| Literature DB >> 28794951 |
Ziyan Jia1,2, Jiannan Pan2, Daqiang Yuan1.
Abstract
By introducing various N-containing compounds as efficient linkers, a series of hyper-crosslinked porous polymers with high surface areas and gas-uptake values were synthesized by using the Friedel-Crafts alkylation reaction. Structural characterization indicated the presence of nitrogen atoms, and gas-sorption experiments revealed that the high gas uptake benefitted from the high surface areas and the incorporation of N-containing linkers as Lewis basic sites. Among these porous polymers, HCP-4 had the highest H2 uptake of 9.29 mmol g-1 at 77 K and 0.1 MPa and the highest C2H2 uptake of 6.69 mmol g-1 at 273 K and 0.1 MPa, whereas HCP-3 showed the best CO2 uptake of 4.42 mmol g-1 at 273 K and 0.1 MPa. To understand better the important role played by nitrogen in these polymers, the isosteric heat of adsorption and adsorption selectivity of CO2 over N2 were calculated. The results showed that the triazine-based polymer HCP-1 had the highest CO2 over N2 selectivity of 75.4 at 295 K and 0.1 MPa, which makes it the most potential candidate for CO2 capture.Entities:
Keywords: Lewis bases; N-containing linkers; adsorption; gas separation; polymers
Year: 2017 PMID: 28794951 PMCID: PMC5542758 DOI: 10.1002/open.201700073
Source DB: PubMed Journal: ChemistryOpen ISSN: 2191-1363 Impact factor: 2.911
Scheme 1Strategy for the design of the HCPs.
Scheme 2Conditions for the synthesis of the HCPs.
Figure 1FTIR spectra of HCP‐1–4.
Figure 2Solid‐state 13C CP/MAS NMR spectra of HCP‐1–4.
Figure 3a) N2‐sorption isotherms of HCP‐1–4 measured at 77 K. b) Pore‐size distributions of HCP‐1–4.
Porosity data for HCP‐1–4.
| Polymer |
|
|
|
|
|---|---|---|---|---|
| HCP‐1 | 1009 | 0.24 | 0.56 | 0.43 |
| HCP‐2 | 1742 | 0.27 | 1.23 | 0.22 |
| HCP‐3 | 1231 | 0.29 | 0.71 | 0.41 |
| HCP‐4 | 1951 | 0.25 | 1.46 | 0.17 |
[a] BET surface area. [b] Micropore volume calculated by the t‐plot method. [c] Pore volume calculated from the N2 isotherm at P/P 0=0.95 and 77 K.
Figure 4Gas‐sorption isotherms of HCP‐1–4: a) H2 at 77 K and 1 bar, b) C2H2 at 273 K and 1 bar, and c) CO2 at 273 K and 1 bar (1 bar=0.1 MPa). Heats of adsorption for HCP‐1–4: d) H2 measured at 77 and 87 K, e) C2H2 measured at 273 and 295 K, and f) CO2 measured at 273 and 295 K.
Gas uptake and selectivity data for HCP‐1–4.
| Polymer | Gas uptake[a] [mmol g−1] |
| CO2/N2 selectivity[c] | |||||
|---|---|---|---|---|---|---|---|---|
| H2 | C2H2 | CO2 | H2 | C2H2 | CO2 | 273 K | 295 K | |
| HCP‐1 | 7.46 | 5.56 | 4.24 | 7.8 | 39.8 | 29.1 | 92.3 | 75.4 |
| HCP‐2 | 8.75 | 6.33 | 4.05 | 7.6 | 25.3 | 19.5 | 28.8 | 23.7 |
| HCP‐3 | 8.04 | 6.22 | 4.42 | 7.6 | 29.3 | 23.5 | 57.5 | 42.9 |
| HCP‐4 | 9.29 | 6.69 | 4.25 | 7.8 | 25.4 | 20.8 | 25.7 | 21.0 |
[a] Data were recorded at 77 K/0.1 MPa for H2, 273 K/0.1 MPa for C2H2, and 273 K/0.1 MPa for CO2. [b] Heat of adsorption at zero loading for H2, C2H2, and CO2, respectively. [c] IAST‐predicted adsorption selectivities at 273 and 295 K, using a 15:85 CO2/N2 ratio at 0.1 MPa.
Figure 5Selectivity of CO2 over N2 calculated by the IAST method at 295 K.