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Mass Transfer

Mass Transfer
Diameter to height ratio for a rashig ring is

1
0.5
2
5

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Mass Transfer
High pressure at the bottom of a distillation tower handling heat sensitive materials results in

Erosion of the tower
Very efficient operation
Thermal decomposition of bottoms
Increased relative volatility

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Mass Transfer
Batch tray dryers suffers from the disadvantage of

All of the listed here
Non-uniform & low production rate
High maintenance cost
High labour cost & low heat economy

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Mass Transfer
Diffusion co-efficient generally depends upon the temperature, pressure & the nature of the components of the system. Its dimension is not the same as that of the

Thermal diffusivity
Kinematic viscosity
Volumetric diffusivity
Mass transfer co-efficient

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Mass Transfer
In rectifying section of a continuous distillation column, the

Vapour is enriched with high boilers
Liquid is stripped of high boilers
None of these
Vapour is enriched with low boilers

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Mass Transfer
Unsaturated air (with dry bulb and wet bulb temperatures being 45°C and 25°C respectively) is passed through a water spray chamber maintained at 23°C. The air will be cooled and

Dehumidified
Humidified at constant wet bulb temperature
None of these
Humidified with wet bulb temperature decreasing

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