Original UNIFAC: Difference between revisions
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<math> V_i = \frac{r_i}{\sum_j r_j x_j} </math> | <math> V_i = \frac{r_i}{\sum_j r_j x_j} </math> | ||
Surface area/mole fraction ratio for component i (j: component index) in the mixture: | |||
<math> F_i = \frac{q_i}{\sum_j q_j x_j} </math> | <math> F_i = \frac{q_i}{\sum_j q_j x_j} </math> | ||
Revision as of 14:19, 5 August 2016
The Original UNIFAC model consists of the following equations[1]:
<math> ln \gamma_i = ln \gamma_i^C + ln \gamma_i^R</math>
<math> ln \gamma_i^C = 1 - V_i + ln V_i - 5 q_i(1 - \frac{V_i}{F_i} + ln \frac{V_i}{F_i}) </math>
Volume/mole fraction ratio for component i (j: component index) in the mixture:
<math> V_i = \frac{r_i}{\sum_j r_j x_j} </math>
Surface area/mole fraction ratio for component i (j: component index) in the mixture:
<math> F_i = \frac{q_i}{\sum_j q_j x_j} </math>
Molecular volume parameter for component i (k: subgroup index) [2]:
<math> r_i = \sum_k \nu_k^{(i)} R_k </math>
Molecular surface area parameter for component i (k: subgroup index):
<math> q_i = \sum_k \nu_k^{(i)} Q_k </math>
<math> ln \gamma_i^R = \sum_i \nu_k^{(i)} (ln \Gamma_k - ln \Gamma^{(i)}_k ) </math>
<math> ln \Gamma_k = Q_k [ 1 - ln (\sum_m \Theta_m \Psi_{mk}) - \sum_m \frac{\Theta_m \Psi_{km}}{\sum_n \Theta_n \Psi_{nm}}] </math>
<math> \Theta_m = \frac{Q_m X_m}{\sum_n Q_n X_n} </math>
<math> X_m = \frac{\sum_j \nu_m^{(j)} x_j}{\sum_j \sum_n \nu_n^{(j)} x_j} </math>
<math> \Psi_{nm} = exp(- { {a_{nm} } \over {T} }) </math>
References
- ↑ Gmehling, Kolbe, Kleiber, Rarey; Chemical Thermodynamics for Process Simulation; February 2012; Wiley ISBN 9783527312771
- ↑ Larsen, Rasmussen, Fredenslund; A Modified UNIFAC Group-Contribution Model for Prediction of Phase Equilibria and Heats of Mixing; Ind. Eng. Chem. Res. 1987, 26 2274-2286 doi:10.1021/ie00071a018