1977
DOI: 10.21236/ada036768
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The Coherent Flame Model for Turbulent Chemical Reactions

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Cited by 211 publications
(106 citation statements)
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“…It will be recognized that the present analysis has elements in common with the coherent flame-sheet model described in Marble & Broadwell (1977) -principally that a portion of the reaction takes place in strained laminar flames. It differs in two basic ways.…”
Section: Discussion Of Related Studiesmentioning
confidence: 99%
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“…It will be recognized that the present analysis has elements in common with the coherent flame-sheet model described in Marble & Broadwell (1977) -principally that a portion of the reaction takes place in strained laminar flames. It differs in two basic ways.…”
Section: Discussion Of Related Studiesmentioning
confidence: 99%
“…that the structure is quasi-steady and that the zones may be considered plane, then the analysis of Marble (described e.g. in Marble & Broadwell 1977) is applicable. The distributions of A and B (still considered to be inert) within the zones are in which y is the coordinate normal to the zone, 6 is the local strain rate, and (co) denotes conditions far from the layer.…”
Section: The Modelmentioning
confidence: 99%
“…In the case of an excess of reactant A, however, Marble & Broadwell (1977) show that the surface moves to the right (see figure 18) with respect to the fluid a t a speed 9 * f-1 f + l ' v(t) = a (7) , where erf a = -For f 2 10, v(t) N ( 9 / t ) * . Product is formed at the reaction surface and tencls to be left behind in a region of increasing reactant A as the surface moves to the right.…”
Section: Appendixmentioning
confidence: 98%
“…In this global sense, the product labels the vorticity for an isolated sheet, regardless of Schmidt number. If the sheet is not isolated, 'flame shortening' (Marble & Broadwell 1977) and the analogous 'vortex sheet shortening' effects can alter the ratio (P/S)local. And, if the flow is three-dimensional, vortex stretching will amplify and rotate the vorticity vector.…”
Section: Dtmentioning
confidence: 99%
“…A problem in some EBU models is associated to a near wall poor performance when simulating complex reactive flows. For this reason Marble and Broadwell (1977) developed a flamelet model for tubulent flow with laminar flames that grow according to the flame front distortions and the wall distance, with transport equations for the progress variable and flame area. This area, the flame area density Σ, is given per unit of volume and the model formulation is a little bit different from the EBU ones.…”
Section: Introductionmentioning
confidence: 99%