Calc.  SED & PREDOM / Ionic Strengt

Comparisons between calculated and measured mean ionic activity coeficients at 25°C

Note that for an unsymmetric electrolyte Xνx Yνy the mean activity coefficient is:

γ ± ν = γ X νx γ Y νy

(where ν = νx + νy). For example, for CaCl2: γ±3 = γCa γCl2, or log γ± = (log γCa + 2 log γCl) / 3.


Moderate concentrations

Measured mean activity coefficients (γ±) at 25°C compared with results obtained using the Davies eqn., the simplified HKF model, and the SIT model. The three models reproduce fairly well the data for concentrations ≤ 0.1 molal (ionic strengths ≤ 0.3 molal for 1:2 or 2:1 electrolytes); for 1:1 electrolytes perhaps even up to ≈ 0.2 molal.

 

1:1 electrolytes: NaCl, HCl and AgNO3

log_gamma_1:1

1:2 and 2:1 electrolytes: CaCl2 and Na2SO4

log_gamma_1:2


Higher Concentrations

Measured mean activity coefficients (γ±) at 25°C compared with results obtained using the Davies eqn., the simplified HKF model, and the SIT model:

 

1:1 electrolytes: NaCl, HCl and AgNO3

log_gamma_1-1 high conc.

1:2 and 2:1 electrolytes: CaCl2 and Na2SO4

log_gamma_1-2 high conc.


Conclusions

The Davies eqn. should only be used at concentrations ≤ 0.1 molal for most electrolytes.

The HKF model uses a specific electrolyte paramater (bγ,MX) to fit experimental data over a wide range of temperatures and concentrations. In Spana this model is simplified by setting the b-parameter to the value for NaCl at the temperature of interest. It is therefore not surprising that the model fits so well the NaCl. This model should be adequate for most electrolytes at concentrations ≤ 0.2 molal over a wide range of temperatures.

The SIT model uses specific ion-interaction paramaters (ε) chosen to fit experimental data 25°C. It is therefore not surprising that the SIT model fits the data so well. The temperature dependence of the (ε) parameters is in general not known, and the SIT model should not be used at temperatures ≠ 25°C.


The experimental γ± data show in the figures may be found in the appendices of:

R.A. Robinson and R.H. Stokes (1970) Electrolyte Solutions, 2nd edn., London: Butterworth & Co., 571 pp. (reprinted in 2002 by Dover Publications, Inc., USA).


back  Models for activity coefficients