of liquid on the trays of a distillation column

Results in higher pressure drop per tray
Both A & B
Leads to high tray efficiency
Neither A nor B

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Process Equipment and Plant Design
Hold up of material in a operating rotary drier is in the range of

0.5 to 0.8
0.05 to 0.15
0.8 to 0.9
0.25 to 0.50

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Process Equipment and Plant Design
In a rotary drier, the average retention time of solid is(where Z = length of the drier, metres ρ = apparent solid density, kg/m³ L = flow rate of dry solids, kg/see. m² drier cross-section H = hold up of solid.)

Z.H/L.ρ
L/Z.H.ρ
H.ρ/L
Z.H.ρ/L

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Process Equipment and Plant Design
Lap joints are preferred for plates having thickness __________ mm.

< 12.5
> 3
43961
> 5

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Process Equipment and Plant Design
__________ strain is measured using a 'strain rosetter'.

Shear
Volumetric
None of these
Linear

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Process Equipment and Plant Design
Which of the following factors affect the pressure drop in a co-current gas-liquid absorption packed tower?

Size, shape, orientation and surface of the packing particles
Fluid flow rates
All of these
Density and viscosity of fluids

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