[version 12][version 11][version 10][version 9][version 8][version 7][version 6]
2.2 Breaking of a dam
In this example we shall solve a problem of a simplified dam break in 2 dimensions using the incompressibleVoF modular solver. The feature of the problem is a transient flow of two fluids separated by a sharp interface, or free surface. The two-phase algorithm in incompressibleVoF is based on the volume of fluid (VoF) method in which a phase transport equation is used to determine the relative volume fraction of the two phases, or phase fraction , in each computational cell. Physical properties are calculated as weighted averages based on this fraction. The nature of the VoF method means that an interface between the phases is not explicitly computed, but rather emerges as a property of the phase fraction field. Since the phase fraction can have any value between 0 and 1, the interface is never precisely defined, but occupies a volume around the region where a sharp interface should exist.
The test setup consists of a column of water at rest located behind a membrane on the left side of a tank. At time , the membrane is removed and the column of water collapses. During the collapse, the water impacts an obstacle at the bottom of the tank and creates a complicated flow structure, including several captured pockets of air. The geometry and the initial setup is shown in Figure 2.15 .
2.2.1 Mesh generation
The user should go to their run directory and copy the damBreak case from the $FOAM_TUTORIALS/incompressibleVoF/damBreakLaminar directory, i.e.
run
cp -r $FOAM_TUTORIALS/incompressibleVoF/damBreakLaminar/damBreak .
17
18vertices
19(
20 (0 0 0)
21 (2 0 0)
22 (2.16438 0 0)
23 (4 0 0)
24 (0 0.32876 0)
25 (2 0.32876 0)
26 (2.16438 0.32876 0)
27 (4 0.32876 0)
28 (0 4 0)
29 (2 4 0)
30 (2.16438 4 0)
31 (4 4 0)
32 (0 0 0.1)
33 (2 0 0.1)
34 (2.16438 0 0.1)
35 (4 0 0.1)
36 (0 0.32876 0.1)
37 (2 0.32876 0.1)
38 (2.16438 0.32876 0.1)
39 (4 0.32876 0.1)
40 (0 4 0.1)
41 (2 4 0.1)
42 (2.16438 4 0.1)
43 (4 4 0.1)
44);
45
46blocks
47(
48 hex (0 1 5 4 12 13 17 16) (23 8 1) simpleGrading (1 1 1)
49 hex (2 3 7 6 14 15 19 18) (19 8 1) simpleGrading (1 1 1)
50 hex (4 5 9 8 16 17 21 20) (23 42 1) simpleGrading (1 1 1)
51 hex (5 6 10 9 17 18 22 21) (4 42 1) simpleGrading (1 1 1)
52 hex (6 7 11 10 18 19 23 22) (19 42 1) simpleGrading (1 1 1)
53);
54
55defaultPatch
56{
57 type empty;
58}
59
60boundary
61(
62 leftWall
63 {
64 type wall;
65 faces
66 (
67 (0 12 16 4)
68 (4 16 20 8)
69 );
70 }
71 rightWall
72 {
73 type wall;
74 faces
75 (
76 (7 19 15 3)
77 (11 23 19 7)
78 );
79 }
80 lowerWall
81 {
82 type wall;
83 faces
84 (
85 (0 1 13 12)
86 (1 5 17 13)
87 (5 6 18 17)
88 (2 14 18 6)
89 (2 3 15 14)
90 );
91 }
92 atmosphere
93 {
94 type patch;
95 faces
96 (
97 (8 20 21 9)
98 (9 21 22 10)
99 (10 22 23 11)
100 );
101 }
102);
103
104
105// ************************************************************************* //
The mesh is written into a set of files in a polyMesh directory in the constant directory. The use can list the contents of the directory to reveal the set of files/
ls constant/polyMesh
2.2.2 Boundary conditions
The boundary file can be read and understood by the user. The user should take a look at its contents, either by opening it in a file editor or printing out in the terminal window using the cat utility.
cat constant/polyMesh/boundary
The leftWall, rightWall and lowerWall patches are each a wall. Like the generic patch, the wall type contains no geometric or topological information about the mesh and only differs from the plain patch in that it identifies the patch as a wall. This is required by some modelling, e.g. turbulent wall functions and some turbulence models which include the distance to the nearest wall in their calculations.
With VoF specifically, surface tension models can include wall adhesion at the contact point between the interface and wall surface. Wall adhesion models can be applied through a special boundary condition on the alpha () field, e.g. the constantAlphaContactAngle boundary condition, which requires the user to specify a static contact angle, theta0.
This example ignores surface tension effects between the wall and interface. This can be done can do this by setting the static contact angle, , but a simpler approach is to apply the zeroGradient condition to alpha on the walls.
The top boundary is free to the atmosphere so needs to permit both outflow and inflow according to the internal flow. We therefore use a combination of boundary conditions for pressure and velocity that does this while maintaining stability. They are:
- prghTotalPressure, applied to the pressure field, minus the hydrostatic component, , given by Equation 6.3 ;
- pressureInletOutletVelocity, applied to velocity , which sets zeroGradient on all components of , except where there is inflow, in which case a fixedValue condition is applied to the tangential component;
- inletOutlet applied to other fields, which is a zeroGradient condition when flow outwards, fixedValue when flow is inwards.
At all wall boundaries, the fixedFluxPressure boundary condition is applied to the pressure field, which adjusts the pressure gradient so that the boundary flux matches the velocity boundary condition for solvers that include body forces such as gravity and surface tension.
The defaultFaces patch representing the front and back planes of the 2D problem, is, as usual, an empty type.
2.2.3 Phases
The fluid phases are specified in the phaseProperties file in the constant directory as follows:
17phases (water air);
18
19sigma 0.07;
20
21
22// ************************************************************************* //
It lists two phases, water and air. Equations for phase fraction are solved for the phases in the list, except the last phase listed, i.e. air in this case. Since there are only two phases, only one phase fraction equation is solved in this case, for the water phase fraction , specified in the file alpha.water in the 0 directory.
The phaseProperties file also contains an entry for the surface tension between the two phases, specified by the keyword sigma in units .
2.2.4 Setting initial fields
Unlike the previous cases, we shall now specify a non-uniform initial condition for the phase fraction where
|
(2.5) |
17defaultFieldValues
18(
19 volScalarFieldValue alpha.water 0
20);
21
22regions
23(
24 boxToCell
25 {
26 box (0 0 -1) (0.1461 0.292 1);
27 fieldValues
28 (
29 volScalarFieldValue alpha.water 1
30 );
31 }
32);
33
34
35// ************************************************************************* //
The defaultFieldValues sets the default value of the fields, i.e. the value the field takes unless specified otherwise in the regions list. That list contains sub-dictionaries with fieldValues that override the defaults in a specified region. Regions are defined by functions that define a set of points, faces, or cells. Here boxToCell creates a box defined by minimum and maximum bounds that defines the set of cells of the water region. The phase fraction is specified as 1 in this region.
The setFields utility reads fields from file and, after re-calculating those fields, will write them back to file. In the damBreak case, the alpha.water field is initially stored in its original form with the name alpha.water.orig. A field file with the .orig extension is read in when the actual file does not exist, so setFields will read alpha.water.orig but write the resulting output to alpha.water (or alpha.water.gz if compression is switched on). This way the original file is not overwritten, so can be reused.
The user should execute setFields like any other utility by:
setFields
2.2.5 Fluid properties
The physical properties for the air and water phases are specified in physicalProperties.air and physicalProperties.water files, respectively, in the constant directory. Physical properties describe characteristics of the fluid in a absence of flow. Each file specifies the viscosity model through the viscosityModel keyword, which is set to constant to indicate the value is unchanging. The viscosity is then specified by the nu keyword in units . The density of each fluid is also specified by the keyword rho in units . The physicalProperties.air file is shown below as an example:
17viscosityModel constant;
18
19nu 1.48e-05;
20
21rho 1;
22
23
24// ************************************************************************* //
If the viscosity does change according to the flow, e.g. as in non-Newtonian or visco-elastic fluids, then those models are specified through the momentumProperties file, as described in section 8.3 .
2.2.6 Gravity
Gravitational acceleration is uniform across the domain and is specified in a file named g in the constant directory. Unlike a normal field file, e.g. U and p, g is a uniformDimensionedVectorField and so simply contains a set of dimensions and a value that represents for this case:
17dimensions [0 1 -2 0 0 0 0];
18value (0 -9.81 0);
19
20
21// ************************************************************************* //
2.2.7 Turbulence modelling
As in the cavity example, the choice of turbulence modelling method is selectable at run-time through the simulationType keyword in momentumTransport dictionary. In this example, we wish to run without turbulence modelling so we set laminar:
17simulationType laminar;
18
19
20// ************************************************************************* //
2.2.8 Time step control
The simulation of the damBreak case is fully transient so the time step requires attention. The Courant number is an important consideration relating to time step. It is dimensionless parameter which can be defined for each cell as:
|
(2.6) |
Time step control is particularly important with interface-capturing. The incompressibleVoF solver module uses the multidimensional universal limiter for explicit solution (MULES), created by Henry Weller, to maintain boundedness of the phase fraction. needs to be limited depending on the choice of MULES algorithm. With the original explicit MULES algorithm, an upper limit of for stability is typically required. However, there is also the semi-implicit version of MULES, specified by the MULESCorr switch in the fvSolution file. For semi-implicit MULES, there is really no upper limit in for stability, but instead the level is determined by requirements of temporal accuracy.
In general it is difficult to specify a fixed time-step to satisfy the criterion since is changing from cell to cell during the simulation. Instead, automatic adjustment of the time step is specified in the controlDict by switching adjustTimeStep to on and specifying the maximum for the phase fields, maxAlphaCo, and other fields, maxCo. In this example, the maxAlphaCo and maxCo are set to 1.0. The upper limit on time step maxDeltaT can be set to a value that will not be exceeded in this simulation, e.g. 1.0.
By using automatic time step control, the steps themselves are never rounded to a convenient value. Consequently if we request that OpenFOAM saves results at a fixed number of time step intervals, the times at which results are saved are somewhat arbitrary. However with automatic time step adjustment, results can be written at fixed times using the adjustableRunTime option for writeControl in the controlDict dictionary. With this option, the automatic time stepping procedure further adjusts their time steps so that it ‘hits’ on the exact times specified by the writeInterval, set to 0.05 in this example. The controlDict dictionary entries are shown below.
17application foamRun;
18
19solver incompressibleVoF;
20
21startFrom startTime;
22
23startTime 0;
24
25stopAt endTime;
26
27endTime 1;
28
29deltaT 0.001;
30
31writeControl adjustableRunTime;
32
33writeInterval 0.05;
34
35purgeWrite 0;
36
37writeFormat binary;
38
39writePrecision 6;
40
41writeCompression off;
42
43timeFormat general;
44
45timePrecision 6;
46
47runTimeModifiable yes;
48
49adjustTimeStep yes;
50
51maxCo 1;
52maxAlphaCo 1;
53
54maxDeltaT 1;
55
56
57// ************************************************************************* //
2.2.9 Discretisation schemes
The MULES method, used by the incompressibleVoF modular solver, maintains boundedness of the phase fraction independently of the underlying numerical scheme, mesh structure, etc. The choice of schemes for convection are therefore not restricted to those that are strongly stable or bounded, such as upwind differencing.
The convection schemes settings are made in the divSchemes sub-dictionary of the fvSchemes dictionary. In this example, the convection term in the momentum equation, , denoted by the div(rhoPhi,U) keyword, uses Gauss linearUpwind grad(U) to produce good accuracy.
The term, represented by the div(phi,alpha) keyword uses a bespoke interfaceCompression scheme where the specified coefficient is a factor that controls the compression of the interface where: 0 corresponds to no compression; 1 corresponds to conservative compression; and, anything larger than 1, relates to enhanced compression of the interface. We generally use a value of 1.0, as in this example.
The other discretised terms use commonly employed schemes so that the fvSchemes dictionary entries is as follows.
17ddtSchemes
18{
19 default Euler;
20}
21
22gradSchemes
23{
24 default Gauss linear;
25}
26
27divSchemes
28{
29 div(rhoPhi,U) Gauss linearUpwind grad(U);
30 div(phi,alpha) Gauss interfaceCompression vanLeer 1;
31 div(((rho*nuEff)*dev2(T(grad(U))))) Gauss linear;
32}
33
34laplacianSchemes
35{
36 default Gauss linear corrected;
37}
38
39interpolationSchemes
40{
41 default linear;
42}
43
44snGradSchemes
45{
46 default corrected;
47}
48
49
50// ************************************************************************* //
2.2.10 Linear-solver control
In the fvSolution file, the sub-dictionary in solvers for alpha.water contains elements that are specific to the MULES algorithm as shown below.
{
nAlphaCorr 2;
nAlphaSubCycles 1;
MULESCorr yes;
nLimiterIter 5;
solver smoothSolver;
smoother symGaussSeidel;
tolerance 1e-8;
relTol 0;
}
MULES calculates two limiters to keep the phase fraction within the lower and upper bounds of 0 and 1. The limiter calculation is iterative, with the number of iterations specified by nLimiterIter. As a rule of thumb, nLimiterIter can be set to 3 + to maintain boundedness.
The semi-implicit version of MULES is activated by the MULESCorr switch. It first calculates an implicit, upwind solution before applying MULES as a higher-order correction. The linear solver must be configured for the implicit, upwind solution, through the solver, smoother, tolerance and relTol parameters.
The nAlphaCorr keyword which controls the number of iterations of the phase fraction equation within a solution step. The iteration is used to overcome nonlinearities in the advection which are present in this case due to the interfaceCompression scheme.
2.2.11 Running the code
Running of the code has been described in the previous tutorial. Try the following, that uses tee, a command that enables output to be written to both standard output and files:
cd $FOAM_RUN/damBreak
foamRun | tee log
2.2.12 Post-processing
Post-processing of the results can now be done in the usual way. The user can monitor the development of the phase fraction alpha.water in time, e.g. see Figure 2.17 .
2.2.13 Running in parallel
The results from the previous example are generated using a fairly coarse mesh. We now wish to increase the mesh resolution and re-run the case. Using a finer mesh, we can then demonstrate the parallel processing capability of OpenFOAM.
The user should first clone the damBreak case, e.g. by
run
foamCloneCase damBreak damBreakFine
blocks
(
hex (0 1 5 4 12 13 17 16) (46 10 1) simpleGrading (1 1 1)
hex (2 3 7 6 14 15 19 18) (40 10 1) simpleGrading (1 1 1)
hex (4 5 9 8 16 17 21 20) (46 76 1) simpleGrading (1 2 1)
hex (5 6 10 9 17 18 22 21) (4 76 1) simpleGrading (1 2 1)
hex (6 7 11 10 18 19 23 22) (40 76 1) simpleGrading (1 2 1)
);
As the mesh has now changed from the damBreak example, the user must re-initialise the phase field alpha.water in the 0 time directory since it contains a number of elements that is inconsistent with the new mesh. Note that there is no need to change the U and p_rgh fields since they are specified as uniform which is independent of the number of elements in the field.
The user should then rerun the setFields utility. However, the mesh size is now inconsistent with the number of elements in the alpha.water file in the 0 directory, so the user must delete that file so that setFields uses the original alpha.water.orig file.
rm 0/alpha.water
setFields
Parallel computing uses domain decomposition, in which the geometry and associated fields are broken into pieces and allocated to separate processors for solution. The first step required to run a parallel case is therefore to decompose the domain using the decomposePar utility. There is a dictionary associated with decomposePar named decomposeParDict which is located in the system directory. Also, sample dictionaries can be found within the etc directory in the OpenFOAM installation, which can be copied to the case directory by running the foamGet script, e.g. (you do not need to do this):
foamGet decomposeParDict
The first entry is numberOfSubdomains which specifies the number of subdomains into which the case will be decomposed, usually corresponding to the number of processors available for the case.
This example uses the simple method of decomposition. It requires the simpleCoeffs to be configured according to the following criteria. The domain is split into pieces, or subdomains, in the , and directions, the number of subdomains in each direction being given by the vector . As this geometry is 2 dimensional, the 3rd direction, , cannot be split, hence must equal 1. The and components of split the domain in the and directions and must be specified so that the number of subdomains specified by and equals the specified numberOfSubdomains, i.e. numberOfSubdomains.
It is beneficial to keep the number of cell faces adjoining the subdomains to a minimum so, for a square geometry, it is best to keep the split between the and directions should be fairly even. For example, let us assume we wish to run on 4 processors. We would set numberOfSubdomains to 4 and n to (2, 2, 1). The user should run decomposePar by the following command.
decomposePar
This example presents running in parallel with the openMPI implementation of the standard message-passing interface (MPI). The following command runs on 4 cores of a local multi-processor CPU.
mpirun -np 4 foamRun -parallel
2.2.14 Post-processing a case run in parallel
When the case runs in parallel, the results are written into time directories within the processor<N> sub-directories. The user can confirm this by listing the time directories for the processor0 directory.
ls processor0
It is possible to post-process an individual sub-domain by treating the individual processor directory as a case in its own right. For example, to view the processor1 sub-domain in ParaView, the user can launch paraFoam by running the following command.
paraFoam -case processor1
Alternatively, the decomposed fields and mesh can be reassembled for post-processing in serial. The reconstructPar utility takes the field files from time directories for the processor sub-domain and builds equivalent field files for the complete domain. The user should run the utility as follows.
reconstructPar