0% found this document useful (0 votes)
75 views5 pages

Observation and Calculatons:: A) Specific Gravity Calculations

The document provides calculations to determine the composition of products from a distillation column separating a 98% ethanol/water mixture. Specific calculations include: - Determining the relative error in the given specific gravity value compared to literature. - Performing a mass balance on the column to determine compositions of distillate and bottoms products, which are 60.75% and 39.24% ethanol, respectively. - Using the Lewis-Sorel method to calculate the operating lines for the top and bottom plates and determine the number of plates needed is 3 based on the compositions. - Calculating the plate efficiency of the column as 58.82% based on inlet and outlet compositions and number of transfer

Uploaded by

Mian Gulshad
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as DOCX, PDF, TXT or read online on Scribd
0% found this document useful (0 votes)
75 views5 pages

Observation and Calculatons:: A) Specific Gravity Calculations

The document provides calculations to determine the composition of products from a distillation column separating a 98% ethanol/water mixture. Specific calculations include: - Determining the relative error in the given specific gravity value compared to literature. - Performing a mass balance on the column to determine compositions of distillate and bottoms products, which are 60.75% and 39.24% ethanol, respectively. - Using the Lewis-Sorel method to calculate the operating lines for the top and bottom plates and determine the number of plates needed is 3 based on the compositions. - Calculating the plate efficiency of the column as 58.82% based on inlet and outlet compositions and number of transfer

Uploaded by

Mian Gulshad
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as DOCX, PDF, TXT or read online on Scribd
You are on page 1/ 5

Observation and Calculatons:

a)Specific Gravity Calculations


Specific Gravity = 1.1

Literature Value of 98%Ethanol at 25ᵒC = 0.79117

1.1−0.79117
Relative Error = ∗100
1.1

= 28.07%

Xf = 0.5

1.1−0.79
Now composition of water in top product = × 100=39.24 %
0.79

So ethanol in top product = 100-39.24 = 60.75%

This gives,

Xd = 0.61

Xw = 0.39

Mass Balance on Column


For 100 kmol of feed, an overall mass balance gives

100 = D + W

Balance on Ethanol gives,

100 x 0.5 = 0.61 D +0.39 W

50 = 0.61 (100 – W) + 0.39 W

50 = 61 – 0.61 W + 0.39 W

11 = 0.22 W

W = 50

100 = D + 50
D = 50

As by reference to example 11.7

Ln = 3D = 3 x 50 = 150

Vn = Ln + D = 150 + 50 = 200

Thus the top operating line from the equation 11.35

yn = 0.75 xn+1 + 0.1525

Since the feed is all liquid at boiling point, this will run down as increased flux to the plate
below.

Lm = Ln + F =150 +100 = 250

Vm = Lm – W =250 – 50 = 200

Using 11.37 equation for bottom plate

ym = 1.25 xm+1 – 0.0975

Part 2
Plates calculation;Graph b/w X&Y
1.2

1 1
0.89
vapour composition(Y)

0.8 0.82
0.8
0.75
0.7 0.7
0.66
0.6 0.62 0.6
0.58
0.53 0.5
0.4 0.43 0.4
0.3
0.2 0.2
0.1
0 0
0 0.2 0.4 0.6 0.8 1 1.2

Liquid Composition(X)

y x y

Lewis Sorel Method:

For top fraction

Top operating line

ln D
Yn = * Xn+1 + * Xd
Vn Vn

150 50
Yn = * Xn+1 + * 0.61
200 200

Yn = 0.75 Xn+1 + 0.1525

Bottom operating line

Lm = Ln + F

Lm = 150 + 100

Lm = 250

Vm = Lm – W

Vm = 250 – 50
Vm = 200

Now

Lm D
Ym = * Xm+1 - * Xw
Vm Vm

250 50
Ym = * Xm+1 – * 0.39
200 200

Ym = 1.25 Xm+1 – 0.0975

For calculation 0f composition and number of plates by lewis Sorel method

XD = yn = 0.61

See equilibrium curve for

Xm at Yn = 0.61

Xn = 0.388

Now

Yn = 0.75 Xn+1 + 0.1525

Yn-1 = 0.291 (0.388) + 0.1525

Yn-1 = 0.4435

Now at Yn-1 = 0.4435

X n-1 = 0.19

c)Plate Efficiency of the Column


The efficiency is given by

N OG
ϵ=
N OL

Where NOG and NOL are given by

y e− y n
N OG=ln ( )
y e− y n−1

x n+1−x e
N OL=ln ( )
x n−x e
Where ye and xe are calculated by

ye = mxn and xe = myn

ye = 0.2067 and xe = 0.3233

So putting values in their respective formulas,

0.2067−0.89
N OG=ln ( )=0.10
0.2067−0.82

0.89−0.3233
N OL=ln ( )=0.17
0.8−0.3233

0.10
ϵ= =0.5882 ×100=58.82%
0.17

You might also like