https://doi.org/10.3390/catal11111355 “CO2 capacity was determined via the measurements of CO2 isotherms of the materials, as shown in Figure 7, where the CO2 adsorption capacity and the adsorption rate together
https://doi.org/10.1016/j.apsusc.2014.06.164 “In order to collect experimental evidence as to whether chemisorption of CO2 on amine-loaded samples would take place, as suggested in a previous publication [4] and in
https://doi.org/10.1016/j.apsusc.2014.06.164 “CO2 adsorption and desorption isotherms were measured for the amino-loaded zeolite (ZX10) at two temperatures, 298 and 348 K, which are shown in Fig. 8(a) and (b), respectively.”
https://doi.org/10.1016/j.apsusc.2014.06.164 “Taking into account the results obtained from the characterization of the pristine and grafted adsorbents, the samples ZX, ZX0.2 and ZX10 were chosen to
https://doi.org/10.1088/1468-6996/9/1/013007 “Several investigations carried out with diverse zeolites (LaM-10, H-ZSM-5, M-ZSM-5 (M = Li+, Na+, K+, Rb+, Cs+), NaX or 13X, 5A, 4A, NaLSX, MCM-48,
https://doi.org/10.1016/j.jmrt.2020.02.061 “The adsorption performance and selectivity of N2 and O2 are indispensable for the exploration of the practical properties of the adsorbent. Adsorption selectivity of CO2/N2 and CO2/O2 is
https://doi.org/10.1016/j.jmrt.2020.02.061 “Adsorption and desorption isotherms measured at pressure up to 115 kPa are presented in Fig. 6. The high degree of coincidence of the adsorption and desorption
https://doi.org/10.3390/app12031558 “All measured isotherms were fitted using three analytical models. Indeed, the adjusting findings show that the parameters of the monolayer model were not acceptable
https://doi.org/10.1016/j.fuel.2022.123953 “CO2 adsorption measurements at 25 °C up to 1 bar were carried out on ASAP 2020 (Micromeritics). In the first time, the CO2 adsorption capacity of kaolinite and
https://doi.org/10.3390/molecules26247520 “CO2 adsorption isotherms obtained at 273 K and 298 K are presented in Figure 7A,B, respectively. The data values of CO2 adsorption capacity are shown in Table 5.
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