What Are Some Empirical Models for Calculating Activity Coefficients?

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SUMMARY

This discussion focuses on empirical models for calculating activity coefficients in non-ideal liquid mixtures, specifically highlighting the Van Laar, Porter, Margules, and Wilson equations. Each model provides a formula for calculating the excess Gibbs energy (G^E) and the corresponding activity coefficients (γ_i) for binary solutions, with some models extendable to multi-component systems. The discussion emphasizes the mathematical relationships involved in these models, particularly the dependence on mole fractions (x_i) and constants (A, B, A', B'). Future additions may include the NRTL and UNIQUAC models.

PREREQUISITES
  • Understanding of excess Gibbs energy and its significance in thermodynamics
  • Familiarity with mole fractions and their role in solution chemistry
  • Basic knowledge of activity coefficients and their calculation
  • Proficiency in mathematical differentiation and logarithmic functions
NEXT STEPS
  • Research the NRTL equation for activity coefficient calculations
  • Explore the UNIQUAC model for non-ideal liquid mixtures
  • Study the application of these models in multi-component systems
  • Examine the impact of temperature and pressure on activity coefficients
USEFUL FOR

Chemical engineers, physical chemists, and researchers involved in thermodynamic modeling of liquid mixtures will benefit from this discussion.

siddharth
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These are some empirical excess Gibbs energy models used to calculate activity coefficients for non-ideal liquid mixtures. I didn't find many on the web, so I thought I'll put them here for future reference

All x_i refer to the mole fraction of the ith species in the solution.
To calculate the activity coefficient \gamma_i from the excess free energy, we have
ln \gamma_i=\left(\frac{\partial\left(nG^{E}/RT\right)}{\partial n_i} \right)_{P,T,n_j}

Most of these are for binary solutions, but some can be extended into multi-component systems.

1) Van Laar equation

\frac{G^{E}}{RT} = \frac{ABx_1x_2}{Ax_1+B_x_2}

So that,

ln \gamma_1 = A\left(1+\frac{Ax_1}{Bx_2}\right)^{-2}

ln \gamma_2 = B\left(1+\frac{Bx_2}{Ax_1}\right)^{-2}

2) Porters equation

\frac{G^{E}}{RT}=Ax_1x_2

So that,

ln \gamma_1 = Ax_2^2

ln \gamma_2= Ax_1^2

3) Margules equation

\frac{G^{E}}{RT}=x_1x_2\left(Ax_1+Bx_2\right)

So that,

ln \gamma_1 = x_2^2\left(A+2\left(B-A\right)x_1\right)

ln \gamma_2 = x_1^2\left(B+2\left(A-B\right)x_2\right)

4) Wilsons equation (*local composition model*)

\frac{G^{E}}{RT}=-x_1ln \left(x_1+A'x_2\right) - x_2ln \left(x_2 + B'x_1\right)

So that,

ln \gamma_1=-ln(x1+A'x_2) + x2 \left(\frac{A'}{x_1+A'x_2} - \frac{B'}{x_2+B'x_1}\right)

ln \gamma_2 = -ln(x2+B'x_1) - x1 \left(\frac{A'}{x_1+A'x_2} - \frac{B'}{x_2+B'x_1}\right)

I'll add the NRTL equation and maybe the UNIQUAC model later. Feel free to correct me if you spot any errors.
 
Last edited:
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This is a nice summery.
 

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