CanteraError inerits from std:exception, so now it has a what() method that is used to print a message describing the exception. Adding an exception to the Cantera error stack now requires explicitly calling the .save() method.
280 lines
8.2 KiB
C++
280 lines
8.2 KiB
C++
/**
|
|
* @file HMW_graph_1.cpp
|
|
*/
|
|
|
|
#include "cantera/thermo.h"
|
|
#include "cantera/thermo/HMWSoln.h"
|
|
|
|
#include "TemperatureTable.h"
|
|
|
|
#include <cstdio>
|
|
|
|
using namespace std;
|
|
using namespace Cantera;
|
|
|
|
void printUsage()
|
|
{
|
|
cout << "usage: HMW_test " << endl;
|
|
cout <<" -> Everything is hardwired" << endl;
|
|
}
|
|
|
|
|
|
int main(int argc, char** argv)
|
|
{
|
|
|
|
int retn = 0;
|
|
int i;
|
|
|
|
try {
|
|
|
|
char iFile[80];
|
|
strcpy(iFile, "HMW_NaCl.xml");
|
|
if (argc > 1) {
|
|
strcpy(iFile, argv[1]);
|
|
}
|
|
double Enth0_RT[20], pmEnth[20], molarEnth;
|
|
|
|
HMWSoln* HMW = new HMWSoln(iFile, "NaCl_electrolyte");
|
|
|
|
|
|
/*
|
|
* Load in and initialize the
|
|
*/
|
|
Cantera::ThermoPhase* solid = newPhase("NaCl_Solid.xml","NaCl(S)");
|
|
|
|
|
|
int nsp = HMW->nSpecies();
|
|
double acMol[100];
|
|
double act[100];
|
|
double mf[100];
|
|
double moll[100];
|
|
for (i = 0; i < 100; i++) {
|
|
acMol[i] = 1.0;
|
|
mf[i] = 0.0;
|
|
act[i] = 1.0;
|
|
moll[i] = 0.0;
|
|
}
|
|
HMW->getMoleFractions(mf);
|
|
string sName;
|
|
|
|
TemperatureTable TTable(15, false, 273.15, 25., 0, 0);
|
|
|
|
|
|
HMW->setState_TP(298.15, 1.01325E5);
|
|
|
|
int i1 = HMW->speciesIndex("Na+");
|
|
int i2 = HMW->speciesIndex("Cl-");
|
|
//int i3 = HMW->speciesIndex("H2O(L)");
|
|
for (i = 1; i < nsp; i++) {
|
|
moll[i] = 0.0;
|
|
}
|
|
HMW->setMolalities(moll);
|
|
|
|
double ISQRT;
|
|
double Is = 0.0;
|
|
|
|
/*
|
|
* Set the Pressure
|
|
*/
|
|
double pres = OneAtm;
|
|
|
|
/*
|
|
* Fix the molality
|
|
*/
|
|
Is = 6.146;
|
|
ISQRT = sqrt(Is);
|
|
moll[i1] = Is;
|
|
moll[i2] = Is;
|
|
HMW->setState_TPM(298.15, pres, moll);
|
|
double Xmol[30];
|
|
HMW->getMoleFractions(Xmol);
|
|
|
|
/*
|
|
* ThermoUnknowns
|
|
*/
|
|
double T;
|
|
double H0_NaCl = 0.0, H0_Naplus = 0.0, H0_Clminus = 0.0, Delta_H0s, H0_H2O = 0.0;
|
|
double H_NaCl = 0.0, H_Naplus = 0.0, H_Clminus = 0.0, H_H2O = 0.0;
|
|
double molarEnth0;
|
|
|
|
printf("A_L/RT: Comparison to Pitzer's book, p. 99, can be made.\n");
|
|
printf(" Agreement to 3-4 sig digits for Aphi and A_L/RT\n");
|
|
printf("\n");
|
|
|
|
printf("Delta_H0: Heat of Solution per mole of salt (standard states)\n");
|
|
printf(" rxn for the ss heat of soln: "
|
|
"NaCl(s) -> Na+(aq) + Cl-(aq)\n");
|
|
|
|
printf("\n");
|
|
printf("Delta_Hs: Heat of Solution per mole of salt\n");
|
|
printf(" rxn for heat of soln: "
|
|
" n1 H2O(l,pure) + n2 NaCl(s) -> n2 MX(aq) + n1 H2O(l) \n");
|
|
printf(" Delta_Hs = (n1 h_H2O_bar + n2 h_MX_bar "
|
|
"- n1 h_H2O_0 - n2 h_MX_0)/n2\n");
|
|
printf("\n");
|
|
printf("phiL: phiL, calculated from the program, is checked\n");
|
|
printf(" against analytical formula in L_standalone program.\n");
|
|
printf(" (comparison against Eq. 12, Silvester and Pitzer)\n");
|
|
|
|
#ifdef DEBUG_HKM
|
|
FILE* ttt = fopen("table.csv","w");
|
|
#endif
|
|
/*
|
|
* Create a Table of NaCl Enthalpy Properties as a Function
|
|
* of the Temperature
|
|
*/
|
|
printf("\n\n");
|
|
printf(" T, Pres, Aphi, A_L/RT,"
|
|
" Delta_H0,"
|
|
" Delta_Hs, L, phiL,"
|
|
" L_rel_molal,"
|
|
" MolarEnth, MolarEnth0\n");
|
|
printf(" Kelvin, bar, sqrt(kg/gmol), sqrt(kg/gmol),"
|
|
" kJ/gmolSalt,"
|
|
" kJ/gmolSalt, kJ/gmolSoln, kJ/gmolSalt,"
|
|
" kJ/gmolSalt, kJ/gmol, kJ/gmol\n");
|
|
#ifdef DEBUG_HKM
|
|
fprintf(ttt,"T, Pres, A_L/RT, Delta_H0, Delta_Hs, phiL\n");
|
|
fprintf(ttt,"Kelvin, bar, sqrt(kg/gmol), kJ/gmolSalt, kJ/gmolSalt, kJ/gmolSalt\n");
|
|
#endif
|
|
for (i = 0; i < TTable.NPoints + 1; i++) {
|
|
if (i == TTable.NPoints) {
|
|
T = 323.15;
|
|
} else {
|
|
T = TTable.T[i];
|
|
}
|
|
/*
|
|
* RT is in units of J/kmolK
|
|
*/
|
|
double RT = GasConstant * T;
|
|
|
|
/*
|
|
* Make sure we are at the saturation pressure or above.
|
|
*/
|
|
|
|
double psat = HMW->satPressure(T);
|
|
|
|
pres = OneAtm;
|
|
if (psat > pres) {
|
|
pres = psat;
|
|
}
|
|
|
|
|
|
HMW->setState_TPM(T, pres, moll);
|
|
|
|
solid->setState_TP(T, pres);
|
|
|
|
/*
|
|
* Get the Standard State DeltaH
|
|
*/
|
|
solid->getEnthalpy_RT(Enth0_RT);
|
|
H0_NaCl = Enth0_RT[0] * RT * 1.0E-6;
|
|
HMW->getEnthalpy_RT(Enth0_RT);
|
|
H0_H2O = Enth0_RT[0] * RT * 1.0E-6;
|
|
H0_Naplus = Enth0_RT[i1] * RT * 1.0E-6;
|
|
H0_Clminus = Enth0_RT[i2] * RT * 1.0E-6;
|
|
|
|
/*
|
|
* Calculate the standard state heat of solution
|
|
* for NaCl(s) -> Na+ + Cl-
|
|
* units: kJ/gmolSalt
|
|
*/
|
|
Delta_H0s = H0_Naplus + H0_Clminus - H0_NaCl;
|
|
|
|
|
|
solid->getPartialMolarEnthalpies(pmEnth);
|
|
H_NaCl = pmEnth[0] * 1.0E-6;
|
|
HMW->getPartialMolarEnthalpies(pmEnth);
|
|
H_H2O = pmEnth[0] * 1.0E-6;
|
|
H_Naplus = pmEnth[i1] * 1.0E-6;
|
|
H_Clminus = pmEnth[i2] * 1.0E-6;
|
|
//double Delta_H_Salt = H_NaCl - (H_Naplus + H_Clminus);
|
|
//double Lfunc = HMW->relative_enthalpy() * 1.0E-6;
|
|
molarEnth = HMW->enthalpy_mole() * 1.0E-6;
|
|
|
|
double Delta_Hs = (Xmol[0] * H_H2O +
|
|
Xmol[i1] * H_Naplus +
|
|
Xmol[i2] * H_Clminus
|
|
- Xmol[0] * H0_H2O
|
|
- Xmol[i1] * H_NaCl);
|
|
Delta_Hs /= Xmol[i1];
|
|
|
|
/*
|
|
* Calculate the relative enthalpy, L, from the
|
|
* partial molar quantities. units kJ/gmolSolution
|
|
*/
|
|
double L = (Xmol[0] * (H_H2O - H0_H2O) +
|
|
Xmol[i1] * (H_Naplus - H0_Naplus) +
|
|
Xmol[i2] * (H_Clminus - H0_Clminus));
|
|
|
|
/*
|
|
* Calculate the apparent relative molal enthalpy, phiL,
|
|
* units of kJ/gmolSaltAdded
|
|
*/
|
|
double phiL = L / Xmol[i1];
|
|
|
|
|
|
double Aphi = HMW->A_Debye_TP() / 3.0;
|
|
double AL = HMW->ADebye_L();
|
|
double LrelMol = HMW->relative_molal_enthalpy() * 1.0E-6;
|
|
|
|
|
|
|
|
for (int k = 0; k < nsp; k++) {
|
|
Enth0_RT[k] *= RT * 1.0E-6;
|
|
}
|
|
|
|
molarEnth0 = 0.0;
|
|
for (int k = 0; k < nsp; k++) {
|
|
molarEnth0 += Xmol[k] * Enth0_RT[k];
|
|
}
|
|
|
|
if (i != TTable.NPoints+1) {
|
|
printf("%13g, %13g, %13g, %13g, %13g, %13g, %13g, "
|
|
"%13g, %13g, %13g, %13g\n",
|
|
T, pres*1.0E-5, Aphi, AL/RT, Delta_H0s, Delta_Hs,
|
|
L, phiL,
|
|
LrelMol,
|
|
molarEnth , molarEnth0);
|
|
|
|
#ifdef DEBUG_HKM
|
|
fprintf(ttt,"%g, %g, %g, %g, %g, %g\n",
|
|
T, pres*1.0E-5, AL/RT, Delta_H0s, Delta_Hs, phiL);
|
|
#endif
|
|
}
|
|
|
|
}
|
|
|
|
printf("Breakdown of Enthalpy Calculation at 323.15 K, 1atm:\n");
|
|
|
|
printf(" Species MoleFrac Molal H0 "
|
|
" partH (partH - H0)\n");
|
|
printf(" H2O(L)");
|
|
printf("%13g %13g %13g %13g %13g\n", Xmol[0], moll[0], H0_H2O , H_H2O, H_H2O-H0_H2O);
|
|
printf(" Na+ ");
|
|
printf("%13g %13g %13g %13g %13g\n", Xmol[i1], moll[i1],
|
|
H0_Naplus , H_Naplus, H_Naplus -H0_Naplus);
|
|
printf(" Cl- ");
|
|
printf("%13g %13g %13g %13g %13g\n", Xmol[i2], moll[i2],
|
|
H0_Clminus , H_Clminus, H_Clminus - H0_Clminus);
|
|
|
|
|
|
|
|
delete HMW;
|
|
HMW = 0;
|
|
delete solid;
|
|
solid = 0;
|
|
Cantera::appdelete();
|
|
|
|
#ifdef DEBUG_HKM
|
|
fclose(ttt);
|
|
#endif
|
|
|
|
return retn;
|
|
|
|
} catch (CanteraError& err) {
|
|
std::cout << err.what() << std::endl;
|
|
Cantera::appdelete();
|
|
return -1;
|
|
}
|
|
}
|