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Process Equipment and Plant Design

Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Both A & B
Pitch
Layout
Neither A nor B

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Process Equipment and Plant Design
Liquid gradient over the tray results due to the

Large reflux ratio
Large plate spacing
Resistance offered to flow of liquids by caps & risers and the flow of gas
Low gas velocity

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Process Equipment and Plant Design
Optimum reflux ratio in a continuous distillation column is determined by the

Total cost consideration (fixed cost of the column plus the cooling water & steam cost)
Flooding limit of the column
Maximum permissible vapour velocity
None of these

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

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

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Process Equipment and Plant Design
The longitudinal stress induced in a thin walled cylinderical vessel under internal pressure is

pd/2t
pd/4t
pd/8t
pd/t

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Process Equipment and Plant Design
A 'rupture disc' is provided in chemical equipments as an accessory meant for

Relieving excess pressure
Enhancing mixing rate
Avoiding vortex formation
Creating turbulence

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