2021
DOI: 10.1002/aic.17300
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Chemical immobilization of amino acids into robust metal–organic framework for efficient SO2 removal

Abstract: Adsorptive removal of trace SO2 emissions from flue‐gases can significantly reduce energy and water consumption and minimize the amount of unmanageable waste, however, this remains a great challenge. Herein, we report a universal strategy of chemical immobilization of amino acids into a robust metal–organic framework to enhance deep desulfurization. The grafted amino acid resulted in the formation of pores with compatible pore sizes and created abundant N‐containing moieties for selective SO2 adsorption. MOF‐8… Show more

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Cited by 20 publications
(27 citation statements)
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References 36 publications
(44 reference statements)
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“…To estimate the affinity between SO 2 molecule and MOF frameworks, the coverage‐dependent isosteric heats ( Q st ) were calculated based on the SO 2 adsorption isotherms at 273, 298, and 323 K using the Clausius‐Clapeyron equation (Figures S8 and S11), and the Langmuir–Freundlich equation was applied to perform the global fitting (Figure S12). At zero coverage, the Q st on Cu‐ATC is calculated to be 60 kJ mol −1 (Figure 3B), which is higher than that of MOF‐808‐His (52 kJ mol −1 ), 7 NH 2 ‐MIL‐125(Ti) (53 kJ mol −1 ), 38 MFM‐300(Sc) (36.2 kJ mol −1 ), 40 and MIL‐101(Cr)‐4F (54 kJ mol −1 ) 9 . In sharp contrast, the Q st value at zero coverage declined to 48 kJ mol −1 on Cu 2 (ATC)∙2H 2 O, also suggesting that the exposed Cu OMSs are strong binding sites for SO 2 .…”
Section: Resultsmentioning
confidence: 85%
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“…To estimate the affinity between SO 2 molecule and MOF frameworks, the coverage‐dependent isosteric heats ( Q st ) were calculated based on the SO 2 adsorption isotherms at 273, 298, and 323 K using the Clausius‐Clapeyron equation (Figures S8 and S11), and the Langmuir–Freundlich equation was applied to perform the global fitting (Figure S12). At zero coverage, the Q st on Cu‐ATC is calculated to be 60 kJ mol −1 (Figure 3B), which is higher than that of MOF‐808‐His (52 kJ mol −1 ), 7 NH 2 ‐MIL‐125(Ti) (53 kJ mol −1 ), 38 MFM‐300(Sc) (36.2 kJ mol −1 ), 40 and MIL‐101(Cr)‐4F (54 kJ mol −1 ) 9 . In sharp contrast, the Q st value at zero coverage declined to 48 kJ mol −1 on Cu 2 (ATC)∙2H 2 O, also suggesting that the exposed Cu OMSs are strong binding sites for SO 2 .…”
Section: Resultsmentioning
confidence: 85%
“…The ideal adsorbed solution theory (IAST) was applied to access the separation selectivity of SO 2 /CO 2 (10/90 and 0.2/99.8, v / v ), SO 2 /CH 4 (10/90, v / v ), and SO 2 /N 2 (10/90, v / v ) mixtures. Notably, as shown in Figure 2E, Cu‐ATC showed exceptionally high SO 2 /CO 2 (10/90, v / v ) IAST selectivity of 114 at 1.0 bar and 298 K, superior to SIFSIX‐2‐Cu‐i (87.1), 21 MOF‐808‐His (90.5), 7 and MFM‐300(In) (50), 37 and comparable to top‐ranking benchmarks including MFM‐520 (125), 31 MIL‐160 (124), 38 and Co‐gallate (143) 35 . Besides, the IAST selectivity for SO 2 /CO 2 (0.2/99.8, v / v ) reached 88 at 298 K and 1.0 bar (Figure S9).…”
Section: Resultsmentioning
confidence: 88%
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“… 25 One strategy to render such MOFs efficient for SO 2 capture is functionalization, as exemplified by MOF-808-His, underlining the importance of investigating the functionalized MOFs whose bare forms may not show significant gas uptake or separation capability. 25 Through functionalization, the pores may provide stronger host–guest interactions as they can be narrower (leading to stronger confinement effects) or grafted favorable interaction sites for sorbates.…”
Section: Resultsmentioning
confidence: 99%