https://doi.org/10.1039/C8TA06224B “To examine the variation of CO2 uptake with temperature and hence to identify the optimal adsorption temperature, quasi-static CO2 adsorption tests were first conducted for PEI-modified
https://doi.org/10.1016/j.jiec.2017.05.018 “CO2 adsorption measurements were carried out at different temperature on HPS-TEPA-60% to test the influence of the adsorption temperature. A better fitting between the data
https://doi.org/10.1016/j.jiec.2017.05.018 ” The influence of temperature on the CO2 capture process was investigated by operating adsorption experiments at 30 °C, 45 °C, 60 °C, 75 °C, 90 °C and 105 °C with
https://doi.org/10.1016/j.apenergy.2016.09.081 “The CO2 adsorption performance of the impregnated materials at different temperatures gives essential information about the best temperature at which the sorbents should be used
https://doi.org/10.1016/j.apenergy.2016.09.081
https://doi.org/10.1039/D0RA04497K “As shown in Fig. 8, the CO2 adsorption kinetics of the SASA-3 change with different temperatures. On account of the thermodynamic theory, the CO2 adsorption capacity of
https://doi.org/10.1016/j.cej.2014.04.063 “TGA experiments have been conducted to determine the CO2 uptake at different adsorption temperatures with 15% CO2 in N2. The results shown in Fig. 10 indicate that CO2 uptake
https://doi.org/10.3390/ma14143885 “The CO2 uptake for the SG and the AC determined at different temperatures has been summarized in Figure 11a. The CO2 uptake (mg/g) varied substantially with changes
https://doi.org/10.3390/en13215804 “The amine loading density (ρN) of functionalized silica SBA-15, which includes the quantities of impregnated and grafted amine, is an essential parameter for evaluating
https://doi.org/10.3390/inorganics10070087 “Figure 7 displays the CO2 adsorption isotherms of HSMs(DC)-0.15-APTES, HSMs(DC)-0.15-NTPEA, and HSMs(DC)-0.15-NH2 modified with amine groups. The amounts of adsorbed CO2 were 1.98 mmol/g for HSMs(DC)-0.15-APTES, 2.22 mmol/g
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