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Landfills produce both carbon dioxide and methane at different stages of their development.
Lean pre-mixtures of methane at different equivalence ratios were divided between two concentric co-flows to obtain annular stratification.
Rhenium supported on γ-alumina has been tested as a catalyst for the partial oxidation and dry reforming of methane at different temperatures.
The fugacity coefficients of pure methane at different temperatures and pressures in the simulations are shown in Fig. 2a, and the fugacity coefficients of the mole fraction of methane in the binary gas mixture at different pressures in the simulations are described in Fig. 2b, c.
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The MEC performance as an energy carrier generator was characterized based on the hydrogen production rate evolution, the variations of microbial distributions, and methane production at different applied potential differences.
These phases catalyze methane oxidation at different rates.
Methane autoignition time in dependence of temperature, reaction pathways with rate of production, sensitivity and flow diagram analysis have been exploited in order to highlight the kinetic controlling steps of methane autoignition at different temperature ranges.
Fig. 6 Methane production at different wall-shear stresses, COD = 400 mg/L.
It could also be found from Fig. 2 that the different variable trend for methane production at different F/I ratio level (shown in Fig. 2a) represented the interaction was significant between F/I ratio and organic loading.
The same variable trend for methane production at different initial pH and F/I ratio level (shown in Fig. 2b) implied interaction was not significant between initial pH and F/I ratio.
The combination of simulation and experimental studies provided a powerful tool to investigate the biogeochemical processes in the methane leakage environment at different temporal and spatial scales.
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