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Process Equipment and Plant Design

Process Equipment and Plant Design
Pressure differential maintained across a continuous rotary vacuum filter is in the range of __________ mm Hg column.

600 to 700
50 to 100
100 to 150
250 to 500

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Process Equipment and Plant Design
In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

2.5 times
Less than
1.25-1.50 times
One-fourth of

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

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

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Process Equipment and Plant Design
1.2 to 3.8 cms is the value of the

Static submergence in case of a bubble cap tray for column operating under pressure (≥ 1 atm.)
Skirt clearance for bubble caps
Downcomer liquid seal in case of a balanced tray design
All of these

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Process Equipment and Plant Design
In shell and tube heat exchangers, straight tie rods are used to

None of these
Account for thermal strain
Fix the tubes in position
Hold baffle in space

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

Creating turbulence
Avoiding vortex formation
Enhancing mixing rate
Relieving excess pressure

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