IJK_Thermal_Multiple_Subresolutions.cpp

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#include <IJK_Thermal_Multiple_Subresolutions.h>
#include <Param.h>
#include <IJK_Navier_Stokes_tools.h>
#include <DebogIJK.h>
 
#include <Probleme_FTD_IJK.h>
#include <Corrige_flux_FT_base.h>
#include <OpConvDiscQuickIJKScalar.h>
 
Implemente_instanciable_sans_constructeur( IJK_Thermal_Multiple_Subresolutions, "IJK_Thermal_Multiple_Subresolutions", IJK_Thermal_Subresolution ) ;
 
IJK_Thermal_Multiple_Subresolutions::IJK_Thermal_Multiple_Subresolutions() {}
 
Sortie& IJK_Thermal_Multiple_Subresolutions::printOn( Sortie& os ) const
{
  IJK_Thermal_Subresolution::printOn( os );
  return os;
}
 
Entree& IJK_Thermal_Multiple_Subresolutions::readOn( Entree& is )
{
  IJK_Thermal_Subresolution::readOn( is );
  /*
   * The main phase is called liquid because it is mainly used in bubbly flows
   * It will directly influence which phase uses the temperature_ field attribute.
   * Correction of temperature_ and temperature_vap_ may be different
   */
  if (main_phase_)
    {
      uniform_lambda_vap_ = lambda_vapour_;
      uniform_alpha_vap_ = lambda_vapour_ / (ref_ijk_ft_->milieu_ijk().get_rho_vapour() * cp_vapour_);
    }
  else
    {
      uniform_lambda_vap_ = lambda_liquid_;
      uniform_lambda_ = lambda_vapour_;
      uniform_alpha_vap_ = lambda_liquid_ / (ref_ijk_ft_->milieu_ijk().get_rho_liquid() * cp_liquid_);
      uniform_alpha_ = lambda_vapour_ / (ref_ijk_ft_->milieu_ijk().get_rho_vapour() * cp_vapour_);
    }
  return is;
}
 
void IJK_Thermal_Multiple_Subresolutions::set_param( Param& param ) const
{
  param.ajouter_flag("main_phase_", &main_phase_);
}
 
void IJK_Thermal_Multiple_Subresolutions::initialize(const Domaine_IJK& splitting)
{
  Cout << que_suis_je() << "::initialize()" << finl;
 
  IJK_Thermal_Subresolution::initialize(splitting);
 
  temperature_vapour_.allocate(splitting, Domaine_IJK::ELEM, 2);
 
  compute_distance_ = compute_distance_ || ghost_fluid_;
 
  Cout << "End of " << que_suis_je() << "::initialize()" << finl;
}
 
void IJK_Thermal_Multiple_Subresolutions::update_thermal_properties()
{
  IJK_Thermal_Subresolution::update_thermal_properties();
}
 
void IJK_Thermal_Multiple_Subresolutions::correct_temperature_vapour_for_eulerian_fluxes()
{
  if (!ghost_fluid_)
    {
      if (override_vapour_mixed_values_)
        {
          const int ni = temperature_vapour_.ni();
          const int nj = temperature_vapour_.nj();
          const int nk = temperature_vapour_.nk();
          for (int k = 0; k < nk; k++)
            for (int j = 0; j < nj; j++)
              for (int i = 0; i < ni; i++)
                {
                  const double indic = ref_ijk_ft_->get_interface().I(i,j,k);
                  if (std::fabs(1.-indic)>1.e-8) // Mixed cells and pure vapour cells
                    { temperature_vapour_(i,j,k) = 0; }
                }
        }
// TODO: Temperature sub-resolution
//          else
//              {
//
//              }
    }
}