IdealGasReactor.cpp

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/**
 *  @file IdealGasReactor.cpp A zero-dimensional reactor
 */

#include "cantera/zeroD/IdealGasReactor.h"
#include "cantera/zeroD/FlowDevice.h"
#include "cantera/zeroD/Wall.h"

using namespace std;

namespace Cantera
{

void IdealGasReactor::setThermoMgr(ThermoPhase& thermo)
{
    //! @TODO: Add a method to ThermoPhase that indicates whether a given
    //! subclass is compatible with this reactor model
    if (thermo.eosType() != cIdealGas) {
        throw CanteraError("IdealGasReactor::setThermoMgr",
                           "Incompatible phase type provided");
    }
    Reactor::setThermoMgr(thermo);
}

void IdealGasReactor::getInitialConditions(double t0, size_t leny, double* y)
{
    if (m_thermo == 0) {
        cout << "Error: reactor is empty." << endl;
        return;
    }
    m_thermo->restoreState(m_state);

    // set the first component to the total mass
    m_mass = m_thermo->density() * m_vol;
    y[0] = m_mass;

    // set the second component to the total volume
    y[1] = m_vol;

    // Set the third component to the temperature
    y[2] = m_thermo->temperature();

    // set components y+3 ... y+K+2 to the mass fractions of each species
    m_thermo->getMassFractions(y+3);

    // set the remaining components to the surface species
    // coverages on the walls
    getSurfaceInitialConditions(y + m_nsp + 3);
}

void IdealGasReactor::initialize(doublereal t0)
{
    Reactor::initialize(t0);
    m_uk.resize(m_nsp, 0.0);
}

void IdealGasReactor::updateState(doublereal* y)
{
    for (size_t i = 0; i < m_nv; i++) {
        AssertFinite(y[i], "IdealGasReactor::updateState",
                     "y[" + int2str(i) + "] is not finite");
    }

    // The components of y are [0] the total mass, [1] the total volume,
    // [2] the temperature, [3...K+3] are the mass fractions of each species,
    // and [K+3...] are the coverages of surface species on each wall.
    m_mass = y[0];
    m_vol = y[1];
    m_thermo->setMassFractions_NoNorm(y+3);
    m_thermo->setState_TR(y[2], m_mass / m_vol);
    updateSurfaceState(y + m_nsp + 3);

    // save parameters needed by other connected reactors
    m_enthalpy = m_thermo->enthalpy_mass();
    m_pressure = m_thermo->pressure();
    m_intEnergy = m_thermo->intEnergy_mass();
    m_thermo->saveState(m_state);
}

void IdealGasReactor::evalEqs(doublereal time, doublereal* y,
                      doublereal* ydot, doublereal* params)
{
    double dmdt = 0.0; // dm/dt (gas phase)
    double mcvdTdt = 0.0; // m * c_v * dT/dt
    double* dYdt = ydot + 3;

    m_thermo->restoreState(m_state);
    applySensitivity(params);
    m_thermo->getPartialMolarIntEnergies(&m_uk[0]);
    const vector_fp& mw = m_thermo->molecularWeights();
    const doublereal* Y = m_thermo->massFractions();

    if (m_chem) {
        m_kin->getNetProductionRates(&m_wdot[0]); // "omega dot"
    }

    evalWalls(time);
    double mdot_surf = evalSurfaces(time, ydot + m_nsp + 3);
    dmdt += mdot_surf;

    // compression work and external heat transfer
    mcvdTdt += - m_pressure * m_vdot - m_Q;

    for (size_t n = 0; n < m_nsp; n++) {
        // heat release from gas phase and surface reations
        mcvdTdt -= m_wdot[n] * m_uk[n] * m_vol;
        mcvdTdt -= m_sdot[n] * m_uk[n];
        // production in gas phase and from surfaces
        dYdt[n] = (m_wdot[n] * m_vol + m_sdot[n]) * mw[n] / m_mass;
        // dilution by net surface mass flux
        dYdt[n] -= Y[n] * mdot_surf / m_mass;
    }

    // add terms for outlets
    for (size_t i = 0; i < m_outlet.size(); i++) {
        double mdot_out = m_outlet[i]->massFlowRate(time);
        dmdt -= mdot_out; // mass flow out of system
        mcvdTdt -= mdot_out * m_pressure * m_vol / m_mass; // flow work
    }

    // add terms for inlets
    for (size_t i = 0; i < m_inlet.size(); i++) {
        double mdot_in = m_inlet[i]->massFlowRate(time);
        dmdt += mdot_in; // mass flow into system
        mcvdTdt += m_inlet[i]->enthalpy_mass() * mdot_in;
        for (size_t n = 0; n < m_nsp; n++) {
            double mdot_spec = m_inlet[i]->outletSpeciesMassFlowRate(n);
            // flow of species into system and dilution by other species
            dYdt[n] += (mdot_spec - mdot_in * Y[n]) / m_mass;

            // In combintion with h_in*mdot_in, flow work plus thermal
            // energy carried with the species
            mcvdTdt -= m_uk[n] / mw[n] * mdot_spec;
        }
    }

    ydot[0] = dmdt;
    ydot[1] = m_vdot;
    if (m_energy) {
        ydot[2] = mcvdTdt / (m_mass * m_thermo->cv_mass());
    } else {
        ydot[2] = 0;
    }

    for (size_t i = 0; i < m_nv; i++) {
        AssertFinite(ydot[i], "IdealGasReactor::evalEqs",
                     "ydot[" + int2str(i) + "] is not finite");
    }

    resetSensitivity(params);
}

size_t IdealGasReactor::componentIndex(const string& nm) const
{
    size_t k = speciesIndex(nm);
    if (k != npos) {
        return k + 3;
    } else if (nm == "m" || nm == "mass") {
        return 0;
    } else if (nm == "V" || nm == "volume") {
        return 1;
    } else if (nm == "T" || nm == "temperature") {
        return 2;
    } else {
        return npos;
    }
}

}