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