Activity Coefficient Calculator

Calculate Solution Non-Ideality

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Margules Equation Calculator

The Margules equation is a simple model for calculating activity coefficients in binary mixtures. It works well for similar-sized molecules with moderate non-ideality. The equation uses two interaction parameters (A₁₂ and A₂₁) that represent the energy differences between like and unlike molecular interactions.

γ₁: -
γ₂: -

Wilson Equation Calculator

The Wilson equation is more advanced than Margules and better suited for polar compounds and associating mixtures. It's based on the local composition concept, which accounts for molecular interactions more realistically. The λ parameters represent energy differences between molecular interactions, making this model effective for a wider range of mixtures.

γ₁: -
γ₂: -

Excess Properties Calculator

Excess properties measure the deviation from ideal behavior in mixtures. The excess Gibbs energy (GE) is particularly important as it relates directly to activity coefficients. This calculator determines GE from known activity coefficients, providing insight into the thermodynamic non-ideality of your solution.

Excess Gibbs Energy: - J/mol

Understanding Activity Coefficients

What are Activity Coefficients?

Activity coefficients (γ) measure how much a solution deviates from ideal behavior:

  • Definition: The ratio of effective concentration (activity) to actual concentration
  • Ideal solutions: γ = 1 for all components at all concentrations
  • Positive deviation: γ > 1 indicates weaker interactions between different molecules than like molecules
  • Negative deviation: γ < 1 indicates stronger interactions between different molecules than like molecules
  • Mathematical expression: ai = γi × xi where ai is activity and xi is mole fraction

Margules Equation

The Margules model is one of the simplest activity coefficient models:

  • Binary mixtures: Works for systems with two components
  • Similar sized molecules: Best for components with comparable molecular volumes
  • Moderate non-ideality: Suitable for systems with modest deviations from Raoult's law
  • Parameters: A12 and A21 represent interaction energies between molecules
  • Symmetrical case: When A12 = A21, the equation simplifies considerably
  • Limitations: Not suitable for highly non-ideal systems or systems with strong specific interactions

Wilson Equation

The Wilson equation offers several advantages for modeling non-ideal solutions:

  • Local composition concept: Accounts for non-random mixing of molecules
  • Polar compounds: Effectively models systems with hydrogen bonding and polar interactions
  • Temperature dependence: Parameters have clear temperature relationships based on molecular interactions
  • Wide applicability: Works well for many liquid mixtures across the entire composition range
  • Parameters: λ1211 and λ2122 represent differences in interaction energies
  • Limitation: Cannot predict liquid-liquid phase splitting

Applications

Activity coefficients are crucial in many chemical engineering applications:

  • Vapor-liquid equilibrium (VLE): Designing distillation columns and evaporators
  • Liquid-liquid extraction: Predicting phase behavior and separation efficiency
  • Chemical equilibrium: Calculating equilibrium constants for reactions in non-ideal solutions
  • Process design: Optimizing operating conditions for chemical processes
  • Azeotrope prediction: Identifying compositions where vapor and liquid have identical compositions
  • Solubility calculations: Predicting the solubility of solids and gases in liquid mixtures

Excess Properties

Excess properties quantify the thermodynamic deviation from ideal mixing:

  • Excess Gibbs energy (GE): The additional free energy due to non-ideal mixing
  • Relationship to activity: GE = RT(x1ln γ1 + x2ln γ2)
  • Excess enthalpy (HE): Heat released or absorbed during mixing beyond ideal behavior
  • Excess entropy (SE): Deviation from ideal entropy of mixing
  • Excess volume (VE): Volume change upon mixing compared to ideal mixing
  • Sign significance: Positive excess properties indicate unfavorable interactions, negative indicate favorable ones

Other Activity Models

Beyond Margules and Wilson, several other models are commonly used:

  • NRTL (Non-Random Two-Liquid): Good for highly non-ideal systems and partially miscible liquids
  • UNIQUAC (UNIversal QUAsi-Chemical): Combines combinatorial and residual contributions
  • UNIFAC: Group contribution method for predicting activity when no experimental data exists
  • Regular Solution Theory: Based on solubility parameters and cohesive energy densities
  • Flory-Huggins: Specifically designed for polymer solutions
  • Electrolyte models: Special models for ionic solutions (e.g., Debye-Hückel, Pitzer)

Essential Activity Coefficient Formulas

Margules Equation

ln γ₁ = x₂²[A₁₂ + 2(A₂₁-A₁₂)x₁]

ln γ₂ = x₁²[A₂₁ + 2(A₁₂-A₂₁)x₂]

Where x₁ and x₂ are mole fractions, A₁₂ and A₂₁ are interaction parameters

Wilson Equation

ln γ₁ = -ln(x₁ + Λ₁₂x₂) + x₂(Λ₁₂/(x₁ + Λ₁₂x₂) - Λ₂₁/(Λ₂₁x₁ + x₂))

Λ₁₂ = exp(-λ₁₂)

Where Λ values are related to molecular interaction energies

Excess Gibbs Energy

GE = RT(x₁ln γ₁ + x₂ln γ₂)

R is the gas constant (8.314 J/mol·K) and T is absolute temperature

Activity Definition

a₁ = γ₁·x₁

a₂ = γ₂·x₂

Activity (a) is the product of activity coefficient (γ) and mole fraction (x)