Convection_Diffusion_Concentration_FT_Disc.h

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#ifndef Convection_Diffusion_Concentration_FT_Disc_included
#define Convection_Diffusion_Concentration_FT_Disc_included
 
#include <Convection_Diffusion_Concentration.h>
#include <TRUST_Ref.h>
#include <ArrOfBit.h>
 
/*! @brief Cette equation corrige le champ de concentration pour tenir compte de la presence d'une interface.
 *
 * @sa Convection_Diffusion_Concentration
 */
class Convection_Diffusion_Concentration_FT_Disc : public Convection_Diffusion_Concentration
{
  Declare_instanciable_sans_constructeur(Convection_Diffusion_Concentration_FT_Disc);
public:
 
  Convection_Diffusion_Concentration_FT_Disc();
  void set_param(Param& titi) const override;
  int lire_motcle_non_standard(const Motcle&, Entree&) override;
  void     mettre_a_jour(double temps) override;
 
protected:
  void ramasse_miette_simple(double temps);
  void mettre_a_jour_chimie();
  void multiplier_valeurs_faces(const ArrOfBit marqueurs_faces, double facteur, double& integrale_avant, DoubleTab& tab);
  void marquer_faces_sous_domaine(const Nom& nom_sous_domaine,
                                  ArrOfBit& marqueur,
                                  int sans_faces_non_std_volume_nul) const;
 
  // Algorithme a utiliser pour tenir compte des interfaces:
  enum Options { RIEN = 0, RAMASSE_MIETTES_SIMPLE = 1 };
  Options option_;
  // Dans quelle phase la masse du constituant se trouve-t-elle (RAMASSE_MIETTES_SIMPLE)
  int phase_a_conserver_;
 
  // Quelle equation du probleme fournit l'indicatrice de phase ?
  OBS_PTR(Equation_base) ref_eq_transport_;
 
  // Liste non vide => cette equation modelise le produit de la reaction avec les equations
  //  dont la liste contient les noms:
  Noms equations_source_chimie_;
  // Constantes cinetiques
  double constante_cinetique_;
  double constante_cinetique_nu_t_;
  Nom nom_equation_nu_t_;
  // Modele pour taux de reactions
  int modele_cinetique_;
  // Domaine de sortie ou on annule la concentration
  Nom nom_domaine_sortie_;
};
#endif