https://doi.org/10.1016/j.fuel.2022.123842 “Catalytic activities of LaNiO3-derived DFMs are evaluated by analyzing the evolution of CH4 and CO production per cycle with reaction temperature (Fig. 7). These parameters
https://doi.org/10.1016/j.fuel.2022.123842 “CO2 adsorption and hydrogenation cycles were carried out in a vertical stainless steel tubular reactor inside a 3-zone tube furnace. The reactor was filled with
https://doi.org/10.1016/j.gce.2021.11.009 “Although DFMs with different adsorptive and catalytic components have been conducted on iCCC-Methane process, the adsorption capacity and methane yield are still relatively low,
https://doi.org/10.1016/j.gce.2021.11.009 “Notably, the reaction pressure also affects CO2 adsorption performance and catalytic activity. Miguel et al. [17] found that by using the mixed bed made of a
https://doi.org/10.1016/j.gce.2021.11.009 “It is well known, components in flue gas, including O2, H2O, SOx and NOx, will affect the adsorption and catalytic performance of DFMs. Considering industrial
https://doi.org/10.1016/j.gce.2021.11.009 “temperature is the most important parameter in methanation process, and should be well controlled in the iCCC-Methane to make the CO2 capture and methanation conversion
https://doi.org/10.1016/j.gce.2021.11.009 “Currently, the iCCC-Methane is mainly carried out in fixed-bed reactors, and various packing modes, such as the multilayer bed mode [17], dual-bed mode [37],
https://doi.org/10.1016/j.gce.2021.11.009 “Meanwhile, the mechanism of iCCC-Methane has been explored to illustrate the synergistic effect of DFMs. Cobo et al. [35] investigated the mechanism of iCCC-Methane on
https://doi.org/10.1016/j.fuel.2022.123842 The following content was copied from the above open access paper. It is noted that using this reported LaNiO3-derived DFMs, the capacity of CO2
Dual functional materials, including Pt as the catalytic sites and Na as the sorbent sites, were used for ICCU-RWGS. Al2O3 was used as the support
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