Table 2.
Different zeolite adsorbents with their operating conditions and performance parameters.
| Year | Adsorbent | Pressure [bar] | Temperature [Co] | CO2 uptake [mmol g−1] | Ref. |
|---|---|---|---|---|---|
| 2002 | CuBTC | 1 | 22 | 5 | [106] |
| 2004 | Zeolite 13X | 1.6 | 25 | 5.1 | [107] |
| 2009 | Zeolite 13X | 1 | 25 | 4.7 | [108] |
| 2010 | Zeolite 13X | 5 | 25 | 3.2 | [109] |
| 2011 | Mesoporous alumina | 1 | 25 | 1.2 | [110] |
| 2012 | N-rich porous carbon | 1 | 25 | 2.3 | [111] |
| 2015 | 5A@ZIF-8 | 1 | 25 | 0.31 | [112] |
| 2015 | Na-RTH zeolite | 1 | 25 | 3.2 | [113] |
| 2017 | ZIF-8 | 1 | 0 | 0.499 | [114] |
| 2017 | Zeolite 13X (13X–F) | 8–20 | 35 | 3.2 | [115] |
| 2017 | Na-Rho | 1 | 25 | 6.1 | [116] |
| 2017 | Zn/Co-ZIF | 1 | 0 | 0.727 | [117] |
| 2017 | Zeolite 13X (13X–C) | 8–20 | 35 | 6.2 | [118] |
| 2017 | Na-A | 1 | 25 | 5.1 | [116] |
| 2017 | ZIF-67 | 1 | 0 | 0.526 | [114] |
| 2017 | Zeolite 13X (13X–B) | 8–20 | 35 | 4.2 | [115] |
| 2017 | NaTEA-ZSM-25 | 1 | 25 | 4.3 | [116] |
| 2017 | Na-ZSM-25 | 1 | 25 | 3.9 | [116] |
| 2017 | Na-ECR-18 | 1 | 25 | 4.4 | [116] |
| 2018 | Zeolite (Serbia) | 4.7 | 25 | 1.17 | [119] |
| 2018 | Basalt-based zeolite 4A |
15 | 20 | 5.9 | [120] |
| 2018 | ZY-CS composite | 4.7 | 25 | 1.7 | [119] |
| 2019 | CS-ZIF-8 | 1.1 | 25 | 0.99 | [121] |
| 2019 | Merlinoite zeolite | 0.1 | 25 | 3.5 | [122] |
| 2020 | ZeY@CS | 1 | 30 | 1.64 | [123] |
| 2020 | Na–Y | 5 | 25 | 7 | [124] |