A model for premixed turbulent combustion based on a joint velocity probability density function (PDF) method and a progress variable is presented. Compared with other methods employing progress variables, the advantage here is that turbulent mixing of the progress variable requires no modeling. Moreover, by applying scale separation, the Lagrangian framework allows to account for the embedded, quasi laminar flame structure in a very natural way. The numerical results presented here are based on a simple closure of the progress variable source term and it is demonstrated that the new modeling approach is robust and shows the correct qualitative behavior
Background and Modeling ApproachTurbulent combustion is central for many engineering applications. Whereas the modeling approach based on mixture fraction and laminar flamelets proofed to be very successful for non-premixed combustion, currently there exists no general approach for premixed flames. In the Eulerian context a common model is the one by Bray, Moss and Libby (BML) [2]. They assume an infinitely thin flame and use a progress variable c ∈ {0, 1} to describe, whether the gas is burnt (c = 1) or unburnt (c = 0). The difficulty is to close the transport equation for the Favre average of c, i.e. to model the turbulent transport and mean source terms. Another modeling approach for premixed combustion is based on laminar flamelets and a level set equation to determine the flame position. For turbulent flames, however, it is not straight forward to achieve closure. The advantage of using joint probability density function (PDF) methods [9] is that reaction source term and turbulent convection appear in closed form. On the other hand, modeling molecular mixing remains a major challenge. In the following, we present a new approach, which is a combination of a hybrid joint PDF method [3,4,6, 10], a transported progress variable, and the flamelet model. The probability density function (PDF) of a progress variable c can be described by a bimodal distribution. Note that the use of such a PDF by the BML model for the temperature implies that the flame is infinitely thin. With such a presumed shape the PDF is specified by the Favre mean value of c, which can be obtained by solvingwhere the operators·, · and · denote Favre averaged, Reynolds averaged and Favre fluctuating quantities, respectively. Moreover, U is the fluid velocity, ρ the density and ω c the mean progress variable source term. A physical interpretation of Eq. (1) is given in [7]. By applying the BML model, the difficulties are the closures of the two terms on the right-hand side, i.e. of turbulent transport and production of c. In our model, each computational particle used by the joint PDF solution algorithm has a property c * ∈ {0, 1} that only indicates the arrival of an embedded quasi laminar flame at the fluid particle ( * denotes a particle property). The flame is therfore not assumed to be infinitely thin and its internal structure can be resolved. Herefore, the relative position of the particl...