https://doi.org/10.1016/j.cej.2014.04.063 “One of the most advantageous features of chemi-sorbents over physi-sorbents is that chemi-sorbents do not suffer from a significant reduction in CO2 adsorption capacities at
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/10.1016/j.cej.2014.04.063 “To investigate the effects of moisture on the performance of PEI–silica adsorbent, a moisture saturator is installed at the entrance of BFB to generate
https://doi.org/10.1016/j.cej.2014.04.063 “24 cycles of adsorption and desorption tests for Batch I PEI–silica adsorbent were carried out at an initial bed temperature of 70 °C under dry
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/ma14143885 “The reliance of Co on the breakthrough profiles is depicted in Figure 10a for silica gel at 4 lpm and 298K. The various CO2 levels in the
https://doi.org/10.3390/ma14143885 “The dependence of the feed flow on the breakthrough period for the SG is depicted in Figure 9a. The volumetric flow rates in the range
https://doi.org/10.1016/j.ces.2014.05.018 “The results of the air capture tests for the two batches of PEI–silica adsorbent are summarized in Table S1 (Supplementary information) and illustrated in Fig. 5, Fig. 6.
https://doi.org/10.1016/j.ces.2014.05.018 “Fig. 1 shows the schematic and a photograph of the BFB reactor system designed and built for the evaluation of CO2 capture and regeneration using solid
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
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