TrioCFD 1.9.9_beta
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Portance_interfaciale_VDF.cpp
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15
16#include <Portance_interfaciale_base.h>
17#include <Portance_interfaciale_VDF.h>
18#include <Milieu_composite.h>
19#include <Champ_Face_VDF.h>
20#include <Pb_Multiphase.h>
21
22Implemente_instanciable(Portance_interfaciale_VDF, "Portance_interfaciale_VDF_Face", Source_Portance_interfaciale_base);
23
24Sortie& Portance_interfaciale_VDF::printOn(Sortie& os) const { return os; }
26
27void Portance_interfaciale_VDF::ajouter_blocs(matrices_t matrices, DoubleTab& secmem, const tabs_t& semi_impl) const
28{
29 const Pb_Multiphase& pbm = ref_cast(Pb_Multiphase, equation().probleme());
30 const bool res_en_T = pbm.resolution_en_T();
31 if (!res_en_T) Process::exit("Portance_interfaciale_VDF::ajouter_blocs NOT YET PORTED TO ENTHALPY EQUATION ! TODO FIXME !!");
32
33 const Champ_Face_VDF& ch = ref_cast(Champ_Face_VDF, equation().inconnue());
34 const Domaine_VDF& domaine = ref_cast(Domaine_VDF, equation().domaine_dis());
35 const IntTab& f_e = domaine.face_voisins(), &e_f = domaine.elem_faces(), &fcl = ch.fcl();
36 const DoubleTab& n_f = domaine.face_normales(), &vf_dir = domaine.volumes_entrelaces_dir(), &xv = domaine.xv();
37 const DoubleVect& pf = equation().milieu().porosite_face(), &vf = domaine.volumes_entrelaces(), &fs = domaine.face_surfaces();
38 const DoubleTab& pvit = ch.passe(),
39 &alpha = pbm.equation_masse().inconnue().passe(),
40 &press = ref_cast(QDM_Multiphase, pbm.equation_qdm()).pression().passe(),
41 &temp = pbm.equation_energie().inconnue().passe(),
42 &rho = equation().milieu().masse_volumique().passe(),
43 &mu = ref_cast(Fluide_base, equation().milieu()).viscosite_dynamique().passe(),
44 &grad_v = equation().probleme().get_champ("gradient_vitesse").valeurs(),
45 &vort = equation().probleme().get_champ("vorticite").valeurs(),
46 * d_bulles = (equation().probleme().has_champ("diametre_bulles")) ? &equation().probleme().get_champ("diametre_bulles").valeurs() : nullptr,
47 * k_turb = (equation().probleme().has_champ("k")) ? &equation().probleme().get_champ("k").passe() : nullptr ;
48 const Milieu_composite& milc = ref_cast(Milieu_composite, equation().milieu());
49
50 int e, f, c, d, i, k, l, n, N = ch.valeurs().line_size(), Np = press.line_size(), D = dimension, Nk = (k_turb) ? (*k_turb).dimension(1) : 1 ,
51 cR = (rho.dimension_tot(0) == 1), cM = (mu.dimension_tot(0) == 1);
52 DoubleTrav vr_l(N,D), scal_ur(N), scal_u(N), pvit_l(N, D), vort_l( D==2 ? 1 :D); // Required for vorticity and u_l-u_g corrections
53 double fac_f, vl_norm;
54 const Portance_interfaciale_base& correlation_pi = ref_cast(Portance_interfaciale_base, correlation_.valeur());
55
56 // Past velocity at elements
57 DoubleTab pvit_elem(0, N * dimension);
58 domaine.domaine().creer_tableau_elements(pvit_elem);
59 ch.get_elem_vector_field(pvit_elem, true);
60
61 // in/out for correlation
64 in.alpha.resize(N), in.T.resize(N), in.p.resize(N), in.rho.resize(N), in.mu.resize(N), in.sigma.resize(N*(N-1)/2), in.k_turb.resize(N), in.d_bulles.resize(N), in.nv.resize(N, N);
65 out.Cl.resize(N, N);
66
67 // For the span methods of the Interface class to retrieve the surface tension
68 const int nbelem_tot = domaine.nb_elem_tot(), nb_max_sat = N * (N-1) /2; // yes!! arithmetic sequence!!
69 DoubleTrav Sigma_tab(nbelem_tot,nb_max_sat);
70
71 // fill the arrays ...
72 for (k = 0; k < N; k++)
73 for (l = k + 1; l < N; l++)
74 {
75 if (milc.has_saturation(k, l))
76 {
77 Saturation_base& z_sat = milc.get_saturation(k, l);
78 const int ind_trav = (k*(N-1)-(k-1)*(k)/2) + (l-k-1); // Yes! upper triangular matrix!
79 // retrieve sigma ...
80 const DoubleTab& sig = z_sat.get_sigma_tab();
81 // fill in the good case
82 for (int ii = 0; ii < nbelem_tot; ii++) Sigma_tab(ii, ind_trav) = sig(ii);
83 }
84 else if (milc.has_interface(k, l))
85 {
86 Interface_base& sat = milc.get_interface(k,l);
87 const int ind_trav = (k*(N-1)-(k-1)*(k)/2) + (l-k-1); // Yes! upper triangular matrix!
88 for (i = 0 ; i<nbelem_tot ; i++)
89 Sigma_tab(i,ind_trav) = res_en_T ? sat.sigma(temp(i,k),press(i,k * (Np > 1))) : sat.sigma_h(temp(i,k),press(i,k * (Np > 1)));
90 }
91 }
92
93
94 for (f = 0 ; f<domaine.nb_faces() ; f++)
95 if (fcl(f, 0) < 2)
96 {
97 in.alpha=0., in.T=0., in.p=0., in.rho=0., in.mu=0., in.sigma=0., in.k_turb=0., in.d_bulles=0., in.nv=0.;
98 for ( c = 0; c < 2 ; c++)
99 if ((e = f_e(f, c)) >= 0 )
100 {
101 for (n = 0; n < N; n++)
102 {
103 in.alpha[n] += vf_dir(f, c)/vf(f) * alpha(e, n);
104 in.p[n] += vf_dir(f, c)/vf(f) * press(e, n * (Np > 1));
105 in.T[n] += vf_dir(f, c)/vf(f) * temp(e, n); // FIXME SI res_en_T
106 in.rho[n] += vf_dir(f, c)/vf(f) * rho(!cR * e, n);
107 in.mu[n] += vf_dir(f, c)/vf(f) * mu(!cM * e, n);
108 in.d_bulles[n] += (d_bulles) ? vf_dir(f, c)/vf(f) *(*d_bulles)(e,n) : 0 ;
109 for (k = n+1; k < N; k++)
110 if (milc.has_interface(n,k))
111 {
112 const int ind_trav = (n*(N-1)-(n-1)*(n)/2) + (k-n-1);
113 in.sigma[ind_trav] += vf_dir(f, c) / vf(f) * Sigma_tab(e, ind_trav);
114 }
115 for (k = 0; k < N; k++)
116 in.nv(k, n) += vf_dir(f, c)/vf(f) * ch.v_norm(pvit_elem, pvit, e, f, k, n, nullptr, nullptr);
117 }
118 for (n = 0; n <Nk; n++) in.k_turb[n] += (k_turb) ? vf_dir(f, c)/vf(f) * (*k_turb)(e,0) : 0;
119 }
120
121 correlation_pi.coefficient(in, out);
122
123 // What about n_l != 0?
124 vort_l = 0;
125
126 if ( (f_e(f, 0)<0) || (f_e(f,1)<0) ) vort_l(0) = f_e(f, 0)>=0 ? vort(f_e(f, 0), n_l) : vort(f_e(f, 1), n_l) ;
127 else
128 {
129 {
130 int orif = domaine.orientation(f);
131 DoubleTrav grad_loc(D);
132 for ( c = 0; c < 2 ; c++)
133 {
134 e = f_e(f, c);
135 for ( d = 0 ; d < e_f.line_size() ; d++)
136 {
137 int fb = e_f(e,d);
138 int orifb = domaine.orientation(fb);
139 if (orifb != orif) grad_loc(orifb) += .25*pvit(fb, n_l)/(xv(fb, orif)-xv(f, orif));
140 }
141 }
142 DoubleTrav grad_ll(D,D);
143 for ( c = 0; c < 2 ; c++)
144 for (int d_U=0; d_U<D; d_U++)
145 for (int d_X=0; d_X<D; d_X++)
146 grad_ll(d_U,d_X) += grad_v( e, N * ( D*d_U+d_X ) + n_l) * vf_dir(f, c)/vf(f);
147 for (int oril = 0 ; oril<D ; oril++)
148 if (oril != orif)
149 grad_ll(oril,orif) = grad_loc(oril);
150 if (D==2) vort_l(0) = grad_ll(1,0) - grad_ll(0,1);
151 else // (D==3)
152 {
153 vort_l(0) = grad_ll(2, 1) - grad_ll(1, 2); // dUz/dy - dUy/dz
154 vort_l(1) = grad_ll(0, 2) - grad_ll(2, 0); // dUx/dz - dUz/dx
155 vort_l(2) = grad_ll(1, 0) - grad_ll(0, 1); // dUy/dx - dUx/dy
156 }
157 }
158 }
159
160 // We also need to calculate relative velocity at the face
161 pvit_l = 0 ;
162 for (d = 0 ; d<D ; d++)
163 for (k = 0 ; k<N ; k++)
164 for ( c = 0; c < 2 ; c++)
165 if ((e = f_e(f, c)) >= 0 )
166 pvit_l(k, d) += vf_dir(f, c)/vf(f)*pvit_elem(e, N*d+k) ;
167 scal_u = 0;
168 for (k = 0 ; k<N ; k++)
169 for (d = 0 ; d<D ; d++)
170 scal_u(k) += pvit_l(k, d)*n_f(f, d)/fs(f);
171 for (k = 0 ; k<N ; k++)
172 for (d = 0 ; d<D ; d++)
173 pvit_l(k, d) += (pvit(f, k) - scal_u(k)) * n_f(f, d)/fs(f) ; // Corect velocity at the face
174 vl_norm = 0;
175 scal_ur = 0;
176 for (d = 0 ; d < D ; d++) vl_norm += pvit_l(n_l, d)*pvit_l(n_l, d);
177 vl_norm = std::sqrt(vl_norm);
178 if (vl_norm > 1.e-6)
179 {
180 for (k = 0; k < N; k++)
181 for (d = 0 ; d < D ; d++) scal_ur(k) += pvit_l(n_l, d)/vl_norm * (pvit_l(k, d) -pvit_l(n_l, d));
182 for (k = 0; k < N; k++)
183 for (d = 0 ; d < D ; d++) vr_l(k, d) = pvit_l(n_l, d)/vl_norm * scal_ur(k) ;
184 }
185 else for (k=0 ; k<N ; k++)
186 for (d=0 ; d<D ; d++) vr_l(k, d) = pvit_l(k, d)-pvit_l(n_l, d) ;
187
188 if (D==2)
189 {
190 // Use local vairables for the calculation of secmem
191 fac_f = beta_*pf(f) * vf(f);
192 for (k = 0; k < N; k++)
193 if (k!= n_l) // gas phase
194 {
195 secmem(f, n_l) += fac_f * n_f(f, 0)/fs(f) * out.Cl(n_l, k) * vr_l(k, 1) * vort_l(0) ;
196 secmem(f, k ) -= fac_f * n_f(f, 0)/fs(f) * out.Cl(n_l, k) * vr_l(k, 1) * vort_l(0) ;
197 secmem(f, n_l) -= fac_f * n_f(f, 1)/fs(f) * out.Cl(n_l, k) * vr_l(k, 0) * vort_l(0) ;
198 secmem(f, k ) += fac_f * n_f(f, 1)/fs(f) * out.Cl(n_l, k) * vr_l(k, 0) * vort_l(0) ;
199 } // 100% explicit
200 }
201
202 if (D==3)
203 {
204 // Use local vairables for the calculation of secmem
205 fac_f = beta_*pf(f) * vf(f);
206 for (k = 0; k < N; k++)
207 if (k!= n_l) // gas phase
208 {
209 secmem(f, n_l) += fac_f * n_f(f, 0)/fs(f) * out.Cl(n_l, k) * (vr_l(k, 1) * vort_l(2) - vr_l(k, 2) * vort_l(1)) ;
210 secmem(f, k ) -= fac_f * n_f(f, 0)/fs(f) * out.Cl(n_l, k) * (vr_l(k, 1) * vort_l(2) - vr_l(k, 2) * vort_l(1)) ;
211 secmem(f, n_l) += fac_f * n_f(f, 1)/fs(f) * out.Cl(n_l, k) * (vr_l(k, 2) * vort_l(0) - vr_l(k, 0) * vort_l(2)) ;
212 secmem(f, k ) -= fac_f * n_f(f, 1)/fs(f) * out.Cl(n_l, k) * (vr_l(k, 2) * vort_l(0) - vr_l(k, 0) * vort_l(2)) ;
213 secmem(f, n_l) += fac_f * n_f(f, 2)/fs(f) * out.Cl(n_l, k) * (vr_l(k, 0) * vort_l(1) - vr_l(k, 1) * vort_l(0)) ;
214 secmem(f, k ) -= fac_f * n_f(f, 2)/fs(f) * out.Cl(n_l, k) * (vr_l(k, 0) * vort_l(1) - vr_l(k, 1) * vort_l(0)) ;
215 } // 100% explicit
216 }
217 }
218}
class Champ_Face_VDF
double v_norm(const DoubleTab &val, const DoubleTab &val_f, int e, int f, int k, int l, double *v_ext, double *dnv) const
virtual DoubleTab & get_elem_vector_field(DoubleTab &, bool passe=false) const
const IntTab & fcl() const
DoubleTab & passe(int i=1) override
Returns field values at instant t-i.
DoubleTab & valeurs() override
Returns the array of field values at the current time.
virtual DoubleTab & valeurs()=0
virtual DoubleTab & passe(int i=1)
Definition Champ_Proto.h:50
class Domaine_VDF
Definition Domaine_VDF.h:61
Class defining operators and methods for all reading operation in an input flow (file,...
Definition Entree.h:42
virtual const Milieu_base & milieu() const =0
virtual const Champ_Inc_base & inconnue() const =0
Probleme_base & probleme()
Returns the problem associated with the equation.
Base class for an incompressible fluid and its properties:
Definition Fluide_base.h:36
double sigma_h(const double h, const double P) const
DoubleTab & get_sigma_tab()
double sigma(const double T, const double P) const
virtual const Champ_base & masse_volumique() const
Returns the mass density of the medium (const version).
DoubleVect & porosite_face()
Definition Milieu_base.h:62
Composite medium representing a multiphase fluid and its properties:
bool has_interface(int k, int l) const
bool has_saturation(int k, int l) const
Interface_base & get_interface(int k, int l) const
Saturation_base & get_saturation(int k, int l) const
const Equation_base & equation() const
Returns the reference to the equation pointed to by MorEqn::mon_equation.
Definition MorEqn.h:62
static int dimension
Definition Objet_U.h:94
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
Multiphase thermohydraulics problem of type "3*N equations":
virtual bool resolution_en_T() const
virtual Equation_base & equation_qdm()
virtual Equation_base & equation_energie()
virtual Equation_base & equation_masse()
void ajouter_blocs(matrices_t matrices, DoubleTab &secmem, const tabs_t &semi_impl={}) const override
Base class for interfacial lift force operators of the form:
virtual void coefficient(const input_t &input, output_t &output) const =0
bool has_champ(const Motcle &nom, OBS_PTR(Champ_base) &ref_champ) const override
const Champ_base & get_champ(const Motcle &nom) const override
static void exit(int exit_code=-1)
Exit routine for TRUST within a Kokkos region.
Definition Process.cpp:466
Carries the terms of the momentum equation for multiphase flow without turbulence modelling.
Base class for output streams.
Definition Sortie.h:52
Interfacial lift force source term of the form:
void resize(_SIZE_ n, RESIZE_OPTIONS opt=RESIZE_OPTIONS::COPY_INIT)
Definition TRUSTTab.tpp:469
int line_size() const
Definition TRUSTVect.tpp:67