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Process Equipment and Plant Design

Process Equipment and Plant Design
Normally, the ratio of the total riser area to the tower cross sectional area (for bubble cap towers of diameter more than 3 ft) is around

0.1-0.2
0.35-0.75
0.4-0.6
0.55-0.85

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

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

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Process Equipment and Plant Design
Filtration rate is affected by the

Pressure drop across the cake & filter medium
Area of filtering surface & the viscosity of filtrate
Cake & filter medium resistance
All of these

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Process Equipment and Plant Design
Spherical shaped pressure vessel is considered to be the most ideal, because it can

Withstand higher pressure for a given metallic shell thickness
Be designed without wind load considerations
Be fabricated very easily
Be supported very easily

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Process Equipment and Plant Design
Circumferential (hoop) stress in a thin cylindrical vessel under internal pressure is __________ the longitudinal stress.

Twice
Half
Eight times
Equal to

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Process Equipment and Plant Design
The maximum liquid gradient over a tray must not exceed

Half the tray spacing
5"
0.5" -1.25"
2"-3.5"

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