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Process Equipment and Plant Design

Process Equipment and Plant Design
What is the value of 'q' for saturated liquid feed to a distillation column?

1
>1

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Process Equipment and Plant Design
The main purpose of providing stepping on the trays is to

Decrease the pressure drop
Facilitate handling of large flow rate of liquid
Increase the residence time
Improve the flow condition

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.5
G0.2
G1.5
G0.8

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Process Equipment and Plant Design
For turbine agitator, the impeller diameter is about

0.95 d
0.1 to 0.2 d
0.65 to 0.85 d
0.3 to 0.5 d

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Process Equipment and Plant Design
For a given design of bubble cap, the number of bubble caps to be used per tray is set by the

Diameter of the column
Plate spacing
All of these
Allowable gas velocity through the slots

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Process Equipment and Plant Design
Normally, the length to diameter ratio of rotary dryers varies form 4 to 10 and for its economic operation, the number of transfer units (NTU) for such dryers varies from

7.5-10.0
1.5-2.5
44119
3.5-5.5

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