Selection of POPs based on pre-porous precursors and POPs used as organocatalysts. Surface area, CO2 uptake, CO2 Heat of adsorption (Qst) and CO2/N2 selectivity.
Sample | SABETa (m2 g−1) | CO2 at 273 K (mmol g−1) | CO2 at 298 K (mmol g−1) | CO2Qst (kJ mol−1) | CO2/N2 selectivityb | Application | Ref. |
---|---|---|---|---|---|---|---|
NPOF-4 | 1249 | 2.50 | 1.40 | 23.2 | 27 | Gas sorption | 65 |
NPOF-4-NO2 | 337 | 2.42 | 1.56 | 32.5 | 139 | Gas sorption | 65 |
NPOF-4-NH2 | 554 | 2.90 | 1.88 | 30.1 | 101 | Gas sorption | 65 |
Azo-COP-1 | 635.8 | 2.44 | 1.48 | 29.3 | 63.7 | Gas sorption | 23 |
Azo-COP-2 | 729.6 | 2.55 | 1.53 | 24.8 | 109.6 | Gas sorption | 23 |
Azo-COP-3 | 493.1 | 1.93 | 1.22 | 32.1 | 78.6 | Gas sorption | 23 |
Azo-COP-4 | 11.1 | 1.75 | 1.12 | 26.8 | 79.3 | Gas sorption | 23 |
Azo-COP-5 | 127.6 | 2.04 | 1.24 | 27.3 | 73.8 | Gas sorption | 23 |
Azo-COP-6 | 679.1 | 2.22 | 1.31 | 25.8 | 72.7 | Gas sorption | 23 |
Azo-COP-7 | 241.6 | 1.91 | 1.16 | 26.1 | 68.5 | Gas sorption | 23 |
Azo-COP-8 | 472.1 | 2.02 | 1.22 | 25.3 | 70.3 | Gas sorption | 23 |
Azo-COP-9 | 649.5 | 2.05 | 1.23 | 25.3 | 69.6 | Gas sorption | 23 |
Azo-COP-10 | 200.2 | 1.91 | 1.15 | 27.9 | 69.6 | Gas sorption | 23 |
Azo-COP-11 | 336.1 | 2.13 | 1.26 | 27.4 | 77.7 | Gas sorption | 23 |
PAF-1 | 4100 | 2.46 | — | — | — | Gas sorption | 67 |
PAF-1-CH3 | 3007 | 2.45 | — | — | — | Gas sorption | 67 |
PAF-1-CH2OH | 1727 | 2.98 | — | — | — | Gas sorption | 67 |
PAF-1-phthalimide | 974 | 2.23 | — | — | — | Gas sorption | 67 |
PAF-1-CH2NH2 | 1263 | 4.37 | — | — | — | Gas sorption | 67 |
PAF-1-CH2N = CMe2 | 1302 | 3.12 | — | — | — | Gas sorption | 67 |
2D-PTNS | 690 | 3.11 | — | 30.7 | 93 | Gas sorption | 68 |
PNOP-1 | 830 | 4.00 | 2.42 | 30.0 | 52.1 | Gas sorption | 76 |
PNOP-2 | 729 | 3.04 | 1.96 | 31.3 | 80.1 | Gas sorption | 76 |
3D-tPOP | 22 | 2.38 | — | — | — | Gas sorption | 78 |
3D-tPOP-NaCl-2.0 | 1058 | 4.42 | 2.62 | 42.1 | — | Gas sorption | 78 |
CXF1-OMe | 626 | 1.49 | — | 26.0 | — | Gas sorption | 89 |
CFX1-OH | 540 | 2.20 | 1.5 | 35.0 | 98 | Gas sorption | 89 |
co-CXF3-OPr | 2609 | 2.40 | — | 23.2 | — | Gas sorption | 89 |
co-CXF3-OH | 1943 | 2.91 | — | 30.0 | — | Gas sorption | 89 |
TMP1 | 923 | 3.50 | 2.04 | 22.2 | 64 | Gas sorption | 69 |
TMP2 | 1094 | 3.70 | 2.18 | 21.1 | 60 | Gas sorption | 69 |
TMP3 | 1372 | 5.07 | 3.27 | 22.0 | 70 | Gas sorption | 69 |
TNHCP1 | 848 | 2.89 | 2.20 | 30.8 | 30 | Gas sorption | 70 |
TNHCP2 | 766 | 3.64 | 2.11 | 32.8 | 42 | Gas sorption | 70 |
TNHCP3 | 751 | 3.53 | 2.23 | 32.7 | 45 | Gas sorption | 70 |
NTP | 1067 | 3.45 | 1.82 | 26 | 18 | Gas sorption | 71 |
3D-CON | 2247 | 6.07 | 3.90 | 31.87 | — | Gas sorption | 71 |
PMDI-cage 1a | 522 | 2.91 | — | 27.0 | 26.9 | Gas sorption | 80 |
Cg-Am | 104 | 0.89 | — | — | — | CO2 conversion | 82 |
Cage-1 | — | 0.10 | — | — | 138 | Gas sorption | 83 |
F1 | — | 0.19 | — | — | 64 | Gas sorption | 79 |
F2 | — | 0,23 | — | — | 42 | Gas sorption | 79 |
F3 | — | 0,16 | — | — | 213 | Gas sorption | 79 |
Noria | 221 | 1.77 | — | 30.4 | — | CO2 conversion | 87 |
NPOP | 773 | 2.09 | 1.36 | 28.9 | 30 | CO2 conversion | 87 |
HRN4 | 156 | 1.39 | — | — | — | CO2 conversion | 88 |
RN4-Az-OH | 340 | 2.04 | — | 30.8 | 19 | CO2 conversion | 88 |
RN4-OH | 720 | 2.25 | — | 29.5 | 20 | CO2 conversion | 88 |
RN4-F | 1230 | 2.59 | — | 28.5 | 35 | CO2 conversion | 88 |
cCTF-400 | 744 | 2.86 | 1.89 | 49 | — | CO2 conversion | 98 |
cCTF-450 | 861 | 2.25 | 1.41 | 46 | — | CO2 conversion | 98 |
cCTF-500 | 1247 | 3.02 | 1.82 | 43 | — | CO2 conversion | 98 |
Py-iPOP-1 | 65 | 0.82 | 0.55 | — | — | CO2 conversion | 100 |
Surface area is calculated based on Brunauer–Emmett–Teller (BET) theory.
The CO2/N2 selectivity calculated using IAST (ideal adsorbed solution theory) for the flue gas mixture, CO2/N2:10/90 (v/v) at 298 K.