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Data 1

x

y

Composition Expressed in :

Enter values of x and y for equilibrium curve in descending order. Mass ratewhen of Feed, F (These values will beflow used only the value of α inMol. the table besidesvolatile is zero)comp.) wt(more

Molal Units 0.9

1,000.0 32

Mol mass (less volatile comp.)

18

Feed composition, X F

0.5

Top Product composition, X D

0.9

Bottom Product composition, X B

0.1

q value

Reflux Ratio,

1

R

Relative Volatility, α

0.35 4.336

Result No. of theoritical plates

#NAME?

Minimum Reflux Ratio

#NAME?

Intercept of top op. line on y-axis

0.667

Mass flow rater of Top Product, D

612.1

Mass flow rate of Bottom Product, B Feed Plate from top Slope of Top Operating Line Slope of Bottom Operating Line

387.9 #NAME? 0.259, 14.5˚ #NAME?

Mole fraction of more volatile component in vapor phase, y

Equilibrium Diagram

0.8

### 0.7

###

0.6

Molal Units 0.5

Mass Units

0.4

Mass Units 0.3

### ###

0.2

###

0.1

0 0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

Afraction Program byvolatile Sharad Vermain liquid phase, x Mole of more component

0.8

0.9

1