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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

None of these
Low viscosity liquids (< 200 poise)
High viscosity liquids (> 600 poise)
Large diameter tanks

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Process Equipment and Plant Design
Excessive liquid gradient on a tray may result in the

Back trapping
Gas blowing beneath cap skit
Maldistribution of gas
All of these

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Process Equipment and Plant Design
In which of the following evaporators, steam is fed inside the tube while the liquor is outside the tube?

Long tube vertical evaporator
None of these
Short tube vertical evaporator
Horizontal tube evaporator

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Process Equipment and Plant Design
Tube side pressure drop in a 1-2 heat exchanger (for turbulent flow of fluids through the tubes) is about __________ times, that in a 1-1 heat exchanger having the same size & number of tubes and operated at the same liquid flow rate.

2
4
1/2
8

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Process Equipment and Plant Design
In the allocated cap area, bubble caps are generally arranged on equilateral triangular pitch. Number of caps fixed on a plate is with a

Neither A nor B
Cap pitch of 1.3-2 times the cap diameter
Clearance of 25-75 mm
Either A or B

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Thick walled vertical
Tall vertical
Thick spherical
Horizontal cylinderical

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