2010
DOI: 10.1016/j.pecs.2010.02.002
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Trends in modeling of porous media combustion

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Cited by 149 publications
(41 citation statements)
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“…The results are interpreted as an increase of S with pressure, which is less pronounced for leaner mixtures. The majority of numerical simulations, applied so far, are based on 1D volume averaged models, while just few models are applied upon 2D and 3D domains [7]. Especially on 3D pore level, few studies about flow dynamics without combustion reactions [9,[14][15][16][17] and combustion [18,19] are available.…”
Section: Literature Reviewmentioning
confidence: 99%
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“…The results are interpreted as an increase of S with pressure, which is less pronounced for leaner mixtures. The majority of numerical simulations, applied so far, are based on 1D volume averaged models, while just few models are applied upon 2D and 3D domains [7]. Especially on 3D pore level, few studies about flow dynamics without combustion reactions [9,[14][15][16][17] and combustion [18,19] are available.…”
Section: Literature Reviewmentioning
confidence: 99%
“…For a constant thermal conductivity λ s and for a temperature difference of T, the heat conduction equation can be written in terms of resistance to heat floẇ q = − T/R (7) where R = x/λ s is the thermal resistance. The thermal resistance is proportional to the length x parallel to the path taken by the heat flow and is inversely proportional to the thermal conductivity of the material.…”
Section: D Volume Averaged Modelmentioning
confidence: 99%
“…The porous media combustion modeling trends up to 1994 [2] are mainly described 1D models only. Takeno, Echigo, and their coworkers [3] are the pioneers in PMC modeling to study the effects of mass flow rate and heat transfer coefficient on flame characteristics in excess enthalpy flames and suggested inserting a porous, highly conductive solid into the flame to conduct heat from the solid to the reactants.…”
Section: Porous Media Combustion Modeling (Pmc Modeling)mentioning
confidence: 99%
“…Thermal conductivities of ceramic foam and alumina pellets are [48]: k con-f ¼ k f (1 À ε f ), k con-p ¼ k p (1 À ε p ), where k f ¼ 30 W/(m K) for SiC; k p ¼ 2.2 W/(m K) for alumina [49].…”
Section: Effect Of Equivalence Ratio On the Temperature Profilementioning
confidence: 99%