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Extractive Distillation Solvent Relative Volatility Calculator

Close-boiling mixtures and azeotropes cannot be separated by conventional distillation because their relative volatility approaches 1.0.

Pure saturation vapor pressure of light component.

Pure saturation vapor pressure of heavy component.

Liquid activity coefficient with entrainer present.

Liquid activity coefficient with entrainer present.

Calculated Result
1.850

Relative Volatility (alpha)

Ideal Relative Volatility

1.050

Entrainer Enhancement

1.76x

Azeotrope Broken?

Yes (alpha != 1.0)

Calculation Breakdown

  1. Ideal Relative Volatility (alpha_ideal)P1_sat / P2_sat = 1.050
  2. Modified Relative Volatility with Entrainer (alpha_12)(γ1 · P1_sat) / (γ2 · P2_sat) = (1.85·101.3) / (1.05·96.5) = 1.850
  3. Azeotrope Separation StatusAzeotrope Broken: Clean distillation separation achievable

What Is the Extractive Distillation Solvent Relative Volatility Calculator?

Extractive distillation introduces a miscible, high-boiling solvent that selectively alters component activity coefficients to widen relative volatility.

How Does the Extractive Distillation Solvent Relative Volatility Calculator Work?

Evaluates modified volatility alpha_12 = (gamma1 * P1_sat) / (gamma2 * P2_sat); values significantly above 1.2 allow practical fractionation.

Extractive Distillation Solvent Relative Volatility Calculator Formula & Variables

The core mathematical equation utilized by this calculator is expressed as:

alpha_{12} = rac{gamma_1 P_1^{ ext{sat}}}{gamma_2 P_2^{ ext{sat}}}, quad alpha_{ ext{ideal}} = rac{P_1^{ ext{sat}}}{P_2^{ ext{sat}}}

Modified relative volatility in non-ideal extractive distillation systems.

How to Use the Extractive Distillation Solvent Relative Volatility Calculator

  1. Input pure saturation vapor pressures in kPa and liquid-phase activity coefficients gamma in the presence of the solvent.

Step-by-Step Example Calculation

Ethanol-Water Azeotrope Breaking with Ethylene Glycol

Input Values:

vaporPressure1Kpa:101.3
vaporPressure2Kpa:96.5
activityCoeff1:1.85
activityCoeff2:1.05
Worked Steps: Ideal volatility = 1.05 (Azeotropic pinch), Modified volatility = 1.85 (Azeotrope broken, clean separation feasible).

Understanding Your Result

Shows modified relative volatility, ideal baseline volatility, solvent enhancement ratio, and whether the azeotrope is successfully broken.

Factors That Affect the Result

  • Solvent-to-feed ratio and polar/hydrogen-bonding interactions govern activity coefficient selectivity.

When Should You Use This Calculator?

  • Separating ethanol-water, cyclohexane-benzene, and close-boiling alkane-alkene petrochemical cuts.

Assumptions & Limitations

  • Assumes ideal gas vapor phase under low-to-moderate operating pressures.

Frequently Asked Questions

Calculation Accuracy & Reference Note

Standard chemical thermodynamics VLE formulation.

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