IdealGasConstPressureReactor.cpp

/**
 *  @file ConstPressureReactor.cpp A constant pressure zero-dimensional
 *      reactor
 */

// Copyright 2001  California Institute of Technology

#include "cantera/zeroD/IdealGasConstPressureReactor.h"
#include "cantera/zeroD/FlowDevice.h"
#include "cantera/zeroD/Wall.h"
#include "cantera/kinetics/InterfaceKinetics.h"
#include "cantera/thermo/SurfPhase.h"

using namespace std;

namespace Cantera
{

void IdealGasConstPressureReactor::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 IdealGasConstPressureReactor::
getInitialConditions(double t0, size_t leny, double* y)
{
    m_init = true;
    if (m_thermo == 0) {
        throw CanteraError("getInitialConditions",
                           "Error: reactor is empty.");
    }
    m_thermo->restoreState(m_state);

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

    // set the second component to the temperature
    y[1] = m_thermo->temperature();

    // set components y+2 ... y+K+1 to the mass fractions Y_k of each species
    m_thermo->getMassFractions(y+2);

    // set the remaining components to the surface species
    // coverages on the walls
    size_t loc = m_nsp + 2;
    SurfPhase* surf;
    for (size_t m = 0; m < m_nwalls; m++) {
        surf = m_wall[m]->surface(m_lr[m]);
        if (surf) {
            m_wall[m]->getCoverages(m_lr[m], y + loc);
            loc += surf->nSpecies();
        }
    }
}

void IdealGasConstPressureReactor::initialize(doublereal t0)
{
    m_thermo->restoreState(m_state);
    m_sdot.resize(m_nsp, 0.0);
    m_wdot.resize(m_nsp, 0.0);
    m_hk.resize(m_nsp, 0.0);
    m_nv = m_nsp + 2;
    for (size_t w = 0; w < m_nwalls; w++)
        if (m_wall[w]->surface(m_lr[w])) {
            m_nv += m_wall[w]->surface(m_lr[w])->nSpecies();
        }

    m_enthalpy = m_thermo->enthalpy_mass();
    m_pressure = m_thermo->pressure();
    m_intEnergy = m_thermo->intEnergy_mass();

    size_t nt = 0, maxnt = 0;
    for (size_t m = 0; m < m_nwalls; m++) {
        if (m_wall[m]->kinetics(m_lr[m])) {
            nt = m_wall[m]->kinetics(m_lr[m])->nTotalSpecies();
            if (nt > maxnt) {
                maxnt = nt;
            }
            if (m_wall[m]->kinetics(m_lr[m])) {
                if (&m_kin->thermo(0) !=
                        &m_wall[m]->kinetics(m_lr[m])->thermo(0)) {
                    throw CanteraError("IdealGasConstPressureReactor::initialize",
                                       "First phase of all kinetics managers must be"
                                       " the gas.");
                }
            }
        }
    }
    m_work.resize(maxnt);
    std::sort(m_pnum.begin(), m_pnum.end());
    m_init = true;
}

void IdealGasConstPressureReactor::updateState(doublereal* y)
{
    // The components of y are [0] the total mass, [1] the temperature,
    // [2...K+2) are the mass fractions of each species, and [K+2...] are the
    // coverages of surface species on each wall.
    m_mass = y[0];
    m_thermo->setMassFractions_NoNorm(y+2);
    m_thermo->setState_TP(y[1], m_pressure);
    m_vol = m_mass / m_thermo->density();

    size_t loc = m_nsp + 2;
    SurfPhase* surf;
    for (size_t m = 0; m < m_nwalls; m++) {
        surf = m_wall[m]->surface(m_lr[m]);
        if (surf) {
            m_wall[m]->setCoverages(m_lr[m], y+loc);
            loc += surf->nSpecies();
        }
    }

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

void IdealGasConstPressureReactor::evalEqs(doublereal time, doublereal* y,
                                   doublereal* ydot, doublereal* params)
{
    size_t nk;
    m_thermo->restoreState(m_state);

    Kinetics* kin;
    size_t npar, ploc;
    double mult;

    // process sensitivity parameters
    if (params) {

        npar = m_pnum.size();
        for (size_t n = 0; n < npar; n++) {
            mult = m_kin->multiplier(m_pnum[n]);
            m_kin->setMultiplier(m_pnum[n], mult*params[n]);
        }
        ploc = npar;
        for (size_t m = 0; m < m_nwalls; m++) {
            if (m_nsens_wall[m] > 0) {
                m_wall[m]->setSensitivityParameters(m_lr[m], params + ploc);
                ploc += m_nsens_wall[m];
            }
        }
    }

    m_Q = 0.0;

    // compute wall terms
    doublereal rs0, sum, wallarea;
    double mcpdTdt = 0.0; // m * c_p * dT/dt
    double dmdt = 0.0; // dm/dt (gas phase)
    double* dYdt = ydot + 2;
    m_thermo->getPartialMolarEnthalpies(&m_hk[0]);

    SurfPhase* surf;
    size_t lr, ns, loc = m_nsp+2, surfloc;
    fill(m_sdot.begin(), m_sdot.end(), 0.0);
    for (size_t i = 0; i < m_nwalls; i++) {
        lr = 1 - 2*m_lr[i];
        m_Q += lr*m_wall[i]->Q(time);
        kin = m_wall[i]->kinetics(m_lr[i]);
        surf = m_wall[i]->surface(m_lr[i]);
        if (surf && kin) {
            rs0 = 1.0/surf->siteDensity();
            nk = surf->nSpecies();
            sum = 0.0;
            surf->setTemperature(m_state[0]);
            m_wall[i]->syncCoverages(m_lr[i]);
            kin->getNetProductionRates(DATA_PTR(m_work));
            ns = kin->surfacePhaseIndex();
            surfloc = kin->kineticsSpeciesIndex(0,ns);
            for (size_t k = 1; k < nk; k++) {
                ydot[loc + k] = m_work[surfloc+k]*rs0*surf->size(k);
                sum -= ydot[loc + k];
            }
            ydot[loc] = sum;
            loc += nk;

            wallarea = m_wall[i]->area();
            for (size_t k = 0; k < m_nsp; k++) {
                m_sdot[k] += m_work[k]*wallarea;
            }
        }
    }

    const vector_fp& mw = m_thermo->molecularWeights();
    const doublereal* Y = m_thermo->massFractions();

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

    double mdot_surf = 0.0; // net mass flux from surface
    for (size_t k = 0; k < m_nsp; k++) {
        // production in gas phase and from surfaces
        dYdt[k] = (m_wdot[k] * m_vol + m_sdot[k]) * mw[k] / m_mass;
        mdot_surf += m_sdot[k] * mw[k];
    }
    dmdt += mdot_surf;

    // external heat transfer
    mcpdTdt -= m_Q;

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

    // add terms for open system
    if (m_open) {
        // outlets
        for (size_t i = 0; i < m_nOutlets; i++) {
            dmdt -= m_outlet[i]->massFlowRate(time); // mass flow out of system
        }

        // inlets
        for (size_t i = 0; i < m_nInlets; i++) {
            double mdot_in = m_inlet[i]->massFlowRate(time);
            dmdt += mdot_in; // mass flow into system
            mcpdTdt += 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;
                mcpdTdt -= m_hk[n] / mw[n] * mdot_spec;
            }
        }
    }

    ydot[0] = dmdt;
    if (m_energy) {
        ydot[1] = mcpdTdt / (m_mass * m_thermo->cp_mass());
    } else {
        ydot[1] = 0.0;
    }

    // reset sensitivity parameters
    if (params) {
        npar = m_pnum.size();
        for (size_t n = 0; n < npar; n++) {
            mult = m_kin->multiplier(m_pnum[n]);
            m_kin->setMultiplier(m_pnum[n], mult/params[n]);
        }
        ploc = npar;
        for (size_t m = 0; m < m_nwalls; m++) {
            if (m_nsens_wall[m] > 0) {
                m_wall[m]->resetSensitivityParameters(m_lr[m]);
                ploc += m_nsens_wall[m];
            }
        }
    }
}

size_t IdealGasConstPressureReactor::componentIndex(const string& nm) const
{
    if (nm == "T") {
        return 1;
    } else {
        return ConstPressureReactor::componentIndex(nm);
    }

}

}