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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffles may be eliminated for

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

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

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

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

Enhancing mixing rate
Relieving excess pressure
Avoiding vortex formation
Creating turbulence

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Process Equipment and Plant Design
LMTD correction factor is used in heat exchanger design for

Fouling fluids
Multipass shell and tube heat exchanger
Counter flow of hot and cold fluids
Double pipe heat exchanger

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Process Equipment and Plant Design
A single pass air heater is connected to a two pass unit. For the air flow rate and other conditions remaining the same, the film heat transfer co-efficient for air will vary in the ratio of

2
None of these
20.8
20.2

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Process Equipment and Plant Design
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

(4p² - πd²/4)/πd
4(0.86p² - πd²/4)/πd
4(0.86p² - πd²)/πd
(p² - πd²/4)/πd

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