Depending on the type of problem you choose, TRUST will solve different sets of equation. It is therefore key to identify which problem corresponds to your application.

Inside the problem bloc, the user have to define first the medium he wants to consider. The medium specified in the bloc should be coherent with the instantiated problem, otherwise you will not be able to run your test case. For example, defining an incompressible medium in a conduction problem is not possible.

After defining the medium, the user should precise the equations he is willing to solve. The equation should be also coherent with the instantiated problem otherwise TRUST will exit with an error message. For example, defining a Navier-Stokes equation in a conduction problem is not possible.

Once the problem, medium and equations are defined, the user will have to specify the post-processing of the current case. Go check-out the Post-Processing section for more informations regarding the post-processing in TRUST.

In this section, the most used problems are introduced. For documentation and for complete problem sets, see Keywords Reference Manual

Conduction Problem

For this kind of problems, TRUST solves the heat equation:

\[\rho C_p \frac{\partial T}{\partial t} = \nabla \cdot \left(\lambda \nabla T\right) + Q \]

where:

\(\rho\): density,
\(C_p\): specific heat capacity at constant pressure,
\(\lambda\): thermal conductivity,
\(Q\) is a heat source term.

Options of Conduction problems

Problem type	Possible mediums	Possible Equations
Pb_Conduction	Solide	Conduction

Example of a Pb_conduction block

Here is an example of a Pb_conduction, taken from the docond_VEF.data file:

# Read a conduction problem pb #
    Read pb 
    {
        # Read solid medium #
        Solide
        {
            rho Champ_Uniforme 1 1000.
            lambda Champ_Uniforme 1 250.
            Cp Champ_Uniforme 1 100.
        }
        
        # Read conduction equation #
        Conduction
        {
            diffusion { }
            initial_conditions { temperature Champ_Uniforme 1 30. }
            boundary_conditions 
            {
                paroi_a_40 paroi_temperature_imposee Champ_Front_Uniforme 1 40.
                paroi_a_20 paroi_temperature_imposee Champ_Front_Uniforme 1 20.
                Paroi_echange paroi_contact pb2 Paroi_echange
            }
        }
        
        # Read post-processing #
        Post_processing
        {
            Probes
            {
                sonde_tsol temperature periode 1. points 2 0.15 0.55 0.55 0.15
                sonde_segs temperature periode 5. segment 10 0. 0.75 0.3 0.75
            }
            fields dt_post 300.
            {
                temperature elem
            }
        }
        
        # Save the data at the end of the calculation to resume later #
        sauvegarde formatte solide.rep
    }

Hydraulic and Thermohydraulics problems

The hydraulic and thermohydraulic problems solve the incompressible Navier-Stokes equation with more or less terms. Complementary transport equations can also be added.

\[\left\{ \begin{array}{c} \nabla \cdot \vec u = 0 \\ \displaystyle{\frac{\partial \vec u}{\partial t} + \nabla \cdot (\vec u \otimes \vec u) + \nabla P^*= \nabla \cdot (\nu \nabla \vec u) } \end{array} \right. \]

Incompressible Navier-Stokes equation, referred as Navier_Stokes_standard in TRUST

\[\displaystyle{\frac{\partial T}{\partial t} + \vec u \nabla T = \nabla \cdot (\alpha \nabla T) + \frac{Q}{\rho C_p}} \]

Heat equation, referred as Convection_Diffusion_Temperature in TRUST

\[\displaystyle{\frac{\partial X}{\partial t} + \vec u \nabla X} = 0 \]

Passive scalar transport equation, referred as Convection_Diffusion_Concentration in TRUST

Where: \(P^* = \frac{P}{\rho} + g z\), \(Q\) is the heat source term, and:

\(\rho\): density
\(\mu\): dynamic viscosity
\(\nu = \frac{\mu}{\rho}\): kinematic viscosity
\(\vec{g} = g z\): gravity vector in cartesian coordinates
\(\alpha = \frac{\lambda}{\rho C_p}\): thermic diffusivity
\(C_p\): specific heat capacity at constant pressure
\(\lambda\): thermic conductivity
\(X\): a transported scalar quantity

Note: Red terms corresponds to convective terms and blue terms to diffusive terms.

Options of Hydraulic and Thermohydraulics problems

Problem type	Possible mediums	Possible Equations
Pb_Hydraulique	Fluide_Incompressible or Fluide_Ostwald	Navier_Stokes_standard
Pb_Hydraulique_Concentration	Fluide_Incompressible or Fluide_Ostwald	Navier_Stokes_standard + Convection_Diffusion_Concentration
Pb_Hydraulique_Concentration_Scalaires_Passifs	Fluide_Incompressible or Fluide_Ostwald	Navier_Stokes_standard + N additional Convection_Diffusion_Concentration
Pb_Thermohydraulique	Fluide_Incompressible or Fluide_Ostwald	Navier_Stokes_standard + Convection_Diffusion_Temperature
Pb_Thermohydraulique_Concentration	Fluide_Incompressible or Fluide_Ostwald	Navier_Stokes_standard + Convection_Diffusion_Temperature + Convection_Diffusion_Concentration
Pb_Thermohydraulique_Concentration_Scalaires_Passifs	Fluide_Incompressible or Fluide_Ostwald	Navier_Stokes_standard + Convection_Diffusion_Temperature + N additional Convection_Diffusion_Concentration

Important remarks:

for Hydraulique or Thermohydraulique problems, an additional Constituant medium should be secondly defined if you ask for a problem with concentration.

Example of a Pb_Thermohydraulique block

Here is an example of Pb_Thermohydraulique, taken from the Source_Generique_PolyMAC test case:

# Read a thermal hydraulic problem pb #
Read pb
{
    # Read incompressible medium #
    fluide_incompressible 
    {
        gravite champ_uniforme 2 0 -9.81
        mu Champ_Uniforme 1 1.85e-5
        rho Champ_Uniforme 1 1.17
        lambda Champ_Uniforme 1 0.0262
        Cp Champ_Uniforme 1 1006
        beta_th Champ_Uniforme 1 3.41e-3
    }
    
    # Read NS equation #
    Navier_Stokes_standard
    {
        solveur_pression petsc gcp { precond null { } seuil 1e30 }
        convection { negligeable }
        diffusion { negligeable }
        initial_conditions { vitesse Champ_Uniforme 2 0. 0. }
        boundary_conditions 
        {
            Obstacle paroi_fixe
            Symetrie symetrie
            Sortie frontiere_ouverte_pression_imposee Champ_front_Uniforme 1 0.
            Entree frontiere_ouverte_vitesse_imposee  Champ_front_Uniforme 2  1. 0.
        }
        sources 
        {
            Source_Qdm Champ_fonc_xyz dom 2 x y
        }
    }
         
    # Read Temperature equation #
    Convection_Diffusion_Temperature
    {
        diffusion { negligeable }
        convection { negligeable }
        boundary_conditions
        {
            Symetrie    paroi_adiabatique
            Obstacle    paroi_adiabatique
            Entree      frontiere_ouverte_temperature_imposee Champ_front_Fonc_xyz 1 1
            Sortie  frontiere_ouverte_temperature_imposee Champ_front_Fonc_xyz 1 0
        }
        initial_conditions { Temperature Champ_Fonc_xyz dom 1 0 }
        sources 
        {
            Puissance_Thermique champ_fonc_xyz dom 1 50+x+y
        }
    }
    
     # Read post-processings #
    Postraitement
    {
        fields dt_post 1e10
        {
            temperature elem
            vitesse elem
            pressure elem
        }
    }
}

Low Mach Number Problems

The Mach number \(Ma = u / c\) measures the ratio of the bulk velocity to the local speed of sound. Typically for \(Ma < 0.1\), the compressibility effects can be neglected and the physical problem may be reduced by using a Low Mach Number formulation. In such cases, the aspect of the problem orients towards simulating a mass variation rather than capturing and solving for the acoustic waves. This is basically the main hypothesis of a Low Mach Number approximation where all acoustic waves are filtered out.

Following a single scale asymptotic analysis referring to the Mach number, the zero Mach order equations are considered where the total pressure is decomposed into a thermodynamic pressure and a hydrodynamic pressure that fluctuates in an order of \(Ma^2\). Note that the hydrodynamic pressure is much smaller than the thermodynamic one. The hydrodynamic pressure alone is used in the momentum equation, while the thermodynamic is used in the equation of state.

TRUST offers two Low Mach Number modelisations; either a Weakly-Compressible (WC) or a Quasi-Compressible (QC) models. The main difference between both models is that the QC model considers a space-uniform thermodynamic pressure. This is not the case in the WC model where the total pressure, which is space/time varying, is used in the equation of state. The last can have a great impact in some situations as the pressure drop and/or the hydro-static pressure can influence significantly the density variation.

The system of equation associated with Low Mach number problem writes:

\[\left\{ \begin{array}{c} \displaystyle{\frac{\partial \rho }{\partial t} + \nabla \cdot (\rho \vec u) =0 }\\ \displaystyle{ \frac{\partial \rho \vec u}{\partial t} + \nabla \cdot (\rho \vec u \vec u) = \nabla \cdot \left(\mu \nabla \vec u \right) - \nabla P -\rho \vec g }\\ \displaystyle{ \rho C_p \left( \frac{\partial T}{\partial t} + \vec u \nabla T \right) = \nabla \cdot \left(\lambda \nabla T\right) + \frac{dP_{tot}}{dt} + Q } \end{array} \right. \]

where: \(P_{tot}=\rho R T\), \(Q\) is a heat source term, and:

\(\rho\): density,
\(\mu\): dynamic viscosity,
\(\vec g=g z\): gravity vector in cartesian coordinates,
\(C_p\): specific heat capacity at constant pressure,
\(\lambda\): thermal conductivity.

Note: Red terms are convective terms and blue terms are diffusive terms.

Remark: The difference between Hydraulique and Thermohydraulique type of problem is whether the last equation of the system (that drive the temperature) is taken into account or not. If it is taken into account you'll have to use a Thermohydraulique type of problem.

Valid .data options for WC and QC problems

Problem type	Possible mediums	Possible Equations
Pb_Hydraulique_Melange_Binaire_QC	Fluide_Quasi_Compressible	Navier_Stokes_QC + Convection_Diffusion_Espece_Binaire_QC
Pb_Hydraulique_Melange_Binaire_WC	Fluide_Quasi_Compressible	Navier_Stokes_WC + Convection_Diffusion_Espece_Binaire_WC
Pb_Thermohydraulique_QC	Fluide_Quasi_Compressible	Navier_Stokes_QC + Convection_Diffusion_Chaleur_QC
Pb_Thermohydraulique_WC	Fluide_Quasi_Compressible	Navier_Stokes_WC + Convection_Diffusion_Chaleur_WC
Pb_Thermohydraulique_Especes_QC	Fluide_Quasi_Compressible	Navier_Stokes_QC + Convection_Diffusion_Chaleur_QC + N additional Convection_Diffusion_Espece_Multi_QC
Pb_Thermohydraulique_Especes_WC	Fluide_Quasi_Compressible	Navier_Stokes_WC + Convection_Diffusion_Chaleur_WC + N additional Convection_Diffusion_Espece_Multi_WC

Example of a Pb_Thermohydraulique_QC block

Here is an example of Pb_thermohydraulique_qc, taken from the DarcyFlow_QC_VDF test case:

Read pb
{
 
    fluide_quasi_compressible {
        pression 111582.205714
        loi_etat gaz_parfait_QC
        {
            Cp 1006.8
            gamma 1.4
            Prandtl 0.494112177122
            rho_constant_pour_debug champ_uniforme 1 1.293
        }
        traitement_pth constant
        traitement_rho_gravite moins_rho_moyen
        mu champ_uniforme 1 1.33e-05
    }
 
    Navier_stokes_qc
    {
        solveur_pression petsc Cholesky { }
        convection { negligeable }
        diffusion { negligeable }
        initial_conditions
        {
            vitesse champ_uniforme 3 0.0 0.2 0.0
        }
        boundary_conditions
        {
            Entree frontiere_ouverte_vitesse_imposee champ_front_uniforme 3 0.0 0.2 0.0
            Sortie frontiere_ouverte_pression_imposee champ_front_uniforme 1 0.0
            Bord paroi_fixe
        }
        sources
        {
            darcy { porosite 0.4 modele_K ErgunDarcy { diametre 1.5e-3 } } ,
            forchheimer { porosite 0.4 Cf 1. modele_K ErgunForchheimer { diametre 1.5e-3 } }
        }
    }
    convection_diffusion_chaleur_qc
    {
        convection { negligeable }
        diffusion { negligeable }
        initial_conditions
        {
            temperature champ_uniforme 1 300.0
        }
        boundary_conditions
        {
            Entree frontiere_ouverte_temperature_imposee champ_front_uniforme 1 300.0
            Sortie frontiere_ouverte T_ext champ_front_uniforme 1 300.0
            Bord paroi_adiabatique
        }
    }
    Post_processing
    {
        Probes
        {
            sonde_vitesse       nodes   vitesse periode 0.0001 point 1 0.08 0.10 0.08
            segment_pression    grav    pression_pa periode 0.0001 segment 50 0.08 0.05 0.08 0.08 0.20 0.08
        }
        Format lata fields dt_post 0.1
        {
            pression_pa elem
        }
    }
}

Multi-Phase Problem

The multiphase type of problem is simply called Pb_Multiphase. This problem allows the resolution of N-phases via a model of 3N equations, based on a Ishii types of model.

An instance of the medium Milieu_composite is required at the begining of the problem's bloc. Inside the medium bloc, you can define any medium. For example, you can define a Fluide_Incompressible or any child class of the Fluide_reel_base class.

An additional Correlations bloc should be secondly defined. Each and every correlations derive from the base class Corellation_base.

Afterwards, the reading of the equations starts. In Pb_Multiphase, the equations solved for each phase are the momentum, mass and energy equations; respectively QDM_Multiphase, Masse_Multiphase and Energie_Multiphase.

The coupling between all equations is done in a strong way: a single matrix for all equations is used to solve the problem. Available discretizations for this type of problem are VDF, PolyMAC and PolyMAC_P0.

You can also call the EOS (private CEA/EDF project) and the CoolProp library to compute the Thermo-Physical Properties via the TPPI interface.

Example of a Pb_Multiphase block

Here is an example of Pb_Multiphase, taken from the CoolProp_water_BICUBIC_HEOS_with_sat test case. Warning: this test case needs a TRUST version linked with the CoolProp library.

# Read a multiphase problem pb #
Read pb
{
    # Read the multi-phase + saturation medium #
    Milieu_composite
    {
        liquide_eau Fluide_generique_coolprop { model BICUBIC&heos fluid Water phase liquid } 
        gaz_eau Fluide_generique_coolprop { model BICUBIC&heos fluid Water }
        saturation_eau saturation_generique_coolprop { model BICUBIC&heos fluid Water phase liquid }
    }
 
    # Read the correlations #
    correlations
    {
    flux_interfacial coef_constant { liquide_eau 1.0e10 gaz_eau 1.0e10 }
    }
    
    # Read the momentum equation #
    QDM_Multiphase
    {   
        evanescence { homogene { alpha_res 1 alpha_res_min 0.5 } } 
        solveur_pression petsc cli_quiet { -pc_type hypre -pc_hypre_type boomeramg }
        convection { amont }
        diffusion  { negligeable } 
        initial_conditions
        {
           vitesse  Champ_fonc_xyz dom 4 2.0*(x>0.5)-2.0*(x[0.5) 2.0*(x>0.5)-2.0*(x[0.5) 0.0 0.0
           pression Champ_fonc_xyz dom 1 1.0e5 
        }
        boundary_conditions
        {
            haut symetrie
            bas symetrie
             gauche frontiere_ouverte_pression_imposee champ_front_uniforme 1 100000.0
            droite frontiere_ouverte_pression_imposee champ_front_uniforme 1 100000.0
        }
    }
        
    # Read the mass equation #
    Masse_Multiphase
    {
        initial_conditions { alpha Champ_Fonc_xyz dom 2 0.95 0.05 }
        convection { amont }
        boundary_conditions
        {
            haut paroi
            bas paroi
            gauche frontiere_ouverte a_ext Champ_Front_Uniforme 2 0.95 0.05
            droite frontiere_ouverte a_ext Champ_Front_Uniforme 2 0.95 0.05
        }
          sources { flux_interfacial }
    }
        
    # Read the energy equation #
    Energie_Multiphase
    {
        diffusion { negligeable }
        convection { amont }
        initial_conditions { temperature Champ_fonc_xyz dom 2 10. 10. }
        boundary_conditions
        {
            haut paroi_adiabatique
            bas paroi_adiabatique
            gauche frontiere_ouverte T_ext Champ_Front_uniforme 2 81.578 61.578
            droite frontiere_ouverte T_ext Champ_Front_uniforme 2 71.578 51.578
        }
         sources { flux_interfacial }
    }
    
    # Read the post-processing #
    Post_processing
    {
        probes
        {
             rho grav masse_volumique periode 1e8 segment 1000 0 0.5 1 0.5
               v grav         vitesse periode 1e8 segment 1000 0 0.5 1 0.5
               p grav        pression periode 1e8 segment 1000 0 0.5 1 0.5
            eint grav energie_interne periode 1e8 segment 1000 0 0.5 1 0.5
        }
        
        Format lml
        fields dt_post 1e-4
        {
            alpha elem
            vitesse elem
            pression elem
            temperature elem
            energie_interne elem
            vitesse_liquide_eau elem
            vitesse_gaz_eau elem
            alpha_gaz_eau elem
            masse_volumique elem
        }
    }
}

Coupled Problems

There are two ways to solve coupled problems with TRUST: either using Probleme_Couple or via the Interface of Code Coupling (ICoCo) and ProblemeTrio.

With Probleme_Couple

In Probleme_Couple, the user has to define the contact boundary/volume between several domains where a TRUST problem (one of the above) is to be defined on each domain. The coupling is managed by TRUST where a point-fixed algorithm is used to converge the coupled simulation.

Here is an example:

First two problems my_problem_1 and my_problem_2 are defined. Each one associated with a separate domain my_domain_1 and my_domain_2, and each one having a different medium my_medium_1 and my_medium_2:

Dimension 2
Pb_ThermoHydraulique my_problem_1
Pb_ThermoHydraulique my_problem_2
 
Domaine my_domain_1
Read_file my_mesh_1.geo ;
 
Domaine my_domain_2
Read_file my_mesh_2.geo ;
 
Associate my_problem_1 my_domain_1
Associate my_problem_2 my_domain_2

Then a coupled problem associated to a single time scheme is defined:

Probleme_Couple my_coupled_problem
 
VEFPreP1B my_discretization
 
Scheme_euler_explicit my_scheme
Read my_scheme { ... }
 
Associate my_coupled_problem my_problem_1
Associate my_coupled_problem my_problem_2
Associate my_coupled_problem my_scheme

Eventually the coupled problem is discretized, the two separated problems specified and the coupled problem is solved:

Discretize my_coupled_problem my_discretization
 
Read my_problem_1
{
   Fluide_Incompressible { ... }
   ...
}
 
Read my_problem_2
{
   Fluide_Incompressible { ... }
   ...
}
 
Solve my_coupled_problem
End

With ICoCo

On the other hand, the user have to write his own coupling algorithm when using ICoCo. In practice, this can be done either by writing a C++ supervisor to manage the coupling, or via its python interface available in TRUST, thanks to the swig wrapper!