Correction for issue #3862
ComponentModifiedFurstElectrolyteEosMod2004.dFBorndN previously added
FBornD() directly to the mole derivative. FBornD() is a derivative with
respect to relative permittivity, not mole number, and scales with phase amount.
The resulting chemical potentials and fugacity coefficients changed when all
mole numbers and the phase volume were multiplied by the same factor.
The correction removes this unweighted term. It retains the 2004 variant’s existing convention of zero solvent-permittivity composition derivatives, consistent with its Born mixed derivatives. Public method signatures, ion diameters and fitted interaction parameters are unchanged. Calculated fugacity coefficients and flash results can change, especially for large phase amounts; the old dependence on the chosen amount basis was erroneous.
Dividing FBornD() by total moles would restore scaling but would still not be
the chain-rule derivative. It is therefore not the correction used here.
Derivation from the implemented free energy
For composition-independent ionic diameters, the Furst-based implementations use
\[F_B=\frac{A_B}{RT}=C(T)X_B\left(\frac{1}{\varepsilon_s}-1\right),\qquad C(T)=\frac{N_Ae^2}{4\pi\varepsilon_0RT},\qquad X_B=\sum_j\frac{n_jz_j^2}{d_j}.\]Here $n_j$ is the amount in mol, $d_j$ the diameter in m, $z_j$ the signed charge number, $T$ the temperature in K, $R$ the molar gas constant, $N_A$ Avogadro’s constant, $e$ the elementary charge and $\varepsilon_0$ the vacuum permittivity. $\varepsilon_s$ is the dimensionless solvent relative permittivity. The sum includes ions; neutral components have $z_j=0$. $F_B$ is extensive and has units of mol under this molar convention; its mole derivative is dimensionless.
Direct differentiation at fixed temperature, total volume and other amounts gives
\[\frac{\mu_i^B}{RT}=\frac{\partial F_B}{\partial n_i}=C(T)\left[\left(\frac{1}{\varepsilon_s}-1\right)\frac{z_i^2}{d_i}-\frac{X_B}{\varepsilon_s^2}\frac{\partial\varepsilon_s}{\partial n_i}\right].\]In code this is FBornX() * XBorni + FBornD() * solventdiElectricdn.
For the solvent mole-average mixing rule,
$S$ denotes the neutral-solvent components included by that mixing rule. $X_B$ scales with amount, while the dielectric derivative scales inversely with amount. Their product is intensive. A neutral component can therefore have a nonzero Born chemical-potential contribution in a mixed solvent even though its charge is zero. For one neutral solvent, this composition derivative vanishes.
The MM implementation uses Born radii rather than diameters, with the equivalent $8\pi$ prefactor. Radius/diameter conventions must be kept consistent. If radii depend on temperature or composition, their derivatives also belong in the corresponding chain rule. A density-dependent permittivity additionally gives a Born pressure contribution through $-RT(\partial F_B/\partial V)$.
These equations are a direct derivation from NeqSim’s implemented free energy; they are not a claim that one dielectric mixing rule is universally accurate.
Related EOS audit
The audit starts from master commit
a7f0e929559b27e70c841b763a77b6bf04c964ff and checks the Born implementations
and their inheritance paths.
| Implementation | Unweighted extensive Born term? | Evidence/scope |
|---|---|---|
| Furst Mod2004 | Yes, corrected | Direct derivative, Euler identity, scaling and two-phase flash regression |
| Base Furst | No | Includes the solvent-permittivity chain rule; scaling regression |
| Electrolyte CPA and Statoil | No | Inherit the base component Born derivative; scaling regression |
| Electrolyte CPA Advanced | No | Uses the inherited chain rule and overridden Born radii/sum; scaling regression |
| Electrolyte CPA Old | No in this path | Source inspection: inherits the base Born derivative |
| Electrolyte CPA MM | No | Explicit chain rule; scaling regression for molar, volume, Looyenga and Lichtenecker solvent mixing |
| Ordinary SRK, PR, CPA and non-electrolyte SAFT models | This specific defect does not apply | Do not inherit the faulty Mod2004 Born implementation |
| Pitzer / activity-coefficient models | This specific defect does not apply | Separate implementation path; not a full derivative qualification |
Passing the scaling checks does not establish complete derivative consistency or accuracy against experimental electrolyte data. It answers the narrower question of whether the same extensive term contaminates the chemical potential.
What modern electrolyte-model development requires
The literature supports explicit ion-solvation contributions with a documented permittivity model, while also showing that their physical interpretation and parameterization remain active research topics:
- Maribo-Mogensen, Thomsen and Kontogeorgis (2015) extend CPA with Debye-Huckel and Born contributions and a self-consistent static-permittivity model. Their reported validation includes activity/osmotic coefficients and phase equilibria. DOI: 10.1002/aic.14829.
- Simonin (2019) compares a semiempirical Born contribution with a nonprimitive ion-dipole model and checks Gibbs-Duhem consistency. The contributions need not agree, including in sign for sufficiently small ions; adding a Born term alone is not proof of physical accuracy. DOI: 10.1063/1.5096598.
- Novak et al. (2023) calculate mixed-solvent MIAC, VLE and LLE with eSAFT-VR Mie. Their results emphasize the importance of the permittivity treatment and the accuracy of the underlying salt-free mixture, particularly for LLE. DOI: 10.1021/acs.iecr.3c00717.
- Novak et al. (2025) compare e-CPA, ePPC-SAFT and eSAFT-VR Mie contributions with explicit-water molecular simulations. Similar total performance can arise from different balances of individual terms; component-level agreement cannot be inferred solely from fitting total activity coefficients. DOI: 10.1016/j.fluid.2025.114339.
The source claims above were checked against the publisher/institutional abstracts. The implementation recommendations below follow from differentiating the model energy and are not presented as verbatim prescriptions from those papers.
Recommended development order:
- Enforce extensivity of free energy and intensivity of chemical potentials over multiple amount scales, including both solvents and ions.
- Use one free-energy expression and differentiate the actual selected permittivity and radius models consistently with respect to $T$, $V$ and every component amount. Validate analytical derivatives against finite differences or an independent automatic-differentiation calculation.
- Check mixed-derivative symmetry, the Euler identity and Gibbs-Duhem behavior, including solvent derivatives. Treat scale invariance as necessary, not sufficient.
- Validate water activity, mean ionic activity, osmotic coefficients, densities, enthalpy/heat capacity and VLE/LLE/SLE against independent data over the intended salt, solvent, temperature and pressure ranges. Declare standard states and concentration bases explicitly.
- Only then compare alternative dielectric decrement, density dependence, ion-pairing or ion-specific radius models, with parameter revalidation.
Remaining Mod2004 limitation
The 2004 phase recalculates solvent permittivity from temperature and neutral composition, but its derivative code suppresses that dependence. Removing the spurious extensive term fixes issue #3862; it does not make the legacy variant the full derivative of its recomputed energy for mixed solvents or thermal perturbations. Restoring these dependencies requires coordinated changes to the Born and long-range derivatives and validation of affected properties. Do not infer modern mixed-solvent/caloric qualification from this correction.
Regression coverage
ElectrolyteBornExtensivityTest checks water/methanol/NaCl liquid states at
amount multipliers from $10^{-6}$ to $10^6$. It checks extensive Born energy,
intensive Born mole derivatives and full log fugacity coefficients, and the
Born Euler identity for these volume-independent solvent-permittivity models.
It also checks the Mod2004 Born derivative against an independent energy finite
difference in a single-solvent state and repeats the methane/water/NaCl TP
flash from issue #3862 at several feed amounts.
The single-solvent finite difference intentionally holds the solvent dielectric constant unchanged at the selected temperature; it does not qualify the omitted mixed-solvent or thermal chain rules described above.