Fluide_Dilatable_base.h

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#ifndef Fluide_Dilatable_base_included
#define Fluide_Dilatable_base_included
 
#include <EDO_Pression_th_base.h>
#include <EOS_Tools_base.h>
 
#include <Loi_Etat_base.h>
#include <Fluide_base.h>
#include <TRUST_Deriv.h>
#include <TRUST_Ref.h>
 
 
class Probleme_base;
 
/*! @brief Base class for a dilatable fluid, inheriting from Fluide_base.
 *
 * @sa Milieu_base Fluide_base
 */
 
class Fluide_Dilatable_base : public Fluide_base
{
  Declare_base(Fluide_Dilatable_base);
public :
  void verifier_coherence_champs(int& err,Nom& message) override;
  void set_Cp(double);
  void update_rho_cp(double temps) override;
  void creer_champs_non_lus() override;
  void initialiser_radiatives(const double temps);
  void warn_syntax_Sutherland();
  int initialiser(const double temps) override;
 
  const DoubleTab& temperature() const;
  const Champ_Don_base& ch_temperature() const;
  Champ_Don_base& ch_temperature();
 
  virtual void calculer_pression_tot();
  void preparer_pas_temps();
  void abortTimeStep() override;
  void set_param(Param& param) const override;
  void discretiser(const Probleme_base& pb, const  Discretisation_base& dis) override;
  void mettre_a_jour(double ) override;
  virtual void update_pressure_fields(double );
  void preparer_calcul() override;
  virtual void completer(const Probleme_base&);
  int lire_motcle_non_standard(const Motcle&, Entree&) override;
  virtual void checkTraitementPth(const Domaine_Cl_dis_base&);
  void prepare_pressure_edo();
  virtual void write_mean_edo(double);
  virtual void write_header_edo();
 
  // Pure virtual methods
  virtual void secmembre_divU_Z(DoubleTab& ) const=0;
  virtual void Resoudre_EDO_PT()=0;
 
  // Post-processing field interface methods
  const Champ_base& get_champ(const Motcle& nom) const override;
  void creer_champ(const Motcle& motlu) override;
  bool has_champ(const Motcle& nom, OBS_PTR(Champ_base) &ref_champ) const override;
  bool has_champ(const Motcle& nom) const override;
  void get_noms_champs_postraitables(Noms& nom,Option opt=NONE) const override;
 
  // Inline methods
  inline const Nom type_fluide() const { return loi_etat_->type_fluide(); }
  inline const OWN_PTR(Loi_Etat_base)& loi_etat() const { return loi_etat_; }
  inline OWN_PTR(Loi_Etat_base)&  loi_etat() { return loi_etat_; }
  inline const Champ_Inc_base& inco_chaleur() const { return ch_inco_chaleur_.valeur(); }
  inline Champ_Inc_base& inco_chaleur() { return ch_inco_chaleur_.valeur(); }
  inline const Champ_Inc_base& vitesse() const { return ch_vitesse_.valeur(); }
  inline const Champ_Don_base& pression_tot() const { return ch_pression_tot_; }
  inline Champ_Don_base& pression_tot() { return ch_pression_tot_; }
  inline const Champ_Don_base& mu_sur_Schmidt() const { return ch_mu_sur_Sc; }
  inline Champ_Don_base& mu_sur_Schmidt() { return ch_mu_sur_Sc; }
  inline const Champ_Don_base& nu_sur_Schmidt() const { return ch_nu_sur_Sc; }
  inline Champ_Don_base& nu_sur_Schmidt() { return ch_nu_sur_Sc; }
  inline const Champ_Don_base& source_masse_espece() const { assert (ch_source_masse_esp_); return ch_source_masse_esp_; }
  inline Champ_Don_base& source_masse_espece() { assert (ch_source_masse_esp_); return ch_source_masse_esp_; }
  inline const Champ_Don_base& source_masse_projection() const { assert (ch_source_masse_proj_); return ch_source_masse_proj_; }
  inline Champ_Don_base& source_masse_projection() { assert (ch_source_masse_proj_); return ch_source_masse_proj_; }
 
  inline bool has_source_masse_espece_champ() const { return bool(ch_source_masse_esp_); }
  inline bool has_source_masse_projection_champ() const { return bool(ch_source_masse_proj_); }
 
  inline const  DoubleTab& rho_n() const { return loi_etat_->rho_n(); }
  inline const  DoubleTab& rho_np1() const { return loi_etat_->rho_np1(); }
  inline void calculer_coeff_T();
  inline void initialiser_inco_ch() { loi_etat_->initialiser_inco_ch(); }
  inline void calculer_Cp() { loi_etat_->calculer_Cp(); }
  inline void calculer_lambda() { loi_etat_->calculer_lambda(); }
  inline void calculer_mu() { loi_etat_->calculer_mu(); }
  inline void calculer_nu() override { loi_etat_->calculer_nu(); }
  inline void calculer_alpha() override { loi_etat_->calculer_alpha(); }
  inline void calculer_mu_sur_Sc() { loi_etat_-> calculer_mu_sur_Sc(); }
  inline void calculer_nu_sur_Sc() { loi_etat_-> calculer_nu_sur_Sc(); }
  inline void calculer_masse_volumique() { loi_etat_->calculer_masse_volumique(); }
  inline void set_pression_th(double Pth) { Pth_n_ = Pth_ = Pth; }
  inline int getTraitementPth() const { return traitement_PTh_; }
  inline double pression_th() const { return Pth_; } // Thermodynamic pressure
  inline const double& get_pression_th() const { return Pth_; } // Reference to thermodynamic pressure (for PDI, can't share a copy...)
  inline double pression_thn() const { return Pth_n_; } // Thermodynamic pressure at the previous time step
  inline double pression_th1() const { return Pth1_; } // Thermodynamic pressure computed to conserve mass
  inline double calculer_H(double hh) const { return loi_etat_->calculer_H(Pth_,hh); }
 
  // Inline methods from EOS_Tools
  inline Probleme_base& get_problem() { return le_probleme_.valeur(); }
  inline const DoubleTab& rho_discvit() const { return eos_tools_->rho_discvit(); }
  inline const DoubleTab& rho_face_n() const { return eos_tools_->rho_face_n(); }
  inline const DoubleTab& rho_face_np1() const { return eos_tools_->rho_face_np1(); }
  inline void calculer_rho_face(const DoubleTab& tab_rho) { eos_tools_->calculer_rho_face_np1(tab_rho); }
  inline void divu_discvit(DoubleTab& secmem1, DoubleTab& secmem2) { eos_tools_->divu_discvit(secmem1,secmem2); }
  inline double moyenne_vol(const DoubleTab& A) const { return eos_tools_->moyenne_vol(A); }
 
  bool is_dilatable() const override { return true; }
 
protected :
  virtual void remplir_champ_pression_tot(int n, const DoubleTab& PHydro, DoubleTab& PTot) = 0;
  void completer_edo(const Probleme_base& );
 
  int traitement_PTh_ = 0; // flag for the treatment of thermodynamic pressure
  double Pth_ = -1., Pth_n_ = -1., Pth1_ = -1.;
  OBS_PTR(Champ_Inc_base) ch_inco_chaleur_, ch_vitesse_, ch_pression_;
  OBS_PTR(Probleme_base) le_probleme_;
  OWN_PTR(Champ_Don_base) ch_pression_tot_, ch_mu_sur_Sc, ch_nu_sur_Sc, ch_rho_gaz_, ch_rho_comme_v_;
  OWN_PTR(Champ_Don_base) ch_source_masse_esp_, ch_source_masse_proj_; /* si besoin */
  OWN_PTR(Loi_Etat_base) loi_etat_;
  OWN_PTR(EOS_Tools_base) eos_tools_;
  OWN_PTR(EDO_Pression_th_base) EDO_Pth_;
  Nom output_file_;
};
 
inline void Fluide_Dilatable_base::calculer_coeff_T()
{
  loi_etat_->remplir_T();
  calculer_Cp();
  calculer_mu();
  calculer_lambda();
  calculer_nu();
  calculer_alpha();
  calculer_mu_sur_Sc();
  calculer_nu_sur_Sc();
}
 
#endif /* Fluide_Dilatable_base_included */