Equilibrium of SrO/SrCO3 and stability
SrO requires temperatures higher than 1000 °C to capture CO2. As shown below, for a CO2 source containing 20% CO2, higher than 1050 °C was
SrO requires temperatures higher than 1000 °C to capture CO2. As shown below, for a CO2 source containing 20% CO2, higher than 1050 °C was
SrO was loaded on Fe2O3 through impregnation. The performance of the derived sorbents were tested in terms of CO2 capture, and in particular about the
https://doi.org/10.1016/j.jece.2019.102927 As shown below, the developed LiNaZr adsorbents showed relatively stable CO2 capture performance after 20 cycles. The two adsorbents were prepared at different calcination
Different ratios of Li and Na were investigated for the development LiNaZr adsorbents, which were prepared through simple impregnation (https://doi.org/10.1016/j.jece.2019.102927). The addition of Na showed
https://doi.org/10.1016/j.jallcom.2021.162419 As shown below, K-promoted LiZr adsorbent had a stable performance during the cycles of CO2 capture. The capacity of CO2 capture was even enhanced
As shown below, in general the presence of water facilitated the capture of CO2 using Na and K promoted LiZr adsorbents (https://doi.org/10.1016/j.jallcom.2021.162419). In particular, when
The addition of K and Na clearly promoted the kinetics of CO2 capture using LiZr based adsorbents. As shown in the following figure, the reaction
https://doi.org/10.1039/C6TA06133H “Cyclic absorption–desorption performances for 15 cycles at 948 K using 100% CO2 and 100% N2 gases were recorded and the results are shown in Fig. 6a. As
https://doi.org/10.1039/C6TA06133H “Detailed results of the CO2 absorption performance of the sample (eutectic-3) at temperatures of 623–923 K are shown in Fig. 5a. As shown, absorption capacity as
https://doi.org/10.1039/C6TA06133H “Schematic illustrations comparing the carbon dioxide sorption and desorption mechanisms of Li4SiO4 nanoparticles and the newly developed nano rods, as well the influence of particle
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