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Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor

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Figure

Fig. 1.  TFRR operating principle and experimental schema
Table 1.  Properties of the honeycomb monolith
Fig. 5 shows the numerical results for a mixed gas flow velocity of 0.5 m/s, methane concentration of 0.5% (by volume), and a switching time of 150 s
Fig. 10.  Axial temperature distribution as gas flows from left to right within the same cycle

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