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

Kinematic viscosity
Volumetric diffusivity
Mass transfer co-efficient
Thermal diffusivity

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Mass Transfer
Inside the distillation column, the

None of these
Liquids are not always at their bubble points
Driving force for the vapour flow is the pressure drop
Pressure increases gradually from bottom to the top of the column

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Mass Transfer
In case of steam distillation, the steam leaving the liquid is not completely saturated with distillate vapour, because

Temperature is less
Mixing of steam with the material being vaporised is not so intimate as to result in equilibrium condition
Saturated steam is used for steam distillation
Total pressure is less

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Mass Transfer
Blowdown in a cooling tower

Increases the scale forming tendencies of water
Means discarding a small fraction of circulating water to prevent and limit the concentration of salt and impurities
All of these
Is undesirable

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