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Fig. 4.11 a N 2 sorption isotherms of PAF-1 and PAF-1-350, PAF-1-380, PAF-1-400, PAF-1-
450; b pore size distributions of PAF-1 and PAF-1-350, PAF-1-380, PAF-1-400, PAF-1-450
derived from N 2 adsorption calculated by Density Functional Theory (DFT); c CO 2 adsorption
and desorption isotherms of PAF-1 and carbonized samples at 273 K; d Q STCO 2 of PAF-1 and car-
bonized samples as a function of the amount of CO 2 adsorbed. Reprinted with permission from
Ref. [ 59 ]. Copyright 2013, Royal Society of Chemistry
different temperature from 350 to 450 °C [ 59 ]. Calculated from the N 2 sorption
results using BET model, the surface areas of PAF-1-350, PAF-1-380, PAF-
1-400, and PAF-1-450 were 4,033, 2,881, 2,292, and 1,191 m 2 g 1 , respec-
tively (Fig. 4.11 a). Calculated by the density functional theory (DFT) method,
the total pore volumes of these samples dropped from 2.43 cm 3 g 1 of PAF-1 to
0.53 cm 3 g 1 of PAF-1-450. Meanwhile, the pore size distribution shrunk from
1.44 nm of PAF-1 to 1.00 nm of PAF-1-450 (Fig. 4.11 b). Especially, the CO 2
uptake of PAF-1-450 reached 4.5 mmol g 1 , at 273 K and 1 bar (Fig. 4.11 c).
As expected, the Qst CO 2 of carbonized PAF-1 increased evidently by comparison
with the original PAF-1 (Fig. 4.11 d).
CCS is a hot topic due to its important environmental sustainability which con-
cerns our daily life. POFs display some advantages in CO 2 capture thanks to their
high surface area, high stability, and adjustable structure. The pioneering studies
provide guidelines for the construction of promising POFs for CCS.
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