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A thick reaction zone model for premixed flames in two-dimensional channels

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arxiv 2406.15190 v2 pith:VEYOGCRF submitted 2024-06-21 physics.flu-dyn

classification physics.flu-dyn
keywords reactionzoneeffectschannelflameflowlambdalaminar
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abstract

Direct interactions between the flow field and the chemical reaction in premixed flames occur when the reaction zone thickness is comparable to, or greater than flow length scales. To study such interactions, a laminar model is considered that has direct bearings to steadily propagating deflagrations in a Hele-Shaw channel with a background plane Poiseuille flow. The study employs asymptotic analyses, pertaining to large activation energy and lubrication theories and considers a distinguished limit where the channel width is comparable to the reaction zone thickness, with account being taken of thermal-expansion and heat-loss effects. The reaction zone structure and burning rates depend on three parameters, namely, the Peclet number, $\mathcal{P}$, the Lewis number, $Le$ and the ratio of channel half-width to reaction zone thickness, $\lambda_*$. When the parameter $\lambda_*$ is small, transport processes are controlled by Taylor's dispersion mechanism and an explicit formula for the effective burning speed $S_T$ is obtained. The formula indicates that $S_T/S_L \propto 1/Le$ for $\mathcal{P}\gg 1$, which interestingly coincides with a recent experimental prediction of the flame speed in a highly turbulent jet flame. The results suggest that the role played by differential diffusion effects is significant both in laminar and turbulent cases. The reason for the peculiar $1/Le$ dependence can be attributed, in our laminar model, to Taylor dispersion. Presumably, this dependence may be attributed to a similar but more general mechanism in the turbulent case, rather than to diffusive-thermal curvature effects. The latter effects play however an important role in determining the flame speed when $\lambda_*$ is large. The magnitude of heat losses at extinction, is multiplied by a factor $1/Le^2$ in comparison with those corresponding to the no-flow case in narrow channels.

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