/** * @file PDSS_SSVol.cpp * Implementation of a pressure dependent standard state * virtual function. */ /* * Copyright (2006) Sandia Corporation. Under the terms of * Contract DE-AC04-94AL85000 with Sandia Corporation, the * U.S. Government retains certain rights in this software. */ #include "cantera/base/ctml.h" #include "cantera/thermo/PDSS_SSVol.h" #include "cantera/thermo/VPStandardStateTP.h" #include using namespace std; namespace Cantera { PDSS_SSVol::PDSS_SSVol(VPStandardStateTP* tp, size_t spindex) : PDSS(tp, spindex), volumeModel_(cSSVOLUME_CONSTANT), m_constMolarVolume(-1.0) { m_pdssType = cPDSS_SSVOL; TCoeff_[0] = 0.0; TCoeff_[1] = 0.0; TCoeff_[2] = 0.0; } PDSS_SSVol::PDSS_SSVol(VPStandardStateTP* tp, size_t spindex, const std::string& inputFile, const std::string& id) : PDSS(tp, spindex), volumeModel_(cSSVOLUME_CONSTANT), m_constMolarVolume(-1.0) { m_pdssType = cPDSS_SSVOL; constructPDSSFile(tp, spindex, inputFile, id); } PDSS_SSVol::PDSS_SSVol(VPStandardStateTP* tp, size_t spindex, const XML_Node& speciesNode, const XML_Node& phaseRoot, bool spInstalled) : PDSS(tp, spindex), volumeModel_(cSSVOLUME_CONSTANT), m_constMolarVolume(-1.0) { m_pdssType = cPDSS_SSVOL; constructPDSSXML(tp, spindex, speciesNode, phaseRoot, spInstalled); } PDSS_SSVol::PDSS_SSVol(const PDSS_SSVol& b) : PDSS(b), volumeModel_(cSSVOLUME_CONSTANT), m_constMolarVolume(-1.0) { /* * Use the assignment operator to do the brunt * of the work for the copy constructor. */ *this = b; } PDSS_SSVol& PDSS_SSVol::operator=(const PDSS_SSVol& b) { if (&b == this) { return *this; } PDSS::operator=(b); volumeModel_ = b.volumeModel_; m_constMolarVolume = b.m_constMolarVolume; TCoeff_ = b.TCoeff_; return *this; } PDSS* PDSS_SSVol::duplMyselfAsPDSS() const { return new PDSS_SSVol(*this); } void PDSS_SSVol::constructPDSSXML(VPStandardStateTP* tp, size_t spindex, const XML_Node& speciesNode, const XML_Node& phaseNode, bool spInstalled) { PDSS::initThermo(); m_p0 = m_tp->speciesThermo().refPressure(m_spindex); if (!spInstalled) { throw CanteraError("PDSS_SSVol::constructPDSSXML", "spInstalled false not handled"); } const XML_Node* ss = speciesNode.findByName("standardState"); if (!ss) { throw CanteraError("PDSS_SSVol::constructPDSSXML", "no standardState Node for species " + speciesNode.name()); } std::string model = ss->attrib("model"); if (model == "constant_incompressible" || model == "constant") { volumeModel_ = cSSVOLUME_CONSTANT; m_constMolarVolume = getFloat(*ss, "molarVolume", "toSI"); } else if (model == "temperature_polynomial") { volumeModel_ = cSSVOLUME_TPOLY; size_t num = getFloatArray(*ss, TCoeff_, true, "toSI", "volumeTemperaturePolynomial"); if (num != 4) { throw CanteraError("PDSS_SSVol::constructPDSSXML", " Didn't get 4 density polynomial numbers for species " + speciesNode.name()); } } else if (model == "density_temperature_polynomial") { volumeModel_ = cSSVOLUME_DENSITY_TPOLY; size_t num = getFloatArray(*ss, TCoeff_, true, "toSI", "densityTemperaturePolynomial"); if (num != 4) { throw CanteraError("PDSS_SSVol::constructPDSSXML", " Didn't get 4 density polynomial numbers for species " + speciesNode.name()); } } else { throw CanteraError("PDSS_SSVol::constructPDSSXML", "standardState model for species isn't constant_incompressible: " + speciesNode.name()); } } void PDSS_SSVol::constructPDSSFile(VPStandardStateTP* tp, size_t spindex, const std::string& inputFile, const std::string& id) { if (inputFile.size() == 0) { throw CanteraError("PDSS_SSVol::initThermo", "input file is null"); } std::string path = findInputFile(inputFile); ifstream fin(path.c_str()); if (!fin) { throw CanteraError("PDSS_SSVol::initThermo","could not open " +path+" for reading."); } /* * The phase object automatically constructs an XML object. * Use this object to store information. */ XML_Node fxml; fxml.build(fin); XML_Node* fxml_phase = findXMLPhase(&fxml, id); if (!fxml_phase) { throw CanteraError("PDSS_SSVol::initThermo", "ERROR: Can not find phase named " + id + " in file named " + inputFile); } XML_Node& speciesList = fxml_phase->child("speciesArray"); XML_Node* speciesDB = get_XML_NameID("speciesData", speciesList["datasrc"], &fxml_phase->root()); const XML_Node* s = speciesDB->findByAttr("name", tp->speciesName(spindex)); constructPDSSXML(tp, spindex, *s, *fxml_phase, true); } void PDSS_SSVol::initThermoXML(const XML_Node& phaseNode, const std::string& id) { PDSS::initThermoXML(phaseNode, id); m_minTemp = m_spthermo->minTemp(m_spindex); m_maxTemp = m_spthermo->maxTemp(m_spindex); m_p0 = m_spthermo->refPressure(m_spindex); m_mw = m_tp->molecularWeight(m_spindex); } void PDSS_SSVol::initThermo() { PDSS::initThermo(); m_p0 = m_tp->speciesThermo().refPressure(m_spindex); m_V0_ptr[m_spindex] = m_constMolarVolume; m_Vss_ptr[m_spindex] = m_constMolarVolume; } doublereal PDSS_SSVol::enthalpy_RT() const { return m_hss_RT_ptr[m_spindex]; } doublereal PDSS_SSVol::intEnergy_mole() const { doublereal pV = m_pres * m_Vss_ptr[m_spindex]; return m_h0_RT_ptr[m_spindex] * GasConstant * m_temp - pV; } doublereal PDSS_SSVol::entropy_R() const { return m_sss_R_ptr[m_spindex]; } doublereal PDSS_SSVol::gibbs_RT() const { return m_gss_RT_ptr[m_spindex]; } doublereal PDSS_SSVol::cp_R() const { return m_cpss_R_ptr[m_spindex]; } doublereal PDSS_SSVol::cv_mole() const { return (cp_mole() - m_V0_ptr[m_spindex]); } doublereal PDSS_SSVol::molarVolume() const { return m_Vss_ptr[m_spindex]; } doublereal PDSS_SSVol::density() const { return m_mw / m_Vss_ptr[m_spindex]; } doublereal PDSS_SSVol::gibbs_RT_ref() const { return m_g0_RT_ptr[m_spindex]; } doublereal PDSS_SSVol::enthalpy_RT_ref() const { return m_h0_RT_ptr[m_spindex]; } doublereal PDSS_SSVol::entropy_R_ref() const { return m_s0_R_ptr[m_spindex]; } doublereal PDSS_SSVol::cp_R_ref() const { return m_cp0_R_ptr[m_spindex]; } doublereal PDSS_SSVol::molarVolume_ref() const { return m_V0_ptr[m_spindex]; } void PDSS_SSVol::calcMolarVolume() const { if (volumeModel_ == cSSVOLUME_CONSTANT) { m_Vss_ptr[m_spindex] = m_constMolarVolume; } else if (volumeModel_ == cSSVOLUME_TPOLY) { m_Vss_ptr[m_spindex] = TCoeff_[0] + m_temp * (TCoeff_[1] + m_temp * (TCoeff_[2] + m_temp * TCoeff_[3])); dVdT_ = TCoeff_[1] + 2.0 * m_temp * TCoeff_[2] + 3.0 * m_temp * m_temp * TCoeff_[3]; d2VdT2_ = 2.0 * TCoeff_[2] + 6.0 * m_temp * TCoeff_[3]; } else if (volumeModel_ == cSSVOLUME_DENSITY_TPOLY) { doublereal dens = TCoeff_[0] + m_temp * (TCoeff_[1] + m_temp * (TCoeff_[2] + m_temp * TCoeff_[3])); m_Vss_ptr[m_spindex] = m_mw / dens; doublereal dens2 = dens * dens; doublereal ddensdT = TCoeff_[1] + 2.0 * m_temp * TCoeff_[2] + 3.0 * m_temp * m_temp * TCoeff_[3]; doublereal d2densdT2 = 2.0 * TCoeff_[2] + 6.0 * m_temp * TCoeff_[3]; dVdT_ = - m_mw / dens2 * ddensdT; d2VdT2_ = 2.0 * m_mw / (dens2 * dens) * ddensdT * ddensdT - m_mw / dens2 * d2densdT2; } else { throw CanteraError("PDSS_SSVol::calcMolarVolume", "unimplemented"); } } void PDSS_SSVol::setPressure(doublereal p) { m_pres = p; doublereal deltaP = m_pres - m_p0; if (fabs(deltaP) < 1.0E-10) { m_hss_RT_ptr[m_spindex] = m_h0_RT_ptr[m_spindex]; m_sss_R_ptr[m_spindex] = m_s0_R_ptr[m_spindex]; m_gss_RT_ptr[m_spindex] = m_hss_RT_ptr[m_spindex] - m_sss_R_ptr[m_spindex]; m_cpss_R_ptr[m_spindex] = m_cp0_R_ptr[m_spindex]; } else { doublereal del_pRT = deltaP / (GasConstant * m_temp); doublereal sV_term = - deltaP / GasConstant * dVdT_; m_hss_RT_ptr[m_spindex] = m_h0_RT_ptr[m_spindex] + sV_term + del_pRT * m_Vss_ptr[m_spindex]; m_sss_R_ptr[m_spindex] = m_s0_R_ptr[m_spindex] + sV_term; m_gss_RT_ptr[m_spindex] = m_hss_RT_ptr[m_spindex] - m_sss_R_ptr[m_spindex]; m_cpss_R_ptr[m_spindex] = m_cp0_R_ptr[m_spindex] - m_temp * deltaP * d2VdT2_; } } void PDSS_SSVol::setTemperature(doublereal temp) { m_temp = temp; m_spthermo->update_one(m_spindex, temp, m_cp0_R_ptr, m_h0_RT_ptr, m_s0_R_ptr); calcMolarVolume(); m_g0_RT_ptr[m_spindex] = m_h0_RT_ptr[m_spindex] - m_s0_R_ptr[m_spindex]; doublereal deltaP = m_pres - m_p0; if (fabs(deltaP) < 1.0E-10) { m_hss_RT_ptr[m_spindex] = m_h0_RT_ptr[m_spindex]; m_sss_R_ptr[m_spindex] = m_s0_R_ptr[m_spindex]; m_gss_RT_ptr[m_spindex] = m_hss_RT_ptr[m_spindex] - m_sss_R_ptr[m_spindex]; m_cpss_R_ptr[m_spindex] = m_cp0_R_ptr[m_spindex]; } else { doublereal del_pRT = deltaP / (GasConstant * m_temp); doublereal sV_term = - deltaP / GasConstant * dVdT_; m_hss_RT_ptr[m_spindex] = m_h0_RT_ptr[m_spindex] + sV_term + del_pRT * m_Vss_ptr[m_spindex]; m_sss_R_ptr[m_spindex] = m_s0_R_ptr[m_spindex] + sV_term; m_gss_RT_ptr[m_spindex] = m_hss_RT_ptr[m_spindex] - m_sss_R_ptr[m_spindex]; m_cpss_R_ptr[m_spindex] = m_cp0_R_ptr[m_spindex] - m_temp * deltaP * d2VdT2_; } } void PDSS_SSVol::setState_TP(doublereal temp, doublereal pres) { m_pres = pres; setTemperature(temp); } void PDSS_SSVol::setState_TR(doublereal temp, doublereal rho) { doublereal rhoStored = m_mw / m_constMolarVolume; if (fabs(rhoStored - rho) / (rhoStored + rho) > 1.0E-4) { throw CanteraError("PDSS_SSVol::setState_TR", "Inconsistent supplied rho"); } setTemperature(temp); } doublereal PDSS_SSVol::satPressure(doublereal t) { return 1.0E-200; } }