The turbulent portion of the circular fuel jet is analyzed for isobaric subsonic flow under fast direct one-step irreversible reaction between unpremixed fuel and oxidant. Mean spatial profiles for the dependent variables are found numerically from the governing nonlinear partial differential equations, based upon an explicit eddy diffusion and upon a mean rate of reactant consumption proportional to the product of the mean mass fraction of fuel, the mean mass fraction of oxidant, and the appropriate local characterization of the mean rate of strain. Experimental results are employed to evaluate the pertinent constants in the theoretical formulation of the model. I. Introduction T HE structure of the turbulent diffusion flame in the circular fuel-jet geometry is studied theoretically. As such, this represents an extension of the work by Bush, Feldman, and Fendell on the structure of turbulent diffusion flames in the planar fuel-jet1 and in the planar mixing-layer2 geometries. In this present paper, as in these previous papers, the emphasis is on the solution of a model formulation of the boundary-value problem for a turbulent diffusion flame in a flow geometry of practical interest, when the model is based upon the premise that the consumption of reactants and the generation of product(s) and chemical exothermicity are controlled by unsteady, inviscid, inertial, large-scale mixing. In this model, in time-average, for a direct one-step irreversible bimolecular chemical reaction, the mean rate of reactant consumption is taken to be related to the product of the mean mass fraction of oxidant, the mean mass fraction of fuel, and the magnitude of the principal mean strain rate (for the parabolic formulation appropriate for the thin shear layers of interest here). It is argued (as in Refs. 1 and 2) that, in general, the magnitude of the principal mean strain rate furnishes a characteristic frequency for the mean rate of local chemical activity in a turbulent diffusion flame in which macroscopic mixing is rate-controll ing. This explicit local algebraic (as opposed to field-type differential) expression adopted for the mean rate of chemical reaction is compatible with the adoption of an explicit local algebraic (eddy viscosity) expression for the mean rate of diffusive transport. The present model was first studied in detail for the planar mixing layer formed by two parallel streams.2 However, whereas the fully developed mixing layer is tractable for analysts, it is not tractable for experimentalists and, therefore, some empirical constants in the theory remained unassigned for lack of data. Experimentalists38 have treated the fuel jet exhausting into an oxidant-conta ining ambient, and, under the assumption that values for empirical factors may be transferable between geometries, solutions were
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