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Chemical Engineering · all questions

Mass Transfer
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Which of the following processes is not an example of adsorption applied to gaseous separations?

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If f is defined as above, then which of the following applies to a feed at dew point?

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Design calculation for multiple component distillation is done by

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Cox chart, which is useful in the design of distillation column particularly for petroleum hydrocarbons, is a plot of (where, P = vapor pressure, T = temperature)

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In batch distillation with constant reflux, overhead product composition __________ with time.

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Back-trapping in a distillation column

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Agitator is provided in a crystalliser for

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Chemisorption (chemical adsorption) is

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Desirable value of absorption factor in an absorber is

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Bound moisture is that liquid which exerts an equilibrium vapor pressure __________ that of the pure liquid at the given temperature.

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A coalescer in a mixer-settler liquid-liquid extraction coloumn

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Tower diameter may be decreased by

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In a moderately sized packed absorption tower, channeling (which is most severe with stacked packings) can be minimised by taking the ratio of tower diameter to packing diameter

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Flash distillation is suitable for the separation of components

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Make up water is required in a cooling tower to replace the water lost by

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In an absorber, HETP does not vary with the

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Use of natural draft cooling tower is practised, when the air has low

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Raoult's law applies to the

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The difference of wet bulb temperature and adiabatic saturation temperature of unsaturated mixture of any system is

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Which of the following can be calculated theoretically using steam table and Dalton's law of partial pressure; if the relative humidity and dry bulb temperature of moist air is known?

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