This class represents 1D flow domains that satisfy the one-dimensional similarity solution for chemically-reacting, axisymmetric flows. More...
#include <Flow1D.h>
This class represents 1D flow domains that satisfy the one-dimensional similarity solution for chemically-reacting, axisymmetric flows.
Public Member Functions | |
Flow1D (ThermoPhase *ph=0, size_t nsp=1, size_t points=1) | |
Create a new flow domain. | |
Flow1D (shared_ptr< ThermoPhase > th, size_t nsp=1, size_t points=1) | |
Delegating constructor. | |
Flow1D (shared_ptr< Solution > sol, const string &id="", size_t points=1) | |
Create a new flow domain. | |
string | domainType () const override |
Domain type flag. | |
string | componentName (size_t n) const override |
Name of the nth component. May be overloaded. | |
size_t | componentIndex (const string &name) const override |
index of component with name name. | |
virtual bool | componentActive (size_t n) const |
Returns true if the specified component is an active part of the solver state. | |
void | show (const double *x) override |
Print the solution. | |
shared_ptr< SolutionArray > | asArray (const double *soln) const override |
Save the state of this domain as a SolutionArray. | |
void | fromArray (SolutionArray &arr, double *soln) override |
Restore the solution for this domain from a SolutionArray. | |
void | setFreeFlow () |
Set flow configuration for freely-propagating flames, using an internal point with a fixed temperature as the condition to determine the inlet mass flux. | |
void | setAxisymmetricFlow () |
Set flow configuration for axisymmetric counterflow flames, using specified inlet mass fluxes. | |
void | setUnstrainedFlow () |
Set flow configuration for burner-stabilized flames, using specified inlet mass fluxes. | |
void | solveEnergyEqn (size_t j=npos) |
virtual size_t | getSolvingStage () const |
Get the solving stage (used by IonFlow specialization) | |
virtual void | setSolvingStage (const size_t stage) |
Solving stage mode for handling ionized species (used by IonFlow specialization) | |
virtual void | solveElectricField (size_t j=npos) |
Set to solve electric field in a point (used by IonFlow specialization) | |
virtual void | fixElectricField (size_t j=npos) |
Set to fix voltage in a point (used by IonFlow specialization) | |
virtual bool | doElectricField (size_t j) const |
Retrieve flag indicating whether electric field is solved or not (used by IonFlow specialization) | |
void | enableRadiation (bool doRadiation) |
Turn radiation on / off. | |
bool | radiationEnabled () const |
Returns true if the radiation term in the energy equation is enabled. | |
double | radiativeHeatLoss (size_t j) const |
Return radiative heat loss at grid point j. | |
void | setBoundaryEmissivities (double e_left, double e_right) |
Set the emissivities for the boundary values. | |
double | leftEmissivity () const |
Return emissivity at left boundary. | |
double | rightEmissivity () const |
Return emissivity at right boundary. | |
void | fixTemperature (size_t j=npos) |
bool | doEnergy (size_t j) |
void | resize (size_t components, size_t points) override |
Change the grid size. Called after grid refinement. | |
void | setGas (const double *x, size_t j) |
Set the gas object state to be consistent with the solution at point j. | |
void | setGasAtMidpoint (const double *x, size_t j) |
Set the gas state to be consistent with the solution at the midpoint between j and j + 1. | |
double | density (size_t j) const |
bool | isFree () const |
Retrieve flag indicating whether flow is freely propagating. | |
bool | isStrained () const |
Retrieve flag indicating whether flow uses radial momentum. | |
void | setViscosityFlag (bool dovisc) |
void | eval (size_t jGlobal, double *xGlobal, double *rsdGlobal, integer *diagGlobal, double rdt) override |
Evaluate the residual functions for axisymmetric stagnation flow. | |
size_t | leftExcessSpecies () const |
Index of the species on the left boundary with the largest mass fraction. | |
size_t | rightExcessSpecies () const |
Index of the species on the right boundary with the largest mass fraction. | |
Problem Specification | |
void | setupGrid (size_t n, const double *z) override |
called to set up initial grid, and after grid refinement | |
void | resetBadValues (double *xg) override |
When called, this function should reset "bad" values in the state vector such as negative species concentrations. | |
ThermoPhase & | phase () |
Kinetics & | kinetics () |
void | setKinetics (shared_ptr< Kinetics > kin) override |
Set the kinetics manager. | |
void | setTransport (shared_ptr< Transport > trans) override |
Set transport model to existing instance. | |
void | setTransportModel (const string &trans) |
Set the transport model. | |
string | transportModel () const |
Retrieve transport model. | |
void | enableSoret (bool withSoret) |
Enable thermal diffusion, also known as Soret diffusion. | |
bool | withSoret () const |
void | setFluxGradientBasis (ThermoBasis fluxGradientBasis) |
Compute species diffusive fluxes with respect to their mass fraction gradients (fluxGradientBasis = ThermoBasis::mass) or mole fraction gradients (fluxGradientBasis = ThermoBasis::molar, default) when using the mixture-averaged transport model. | |
ThermoBasis | fluxGradientBasis () const |
Compute species diffusive fluxes with respect to their mass fraction gradients (fluxGradientBasis = ThermoBasis::mass) or mole fraction gradients (fluxGradientBasis = ThermoBasis::molar, default) when using the mixture-averaged transport model. | |
void | setPressure (double p) |
Set the pressure. | |
double | pressure () const |
The current pressure [Pa]. | |
void | _getInitialSoln (double *x) override |
Write the initial solution estimate into array x. | |
void | _finalize (const double *x) override |
In some cases, a domain may need to set parameters that depend on the initial solution estimate. | |
void | setFixedTempProfile (vector< double > &zfixed, vector< double > &tfixed) |
Sometimes it is desired to carry out the simulation using a specified temperature profile, rather than computing it by solving the energy equation. | |
void | setTemperature (size_t j, double t) |
Set the temperature fixed point at grid point j, and disable the energy equation so that the solution will be held to this value. | |
double | T_fixed (size_t j) const |
The fixed temperature value at point j. | |
Two-Point control method | |
In this method two control points are designated in the 1D domain, and the value of the temperature at these points is fixed. The values of the control points are imposed and thus serve as a boundary condition that affects the solution of the governing equations in the 1D domain. The imposition of fixed points in the domain means that the original set of governing equations' boundary conditions would over-determine the problem. Thus, the boundary conditions are changed to reflect the fact that the control points are serving as internal boundary conditions. The imposition of the two internal boundary conditions requires that two other boundary conditions be changed. The first is the boundary condition for the continuity equation at the left boundary, which is changed to be a value that is derived from the solution at the left boundary. The second is the continuity boundary condition at the right boundary, which is also determined from the flow solution by using the oxidizer axial velocity equation variable to compute the mass flux at the right boundary. This method is based on the work of Nishioka et al. [32] . | |
double | leftControlPointTemperature () const |
Returns the temperature at the left control point. | |
double | leftControlPointCoordinate () const |
Returns the z-coordinate of the left control point. | |
void | setLeftControlPointTemperature (double temperature) |
Sets the temperature of the left control point. | |
void | setLeftControlPointCoordinate (double z_left) |
Sets the coordinate of the left control point. | |
double | rightControlPointTemperature () const |
Returns the temperature at the right control point. | |
double | rightControlPointCoordinate () const |
Returns the z-coordinate of the right control point. | |
void | setRightControlPointTemperature (double temperature) |
Sets the temperature of the right control point. | |
void | setRightControlPointCoordinate (double z_right) |
Sets the coordinate of the right control point. | |
void | enableTwoPointControl (bool twoPointControl) |
Sets the status of the two-point control. | |
bool | twoPointControlEnabled () const |
Returns the status of the two-point control. | |
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Domain1D (size_t nv=1, size_t points=1, double time=0.0) | |
Constructor. | |
Domain1D (const Domain1D &)=delete | |
Domain1D & | operator= (const Domain1D &)=delete |
virtual string | domainType () const |
Domain type flag. | |
string | type () const |
String indicating the domain implemented. | |
size_t | domainIndex () |
The left-to-right location of this domain. | |
virtual bool | isConnector () |
True if the domain is a connector domain. | |
void | setSolution (shared_ptr< Solution > sol) |
Set the solution manager. | |
virtual void | setKinetics (shared_ptr< Kinetics > kin) |
Set the kinetics manager. | |
virtual void | setTransport (shared_ptr< Transport > trans) |
Set transport model to existing instance. | |
const OneDim & | container () const |
The container holding this domain. | |
void | setContainer (OneDim *c, size_t index) |
Specify the container object for this domain, and the position of this domain in the list. | |
void | setBandwidth (int bw=-1) |
Set the Jacobian bandwidth. See the discussion of method bandwidth(). | |
size_t | bandwidth () |
Set the Jacobian bandwidth for this domain. | |
virtual void | init () |
Initialize. | |
virtual void | setInitialState (double *xlocal=0) |
virtual void | setState (size_t point, const double *state, double *x) |
virtual void | resetBadValues (double *xg) |
When called, this function should reset "bad" values in the state vector such as negative species concentrations. | |
virtual void | resize (size_t nv, size_t np) |
Resize the domain to have nv components and np grid points. | |
Refiner & | refiner () |
Return a reference to the grid refiner. | |
size_t | nComponents () const |
Number of components at each grid point. | |
void | checkComponentIndex (size_t n) const |
Check that the specified component index is in range. | |
void | checkComponentArraySize (size_t nn) const |
Check that an array size is at least nComponents(). | |
size_t | nPoints () const |
Number of grid points in this domain. | |
void | checkPointIndex (size_t n) const |
Check that the specified point index is in range. | |
void | checkPointArraySize (size_t nn) const |
Check that an array size is at least nPoints(). | |
virtual string | componentName (size_t n) const |
Name of the nth component. May be overloaded. | |
void | setComponentName (size_t n, const string &name) |
virtual size_t | componentIndex (const string &name) const |
index of component with name name. | |
void | setBounds (size_t n, double lower, double upper) |
void | setTransientTolerances (double rtol, double atol, size_t n=npos) |
Set tolerances for time-stepping mode. | |
void | setSteadyTolerances (double rtol, double atol, size_t n=npos) |
Set tolerances for steady-state mode. | |
double | rtol (size_t n) |
Relative tolerance of the nth component. | |
double | atol (size_t n) |
Absolute tolerance of the nth component. | |
double | steady_rtol (size_t n) |
Steady relative tolerance of the nth component. | |
double | steady_atol (size_t n) |
Steady absolute tolerance of the nth component. | |
double | transient_rtol (size_t n) |
Transient relative tolerance of the nth component. | |
double | transient_atol (size_t n) |
Transient absolute tolerance of the nth component. | |
double | upperBound (size_t n) const |
Upper bound on the nth component. | |
double | lowerBound (size_t n) const |
Lower bound on the nth component. | |
void | initTimeInteg (double dt, const double *x0) |
Prepare to do time stepping with time step dt. | |
void | setSteadyMode () |
Prepare to solve the steady-state problem. | |
bool | steady () |
True if in steady-state mode. | |
bool | transient () |
True if not in steady-state mode. | |
void | needJacUpdate () |
Set this if something has changed in the governing equations (for example, the value of a constant has been changed, so that the last-computed Jacobian is no longer valid. | |
virtual void | eval (size_t j, double *x, double *r, integer *mask, double rdt=0.0) |
Evaluate the residual function at point j. | |
size_t | index (size_t n, size_t j) const |
double | value (const double *x, size_t n, size_t j) const |
virtual void | setJac (MultiJac *jac) |
virtual shared_ptr< SolutionArray > | asArray (const double *soln) const |
Save the state of this domain as a SolutionArray. | |
shared_ptr< SolutionArray > | toArray (bool normalize=false) const |
Save the state of this domain to a SolutionArray. | |
virtual void | fromArray (SolutionArray &arr, double *soln) |
Restore the solution for this domain from a SolutionArray. | |
void | fromArray (const shared_ptr< SolutionArray > &arr) |
Restore the solution for this domain from a SolutionArray. | |
shared_ptr< Solution > | solution () const |
Return thermo/kinetics/transport manager used in the domain. | |
size_t | size () const |
void | locate () |
Find the index of the first grid point in this domain, and the start of its variables in the global solution vector. | |
virtual size_t | loc (size_t j=0) const |
Location of the start of the local solution vector in the global solution vector,. | |
size_t | firstPoint () const |
The index of the first (that is, left-most) grid point belonging to this domain. | |
size_t | lastPoint () const |
The index of the last (that is, right-most) grid point belonging to this domain. | |
void | linkLeft (Domain1D *left) |
Set the left neighbor to domain 'left. | |
void | linkRight (Domain1D *right) |
Set the right neighbor to domain 'right.'. | |
void | append (Domain1D *right) |
Append domain 'right' to this one, and update all links. | |
Domain1D * | left () const |
Return a pointer to the left neighbor. | |
Domain1D * | right () const |
Return a pointer to the right neighbor. | |
double | prevSoln (size_t n, size_t j) const |
Value of component n at point j in the previous solution. | |
void | setID (const string &s) |
Specify an identifying tag for this domain. | |
string | id () const |
virtual void | show (std::ostream &s, const double *x) |
Print the solution. | |
virtual void | show (const double *x) |
Print the solution. | |
double | z (size_t jlocal) const |
double | zmin () const |
double | zmax () const |
void | setProfile (const string &name, double *values, double *soln) |
vector< double > & | grid () |
const vector< double > & | grid () const |
double | grid (size_t point) const |
virtual void | setupGrid (size_t n, const double *z) |
called to set up initial grid, and after grid refinement | |
virtual void | _getInitialSoln (double *x) |
Writes some or all initial solution values into the global solution array, beginning at the location pointed to by x. | |
virtual double | initialValue (size_t n, size_t j) |
Initial value of solution component n at grid point j. | |
virtual void | _finalize (const double *x) |
In some cases, a domain may need to set parameters that depend on the initial solution estimate. | |
void | forceFullUpdate (bool update) |
In some cases, for computational efficiency some properties (such as transport coefficients) may not be updated during Jacobian evaluations. | |
void | setData (shared_ptr< vector< double > > &data) |
Set shared data pointer. | |
Public Attributes | |
double | m_zfixed = Undef |
Location of the point where temperature is fixed. | |
double | m_tfixed = -1.0 |
Temperature at the point used to fix the flame location. | |
Protected Member Functions | |
AnyMap | getMeta () const override |
Retrieve meta data. | |
void | setMeta (const AnyMap &state) override |
Retrieve meta data. | |
virtual void | evalContinuity (size_t j, double *x, double *r, int *diag, double rdt) |
Alternate version of evalContinuity with legacy signature. | |
virtual void | evalUo (double *x, double *rsd, int *diag, double rdt, size_t jmin, size_t jmax) |
Evaluate the oxidizer axial velocity equation residual. | |
double | shear (const double *x, size_t j) const |
double | divHeatFlux (const double *x, size_t j) const |
size_t | mindex (size_t k, size_t j, size_t m) |
virtual void | grad_hk (const double *x, size_t j) |
Get the gradient of species specific molar enthalpies. | |
Updates of cached properties | |
These methods are called by eval() to update cached properties and data that are used for the evaluation of the governing equations. | |
void | updateThermo (const double *x, size_t j0, size_t j1) |
Update the thermodynamic properties from point j0 to point j1 (inclusive), based on solution x. | |
virtual void | updateTransport (double *x, size_t j0, size_t j1) |
Update the transport properties at grid points in the range from j0 to j1 , based on solution x . | |
virtual void | updateDiffFluxes (const double *x, size_t j0, size_t j1) |
Update the diffusive mass fluxes. | |
virtual void | updateProperties (size_t jg, double *x, size_t jmin, size_t jmax) |
Update the properties (thermo, transport, and diffusion flux). | |
void | computeRadiation (double *x, size_t jmin, size_t jmax) |
Computes the radiative heat loss vector over points jmin to jmax and stores the data in the qdotRadiation variable. | |
Governing Equations | |
Methods called by eval() to calculate residuals for individual governing equations. | |
virtual void | evalContinuity (double *x, double *rsd, int *diag, double rdt, size_t jmin, size_t jmax) |
Evaluate the continuity equation residual. | |
virtual void | evalMomentum (double *x, double *rsd, int *diag, double rdt, size_t jmin, size_t jmax) |
Evaluate the momentum equation residual. | |
virtual void | evalLambda (double *x, double *rsd, int *diag, double rdt, size_t jmin, size_t jmax) |
Evaluate the lambda equation residual. | |
virtual void | evalEnergy (double *x, double *rsd, int *diag, double rdt, size_t jmin, size_t jmax) |
Evaluate the energy equation residual. | |
virtual void | evalSpecies (double *x, double *rsd, int *diag, double rdt, size_t jmin, size_t jmax) |
Evaluate the species equations' residuals. | |
virtual void | evalElectricField (double *x, double *rsd, int *diag, double rdt, size_t jmin, size_t jmax) |
Evaluate the electric field equation residual to be zero everywhere. | |
Solution components | |
double | T (const double *x, size_t j) const |
double & | T (double *x, size_t j) |
double | T_prev (size_t j) const |
double | rho_u (const double *x, size_t j) const |
double | u (const double *x, size_t j) const |
double | V (const double *x, size_t j) const |
double | V_prev (size_t j) const |
double | lambda (const double *x, size_t j) const |
double | Uo (const double *x, size_t j) const |
Solution component for oxidizer velocity,. | |
double | Y (const double *x, size_t k, size_t j) const |
double & | Y (double *x, size_t k, size_t j) |
double | Y_prev (size_t k, size_t j) const |
double | X (const double *x, size_t k, size_t j) const |
double | flux (size_t k, size_t j) const |
Convective spatial derivatives | |
These use upwind differencing, assuming u(z) is negative | |
double | dVdz (const double *x, size_t j) const |
double | dYdz (const double *x, size_t k, size_t j) const |
double | dTdz (const double *x, size_t j) const |
virtual AnyMap | getMeta () const |
Retrieve meta data. | |
virtual void | setMeta (const AnyMap &meta) |
Retrieve meta data. | |
Protected Attributes | |
double | m_press = -1.0 |
vector< double > | m_dz |
vector< double > | m_rho |
Vector of size m_nsp to cache densities. | |
vector< double > | m_wtm |
Vector of size m_nsp to cache mean molecular weights. | |
vector< double > | m_wt |
vector< double > | m_cp |
Vector of size m_nsp to cache specific heat capacities. | |
vector< double > | m_visc |
vector< double > | m_tcon |
vector< double > | m_diff |
Array of size m_nsp by m_points for saving density times diffusion coefficient times species molar mass divided by mean molecular weight. | |
vector< double > | m_multidiff |
Array2D | m_dthermal |
Array2D | m_flux |
Array2D | m_hk |
Array of size m_nsp by m_points for saving molar enthalpies. | |
Array2D | m_dhk_dz |
Array of size m_nsp by m_points-1 for saving enthalpy fluxes. | |
Array2D | m_wdot |
Array of size m_nsp by m_points for saving species production rates. | |
size_t | m_nsp |
Number of species in the mechanism. | |
ThermoPhase * | m_thermo = nullptr |
Kinetics * | m_kin = nullptr |
Transport * | m_trans = nullptr |
double | m_epsilon_left = 0.0 |
double | m_epsilon_right = 0.0 |
vector< size_t > | m_kRadiating |
Indices within the ThermoPhase of the radiating species. | |
vector< bool > | m_do_energy |
bool | m_do_soret = false |
ThermoBasis | m_fluxGradientBasis = ThermoBasis::molar |
vector< bool > | m_do_species |
bool | m_do_multicomponent = false |
bool | m_do_radiation = false |
flag for the radiative heat loss | |
vector< double > | m_qdotRadiation |
radiative heat loss vector | |
vector< double > | m_fixedtemp |
vector< double > | m_zfix |
vector< double > | m_tfix |
size_t | m_kExcessLeft = 0 |
Index of species with a large mass fraction at each boundary, for which the mass fraction may be calculated as 1 minus the sum of the other mass fractions. | |
size_t | m_kExcessRight = 0 |
bool | m_dovisc |
bool | m_isFree |
bool | m_usesLambda |
bool | m_twoPointControl = false |
Flag for activating two-point flame control. | |
double | m_zLeft = Undef |
Location of the left control point when two-point control is enabled. | |
double | m_tLeft = Undef |
Temperature of the left control point when two-point control is enabled. | |
double | m_zRight = Undef |
Location of the right control point when two-point control is enabled. | |
double | m_tRight = Undef |
Temperature of the right control point when two-point control is enabled. | |
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shared_ptr< vector< double > > | m_state |
data pointer shared from OneDim | |
double | m_rdt = 0.0 |
size_t | m_nv = 0 |
size_t | m_points |
Number of grid points. | |
vector< double > | m_slast |
vector< double > | m_max |
vector< double > | m_min |
vector< double > | m_rtol_ss |
vector< double > | m_rtol_ts |
vector< double > | m_atol_ss |
vector< double > | m_atol_ts |
vector< double > | m_z |
OneDim * | m_container = nullptr |
size_t | m_index |
size_t | m_iloc = 0 |
Starting location within the solution vector for unknowns that correspond to this domain. | |
size_t | m_jstart = 0 |
Domain1D * | m_left = nullptr |
Domain1D * | m_right = nullptr |
string | m_id |
Identity tag for the domain. | |
unique_ptr< Refiner > | m_refiner |
vector< string > | m_name |
int | m_bw = -1 |
bool | m_force_full_update = false |
shared_ptr< Solution > | m_solution |
Composite thermo/kinetics/transport handler. | |
Private Attributes | |
vector< double > | m_ybar |
Flow1D | ( | ThermoPhase * | ph = 0 , |
size_t | nsp = 1 , |
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size_t | points = 1 |
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Create a new flow domain.
ph | Object representing the gas phase. This object will be used to evaluate all thermodynamic, kinetic, and transport properties. |
nsp | Number of species. |
points | Initial number of grid points |
Definition at line 19 of file Flow1D.cpp.
Flow1D | ( | shared_ptr< ThermoPhase > | th, |
size_t | nsp = 1 , |
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size_t | points = 1 |
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Delegating constructor.
Definition at line 93 of file Flow1D.cpp.
Create a new flow domain.
sol | Solution object used to evaluate all thermodynamic, kinetic, and transport properties |
id | name of flow domain |
points | initial number of grid points |
Definition at line 101 of file Flow1D.cpp.
~Flow1D | ( | ) |
Definition at line 119 of file Flow1D.cpp.
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Domain type flag.
string
. Reimplemented from Domain1D.
Reimplemented in IonFlow.
Definition at line 126 of file Flow1D.cpp.
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called to set up initial grid, and after grid refinement
Reimplemented from Domain1D.
Definition at line 188 of file Flow1D.cpp.
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When called, this function should reset "bad" values in the state vector such as negative species concentrations.
This function may be called after a failed solution attempt.
Reimplemented from Domain1D.
Definition at line 203 of file Flow1D.cpp.
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Set the kinetics manager.
Reimplemented from Domain1D.
Definition at line 136 of file Flow1D.cpp.
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Set transport model to existing instance.
Reimplemented from Domain1D.
Definition at line 142 of file Flow1D.cpp.
void setTransportModel | ( | const string & | trans | ) |
string transportModel | ( | ) | const |
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void setFluxGradientBasis | ( | ThermoBasis | fluxGradientBasis | ) |
Compute species diffusive fluxes with respect to their mass fraction gradients (fluxGradientBasis = ThermoBasis::mass) or mole fraction gradients (fluxGradientBasis = ThermoBasis::molar, default) when using the mixture-averaged transport model.
fluxGradientBasis | set flux computation to mass or mole basis |
Definition at line 222 of file Flow1D.cpp.
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Compute species diffusive fluxes with respect to their mass fraction gradients (fluxGradientBasis = ThermoBasis::mass) or mole fraction gradients (fluxGradientBasis = ThermoBasis::molar, default) when using the mixture-averaged transport model.
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Write the initial solution estimate into array x.
Reimplemented from Domain1D.
Definition at line 232 of file Flow1D.cpp.
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In some cases, a domain may need to set parameters that depend on the initial solution estimate.
In such cases, the parameters may be set in method _finalize. This method is called just before the Newton solver is called, and the x array is guaranteed to be the local solution vector for this domain that will be used as the initial guess. If no such parameters need to be set, then method _finalize does not need to be overloaded.
Reimplemented from Domain1D.
Reimplemented in IonFlow.
Definition at line 261 of file Flow1D.cpp.
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Name of the nth component. May be overloaded.
Reimplemented from Domain1D.
Definition at line 797 of file Flow1D.cpp.
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index of component with name name.
Reimplemented from Domain1D.
Definition at line 821 of file Flow1D.cpp.
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Returns true if the specified component is an active part of the solver state.
Reimplemented in IonFlow.
Definition at line 846 of file Flow1D.cpp.
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Save the state of this domain as a SolutionArray.
soln | local solution vector for this domain |
Reimplemented from Domain1D.
Definition at line 922 of file Flow1D.cpp.
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Restore the solution for this domain from a SolutionArray.
[in] | arr | SolutionArray defining the state of this domain |
[out] | soln | Value of the solution vector, local to this domain |
Reimplemented from Domain1D.
Definition at line 956 of file Flow1D.cpp.
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void solveEnergyEqn | ( | size_t | j = npos | ) |
Definition at line 1062 of file Flow1D.cpp.
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Get the solving stage (used by IonFlow specialization)
Reimplemented in IonFlow.
Definition at line 1086 of file Flow1D.cpp.
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Solving stage mode for handling ionized species (used by IonFlow specialization)
stage=1
: the fluxes of charged species are set to zerostage=2
: the electric field equation is solved, and the drift flux for ionized species is evaluated Reimplemented in IonFlow.
Definition at line 1092 of file Flow1D.cpp.
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Set to solve electric field in a point (used by IonFlow specialization)
Reimplemented in IonFlow.
Definition at line 1098 of file Flow1D.cpp.
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Set to fix voltage in a point (used by IonFlow specialization)
Reimplemented in IonFlow.
Definition at line 1104 of file Flow1D.cpp.
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Retrieve flag indicating whether electric field is solved or not (used by IonFlow specialization)
Reimplemented in IonFlow.
Definition at line 1110 of file Flow1D.cpp.
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void setBoundaryEmissivities | ( | double | e_left, |
double | e_right | ||
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Set the emissivities for the boundary values.
Reads the emissivities for the left and right boundary values in the radiative term and writes them into the variables, which are used for the calculation.
Definition at line 1116 of file Flow1D.cpp.
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void fixTemperature | ( | size_t | j = npos | ) |
Definition at line 1130 of file Flow1D.cpp.
double leftControlPointTemperature | ( | ) | const |
Returns the temperature at the left control point.
Definition at line 1167 of file Flow1D.cpp.
double leftControlPointCoordinate | ( | ) | const |
Returns the z-coordinate of the left control point.
Definition at line 1182 of file Flow1D.cpp.
void setLeftControlPointTemperature | ( | double | temperature | ) |
Sets the temperature of the left control point.
Definition at line 1197 of file Flow1D.cpp.
void setLeftControlPointCoordinate | ( | double | z_left | ) |
Sets the coordinate of the left control point.
Definition at line 1212 of file Flow1D.cpp.
double rightControlPointTemperature | ( | ) | const |
Returns the temperature at the right control point.
Definition at line 1222 of file Flow1D.cpp.
double rightControlPointCoordinate | ( | ) | const |
Returns the z-coordinate of the right control point.
Definition at line 1237 of file Flow1D.cpp.
void setRightControlPointTemperature | ( | double | temperature | ) |
Sets the temperature of the right control point.
Definition at line 1252 of file Flow1D.cpp.
void setRightControlPointCoordinate | ( | double | z_right | ) |
Sets the coordinate of the right control point.
Definition at line 1267 of file Flow1D.cpp.
void enableTwoPointControl | ( | bool | twoPointControl | ) |
Sets the status of the two-point control.
Definition at line 1277 of file Flow1D.cpp.
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Change the grid size. Called after grid refinement.
Reimplemented from Domain1D.
Reimplemented in IonFlow.
Definition at line 162 of file Flow1D.cpp.
void setGas | ( | const double * | x, |
size_t | j | ||
) |
Set the gas object state to be consistent with the solution at point j.
Definition at line 241 of file Flow1D.cpp.
void setGasAtMidpoint | ( | const double * | x, |
size_t | j | ||
) |
Set the gas state to be consistent with the solution at the midpoint between j and j + 1.
Definition at line 249 of file Flow1D.cpp.
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Evaluate the residual functions for axisymmetric stagnation flow.
If jGlobal == npos, the residual function is evaluated at all grid points. Otherwise, the residual function is only evaluated at grid points j-1, j, and j+1. This option is used to efficiently evaluate the Jacobian numerically.
These residuals at all the boundary grid points are evaluated using a default boundary condition that may be modified by a boundary object that is attached to the domain. The boundary object connected will modify these equations by subtracting the boundary object's values for V, T, mdot, etc. As a result, these residual equations will force the solution variables to the values of the connected boundary object.
jGlobal | Global grid point at which to update the residual | |
[in] | xGlobal | Global state vector |
[out] | rsdGlobal | Global residual vector |
[out] | diagGlobal | Global boolean mask indicating whether each solution component has a time derivative (1) or not (0). |
[in] | rdt | Reciprocal of the timestep (rdt=0 implies steady-state.) |
Reimplemented from Domain1D.
Reimplemented in StFlow.
Definition at line 308 of file Flow1D.cpp.
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Update the thermodynamic properties from point j0 to point j1 (inclusive), based on solution x.
The gas state is set to be consistent with the solution at the points from j0 to j1.
Properties that are computed and cached are:
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Update the transport properties at grid points in the range from j0
to j1
, based on solution x
.
Reimplemented in IonFlow.
Definition at line 371 of file Flow1D.cpp.
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Update the diffusive mass fluxes.
Reimplemented in IonFlow.
Definition at line 419 of file Flow1D.cpp.
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Update the properties (thermo, transport, and diffusion flux).
This function is called in eval after the points which need to be updated are defined.
Definition at line 347 of file Flow1D.cpp.
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Computes the radiative heat loss vector over points jmin to jmax and stores the data in the qdotRadiation variable.
The simple radiation model used was established by Liu and Rogg [23]. This model considers the radiation of CO2 and H2O.
This model uses the optically thin limit and the gray-gas approximation to simply calculate a volume specified heat flux out of the Planck absorption coefficients, the boundary emissivities and the temperature. Polynomial lines calculate the species Planck coefficients for H2O and CO2. The data for the lines are taken from the RADCAL program [9]. The coefficients for the polynomials are taken from TNF Workshop material.
Definition at line 465 of file Flow1D.cpp.
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Evaluate the continuity equation residual.
This function calculates the residual of the continuity equation
\[ \frac{d(\rho u)}{dz} + 2\rho V = 0 \]
Axisymmetric flame: The continuity equation propagates information from right-to-left. The \( \rho u \) at point 0 is dependent on \( \rho u \) at point 1, but not on \( \dot{m} \) from the inlet.
Freely-propagating flame: The continuity equation propagates information away from a fixed temperature point that is set in the domain.
Unstrained flame: A specified mass flux; the main example being burner-stabilized flames.
The default boundary condition for the continuity equation is ( \( u = 0 \)) at the left and right boundary.
[in] | x | Local domain state vector, includes variables like temperature, density, etc. |
[out] | rsd | Local domain residual vector that stores the continuity equation residuals. |
[out] | diag | Local domain diagonal matrix that controls whether an entry has a time-derivative (used by the solver). |
[in] | rdt | Reciprocal of the timestep. |
[in] | jmin | The index for the starting point in the local domain grid. |
[in] | jmax | The index for the ending point in the local domain grid. |
Definition at line 512 of file Flow1D.cpp.
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Evaluate the momentum equation residual.
The function calculates the radial momentum equation defined as
\[ \rho u \frac{dV}{dz} + \rho V^2 = \frac{d}{dz}\left( \mu \frac{dV}{dz} \right) - \Lambda \]
The radial momentum equation is used for axisymmetric flows, and incorporates terms for time and spatial variations of radial velocity ( \( V \)). The default boundary condition is zero radial velocity ( \( V \)) at the left and right boundary.
For argument explanation, see evalContinuity().
Definition at line 571 of file Flow1D.cpp.
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Evaluate the lambda equation residual.
The function calculates the lambda equation as
\[ \frac{d\Lambda}{dz} = 0 \]
The lambda equation serves as an eigenvalue that allows the momentum equation and continuity equations to be simultaneously satisfied in axisymmetric flows. The lambda equation propagates information from left-to-right. The default boundary condition is \( \Lambda = 0 \) at the left and zero flux at the right boundary.
For argument explanation, see evalContinuity().
Definition at line 603 of file Flow1D.cpp.
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Evaluate the energy equation residual.
The function calculates the energy equation:
\[ \rho c_p u \frac{dT}{dz} = \frac{d}{dz}\left( \lambda \frac{dT}{dz} \right) - \sum_k h_kW_k\dot{\omega}_k - \sum_k j_k \frac{dh_k}{dz} \]
The energy equation includes contributions from chemical reactions and diffusion. Default is zero temperature ( \( T \)) at the left and right boundaries. These boundary values are updated by the specific boundary object connected to the domain.
For argument explanation, see evalContinuity().
Definition at line 646 of file Flow1D.cpp.
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Evaluate the species equations' residuals.
The function calculates the species equations as
\[ \rho u \frac{dY_k}{dz} + \frac{dj_k}{dz} = W_k\dot{\omega}_k \]
The species equations include terms for temporal and spatial variations of species mass fractions ( \( Y_k \)). The default boundary condition is zero flux for species at the left and right boundary.
For argument explanation, see evalContinuity().
Reimplemented in IonFlow.
Definition at line 726 of file Flow1D.cpp.
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Evaluate the electric field equation residual to be zero everywhere.
The electric field equation is implemented in the IonFlow class. The default boundary condition is zero electric field ( \( E \)) at the boundary, and \( E \) is zero within the domain.
For argument explanation, see evalContinuity().
Reimplemented in IonFlow.
Definition at line 765 of file Flow1D.cpp.
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Alternate version of evalContinuity with legacy signature.
Implemented by StFlow; included here to prevent compiler warnings about shadowed virtual functions.
Reimplemented in StFlow.
Definition at line 774 of file Flow1D.cpp.
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Evaluate the oxidizer axial velocity equation residual.
The function calculates the oxidizer axial velocity equation as
\[ \frac{dU_{o}}{dz} = 0 \]
This equation serves as a dummy equation that is used only in the context of two-point flame control, and serves as the way for two interior control points to be specified while maintaining block tridiagonal structure. The default boundary condition is \( U_o = 0 \) at the right and zero flux at the left boundary.
For argument explanation, see evalContinuity().
Definition at line 684 of file Flow1D.cpp.
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Get the gradient of species specific molar enthalpies.
Definition at line 1154 of file Flow1D.cpp.
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Indices within the ThermoPhase of the radiating species.
First index is for CO2, second is for H2O.
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double m_zfixed = Undef |
double m_tfixed = -1.0 |