All Exams Test series for 1 year @ ₹349 only
Question

The vapor-liquid equilibrium curve of a binary mixture A-B, may be approximated by a linear equation over a narrow range of liquid mole fractions ($0.2 < x_A < 0.3$) as follows $$y_A^* = 1.325x_A + 0.121$$ Here $y_A^*$ is the mole fraction of A in the vapor. $100 \text{ moles}$ of a feed ($x_{A,F} = 0.28$) is batch distilled to a final residue ($x_{A,W} = 0.2$). Using the Rayleigh equation, the number of moles of the residue left behind in the distillation unit, up to 2 digits after the decimal point, is _________________

Rayleigh Equation for Batch Distillation

The Rayleigh equation is used to calculate the composition and amount of liquid remaining in a batch distillation process. It is expressed as:

$ \ln \left( \frac{W}{F} \right) = \int_{x_F}^{x_W} \frac{dx_A}{y_A^* - x_A} $

Where:

  • $F$ is the initial moles of the feed.
  • $W$ is the final moles of the residue.
  • $x_F$ is the mole fraction of component A in the feed.
  • $x_W$ is the mole fraction of component A in the residue.
  • $y_A^*$ is the mole fraction of component A in the vapor in equilibrium with the liquid of composition $x_A$.

Batch Distillation Parameters

The problem provides the following information:

  • Initial feed moles, $F = 100 \text{ moles}$.
  • Feed composition, $x_{A,F} = 0.28$.
  • Final residue composition, $x_{A,W} = 0.2$.
  • Linear vapor-liquid equilibrium (VLE) approximation: $y_A^* = 1.325x_A + 0.121$.

First, we determine the term $(y_A^* - x_A)$ from the given VLE equation:

$ y_A^* - x_A = (1.325x_A + 0.121) - x_A = 0.325x_A + 0.121 $

Integral Calculation

Substitute this expression into the Rayleigh equation integral:

$ \ln \left( \frac{W}{F} \right) = \int_{0.28}^{0.2} \frac{dx_A}{0.325x_A + 0.121} $

To solve this integral, we use the substitution $u = 0.325x_A + 0.121$. Differentiating gives $du = 0.325 dx_A$, which implies $dx_A = \frac{du}{0.325}$.

The integral transforms to:

$ \int \frac{1}{u} \frac{du}{0.325} = \frac{1}{0.325} \int \frac{du}{u} = \frac{1}{0.325} \ln|u| $

Substituting back for $u$, the antiderivative is $\frac{1}{0.325} \ln(0.325x_A + 0.121)$. Since $0.325x_A + 0.121$ is positive for the given range of $x_A$, the absolute value is not needed.

Now, evaluate the definite integral using the limits $x_F = 0.28$ and $x_W = 0.2$:

$ \left[ \frac{1}{0.325} \ln(0.325x_A + 0.121) \right]_{0.28}^{0.2} $

$ = \frac{1}{0.325} \left[ \ln(0.325 \times 0.2 + 0.121) - \ln(0.325 \times 0.28 + 0.121) \right] $

$ = \frac{1}{0.325} \left[ \ln(0.065 + 0.121) - \ln(0.091 + 0.121) \right] $

$ = \frac{1}{0.325} \left[ \ln(0.186) - \ln(0.212) \right] $

$ = \frac{1}{0.325} \ln \left( \frac{0.186}{0.212} \right) $

$ \approx \frac{1}{0.325} \ln(0.877358) \approx \frac{1}{0.325} (-0.13083) \approx -0.40255 $

Calculate Final Residue Moles

The result of the integral gives $\ln \left( \frac{W}{F} \right) \approx -0.40255$.

To find the ratio $W/F$, we take the exponential of this value:

$ \frac{W}{F} = e^{-0.40255} \approx 0.66853 $

Given the initial feed $F = 100$ moles, we can now calculate the final residue moles $W$:

$ W = F \times 0.66853 = 100 \times 0.66853 \approx 66.853 \text{ moles} $

Rounding the result to two decimal places, the number of moles of residue left behind is $66.85$.

Was this answer helpful?

Important Questions from Distillation

  1. A binary mixture of butane and butadiene is to be separated in an extractive distillation using furfural. Furfural lowers the activity of butadiene more than it does for butane. Consider the distillation sequence shown in the figure.


    Match the component labels in Group I with chemical species in Group II.
     

    Group IGroup II
    P. Component X1. Butane
    Q. Component Y2. Butadiene
    R. Component Z3. Furfural
  2. A continuous distillation column is used to separate an equimolar mixture of diethylamine (DEA) and methanol. The feed enters the column as saturated liquid at a flow rate of $30 \text{ mol s}^{-1}$. It is desired to obtain $92 \text{ mol}\%$ DEA as distillate. The rate of withdrawal of the distillate from the column is $10 \text{ mol s}^{-1}$. The equilibrium curve for the conditions in the column is given below. The latent heat of vaporization of the reboiler contents is $35 \text{ kJ mol}^{-1}$. Neglect heat loss to the surroundings and assume constant molal overflow. Which one of the following is the minimum reboiler heat duty (in kW)?

  3. A binary AB liquid mixture containing 30 mol% A is subjected to differential (Rayleigh) distillation at atmospheric pressure in order to recover 60 mol% A in the distillate. Assuming a constant relative volatility $ \alpha_{AB} = 2.2 $, the average composition of the collected distillate is _______ mol% A (rounded off to nearest integer).
  4. Identify the WRONG statement amongst the following:
  5. A binary feed consisting of $25$ mol% liquid and $75$ mol% vapour is separated in a staged distillation column. The mole fraction of the more volatile component in the distillate product is $0.95$. The molar flow rate of distillate is $50$% of the feed flow rate and the McCabe-Thiele method can be used to analyze the column. The q-line intersects the operating line of the enriching section at $(0.35, 0.5)$ on the x-y diagram. The slope of the stripping section operating line (up to one decimal place) is ____________

Need Expert Advice?

Start Your Preparation with Prepp Mobile App

Download the app from Google Play & App Store
Download the app from Google Play & App Store
Prepp Mobile App