TrioCFD 1.9.9_beta
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Dispersion_bulles_turbulente_Burns.cpp
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15
16#include <Dispersion_bulles_turbulente_Burns.h>
17#include <Pb_Multiphase.h>
18#include <QDM_Multiphase.h>
19#include <TRUSTTrav.h>
20#include <Frottement_interfacial_base.h>
21#include <Sources_helpers_Multiphase.h>
22#include <math.h>
23
24Implemente_instanciable(Dispersion_bulles_turbulente_Burns, "Dispersion_bulles_turbulente_Burns", Dispersion_bulles_base);
25
27{
28 return os;
29}
30
32{
33 Param param(que_suis_je());
34 param.ajouter("minimum", &minimum_);
35 param.ajouter("a_res", &a_res_);
36 param.ajouter("g_", &g_);
37 param.ajouter("coefBIA_", &coefBIA_);
38 param.ajouter("Prt", &Prt_);
39 param.lire_avec_accolades_depuis(is);
40
42
43 const Pb_Multiphase& pbm = ref_cast(Pb_Multiphase, pb_.valeur());
44 if (pbm.has_correlation("frottement_interfacial"))
45 correlation_drag_ = pbm.get_correlation("frottement_interfacial");
46 else
47 Correlation_base::typer_lire_correlation(correlation_drag_, pbm, "frottement_interfacial", is);
48
49 return is;
50}
51
53{
54 if ((a_res_ == -1)
55 && (ref_cast(QDM_Multiphase, pb_->equation(0)).alpha_res()<0.99) ) // Not in homogeneous calculation
56 a_res_ = std::min(1., std::max(1.e-4, ref_cast(QDM_Multiphase, pb_->equation(0)).alpha_res()*100.));
57 else if (a_res_ == -1)
58 a_res_ = 1.e-6;
59}
60
62{
63 const Frottement_interfacial_base& corr = ref_cast(Frottement_interfacial_base, correlation_drag_.valeur());
64 int N = out.Ctd.dimension(0);
65
66 DoubleTrav coeff_drag(N, N, 2);
67 corr.coefficient(in.alpha, in.p, in.T, in.rho, in.mu, in.sigma, in.dh, in.nv, in.d_bulles, coeff_drag);
68
69 out.Ctd = 0;
70
71 for (int k = 0; k < N; k++)
72 if (k != n_l)
73 {
74 double nuBIA = 0.;
75
76 if ((bool)coefBIA_)
77 {
78 // Computation of nuBIA = (k_WIT + k_WIF)/omega_WIT
79 const double u_r = in.nv(k, n_l); // relative velocity
80 const double Reb = in.rho[n_l]*in.d_bulles[k]*u_r/in.mu[n_l]; // bubble Reynolds number
81 const int ind_trav = sigma_pair_index(k, n_l, N);
82 const double Eo = eotvos_number(g_, in.rho[n_l], in.rho[k], in.d_bulles[k], in.sigma[ind_trav]);
83 const double Cd = (u_r != 0) ? std::max(std::min(16./Reb*(1. + 0.15*std::pow(Reb, 0.687)), 48./Reb), 8.*Eo/(3.*(Eo + 4.))) : 0.; // if u_r=0, no drag, so no WIT, so dissipation=0
84 const double omega_WIT = 2.0*in.mu[n_l]*Cd*Reb/(C_lambda_*C_lambda_*in.d_bulles[k]*in.d_bulles[k]); // specific dissipation of WIT (defined as epsilon_WIT/kWIT)
85 //double k_WIF = 1./2. * in.alpha[k] * (u_r*u_r * 0.5 + 3./2.*0.25*gamma_*gamma_*gamma_); // energie cinetique turbulente de la composante WIF
86 nuBIA = coefBIA_ * (omega_WIT == 0.0 ? 0.0 : in.k_WIT/omega_WIT); // eddy viscosity equivalent for bubble induced agitation (BIA)
87 }
88
89 // Computation of turbulent dispersion coefficients
90 out.Ctd(k, n_l) = std::max(minimum_,
91 (in.alpha[k] > a_res_) ? (nuBIA + in.nut[n_l])/Prt_*coeff_drag(k, n_l, 0)/in.alpha[k] : (nuBIA + in.nut[n_l])/Prt_*coeff_drag(k, n_l, 0)*in.alpha[k]/(a_res_*a_res_));
92 out.Ctd(n_l, k) = std::max(minimum_,
93 (in.alpha[n_l] > a_res_) ? (nuBIA + in.nut[n_l])/Prt_*coeff_drag(n_l, k, 0)/in.alpha[n_l]: (nuBIA + in.nut[n_l])/Prt_*coeff_drag(n_l, k, 0)*in.alpha[n_l]/(a_res_*a_res_));
94 }
95}
static void typer_lire_correlation(OWN_PTR(Correlation_base)&, const Probleme_base &, const Nom &, Entree &)
Base class for turbulent bubble dispersion operators, where the force.
int find_liquid_phase() const
Finds the continuous liquid phase index in a multiphase problem.
class Dispersion_bulles_turbulente_Burns from Burns et al. (2004)Bubble turbulent dispersion coeffici...
void coefficient(const input_t &input, output_t &output) const override
Class defining operators and methods for all reading operation in an input flow (file,...
Definition Entree.h:42
Frottement_interfacial_base class: utility for interfacial friction operators taking the form.
virtual void coefficient(const DoubleTab &alpha, const DoubleTab &p, const DoubleTab &T, const DoubleTab &rho, const DoubleTab &mu, const DoubleTab &sigma, double Dh, const DoubleTab &ndv, const DoubleTab &d_bulles, DoubleTab &coeff) const =0
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
int has_correlation(std::string nom_correlation) const
const Correlation_base & get_correlation(std::string nom_correlation) const
Carries the terms of the momentum equation for multiphase flow without turbulence modelling.
Base class for output streams.
Definition Sortie.h:52
_SIZE_ dimension(int d) const
Definition TRUSTTab.tpp:133