Fluidization XVII
Modeling Sorption Enhanced Methanation in Dual Interconnected Fluidized Beds with Different Sorbents
Authors
CO2 DIFB-SEM chemical looping was simulated in AspenPlus, investigating two possible sorbents: CaO derived from limestone and a commercial zeolite 3A. Two âFluidBedâ blocks, including all significant reaction kinetics, simulated the methanator in a range of temperature from 250°C to 350°C and the regenerator at 450 °C, where the spent sorbent is continuously recirculated for dehydration. The analysis was carried out focusing on the outlet gas quality in terms of contaminants for the direct injection in the natural gas grid, introducing dimensionless parameters characterizing the gas and the solid sorbent feeds.
Results showed that the effect of the undesired CaO carbonation prevailed over the CaO hydration one; however, with a sub-stochiometric H2 gas feed, an optimal condition was identified under which the outlet stream met the network specification. As for zeolites, due to the low adsorption capacity, the results suggested that only with a significantly higher amount of sorbent the SEM effect could be appreciable. These results highlighted the need for research on novel sorbents: selectivity towards water adsorption with respect to CO2 appears to be crucial, suggesting that engineered zeolites might be preferable for this technology.