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. 2023 Feb 15;13(9):5687–5722. doi: 10.1039/d2ra07940b

DAC studies associated with first category of chemisorption materials.

Supports PEI type CO2 con. ppm Adsorption T (°C) Desorption T (°C) CO2 purity CO2 capacity mg g−1 Stability mg g−1 Ref.
Nanosilica Ba 90 130/150 142–156 136
Nanosilica Ba 70 85 Pure 147 Minimal leaching 119
Nanosilica La 70 85 Pure 173 Leaching of amine 119
Nanosilica PEI ∼400 ∼25, dry ∼110 103.8 72.6b 129
Nanosilica A-PEI ∼400 ∼25, dry ∼110 99.46 90.2b 129
Nanosilica T-PEI ∼400 ∼25, dry ∼110 96.38 95b 129
MSiNTc 75 121 140
MMSVd 90 166.8 141
Fumed silica FS-PEI-33 23 °C, RH 67% 77.89 4% – 4th cyclee 121
Fumed silica FS-PEI-50 23 °C, RH 67% 62.05 4% – 4th cyclee 121
Fumed silica PEI-H + PEG 50 °C, dry 29.9 Stable-20 cycle 124
SBA-15 PEI 400 75 °C, dry 50–110 22.44 Stable-20 cycle 124
SBA-15 PEI + PEG200 400 30 °C, dry 34.77 125
Zr-SBA-15 PEI 400 25 °C, dry 37.44 4% – 4th cyclee 138
SBA-15 PPI 400 35 °C, dry 110 33.44 Stable-50 cycle 137
Alumina SynA-PEI-50 400 25 °C, dry 76.5 Constant – 3rd cycle 133
γ-alumina PEI 30 °C, RH 50% 86.25 139
HP20 resin PEI 400 25 °C 99.3 2% – 5th cyclee 142
Mesoporous carbon PEI 400 25 °C, humid 99 3% – 10th cyclee 143
Carbon nanotube PEI 400 30 °C, dry 47 3% – 10th cyclee 144
a

B-branched PEI; L-linear PEI and different capacities based on different adsorption temperatures, loading, molecules weights.

b

CO2 capacity after the 4th cycle.

c

Mesoporous silica nanotube.

d

Mesoporous multilamellar silica vesicle.

e

Capacity reduction in the indicated cycle.