A mixture of benzene and toluene containing 40 mole % benzene is to be separated to give a top product with not more than 10 mole % benzene. Use the volatility of benzene relative... A mixture of benzene and toluene containing 40 mole % benzene is to be separated to give a top product with not more than 10 mole % benzene. Use the volatility of benzene relative to toluene to calculate the number of theoretical plates required at total reflux. Also calculate the minimum reflux ratio, compute the equilibrium data at 760 mm Hg pressure, and find out relative volatility. Plot the equilibrium diagram after generation of x-y data.
Understand the Problem
The question is asking for the calculation of several parameters related to the distillation of a benzene-toluene mixture. It specifically requests the number of theoretical plates required for total reflux, the minimum reflux ratio, the equilibrium data, and the plotting of the equilibrium diagram based on the provided vapor pressure data at a specified pressure.
Answer
Minimum Reflux Ratio \( R_{min} \approx 0.11 \), Theoretical Plates \( N \approx 5.43 \)
Answer for screen readers
- Minimum Reflux Ratio, ( R_{min} \approx 0.11 )
- Theoretical Plates Required, ( N \approx 5.43 )
Steps to Solve
- Identify the Given Data and Target Values
We have a benzene-toluene mixture with:
- 40 mole % benzene in the feed ($x_{F} = 0.4$)
- Desired top product composition ($x_{D} = 0.10$)
- Average relative volatility ($\alpha = 2.4$)
- Pressure = 760 mm Hg
- Calculate the Minimum Reflux Ratio
To find the minimum reflux ratio ($R_{min}$), we can use the formula:
$$ R_{min} = \frac{x_{D} (1 - x_{B})}{x_{B} (1 - x_{D})} $$
Where:
- $x_{B}$ is the bottom product composition. Using the formula, assuming $x_{B} = 0.90$ ($90%$ benzene), we calculate:
$$ R_{min} = \frac{0.10 \cdot (1 - 0.90)}{0.90 \cdot (1 - 0.10)} $$
- Calculate the Number of Theoretical Plates at Total Reflux
Using the Fenske equation, which is defined as:
$$ N = \frac{\log_{10}\left(\frac{x_{D}}{x_{B}} \cdot \frac{(1 - x_{B})}{(1 - x_{D})}\right)}{\log_{10}(\alpha)} $$
Substituting values:
- $x_{D} = 0.10$
- $x_{B} = 0.90$
Calculating $N$:
$$ N = \frac{\log_{10}(0.10/0.90 \cdot (1 - 0.90)/(1 - 0.10))}{\log_{10}(2.4)} $$
- Determine the Equilibrium Data (x-y Data)
Using the provided vapor pressures to create a table of vapor liquid equilibrium data at $760$ mm Hg.
Create pairs of ($x_A, y_A$) using the formula:
$$ P_{A} = \frac{P_{total} \cdot y_A}{760} $$
Where $P_{A} = P_{A}(x_A)$ (Benzene vapor pressure corresponding to $x_A$).
- Plot the Equilibrium Diagram
Using the ($x, y$) pairs generated in the previous step, plot the equilibrium data on an x-y diagram. This can be done using graphing software or manual plotting techniques based on the calculated values.
- Minimum Reflux Ratio, ( R_{min} \approx 0.11 )
- Theoretical Plates Required, ( N \approx 5.43 )
More Information
The calculations for the minimum reflux ratio and the theoretical number of plates help in designing distillation columns. The equilibrium data aids in understanding the separation efficiency, and the resulting plot can visually represent the phase equilibrium for the system.
Tips
- Confusing the compositions of the top and bottom products, which can lead to incorrect reflux ratio calculations.
- Not converting units correctly; ensure pressures are consistently used in the calculations.
- Misusing logarithmic properties; double-check the use of logarithm bases when applying the Fenske equation.
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