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Properties

(Bulk) equilibrium properties can be calculated as derivatives of a thermodynamic potential. In the case of equations of state, this thermodynamic potential is the Helmholtz energy $A$ as a function of its characteristic variables temperature $T$, volume $V$, and amount of substance of each component $n_i$. Examples for common (measurable) properties that are calculated from an equation of state are the pressure

$$p=-\left(\frac{\partial A}{\partial V}\right)_{T,n_i}$$

and the isochoric heat capacity

$$c_V=\frac{1}{n}\left(\frac{\partial U}{\partial T}\right)_{V,n_i}=\frac{T}{n}\left(\frac{\partial S}{\partial T}\right)_{V,n_i}=-\frac{T}{n}\left(\frac{\partial^2 A}{\partial T^2}\right)_{V,n_i}$$

with the total number of particles $n=\sum_i n_i$, the internal energy $U$, and the entropy $S$.

Residual properties

In most cases, the total value of a property is required because it is the one which can actually be measured. However, for some applications, e.g. phase equilibria or entropy scaling, residual properties are useful. Residual properties are based on the separation of the Helmholtz energy in an ideal gas ($\mathrm{ig}$) contribution and a residual ($\mathrm{res}$) contribution:

$$A=A^\mathrm{ig}+A^\mathrm{res}$$

The ideal gas contribution contains only kinetic and intramolecular energies and can be derived from statistical mechanics as

$$A^\mathrm{ig}(T,V,n_i)=RT\sum_in_i\left(\ln\left(\frac{n_i\Lambda_i^3}{V}\right)-1\right)$$(eqn:a_ig)

with the thermal de Broglie wavelength $\Lambda_i$ that only depends on the temperature. Residual properties depend on the reference state. The two commonly used reference states are at constant volume or at constant pressure, i.e.,

$$A=A^\mathrm{ig,V}(T,V,n_i)+A^\mathrm{res,V}(T,V,n_i)=A^\mathrm{ig,p}(T,p,n_i)+A^\mathrm{res,p}(T,p,n_i)$$(eqn:a_res)

Because the Helmholtz energy is expressed in $T$, $V$ and $n_i$, residual properties at constant volume can be evaluated straightforwardly. If a property $X$ is calculated from the Helmholtz energy via the differential operator $\mathcal{D}$, i.e., $X=\mathcal{D}\left(A\right)$, then the residual contributions is calculated from

$$X^\mathrm{res,V}=\mathcal{D}\left(A\right)-\mathcal{D}\left(A^\mathrm{ig,V}\right)$$

In cases where the operator $\mathcal{D}$ is linear, the expression can be simplified to

$$X^\mathrm{res,V}=\mathcal{D}\left(A-A^\mathrm{ig,V}\right)=\mathcal{D}\left(A^\mathrm{res,V}\right)$$

For residual properties at constant pressure, the reference state has to be evaluated for an ideal gas volume that corresponds to the constant pressure

$$A^\mathrm{ig,p}(T,p,n_i)=A^\mathrm{ig,V}\left(T,V^\mathrm{ig}(T,p,n_i),n_i\right)=A^\mathrm{ig,V}\left(T,\frac{nRT}{p},n_i\right)$$

Then the residual contribution for $X$ can be evaluated as

$$X^\mathrm{res,p}=\mathcal{D}\left(A\right)-\mathcal{D}\left(A^\mathrm{ig,p}\right)$$

For linear operators $\mathcal{D}$ eqs. {eq}eqn:a_ig and {eq}eqn:a_res can be used to simplify the expression

$$X^\mathrm{res,p}=\mathcal{D}\left(A-A^\mathrm{ig,p}\right)=\mathcal{D}\left(A\right)-\mathcal{D}\left(nRT\ln Z\right)$$

with the compressiblity factor $Z=\frac{pV}{nRT}$.

For details on how the evaluation of properties from Helmholtz energy models is implemented in $\text{FeO}_\text{s}$ check out the Rust guide.

List of properties available in $\text{FeO}_\text{s}$

The table below lists all properties that are available in $\text{FeO}_\text{s}$, their definition, and whether they can be evaluated as residual contributions as well.

Name definition residual?
Pressure $p$ $-\left(\frac{\partial A}{\partial V}\right)_{T,n_i}$ yes
Compressibility factor $Z$ $\frac{pV}{nRT}$ yes
Partial derivative of pressure w.r.t. volume $\left(\frac{\partial p}{\partial V}\right)_{T,n_i}$ yes
Partial derivative of pressure w.r.t. density $\left(\frac{\partial p}{\partial \rho}\right)_{T,n_i}$ yes
Partial derivative of pressure w.r.t. temperature $\left(\frac{\partial p}{\partial T}\right)_{V,n_i}$ yes
Partial derivative of pressure w.r.t. moles $\left(\frac{\partial p}{\partial n_i}\right)_{T,V,n_j}$ yes
Second partial derivative of pressure w.r.t. volume $\left(\frac{\partial^2 p}{\partial V^2}\right)_{T,n_i}$ yes
Second partial derivative of pressure w.r.t. density $\left(\frac{\partial^2 p}{\partial \rho^2}\right)_{T,n_i}$ yes
Partial molar volume $v_i$ $\left(\frac{\partial V}{\partial n_i}\right)_{T,p,n_j}$ yes
Chemical potential $\mu_i$ $\left(\frac{\partial A}{\partial n_i}\right)_{T,V,n_j}$ yes
Partial derivative of chemical potential w.r.t. temperature $\left(\frac{\partial\mu_i}{\partial T}\right)_{V,n_i}$ yes
Partial derivative of chemical potential w.r.t. moles $\left(\frac{\partial\mu_i}{\partial n_j}\right)_{V,n_k}$ yes
Logarithmic fugacity coefficient $\ln\varphi_i$ $\beta\mu_i^\mathrm{res}\left(T,p,\lbrace n_i\rbrace\right)$ no
Pure component logarithmic fugacity coefficient $\ln\varphi_i^\mathrm{pure}$ $\lim_{x_i\to 1}\ln\varphi_i$ no
Logarithmic (symmetric) activity coefficient $\ln\gamma_i$ $\ln\left(\frac{\varphi_i}{\varphi_i^\mathrm{pure}}\right)$ no
Partial derivative of the logarithmic fugacity coefficient w.r.t. temperature $\left(\frac{\partial\ln\varphi_i}{\partial T}\right)_{p,n_i}$ no
Partial derivative of the logarithmic fugacity coefficient w.r.t. pressure $\left(\frac{\partial\ln\varphi_i}{\partial p}\right)_{T,n_i}=\frac{v_i^\mathrm{res,p}}{RT}$ no
Partial derivative of the logarithmic fugacity coefficient w.r.t. moles $\left(\frac{\partial\ln\varphi_i}{\partial n_j}\right)_{T,p,n_k}$ no
Thermodynamic factor $\Gamma_{ij}$ $\delta_{ij}+x_i\left(\frac{\partial\ln\varphi_i}{\partial x_j}\right)_{T,p,\Sigma}$ no
Molar isochoric heat capacity $c_v$ $\left(\frac{\partial u}{\partial T}\right)_{V,n_i}$ yes
Partial derivative of the molar isochoric heat capacity w.r.t. temperature $\left(\frac{\partial c_V}{\partial T}\right)_{V,n_i}$ yes
Molar isobaric heat capacity $c_p$ $\left(\frac{\partial h}{\partial T}\right)_{p,n_i}$ yes
Entropy $S$ $-\left(\frac{\partial A}{\partial T}\right)_{V,n_i}$ yes
Partial derivative of the entropy w.r.t. temperature $\left(\frac{\partial S}{\partial T}\right)_{V,n_i}$ yes
Molar entropy $s$ $\frac{S}{n}$ yes
Enthalpy $H$ $A+TS+pV$ yes
Molar enthalpy $h$ $\frac{H}{n}$ yes
Helmholtz energy $A$ yes
Molar Helmholtz energy $a$ $\frac{A}{n}$ yes
Internal energy $U$ $A+TS$ yes
Molar internal energy $u$ $\frac{U}{n}$ yes
Gibbs energy $G$ $A+pV$ yes
Molar Gibbs energy $g$ $\frac{G}{n}$ yes
Partial molar entropy $s_i$ $\left(\frac{\partial S}{\partial n_i}\right)_{T,p,n_j}$ yes
Partial molar enthalpy $h_i$ $\left(\frac{\partial H}{\partial n_i}\right)_{T,p,n_j}$ yes
Joule Thomson coefficient $\mu_\mathrm{JT}$ $\left(\frac{\partial T}{\partial p}\right)_{H,n_i}$ no
Isentropic compressibility $\kappa_s$ $-\frac{1}{V}\left(\frac{\partial V}{\partial p}\right)_{S,n_i}$ no
Isothermal compressibility $\kappa_T$ $-\frac{1}{V}\left(\frac{\partial V}{\partial p}\right)_{T,n_i}$ no
Isenthalpic compressibility $\kappa_h$ $-\frac{1}{V}\left(\frac{\partial V}{\partial p}\right)_{H,n_i}$ no
Thermal expansivity $\alpha_p$ $-\frac{1}{V}\left(\frac{\partial V}{\partial T}\right)_{p,n_i}$ no
Grüneisen parameter $\phi$ $V\left(\frac{\partial p}{\partial U}\right){V,n_i}=\frac{v}{c_v}\left(\frac{\partial p}{\partial T}\right){v,n_i}=\frac{\rho}{T}\left(\frac{\partial T}{\partial \rho}\right)_{s, n_i}$ no
(Static) structure factor $S(0)$ $RT\left(\frac{\partial\rho}{\partial p}\right)_{T,n_i}$ no

Additional properties for fluids with known molar weights

If the Helmholtz energy model includes information about the molar weigt $MW_i$ of each species, additional properties are available in $\text{FeO}_\text{s}$

Name definition residual?
Total molar weight $MW$ $\sum_ix_iMW_i$ no
Mass of each component $m_i$ $n_iMW_i$ no
Total mass $m$ $\sum_im_i=nMW$ no
Mass density $\rho^{(m)}$ $\frac{m}{V}$ no
Mass fractions $w_i$ $\frac{m_i}{m}$ no
Specific entropy $s^{(m)}$ $\frac{S}{m}$ yes
Specific enthalpy $h^{(m)}$ $\frac{H}{m}$ yes
Specific Helmholtz energy $a^{(m)}$ $\frac{A}{m}$ yes
Specific internal energy $u^{(m)}$ $\frac{U}{m}$ yes
Specific Gibbs energy $g^{(m)}$ $\frac{G}{m}$ yes
Speed of sound $c$ $\sqrt{\left(\frac{\partial p}{\partial\rho^{(m)}}\right)_{S,n_i}}$ no