Exploring the Effect of Ionic Liquid Conformation on the Selective CO2 Capture of Supported Ionic Liquid-Phase Adsorbents Based on ZIFs

The CO<sub>2</sub> adsorption capacity and the CO<sub>2</sub>/N<sub>2</sub> selectivity of a series of Supported Ionic Liquid-Phase adsorbents (SILPs), including the novel inversely structured SILP "Inverse SILPs", are thoroughly investigated. ZIF-8, ZIF-69 and ZIF-70 were involved as the solid matrix, while ILs, having tricyanomethanide (TCM) as an anion and alkyl-methylimidazolium of different alkyl chain lengths (C<sub>2</sub>, C<sub>6</sub>, C<sub>8</sub>) as a cation, were used as the liquid constituents of the SILPs. The ultimate target of the work was to ratify a few recently reported cases of enhanced CO<sub>2</sub> absorptivity in ILs due to their incorporation in ZIFs and to corroborate phenomena of CO<sub>2</sub>/N<sub>2</sub> selectivity improvements in ZIFs, due to the presence of ILs. This ambiguity originates from the vague assumption that the pores of the ZIF are filled with the IL phase, and the free pore volume of a SILP is almost zero. Yet, through the integration of theoretical predictions with N<sub>2</sub> porosimetry analysis of an actual sample, it is suggested that a thin layer of IL covered the exterior surface of a ZIF crystal. This layer could act as an impermeable barrier for N<sub>2</sub>, inhibiting the gas molecules from reaching the empty cavities laying underneath the liquid film during porosimetry analysis. This consideration is based on the fact that the solubility of N<sub>2</sub> in the IL is very low, and the diffusivity at 77 K is negligible. In this context, the observed result reflects an averaged adsorptivity of both the IL phase and the empty pores of the ZIF. Therefore, it is incorrect to attribute the adsorption capacity of the SILP solely to the mass of the IL that 'hypothetically' nests inside the pore cavities. In fact, the CO<sub>2</sub> adsorption capacity of SILPs is always less than the average adsorptivity of an ideal ZIF/IL mixture, where the two phases do not interact. This reduction occurs because some ZIF pores may become inaccessible, particularly when the IL forms a layer on the pore walls, leaving only a small empty core accessible to CO<sub>2</sub> molecules. Additionally, the IL layer masks the active sites on the ZIF's pore walls. It should also be noted that the CO<sub>2</sub>/N<sub>2</sub> selectivity increases only when the ZIF's pores are completely filled with the IL phase. This is because ILs have a higher CO<sub>2</sub>/N<sub>2</sub> selectivity compared to the bare ZIF.

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Journal
Materials
Published
2024-09-30
DOI
https://doi.org/10.3390/ma17194829
Citations
2
Primary Topic
Carbon Dioxide Capture Technologies
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article
Field-Weighted Citation Impact
0.43
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article

Exploring the Effect of Ionic Liquid Conformation on the Selective CO2 Capture of Supported Ionic Liquid-Phase Adsorbents Based on ZIFs

George V. Theodorakopoulos, K. Beltsios, Charitomeni M. Veziri, George E. Romanos
2 citations
Materials
Carbon Dioxide Capture Technologies
0.43
article

Exploring the Effect of Ionic Liquid Conformation on the Selective CO2 Capture of Supported Ionic Liquid-Phase Adsorbents Based on ZIFs

George V. Theodorakopoulos, K. Beltsios, Charitomeni M. Veziri, George E. Romanos
article en
2 citations

Abstract

The CO<sub>2</sub> adsorption capacity and the CO<sub>2</sub>/N<sub>2</sub> selectivity of a series of Supported Ionic Liquid-Phase adsorbents (SILPs), including the novel inversely structured SILP "Inverse SILPs", are thoroughly investigated. ZIF-8, ZIF-69 and ZIF-70 were involved as the solid matrix, while ILs, having tricyanomethanide (TCM) as an anion and alkyl-methylimidazolium of different alkyl chain lengths (C<sub>2</sub>, C<sub>6</sub>, C<sub>8</sub>) as a cation, were used as the liquid constituents of the SILPs. The ultimate target of the work was to ratify a few recently reported cases of enhanced CO<sub>2</sub> absorptivity in ILs due to their incorporation in ZIFs and to corroborate phenomena of CO<sub>2</sub>/N<sub>2</sub> selectivity improvements in ZIFs, due to the presence of ILs. This ambiguity originates from the vague assumption that the pores of the ZIF are filled with the IL phase, and the free pore volume of a SILP is almost zero. Yet, through the integration of theoretical predictions with N<sub>2</sub> porosimetry analysis of an actual sample, it is suggested that a thin layer of IL covered the exterior surface of a ZIF crystal. This layer could act as an impermeable barrier for N<sub>2</sub>, inhibiting the gas molecules from reaching the empty cavities laying underneath the liquid film during porosimetry analysis. This consideration is based on the fact that the solubility of N<sub>2</sub> in the IL is very low, and the diffusivity at 77 K is negligible. In this context, the observed result reflects an averaged adsorptivity of both the IL phase and the empty pores of the ZIF. Therefore, it is incorrect to attribute the adsorption capacity of the SILP solely to the mass of the IL that 'hypothetically' nests inside the pore cavities. In fact, the CO<sub>2</sub> adsorption capacity of SILPs is always less than the average adsorptivity of an ideal ZIF/IL mixture, where the two phases do not interact. This reduction occurs because some ZIF pores may become inaccessible, particularly when the IL forms a layer on the pore walls, leaving only a small empty core accessible to CO<sub>2</sub> molecules. Additionally, the IL layer masks the active sites on the ZIF's pore walls. It should also be noted that the CO<sub>2</sub>/N<sub>2</sub> selectivity increases only when the ZIF's pores are completely filled with the IL phase. This is because ILs have a higher CO<sub>2</sub>/N<sub>2</sub> selectivity compared to the bare ZIF.

MaterialsVol. 17(19)
National Technical University of Athens (GR), National Centre of Scientific Research "Demokritos" (GR)
Clean water and sanitation
Openalex Percentile: Top 42%
Carbon Dioxide Capture Technologies
0.43
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