Donnan Equilibrium
membrane_toolkit.core.donnan.donnan_equilibrium(C_bulk, C_fix, z_counter=1, z_co=-1, nu_counter=1, nu_co=1, z_fix=-1, gamma=1)
¶
Calculate the Donnan equilibrium at the interface between Phase1 and Phase2.
Parameters:
Name | Type | Description | Default |
---|---|---|---|
C_bulk |
float |
bulk salt concentration [mol/L] |
required |
C_fix |
float |
fixed charge concentration, without sign [mol/L] |
required |
z_counter |
int |
signed charge of the counter-ion. Default = +1 [dimensionless] |
1 |
z_co |
int |
signed charge of the co-ion. By definition, this must have the same sign as the co-ion. Default = -1 [dimensionless] |
-1 |
nu_counter |
int |
stoichiometric coefficient of the counter-ion. Default = 1 [dimensionless] |
1 |
nu_co |
int |
stoichiometric coefficient of the co-ion. Default = 1 [dimensionless] |
1 |
z_fix |
int |
signed charge of the fixed groups. Default = -1 [dimensionless] |
-1 |
gamma |
float |
stoichiometrically-weighted ratio of salt activity coefficient in solution to that in the membrane Default = 1 [dimensionless]. |
1 |
Returns:
Type | Description |
---|---|
float |
The co-ion concentration in the membrane [mol/L]. Note that for salts containing one or more multivalent ions, this is not the same as the mobile salt concentration. |
Exceptions:
Type | Description |
---|---|
AssertionError |
If the input stoichiometry is incorrect. Both must be positive, and must have opposite signs, and + must equal zero. |
Notes
The Donnan equilibrium between a membrane with fixed charged concentration (mol per L water sorbed) and a salt solution of bulk concentration (mol/L) is given by:
where subscripts and indicate the co-ion (same charge as the membrane) and counter-ion (opposite charge to the membrane), (dimensionless) are stoichiometric coefficients, and overbars indicate membrane-phase quantities, in units of moles per liter of water sorbed by the membrane. (dimensionless) is the ratio of activity coefficients in the bulk solution to those in the membrane, given by:
Traditionally, is either set to 1 (implying that ion activity coefficients are the same in the membrane and in bulk solution), or the ions are assumed to behave ideally in the membrane (activity coefficient in the membrane equal to 1), in which case $\Gamma$ equals the bulk solution activity coefficient. More recently, Manning theory has been used to compute the membrane-phase activity coefficients, making possible a direct calculation of .
References
Donnan, F. G. The theory of membrane equilibria. Chem. Rev. 1924, 1 (1), 73–90.
Kamcev, J.; Galizia, M.; Benedetti, F. M.; Jang, E.-S.; Paul, D. R.; Freeman, B.; Manning, G. S. Partitioning of Mobile Ions Between Ion Exchange Polymers and Aqueous Salt Solutions: Importance of Counter-ion Condensation. Phys. Chem. Chem. Phys. 2016, No. 8, 6021–6031.
Galizia, M.; Manning, G. S.; Paul, D. R.; Freeman, B. D. Ion partitioning between brines and ion exchange polymers. Polymer (Guildf). 2019, 165 (January), 91–100.
Kingsbury, R. S.; Coronell, O. Modelling and validation of concentration dependence of ion exchange membrane permselectivity: significance of convection and Manning’s counter-ion condensation theory. Submitted.
Source code in membrane_toolkit/core/donnan.py
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