Physics, asked by prakasam9667, 1 year ago

How to calculate relative volatility for multicomponent?

Answers

Answered by putulshaw1978
0

Multicomponent Distillation

 need more than one distillation tower, for

n

components, n-1 fractionators are required

 Specification Limitations

The following are established at the beginning

1. Temperature, pressure, composition, and rate of

the feed.

2. Pressure of the distillation

3. Feed to be introduced on that tray which will

result in the least total number of trays

(optimum feed-tray location)

4. Heat loses (even if assumed to be zero)

Under these circumstances only three additional items of

the following list need to be specified, any other items

must be calculated.

1. Total number of trays.

2. Reflux ratio

3. Reboil ratio (ratio of vapor produced by the

reboiler to residue withdrawn)

4. Concentration of one component in one product

(a maximum of two may be chosen)

5. Ratio of flow of one component in the distillate

to the flow of the same component in the

residue, or split of the component (a maximum

of two may be chosen)

6. Ratio of total distillate to total residue

109

 Key components

The feed components are listed in order of their relative

volatility. The more volatile components are called

light, the less volatile are heavy. The components

separated in a tower are called light key (more volatile)

and heavy key (less volatile). Any components lighter

than the light key are called light components, while

those heavier than the heavy key are called heavy

components.

In hydrocarbon systems, because of nonidealities, the

equilibrium data are often represented by

y

A = KA

x

A, y

B= K

B

x

B, y

C = K

C

x

C, y

D = K

D

x

D

where KA is the vapor-liquid equilibrium constant or

distribution coefficient for component A. K is a function

of temperature and pressure, but is assumed to be

independent of composition, which is sufficiently

accurate for most engineering calculations. For an ideal

system, K

A = P

A*/P

T = vapor pressure/total pressure.

The relative volatility in multicomponent distillation is

always computed with respect to the heavy key

 j

j

hk

je je

hke hke

K

K

y

x

y x

  /

/ (1)

The value of

 is greater than 1 for any component

lighter than the heavy key and less than 1 for any heavier

component

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