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cantera/test_problems/surfSolverTest/haca2.xml

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<?xml version="1.0"?>
<ctml>
<validate reactions="yes" species="yes"/>
<!-- phase gas -->
<phase dim="3" id="gas">
<elementArray datasrc="elements.xml">O H C N Ar</elementArray>
<speciesArray datasrc="gri30.xml#species_data">H N2 CH3 CH4 C2H2 H2 OH H2O CO O2</speciesArray>
<state>
<temperature units="K">1400.0</temperature>
<pressure units="Pa">101325.0</pressure>
<moleFractions>H:0.01, N2:0.8899, H2:0.04, CH4:0.01 C2H2:0.01 OH:0.0001 H2O:0.04 O2:0.001</moleFractions>
</state>
<thermo model="IdealGas"/>
<kinetics model="GasKinetics"/>
<transport model="None"/>
</phase>
<!-- phase soot -->
<phase dim="3" id="soot">
<elementArray datasrc="elements.xml">O H C N Ar</elementArray>
<speciesArray datasrc="#species_data">CB-CB3</speciesArray>
<thermo model="StoichSubstance">
<density units="g/cm3">3.52</density>
</thermo>
<transport model="None"/>
<kinetics model="none"/>
</phase>
<!-- phase soot_interface -->
<phase dim="2" id="soot_interface">
<elementArray datasrc="elements.xml">O H C N Ar </elementArray>
<speciesArray datasrc="#species_data">Csoot-* Csoot-H</speciesArray>
<reactionArray datasrc="#reaction_data"/>
<state>
<temperature units="K">1000.0</temperature>
<coverages>Csoot-*:0.1, Csoot-H:0.9</coverages>
</state>
<thermo model="Surface">
<site_density units="mol/cm2">3.8000000000000001e-09</site_density>
</thermo>
<kinetics model="Interface"/>
<transport model="None"/>
<phaseArray>gas soot</phaseArray>
</phase>
<!-- species definitions -->
<speciesData id="species_data">
<!-- species CB-CB3 -->
<species name="CB-CB3">
<atomArray>C:1 </atomArray>
<thermo>
<const_cp Tmax="5000.0" Tmin="100.0">
<t0 units="K">1000.0</t0>
<h0 units="kcal/mol">9.2200000000000006</h0>
<s0 units="cal/mol/K">-3.02</s0>
<cp0 units="cal/mol/K">5.9500000000000002</cp0>
</const_cp>
</thermo>
</species>
<!-- species Csoot-* -->
<species name="Csoot-*">
<atomArray>H:0 C:1 </atomArray>
<thermo>
<const_cp Tmax="5000.0" Tmin="100.0">
<t0 units="K">1000.0</t0>
<h0 units="kcal/mol">51.700000000000003</h0>
<s0 units="cal/mol/K">19.5</s0>
<cp0 units="cal/mol/K">8.4100000000000001</cp0>
</const_cp>
</thermo>
</species>
<!-- species Csoot-H -->
<species name="Csoot-H">
<atomArray>H:1 C:1 </atomArray>
<thermo>
<const_cp Tmax="5000.0" Tmin="100.0">
<t0 units="K">1000.0</t0>
<h0 units="kcal/mol">11.4</h0>
<s0 units="cal/mol/K">21.0</s0>
<cp0 units="cal/mol/K">8.4100000000000001</cp0>
</const_cp>
</thermo>
</species>
</speciesData>
<reactionData id="reaction_data">
<!-- reaction 0001 -->
<reaction reversible="no" type="surface" id="0001">
<equation>Csoot-H + H =] Csoot-* + H2</equation>
<rateCoeff>
<Arrhenius>
<A>4.170000E+10</A>
<b>0.0</b>
<E units="kcal/mol">13.000000</E>
</Arrhenius>
</rateCoeff>
<reactants>Csoot-H:1.0 H:1</reactants>
<products>H2:1 Csoot-*:1.0</products>
</reaction>
<!-- reaction 0002 -->
<reaction reversible="no" type="surface" id="0002">
<equation>Csoot-* + H2 =] Csoot-H + H</equation>
<rateCoeff>
<Arrhenius>
<A>3.900000E+09</A>
<b>0.0</b>
<E units="kcal/mol">11.000000</E>
</Arrhenius>
</rateCoeff>
<reactants>H2:1 Csoot-*:1.0</reactants>
<products>Csoot-H:1.0 H:1</products>
</reaction>
<!-- reaction 0003 -->
<reaction reversible="no" type="surface" id="0003">
<equation>Csoot-H + OH =] Csoot-* + H2O</equation>
<rateCoeff>
<Arrhenius>
<A>1.000000E+07</A>
<b>0.73399999999999999</b>
<E units="kcal/mol">1.430000</E>
</Arrhenius>
</rateCoeff>
<reactants>Csoot-H:1.0 OH:1</reactants>
<products>Csoot-*:1.0 H2O:1</products>
</reaction>
<!-- reaction 0004 -->
<reaction reversible="no" type="surface" id="0004">
<equation>Csoot-* + H2O =] Csoot-H + OH</equation>
<rateCoeff>
<Arrhenius>
<A>3.680000E+05</A>
<b>1.139</b>
<E units="kcal/mol">17.100000</E>
</Arrhenius>
</rateCoeff>
<reactants>Csoot-*:1.0 H2O:1</reactants>
<products>Csoot-H:1.0 OH:1</products>
</reaction>
<!-- reaction 0005 -->
<reaction reversible="no" type="surface" id="0005">
<equation>Csoot-* + H =] Csoot-H</equation>
<rateCoeff>
<Arrhenius>
<A>2.000000E+10</A>
<b>0.0</b>
<E units="kcal/mol">0.000000</E>
</Arrhenius>
</rateCoeff>
<reactants>H:1 Csoot-*:1.0</reactants>
<products>Csoot-H:1.0</products>
</reaction>
<!-- reaction 0006 -->
<reaction reversible="no" type="surface" id="0006">
<equation>Csoot-* + C2H2 =] Csoot-H + H + 2 CB-CB3</equation>
<rateCoeff>
<Arrhenius>
<A>8.000000E+04</A>
<b>1.5600000000000001</b>
<E units="kcal/mol">3.800000</E>
</Arrhenius>
</rateCoeff>
<reactants>Csoot-*:1.0 C2H2:1</reactants>
<products>Csoot-H:1.0 H:1 CB-CB3:2.0</products>
</reaction>
<!-- reaction 0007 -->
<reaction reversible="no" type="surface" id="0007">
<equation>Csoot-* + O2 + 2 CB-CB3 =] Csoot-* + 2 CO</equation>
<rateCoeff>
<Arrhenius>
<A>2.200000E+09</A>
<b>0.0</b>
<E units="kcal/mol">7.500000</E>
</Arrhenius>
</rateCoeff>
<reactants>CB-CB3:2.0 Csoot-*:1.0 O2:1</reactants>
<products>Csoot-*:1.0 CO:2.0</products>
</reaction>
<!-- reaction 0008 -->
<reaction reversible="no" type="surface" id="0008">
<equation>OH + Csoot-H + CB-CB3 =] Csoot-* + CO + H2</equation>
<rateCoeff>
<Arrhenius type="stick" species="OH">
<A>1.300000E-01</A>
<b>0.0</b>
<E units="kcal/mol">0.000000</E>
</Arrhenius>
</rateCoeff>
<reactants>Csoot-H:1 CB-CB3:1 OH:1.0</reactants>
<products>H2:1 Csoot-*:1.0 CO:1</products>
</reaction>
</reactionData>
</ctml>