|
|
The Lagrangian solution method solves the composition PDF transport equation by stochastically tracking Lagrangian particles through the domain. It is computationally expensive since a large number of particles are required to represent the PDF, and a large number of iterations are necessary to reduce statistical errors and explicitly convect the particles through the domain. The Eulerian PDF transport model overcomes these limitations by assuming a shape for the PDF, which allows Eulerian transport equations to be derived. Stochastic errors are eliminated and the transport equations are solved implicitly, which is computationally economical. The multi-dimensional PDF shape is assumed as a product of delta functions. As with the Lagrangian PDF model, the highly non-linear chemical source term is closed. However, the turbulent scalar flux and molecular mixing terms must be modeled, and are closed with the gradient diffusion and the IEM models, respectively.
The composition PDF of
dimension (
species and enthalpy) is represented as a collection of
delta functions (or modes). This presumed PDF has the following form:
where
is the probability in each mode,
is the conditional mean composition of specie
in the
th mode,
is the composition space variable of specie
, and
is the delta function.
The Eulerian PDF transport equations are derived by substituting Equation
11.4-1 into the closed composition PDF transport equation (Equation
11.2-1 with Equations
11.2-2 and
11.3-6). The unknown terms,
and
, are determined by forcing lower moments of this transported PDF to match the RANS lower moment transport equations, using the Direct Quadrature Method of Moments (DQMOM) approach [
103,
218]. The resulting transport equations are:
where
is the probability of the
th mode, and
is the
th specie probability weighted conditional mean composition of the
th mode.
is the effective turbulent diffusivity. The terms
,
and
represent mixing, reaction and correction terms respectively. Note that only
probability equations are solved and the
th probability is calculated as one minus the sum of the
solved probabilities.
Reaction
The reaction source term
in Equation
11.4-3 for the
th composition and the
th mode is calculated as,
|
|
(11.4-4) |
where
is the net reaction rate for the
th component.
Mixing
The micro-mixing term
is modeled with the IEM mixing model:
|
|
(11.4-5) |
where
is the turbulence time-scale and
is the mixing constant.
Hence, for the two-mode DQMOM-IEM model, the mixing terms for component
are,
The default value of
is 2, which is appropriate for gas-phase combustion. For reactions in liquids, where the diffusivities are much smaller than gases, the
Liquid Micro-Mixing option interpolates
from model turbulence [
278] and scalar [
103] spectra.
Correction
Using assumptions to ensure realizability and boundedness, the correction terms
in Equation
11.4-3 for the
th composition are determined from the linear system,
where
are the non-negative integer lower moments (1..
) for each component
. Note that the condition of the matrix decreases with increasing
, which reduces the stability of higher mode simulations.
The dissipation term
in Equation
11.4-7 is calculated as,
|
|
(11.4-8) |
For the two-mode DQMOM-IEM model, the correction terms for the
th component are,
Calculation of Composition Mean and Variance
The mean composition (specie
or energy) is calculated as,
![]() |
(11.4-10) |
and its variance is calculated as
![]() |
(11.4-11) |