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Process Equipment and Plant Design

Process Equipment and Plant Design
The minimum baffle height should be

Twice the impeller diameter
3/4 of the tank height
Equal to the impeller diameter
Twice the tank diameter

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

All of these
Fluid rates and fluid properties
Operating pressure and column diameter
Type & size of packing

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Process Equipment and Plant Design
With increase in gas flow rate to fabric surface area ratio (Nm³/hr/m² fabric surface area), the size & the cost of a bag filter

Remain unaffected
Decreases
Increases
None of these

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Process Equipment and Plant Design
Floating head heat exchangers are used for the

Counter-current heat transfer systems
Cases where temperature difference between the shell and the tubes is more (>50°C)
Co-current heat transfer systems
Heat transfer between corrosive fluids

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

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

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Process Equipment and Plant Design
The circumferential (hoop) stress in a thin walled cylinderical vessel under internal pressure is

pd/3t
pd/t
pd/2t
pd/4t

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