cantera/test_problems/simpleTransport/HMW_NaCl_pdss.xml

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XML

<?xml version="1.0"?>
<!--
NaCl modeling Based on the Silvester&Pitzer 1977 treatment:
(L. F. Silvester, K. S. Pitzer, "Thermodynamics of Electrolytes:
8. High-Temperature Properties, including Enthalpy and Heat
Capacity, with application to sodium chloride",
J. Phys. Chem., 81, 19 1822 - 1828 (1977)
-->
<ctml>
<phase id="NaCl_electrolyte" dim="3">
<speciesArray datasrc="#species_waterSolution">
H2O(L) Na+ Cl- H+ OH-
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 101325.0 </pressure>
<soluteMolalities>
Na+:6.0954
Cl-:6.0954
H+:2.1628E-9
OH-:1.3977E-6
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients model="Pitzer" TempModel="complex1">
<!-- Pitzer Coefficients
These coefficients are from Pitzer's main
paper, in his book.
-->
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters cation="Na+" anion="Cl-">
<beta0> 0.0765, 0.008946, -3.3158E-6,
-777.03, -4.4706
</beta0>
<beta1> 0.2664, 6.1608E-5, 1.0715E-6, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.00127, -4.655E-5, 0.0,
33.317, 0.09421
</Cphi>
<Alpha1> 2.0 </Alpha1>
</binarySaltParameters>
<binarySaltParameters cation="H+" anion="Cl-">
<beta0> 0.1775, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.2945, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.0008, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2.0 </Alpha1>
</binarySaltParameters>
<binarySaltParameters cation="Na+" anion="OH-">
<beta0> 0.0864, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.253, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.0044, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2.0 </Alpha1>
</binarySaltParameters>
<thetaAnion anion1="Cl-" anion2="OH-">
<Theta> -0.05 </Theta>
</thetaAnion>
<psiCommonCation cation="Na+" anion1="Cl-" anion2="OH-">
<Theta> -0.05 </Theta>
<Psi> -0.006 </Psi>
</psiCommonCation>
<thetaCation cation1="Na+" cation2="H+">
<Theta> 0.036 </Theta>
</thetaCation>
<psiCommonAnion anion="Cl-" cation1="Na+" cation2="H+">
<Theta> 0.036 </Theta>
<Psi> -0.004 </Psi>
</psiCommonAnion>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H C E Fe Si N Na Cl </elementArray>
<kinetics model="none" >
</kinetics>
<transport model="Simple">
<compositionDependence model="solvent"/>
<!--
<compositionDependence model="Mixture_Averaged"/>
-->
</transport>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<!-- H2O(L) liquid standard state -> pure H2O
The origin of the NASA polynomial is a bit murky. It does
fit the vapor pressure curve at 298K adequately.
-->
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA Tmax="600.0" Tmin="273.14999999999998" P0="100000.0">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterIAPWS">
<!--
Molar volume in m3 kmol-1.
(this is from Pitzer, Peiper, and Busey. However,
the result can be easily derived from ~ 1gm/cm**3)
<molarVolume> 0.018068 </molarVolume>
-->
</standardState>
<transport>
<viscosity model="Constant" units="centipoise"> 1.0E0 </viscosity>
<thermalConductivity model="Constant"> 0.58 </thermalConductivity>
<speciesDiffusivity model="Constant"> 1.0E-5 </speciesDiffusivity>
</transport>
</species>
<species name="Na+">
<!-- Na+ (aq) standard state based on the unity molality convention
xxx
-->
<atomArray> Na:1 E:-1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax=" 640." Tmin=" 273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591. </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433. </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal K/gmol/bar"> 3.256 </a3>
<a4 units="cal K/gmol"> -27260. </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal K/gmol"> -29810. </c2>
<omega_Pr_Tr units="cal/gmol"> 33060. </omega_Pr_Tr>
</standardState>
<transport>
<speciesDiffusivity model="Constant"> 1.0E-5 </speciesDiffusivity>
</transport>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<atomArray> Cl:1 E:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax=" 623.15" Tmin=" 298.00">
<DG0_f_Pr_Tr units="cal/gmol"> -31379. </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -39933. </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.4032 </a1>
<a2 units="cal/gmol"> 480.1 </a2>
<a3 units="cal K/gmol/bar"> 5.563 </a3>
<a4 units="cal K/gmol"> -28470. </a4>
<c1 units="cal/gmol/K"> -4.4 </c1>
<c2 units="cal K/gmol"> -57140. </c2>
<omega_Pr_Tr units="cal/gmol"> 145600. </omega_Pr_Tr>
</standardState>
<transport>
<speciesDiffusivity model="Constant"> 1.0E-5 </speciesDiffusivity>
</transport>
<source>
ref:G9
</source>
</species>
<species name="H+">
<atomArray> H:1 E:-1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax=" 623.15" Tmin=" 298.00">
<DG0_f_Pr_Tr units="cal/gmol"> 0.0 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> 0.0 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 0.0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.0 </a1>
<a2 units="cal/gmol"> 0.0 </a2>
<a3 units="cal K/gmol/bar"> 0.0 </a3>
<a4 units="cal K/gmol"> 0.0 </a4>
<c1 units="cal/gmol/K"> 0.0 </c1>
<c2 units="cal K/gmol"> 0.0 </c2>
<omega_Pr_Tr units="cal/gmol"> 0.0 </omega_Pr_Tr>
</standardState>
<transport>
<speciesDiffusivity model="Constant"> 1.0E-5 </speciesDiffusivity>
</transport>
<source>
ref:G9
</source>
</species>
<species name="OH-">
<atomArray> O:1 H:1 E:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax=" 623.15" Tmin=" 298.00">
<DG0_f_Pr_Tr units="cal/gmol"> -37595. </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977. </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal K/gmol/bar"> 1.8423 </a3>
<a4 units="cal K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal K/gmol"> -103460. </c2>
<omega_Pr_Tr units="cal/gmol"> 172460. </omega_Pr_Tr>
</standardState>
<transport>
<speciesDiffusivity model="Constant"> 1.0E-5 </speciesDiffusivity>
</transport>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>