TrioCFD 1.9.9_beta
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Correction_Tomiyama_PolyMAC_MPFA.cpp
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15
16#include <Correction_Tomiyama_PolyMAC_MPFA.h>
17#include <Champ_Face_PolyMAC_MPFA.h>
18#include <Milieu_composite.h>
19#include <Pb_Multiphase.h>
20#include <math.h>
21
22Implemente_instanciable(Correction_Tomiyama_PolyMAC_MPFA, "Correction_Tomiyama_Face_PolyMAC_MPFA", Source_base);
23// XD Correction_Tomiyama source_base Correction_Tomiyama BRACE Tomiyama correction source term for multiphase problem
24
26{
27 return os;
28}
29
31{
32 Param param(que_suis_je());
33 param.ajouter("secu_diam", &secu_diam_);
34 param.lire_avec_accolades_depuis(is);
35
36 //identification of phases
37 Pb_Multiphase *pbm = sub_type(Pb_Multiphase, equation().probleme()) ? &ref_cast(Pb_Multiphase, equation().probleme()) : nullptr;
38
39 if (!pbm || pbm->nb_phases() == 1) Process::exit(que_suis_je() + " : not needed for single-phase flow!");
40 for (int n = 0; n < pbm->nb_phases(); n++) //search for n_l, n_g : {liquid,gas}_continu phase with priority
41 if (pbm->nom_phase(n).debute_par("liquide") && (n_l < 0 || pbm->nom_phase(n).finit_par("continu"))) n_l = n;
42
43 if (n_l < 0) Process::exit(que_suis_je() + " : liquid phase not found!");
44
45 pbm->creer_champ("distance_paroi_globale"); // Need the wall distance field
46
47 return is;
48}
49
50void Correction_Tomiyama_PolyMAC_MPFA::completer() // We must wait for all readOn's to be sure that the bubble dispersion and lift correlations are created
51{
52 const Pb_Multiphase& pbm = ref_cast(Pb_Multiphase, equation().probleme());
53
54 if (!pbm.has_champ("diametre_bulles")) Process::exit("Correction_Lubchenko_PolyMAC_MPFA::completer() : a bubble diameter must be defined !");
55}
56
57void Correction_Tomiyama_PolyMAC_MPFA::ajouter_blocs(matrices_t matrices, DoubleTab& secmem, const tabs_t& semi_impl) const
58{
59 const Champ_Face_PolyMAC_MPFA& ch = ref_cast(Champ_Face_PolyMAC_MPFA, equation().inconnue());
60 const Milieu_composite& milc = ref_cast(Milieu_composite, equation().milieu());
61 const DoubleTab& pvit = ch.passe(),
62 &alpha = ref_cast(Pb_Multiphase, equation().probleme()).equation_masse().inconnue().passe(),
63 &rho = equation().milieu().masse_volumique().passe(),
64 &d_bulles = equation().probleme().get_champ("diametre_bulles").valeurs();
65 const Domaine_VF& domaine = ref_cast(Domaine_VF, equation().domaine_dis());
66 const IntTab& f_e = domaine.face_voisins(),
67 &fcl = ch.fcl();
68 const DoubleVect& pe = equation().milieu().porosite_elem(),
69 &pf = equation().milieu().porosite_face(),
70 &ve = domaine.volumes(),
71 &vf = domaine.volumes_entrelaces(),
72 &fs = domaine.face_surfaces();
73 const DoubleTab& vf_dir = domaine.volumes_entrelaces_dir(),
74 &n_f = domaine.face_normales(),
75 &y_elem = domaine.y_elem(),
76 &y_faces = domaine.y_faces(),
77 &n_y_elem = domaine.normale_paroi_elem(),
78 &n_y_faces = domaine.normale_paroi_faces();
79 int N = pvit.line_size() ,
80 D = dimension,
81 nf_tot = domaine.nb_faces_tot(),
82 nf = domaine.nb_faces(),
83 ne_tot = domaine.nb_elem_tot();
84
85 DoubleTrav dv(N, N), pvit_l(N,D), scal_u(N), sigma_l(N,ne_tot) ;
86 int e, f, c, k, d, i;
87
88 double fac, a_l, rho_l, rho_k, db_l, secmem_l, Eo, Cw, dist, correction, sig_face;
89
90 // And for the span methods of the Saturation class
91 for (k = 0; k < N; k++)
92 {
93 if (milc.has_saturation(k, n_l))
94 {
95 const Saturation_base& z_sat = milc.get_saturation(k, n_l);
96 const DoubleTab& sig = z_sat.get_sigma_tab();
97 for (int ii = 0; ii < ne_tot; ii++) sigma_l(k,ii) = sig(ii);
98 }
99 else if (milc.has_interface(k, n_l))
100 {
101 Interface_base& sat = milc.get_interface(k,n_l);
102 const DoubleTab& sig = sat.get_sigma_tab();
103 for (int ii = 0; ii < ne_tot; ii++) sigma_l(k,ii) = sig(ii);
104 }
105 }
106
107 for (f = 0; f < nf; f++)
108 if (fcl(f, 0) < 2)
109 {
110 // Calculation of correct velocity at the face
111 pvit_l = 0 ;
112 for (d = 0 ; d<D ; d++)
113 for (k = 0 ; k<N ; k++)
114 for (c=0 ; c<2 && (e = f_e(f, c)) >= 0; c++)
115 pvit_l(k, d) += vf_dir(f, c)/vf(f)*pvit(nf_tot+D*e+d, k) ;
116 scal_u = 0;
117 for (k = 0 ; k<N ; k++)
118 for (d = 0 ; d<D ; d++)
119 scal_u(k) += pvit_l(k, d)*n_f(f, d)/fs(f);
120 for (k = 0 ; k<N ; k++)
121 for (d = 0 ; d<D ; d++)
122 pvit_l(k, d) += (pvit(f, k) - scal_u(k)) * n_f(f, d)/fs(f) ;
123
124 // Retract component normal to the wall
125 scal_u = 0;
126 for (k = 0 ; k<N ; k++)
127 for (d = 0 ; d<D ; d++)
128 scal_u(k) += pvit_l(k, d)*n_y_faces(f, d);
129 for (k = 0 ; k<N ; k++)
130 for (d = 0 ; d<D ; d++)
131 pvit_l(k, d) -= scal_u(k)*n_y_faces(f, d) ;
132
133 // Calculation of liquid-gas velocity difference
134 dv = 0.;
135 for ( k = 0; k < N; k++)
136 if (k != n_l)
137 {
138 for (d = 0 ; d<D ; d++) dv(k, n_l) += (pvit_l(k, d)-pvit_l(n_l, d)) * (pvit_l(k, d)-pvit_l(n_l, d));
139 dv(k, n_l) = std::sqrt(dv(k, n_l));
140 }
141
142 for (k = 0; k < N; k++)
143 if (k != n_l)
144 {
145 fac = 0 ;
146 for (d = 0 ; d<D ; d++) fac += n_y_faces(f, d) * n_f(f, d)/fs(f);
147
148 fac *= pf(f) * vf(f) ;
149 a_l = ( alpha(f_e(f, 0), k)*vf_dir(f,0) + ((e = f_e(f, 1))>0 ? alpha(e, k)*vf_dir(f,1) : 0) ) / vf(f);
150 rho_l=( rho(f_e(f, 0), n_l)*vf_dir(f,0) + ((e = f_e(f, 1))>0 ? rho(e, n_l)*vf_dir(f,1) : 0) ) / vf(f);
151 rho_k=( rho(f_e(f, 0), k)*vf_dir(f,0) + ((e = f_e(f, 1))>0 ? rho(e, k)*vf_dir(f,1) : 0) ) / vf(f);
152 db_l= ( d_bulles(f_e(f, 0), k)*vf_dir(f,0) + ((e = f_e(f, 1))>0 ? d_bulles(e, k)*vf_dir(f,1):0) ) / vf(f);
153 sig_face = (sigma_l(k,f_e(f, 0)) * vf_dir(f,0) + ((e = f_e(f, 1))>0 ? sigma_l(k,e)*vf_dir(f,1) : 0) ) / vf(f) ;
154
155 Eo = ( rho_l - rho_k ) * g_ * 2. * db_l / sig_face ;
156
157 dist = std::max(y_faces(f), secu_diam_ * db_l);
158 correction = std::max(1.- y_faces(f)/db_l, 0.) ;
159
160 if (Eo < 1.) {Cw = 0.74 ;}
161 else if (Eo < 5.) {Cw = exp(-0.933 * Eo + 0.179) ;}
162 else if (Eo < 33.) {Cw = 0.00599 * Eo -0.187 ;}
163 else {Cw = 0.179 ;}
164
165 secmem_l = fac * a_l * rho_l * dv(k,n_l) * dv(k,n_l) * db_l / 2. * Cw / dist / dist * correction ;
166
167 secmem(f, k) += secmem_l;
168 secmem(f, n_l) -= secmem_l;
169 }
170
171 }
172
173 for ( e = 0; e < ne_tot; e++)
174 {
175 pvit_l = 0;
176 // Fill velocity at the element
177 for (d = 0 ; d<D ; d++)
178 for (k = 0 ; k<N ; k++)
179 pvit_l(k, d) += pvit(nf_tot+D*e+d, k) ;
180
181 // Retract component normal to the wall
182 scal_u = 0;
183 for (k = 0 ; k<N ; k++)
184 for (d = 0 ; d<D ; d++)
185 scal_u(k) += pvit_l(k, d)*n_y_elem(e, d);
186 for (k = 0 ; k<N ; k++)
187 for (d = 0 ; d<D ; d++)
188 pvit_l(k, d) -= scal_u(k)*n_y_elem(e, d) ;
189
190 // Calculation of norm of velocity
191 dv = 0.;
192 for ( k = 0; k < N; k++)
193 if (k != n_l)
194 {
195 for (d = 0 ; d<D ; d++) dv(k, n_l) += (pvit_l(k, d)-pvit_l(n_l, d)) * (pvit_l(k, d)-pvit_l(n_l, d));
196 dv(k, n_l) = std::sqrt(dv(k, n_l));
197 }
198
199 for (k = 0; k < N; k++)
200 if (k != n_l)
201 {
202 fac = pe(e) * ve(e) ;
203 Eo = ( rho(e, n_l) - rho(e, k) ) * g_ * 2. * d_bulles(e, k) / sigma_l(k,e) ;
204
205
206 dist = std::max(y_elem(e), secu_diam_ * d_bulles(e, k)); // numerical safety threshold
207 correction = std::max(1.- y_elem(e)/d_bulles(e, k), 0.) ;
208
209 if (Eo < 1.) {Cw = 0.74 ;}
210 else if (Eo < 5.) {Cw = exp(-0.933 * Eo + 0.179) ;}
211 else if (Eo < 33.) {Cw = 0.00599 * Eo -0.187 ;}
212 else {Cw = 0.179 ;}
213
214 secmem_l = fac * alpha(e,k) * rho(e,n_l) * dv(k,n_l) * dv(k,n_l) * d_bulles(e, k) / 2. * Cw / dist / dist * correction ;
215
216 for ( d = 0, i = nf_tot + D * e; d < D; d++, i++)
217 {
218 secmem(i , k) += secmem_l * n_y_elem(e, d);
219 secmem(i , n_l) -= secmem_l * n_y_elem(e, d);
220 }
221 }
222 }
223}
: class Champ_Face_PolyMAC_MPFA
const IntTab & fcl() const
DoubleTab & passe(int i=1) override
Returns field values at instant t-i.
virtual DoubleTab & valeurs()=0
virtual DoubleTab & passe(int i=1)
Definition Champ_Proto.h:50
class Correction_Tomiyama_PolyMAC_MPFA
void completer() override
Updates internal references of the Source_base object.
void ajouter_blocs(matrices_t matrices, DoubleTab &secmem, const tabs_t &semi_impl={}) const override
class Domaine_VF
Definition Domaine_VF.h:44
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
Probleme_base & probleme()
Returns the problem associated with the equation.
DoubleTab & get_sigma_tab()
DoubleVect & porosite_elem()
Definition Milieu_base.h:58
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
virtual int debute_par(const char *const n) const
Definition Nom.cpp:314
static int dimension
Definition Objet_U.h:94
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
Multiphase thermohydraulics problem of type "3*N equations":
const Nom & nom_phase(int i) const
int nb_phases() const
bool has_champ(const Motcle &nom, OBS_PTR(Champ_base) &ref_champ) const override
void creer_champ(const Motcle &motlu) 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
Base class for output streams.
Definition Sortie.h:52
Source_base A Source_base object is a term appearing on the right-hand side of an.
Definition Source_base.h:42
int line_size() const
Definition TRUSTVect.tpp:67