TrioCFD 1.9.9_beta
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Multiplicateur_diphasique_Friedel.cpp
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15
16#include <Multiplicateur_diphasique_Friedel.h>
17#include <Pb_Multiphase.h>
18#include <cmath>
19
20Implemente_instanciable(Multiplicateur_diphasique_Friedel, "Multiplicateur_diphasique_Friedel", Multiplicateur_diphasique_base);
21
23{
24 return os;
25}
26
28{
29 Param param(que_suis_je());
30 param.ajouter("alpha_min", &alpha_min_);
31 param.ajouter("alpha_max", &alpha_max_);
32 param.ajouter("min_lottes_flinn", &min_lottes_flinn_);
33 param.ajouter("min_sensas", &min_sensas_);
34 param.lire_avec_accolades_depuis(is);
35
36 const Pb_Multiphase *pbm = sub_type(Pb_Multiphase, pb_.valeur()) ? &ref_cast(Pb_Multiphase, pb_.valeur()) : nullptr;
37
38 if (!pbm || pbm->nb_phases() == 1) n_l = 0, n_g = -1; //not a Pb_Multiphase -> single-phase liquid
39 else for (int n = 0; n < pbm->nb_phases(); n++) //search for n_l, n_g: continuous {liquid,gas} phase with priority
40 if (pbm->nom_phase(n).debute_par("liquide") && (n_l < 0 || pbm->nom_phase(n).finit_par("continu"))) n_l = n;
41 else if (pbm->nom_phase(n).debute_par("gaz") && (n_g < 0 || pbm->nom_phase(n).finit_par("continu"))) n_g = n;
42
43 if (n_l < 0) Process::exit(que_suis_je() + " : main phase not found!");
44
45 return is;
46}
47
48void Multiplicateur_diphasique_Friedel::coefficient(const double *alpha, const double *rho, const double *v, const double *f,
49 const double *mu, const double Dh, const double sigma, const double *Fk,
50 const double Fm, DoubleTab& coeff) const
51{
52 int min_ = min_sensas_ || min_lottes_flinn_;
53 double G = alpha[n_l] * rho[n_l] * std::fabs(v[n_l]) + alpha[n_g] * rho[n_g] * std::fabs(v[n_g]), //total mass flux
54 x = G ? alpha[n_g] * rho[n_g] * v[n_g] / G : 0, //quality
55 E = (1 - x) * (1 - x) + x * x * (rho[n_l] * f[n_g] / rho[n_g] / f[n_l]),
56 F = std::pow(x, 0.78) * std::pow(1 - x, 0.224),
57 H = std::pow(rho[n_l] / rho[n_g], 0.91) * std::pow(mu[n_g] / mu[n_l], 0.19) * std::pow(1 - mu[n_g] / mu[n_l], 0.7),
58 rho_m = 1.0 / (x / rho[n_g] + (1.0 - x) / rho[n_l]), //mixture density
59 Fr = G * G / (9.81 * Dh * rho_m * rho_m), We = G * G * Dh / (sigma * rho_m), //Froude, Weber,
60 Phi2 = E + 3.24 * F * H * std::pow(Fr, -0.0454) * std::pow(We, -0.035), //the multiplier!
61 frac_g = std::min(std::max((alpha[n_g] - alpha_min_) / (alpha_max_ - alpha_min_), 0.), 1.), frac_l = 1 - frac_g, //fraction applied to the vapor
62 mul = min_sensas_ ? std::min(1., 1.4429 * std::pow(alpha[n_l], 0.6492)) : 1;
63 coeff = 0;
64 if (min_ && Fk[n_l] * mul < Phi2 * Fm * (alpha[n_l] * alpha[n_l])) /* Lottes-Flinn/SENSAS gives a lower friction on the liquid -> use it*/
65 coeff(n_l, 0) = frac_l * min_ / (alpha[n_l] * alpha[n_l]), coeff(n_g, 0) = frac_g * min_ / (alpha[n_l] * alpha[n_l]);
66 else coeff(n_l, 1) = frac_l * Phi2, coeff(n_g, 1) = frac_g * Phi2; //applied to liquid and/or vapor
67}
Class defining operators and methods for all reading operation in an input flow (file,...
Definition Entree.h:42
Two-phase multiplier using the Friedel correlation:
void coefficient(const double *alpha, const double *rho, const double *v, const double *f, const double *mu, const double Dh, const double gamma, const double *Fk, const double Fm, DoubleTab &coeff) const override
Two-phase multiplier correlations of the form:
virtual int debute_par(const char *const n) const
Definition Nom.cpp:314
const Nom & que_suis_je() const
Returns the string identifying the class.
Definition Objet_U.cpp:104
virtual Entree & readOn(Entree &)
Reads an Objet_U from an input stream. Virtual method to override.
Definition Objet_U.cpp:289
virtual Sortie & printOn(Sortie &) const
Writes the object to an output stream. Virtual method to override.
Definition Objet_U.cpp:278
const Nom & nom_phase(int i) const
int nb_phases() const
static void exit(int exit_code=-1)
Exit routine for TRUST within a Kokkos region.
Definition Process.cpp:466
Base class for output streams.
Definition Sortie.h:52