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. 2021 Aug 10;121(17):10666–10741. doi: 10.1021/acs.chemrev.0c01266

Table 11. Ranking of Top 10 Materials Based on Maximum Productivity.

index 4-step VSA with LPPa (Khurana and Farooq88) 4-step Skarstrom PSAb (Park et al.94) 4-step VSA with LPPa (Subramanian Balashankar and Rajendran121) 4-step VSA with LPPa (Burns et al.124) modified Skarstromc (Yancy-Caballero et al.126) FVSAc (Yancy-Caballero et al.126) 5-step PSAc (Yancy-Caballero et al.126)
1 UTSA-16 SENWOZ h8315144 GAYFOD UTSA-16 Cu-TDPAT UTSA-16
2 NaA SENWIT h8328529 WUNSII zeolite 13X UTSA-16 zeolite 13X
3 h8155527, h8124767 WONZOP IZA-MON IISERP-MOF2 Cu-TDPAT Zn-MOF-74 Cu-TDPAT
4 ZIF-36-FRL UTEWUM IZA-RRO UTSA-16 Ni-MOF-74 zeolite 13X Zn-MOF-74
5 NAB OJICUG IZA-JBW YEZFIU Mg-MOF-74 Ti-MIL-91 Ti-MIL-91
6 CaX BIBXUH h8206103 IGAHED02 SIFSIX-3-Ni SIFSIX-3-Ni SIFSIX-3-Ni
7 ZIF-78 SENWAL IZA-WEI XAVQIU01 SIFSIX-2-Cu-i   Mg-MOF-74
8 h8272272 FEFDAX h8313037 NaA Ti-MIL-91    
9 Zn-MOF-74 RAXCOK ZIF-Im-h8055553 HUTTIA Zn-MOF-74    
10 MgX CUHPUR ZIF-Im-h8164555 ZEGSUB      
a

4-step VSA with LPP using a packed-bed adsorbent system. Feed composition: 15% CO2/85% N2 at 298 K. Optimization constraints: 95% CO2 purity and 90% CO2 recovery.

b

4-step PSA using a hollow fiber adsorbent model. Feed composition: 14% CO2/86% N2 at 243 K. No optimization constraint imposed on purity and recovery.

c

PSA cycles using packed-bed adsorbent system. Feed composition: 15% CO2/85% N2 at 313 K. Optimization constraints: 90% CO2 purity and 90% CO2 recovery.