ANSYS FLUENT requires additional inputs that are used in the creation of the look-up tables. Several of these inputs control the number of discrete values for which the look-up tables will be computed. These parameters
are input in the
Table tab of the
Species Model dialog box (e.g., Figure
16.7.1).
Figure 16.7.1: The
Species Model Dialog Box (
Table) Tab
 |
The look-up table parameters are as follows:
-
Number of Mean Mixture Fraction Points
is the number of discrete values of
at which the look-up tables will be computed. For a two-mixture-fraction model, this value is the number of points in the instantaneous state profile used to compute the PDF if you choose the
PDF model (see Section
16.10.4). Increasing the number of points will yield a more accurate PDF shape, but the calculation will take longer. The mean mixture fraction points will be automatically clustered around the stoichiometric mixture fraction value.
-
Number of Mixture Fraction Variance Points
is the number of discrete values of
at which the look-up tables will be computed. Lower resolution is acceptable because the variation along the
axis is, in general, slower than the variation along the
axis of the look-up tables. This option is available only when no secondary stream has been defined.
-
Number of Secondary Mixture Fraction Points
is the number of discrete values of
at which the look-up tables will be computed. Like the
Number of Mean Mixture Fraction Points,
ANSYS FLUENT will use the
Number of Secondary Mixture Fraction Points to compute the equilibrium state-relation if you choose the
PDF option (see Section
16.10.4) for a two-mixture-fraction model. A larger number of points will give a more accurate shape for the PDF, but with a longer calculation time. This option is available only when a secondary stream has been defined.
-
Maximum Number of Species
is the maximum number of species that will be included in the look-up tables. The maximum number of species that can be included is 100. Note that the maximum number of species for the equilibrium computations is 500, and the maximum number of species for the flamelet generation and importing is 300.
ANSYS FLUENT will automatically select the species with the largest mole fractions to include in the PDF table.
-
Number of Mean Enthalpy Points
is the number of discrete values of enthalpy at which the look-up tables will be computed. This input is required only if you are modeling a non-adiabatic system. In general, you should choose the The number of points required will depend on the chemical system that you are considering, with more points required in high heat release systems (e.g., hydrogen/oxygen flames). This option is not available with the unsteady flamelet model.
-
Minimum Temperature
is used to determine the lowest temperature for which the look-up tables are generated (see
this figure in the separate
Theory Guide). Your input should correspond to the minimum temperature expected in the domain (e.g., an inlet or wall temperature). The minimum temperature should be set 10-20 K below the minimum system temperature. This option is available only if you are modeling a non-adiabatic system. This option is not available with the unsteady flamelet model.
-
Include Equilibrium Flamelet
specifies that an equilibrium flamelet (i.e.,
) will be generated in
ANSYS FLUENT and appended to the flamelet library before the PDF table is calculated. This option is available when generating or importing multiple flamelets, as well as when a single flamelet is considered. In the latter case, the PDF table will consist of two scalar dissipation slices, namely the equilibrium slice at
, and the flamelet slice. This option is not available with the equilibrium chemistry model or the unsteady flamelet model.
When you are satisfied with your inputs, click
Calculate PDF Table to generate the look-up tables.
The computations performed for a single-mixture-fraction calculation culminate in the discrete integration of
this equation (or
this equation in the separate
Theory Guide) as represented in
this figure (or
this figure in the separate
Theory Guide). For a two-mixture-fraction calculation,
ANSYS FLUENT will calculate the physical properties using
this equation or its adiabatic equivalent. The computation time will be shortest for adiabatic single-mixture-fraction equilibrium calculations and longest for non-adiabatic calculations involving multiple flamelet generation. Below, sample outputs are shown for an adiabatic single-mixture-fraction equilibrium calculation and a non-adiabatic calculation with laminar flamelets:
Generating PDF lookup table
Type of the PDF Table: Adiabatic Table (Two Streams)
Calculating table .....
1271 points calculated
22 species added
PDF Table successfully generated!
|
Generating PDF lookup table
Type of the PDF Table: Nonadiabatic Table with Strained Flamelet Model (Two St
Calculating table .....
calculating temperature limits .....
calculating temperature limits .....
calculating scalar dissipation slices .....
- scalar dissipation slice 9
calculating equilibrium slice .....
Performing PDF integrations.....
16810 points calculated
17 species added
PDF Table successfully generated!
Initializing PDF table arrays and structures.
|
-
|
Note that there is a significant difference in run-time between the one-mixture fraction model and the two-mixture fraction model. In the one-mixture fraction model, the PDF table contains the
mean data of density, temperature, and specific heats, and is three-dimensional for an equilibrium nonadiabatic case (mean mixture fraction, mixture fraction variance, and mean heat loss). For this case,
ANSYS FLUENT updates properties every flow iteration. In the case of the two-mixture fraction model, only the instantaneous state relationships are stored and mean properties are calculated from these by performing PDF integrations in every cell of the
ANSYS FLUENT simulation. Since this is computationally expensive,
ANSYS FLUENT provides the option of only updating properties after a specified number of iterations.
|
After completing the calculation at the specified number of mixture fraction points,
ANSYS FLUENT reports that the calculation succeeded. In a single-mixture-fraction case, the resulting look-up tables take the form illustrated in
this figure in the separate
Theory Guide (or
this figure , for non-adiabatic systems). These look-up tables can be plotted using the available graphics tools, as described in Section
16.7.4.
Note that in non-adiabatic calculations, the console window will report that the temperature limits and enthalpy slices have been calculated.
For a two-mixture-fraction case, the resulting look-up tables take the form illustrated in
this figure in the separate
Theory Guide (or
this figure , for non-adiabatic systems).
Previous:
16.6.4 Postprocessing the Flamelet
Up:
16. Modeling Non-Premixed Combustion
Next:
16.7.1 Full Tabulation of
Release 12.0 © ANSYS, Inc. 2009-01-29