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Mass Transfer

Mass Transfer
The-relative volatility for separation of a non-ideal binary mixture by distillation should be

< 1
1
> 1

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Mass Transfer
When both the fluids flow concurrently in an absorber, the slope of the operating line is

+ ve
- ve
-1
1

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Mass Transfer
In a forced draft cooling tower, water is cooled from 95 to 80°F by exposure to air with a wet bulb temperature of 70°F. In this case, the

Neither A nor B
Approach is 10°F
Both A & B
Range is 15°F

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Mass Transfer
McCabe-Thiele method of binary distillation does not assume that the

Molar latent heats of all components are equal
Sensible heat changes are negligible compared with latent heat changes
None of these
Heat of mixing is negligible

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Mass Transfer
Azeotropism for ethyl alcohol-water system disappears by

Increasing temperature
Increasing pressure
No means
Decreasing pressure

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Mass Transfer
The adiabatic saturation curve for a vapour-gas mixture is

None of these
Slightly concave upward
Straight line
Slightly concave downward

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