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1 Differential Distillation Rayleigh Equation ( ) i i i dx dL L y x ……… (1) Integrating: 1 1 ( ) i o io x L i i i L x dx dL L y x 1 1 ln ( ) i io x i o i i x dx L L y x ……… (2) Where: o L Initial amount of liquid in pot, , moles 1 L Remaining amount of liquid in pot, , moles dL Amount of liquid vaporized in time d , i i dx dy Change in concentration for time interval d Solution of the relation depends on the form of the equilibrium relationship: ( ) i i y fx a) When i i i y mx 1 1 1 1 1 ln ( ) ( ) ( 1) i i i io io io x x x i i i o i i i i i i i x x x dx dx dx L L y x mx x m x 1 1 1 ln ln ( 1) i o i io x L L m x ……… (3) Rewritten in another form: 1 1 1 1 i m i o io x L L x ……… (4) b) For i i i i y mx c 1 1 1 1 ln ( ) ( ) ( 1) i i i io io io x x x i i i o i i i i i i i i i x x x dx dx dx L L y x mx c x m x c 1 1 ( 1) 1 ln ln ( 1) ( 1) i i i o i i io i m x c L L m m x c ……… (5)

Differential distillation

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Page 1: Differential distillation

1

Differential Distillation

Rayleigh Equation

( )

i

i i

dxdL

L y x

……… (1) Integrating:

11

( )

i

o io

xL

i

i iL x

dxdL

L y x

1

1ln( )

i

io

x

i

o i ix

dxL

L y x

……… (2)

Where: oL Initial amount of liquid in pot, ,moles 1L Remaining amount of liquid in pot, ,moles dL Amount of liquid vaporized in time d ,i idx dy Change in concentration for time interval d Solution of the relation depends on the form of the equilibrium relationship: ( )i iy f x

a) When i i iy m x 1 1 1

1 1ln

( ) ( ) ( 1)

i i i

io io io

x x x

i i i

o i i i i i i ix x x

dx dx dxL

L y x m x x m x

11 1ln ln

( 1)

i

o i io

xL

L m x

……… (3)

Rewritten in another form: 1

111

imi

o io

xL

L x

……… (4)

b) For i i i iy m x c

1 1 1

1ln( ) ( ) ( 1)

i i i

io io io

x x x

i i i

o i i i i i i i i ix x x

dx dx dxL

L y x m x c x m x c

11 ( 1)1

ln ln( 1) ( 1)

i i i

o i i io i

m x cL

L m m x c

……… (5)

Page 2: Differential distillation

2

c) When the relative volatility ij is constant and the equilibrium expressed is as:

1 ( 1)

ij i

i

ij i

xy

x

1 1

1 1

1ln( )

( )1 ( 1)

(1 ( 1) ) (1 ( 1) )

( 1 ) ( 1)(1 )

i i

io io

i i

io io

x x

i i

ij io i ix xi

ij i i

x x

ij i i ij i i

i ij ij i i i ij ix x

L dx dx

xL y xx

x

x dx x dx

x x x x x

1 1 ( 1)

( 1)(1 ) ( 1)(1 )

i i

io io

x x

ij i ii

i ij i i ij ix x

x dxdx

x x x x

1 11

( 1) (1 ) (1 )

i i

io io

x x

i i

ij i i ix x

dx dx

x x x

The integration becomes:

11

1 1

1 11ln ln ln

( 1) 1 1

io i io

o ij i io i

x x xL

L x x x

1

1 1

1 11ln ( 1) ln

( 1) 1 1

io i ioij

ij i io i

x x x

x x x

1

1

11ln ln

( 1) 1

i ioij

ij io i

x x

x x

And finally:

1 11 11ln ln ln

( 1) 1

i iij

o ij io io

x xL

L x x

……… (6)

Page 3: Differential distillation

3

d) Graphical integration is applied when the equilibrium data ( , )i ix y is given in tabular

form:

For each equilibrium point ( , )i ix y the value 1

i iy x

is calculated:

1

i iy x

i iy x iy ix

- - - -

- - - -

- - - -

A plot of1

i iy x

versus[ ]ix is then made and the area under the curve between 1[ ]ix and

[ ]iox gives 1lno

L

L.