PDRFoam.C
Go to the documentation of this file.
1/*---------------------------------------------------------------------------*\
2 ========= |
3 \\ / F ield | OpenFOAM: The Open Source CFD Toolbox
4 \\ / O peration |
5 \\ / A nd | www.openfoam.com
6 \\/ M anipulation |
7-------------------------------------------------------------------------------
8 Copyright (C) 2011-2017 OpenFOAM Foundation
9-------------------------------------------------------------------------------
10License
11 This file is part of OpenFOAM.
12
13 OpenFOAM is free software: you can redistribute it and/or modify it
14 under the terms of the GNU General Public License as published by
15 the Free Software Foundation, either version 3 of the License, or
16 (at your option) any later version.
17
18 OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
19 ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
20 FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
21 for more details.
22
23 You should have received a copy of the GNU General Public License
24 along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
25
26Application
27 PDRFoam
28
29Group
30 grpCombustionSolvers
31
32Description
33 Solver for compressible premixed/partially-premixed combustion with
34 turbulence modelling.
35
36 Combusting RANS code using the b-Xi two-equation model.
37 Xi may be obtained by either the solution of the Xi transport
38 equation or from an algebraic expression. Both approaches are
39 based on Gulder's flame speed correlation which has been shown
40 to be appropriate by comparison with the results from the
41 spectral model.
42
43 Strain effects are incorporated directly into the Xi equation
44 but not in the algebraic approximation. Further work need to be
45 done on this issue, particularly regarding the enhanced removal rate
46 caused by flame compression. Analysis using results of the spectral
47 model will be required.
48
49 For cases involving very lean Propane flames or other flames which are
50 very strain-sensitive, a transport equation for the laminar flame
51 speed is present. This equation is derived using heuristic arguments
52 involving the strain time scale and the strain-rate at extinction.
53 the transport velocity is the same as that for the Xi equation.
54
55 For large flames e.g. explosions additional modelling for the flame
56 wrinkling due to surface instabilities may be applied.
57
58 PDR (porosity/distributed resistance) modelling is included to handle
59 regions containing blockages which cannot be resolved by the mesh.
60
61 The fields used by this solver are:
62 \plaintable
63 betav | Volume porosity
64 Lobs | Average diameter of obstacle in cell (m)
65 Aw | Obstacle surface area per unit volume (1/m)
66 CR | Drag tensor (1/m)
67 CT | Turbulence generation parameter (1/m)
68 Nv | Number of obstacles in cell per unit volume (m^-2)
69 nsv | Tensor whose diagonal indicates the number to subtract from
70 | Nv to get the number of obstacles crossing the flow in each
71 | direction.
72 \endplaintable
73
74\*---------------------------------------------------------------------------*/
75
76#include "fvCFD.H"
77#include "psiuReactionThermo.H"
79#include "laminarFlameSpeed.H"
80#include "XiModel.H"
81#include "PDRDragModel.H"
82#include "ignition.H"
83#include "bound.H"
84#include "pimpleControl.H"
85#include "fvOptions.H"
86
87// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
88
89int main(int argc, char *argv[])
90{
91 argList::addNote
92 (
93 "Solver for compressible premixed/partially-premixed combustion with"
94 " turbulence modelling."
95 );
96
97 #include "postProcess.H"
98
99 #include "addCheckCaseOptions.H"
100 #include "setRootCaseLists.H"
101 #include "createTime.H"
102 #include "createMesh.H"
103 #include "createControl.H"
104 #include "readCombustionProperties.H"
105 #include "readGravitationalAcceleration.H"
106 #include "createFields.H"
107 #include "createFieldRefs.H"
108 #include "initContinuityErrs.H"
109 #include "createTimeControls.H"
110 #include "compressibleCourantNo.H"
111 #include "setInitialDeltaT.H"
112
113 turbulence->validate();
114 scalar StCoNum = 0.0;
115
116 // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
117
118 Info<< "\nStarting time loop\n" << endl;
119
120 while (runTime.run())
121 {
122 #include "readTimeControls.H"
123 #include "compressibleCourantNo.H"
124 #include "setDeltaT.H"
125
126 ++runTime;
127 Info<< "\n\nTime = " << runTime.timeName() << endl;
128
129 #include "rhoEqn.H"
130
131 // --- Pressure-velocity PIMPLE corrector loop
132 while (pimple.loop())
133 {
134 #include "UEqn.H"
135
136 // --- Pressure corrector loop
137 while (pimple.correct())
138 {
139 #include "bEqn.H"
140 #include "ftEqn.H"
141 #include "EauEqn.H"
142 #include "EaEqn.H"
143
144 if (!ign.ignited())
145 {
146 thermo.heu() == thermo.he();
147 }
148
149 #include "pEqn.H"
150 }
151
152 if (pimple.turbCorr())
153 {
154 turbulence->correct();
155 }
156 }
157
158 runTime.write();
159
160 runTime.printExecutionTime(Info);
161 }
162
163 Info<< "End\n";
164
165 return 0;
166}
167
168
169// ************************************************************************* //
Required Classes.
Bound the given scalar field if it has gone unbounded.
pimpleControl & pimple
Basic thermodynamics type based on the use of fitting functions for cp, h, s obtained from the templa...
engineTime & runTime
Required Variables.
Read the control parameters used by setDeltaT.
compressible::turbulenceModel & turbulence
messageStream Info
Information stream (stdout output on master, null elsewhere)
Ostream & endl(Ostream &os)
Add newline and flush stream.
Definition: Ostream.H:372
Execute application functionObjects to post-process existing results.
Read the control parameters used by setDeltaT.