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Process Equipment and Plant Design

Process Equipment and Plant Design
Baffle width is normally taken as __________ times the tank diameter.

0.4-0.5
0.45-0.6
0.2-0.45
0.1-0.12

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Process Equipment and Plant Design
In a shell and tube heat exchanger having square pitch, the shell side equivalent diameter is given by (where, P = pitch, d = outside diameter of the tube)

Πd/4P²
(P² - πd²/4)/πd
4P²/πd
4(P² - πd²/4)/πd

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Process Equipment and Plant Design
__________ of water makes it a widely used coolant in heat exchangers.

Low viscosity
Low dirt factor
Low corrosiveness
High specific heat

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Process Equipment and Plant Design
Stage efficiency for packed tower varies with the

All of these
Operating pressure and column diameter
Type & size of packing
Fluid rates and fluid properties

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Process Equipment and Plant Design
In a shell and tube heat exchanger, the overall heat transfer co-efficient is proportional to the tube side (volumetric flow rate)0.8. This is valid, only when the ratio of the tube side film resistance to the total resistance is almost equal to

1
∞
2
20.8

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Process Equipment and Plant Design
Generally, as the length of the liquid path on a tray is increased beyond 5 ft, the overall column efficiency

Remains same
Increases
Decreases
May increase or decrease depending upon the plate spacing

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