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. 2024 Jun;11(21):e2401070.
doi: 10.1002/advs.202401070. Epub 2024 Mar 25.

A Scalable Robust Microporous Al-MOF for Post-Combustion Carbon Capture

Affiliations

A Scalable Robust Microporous Al-MOF for Post-Combustion Carbon Capture

Bingbing Chen et al. Adv Sci (Weinh). 2024 Jun.

Abstract

Herein, a robust microporous aluminum tetracarboxylate framework, MIL-120(Al)-AP, (MIL, AP: Institute Lavoisier and Ambient Pressure synthesis, respectively) is reported, which exhibits high CO2 uptake (1.9 mmol g-1 at 0.1 bar, 298 K). In situ Synchrotron X-ray diffraction measurements together with Monte Carlo simulations reveal that this structure offers a favorable CO2 capture configuration with the pores being decorated with a high density of µ2-OH groups and accessible aromatic rings. Meanwhile, based on calculations and experimental evidence, moderate host-guest interactions Qst (CO2) value of MIL-120(Al)-AP (-40 kJ mol-1) is deduced, suggesting a relatively low energy penalty for full regeneration. Moreover, an environmentally friendly ambient pressure green route, relying on inexpensive raw materials, is developed to prepare MIL-120(Al)-AP at the kilogram scale with a high yield while the Metal- Organic Framework (MOF) is further shaped with inorganic binders as millimeter-sized mechanically stable beads. First evidences of its efficient CO2/N2 separation ability are validated by breakthrough experiments while operando IR experiments indicate a kinetically favorable CO2 adsorption over water. Finally, a techno-economic analysis gives an estimated production cost of ≈ 13 $ kg-1, significantly lower than for other benchmark MOFs. These advancements make MIL-120(Al)-AP an excellent candidate as an adsorbent for industrial-scale CO2 capture processes.

Keywords: CCS; CO2; MOFs; scale‐up; shaping; techno‐economic analysis.

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Conflict of interest statement

The authors declare that they have no conflict of interest.

Figures

Figure 1
Figure 1
Crystal structure of MIL‐120(Al). A) General view along [0 0 1] highlighting the MOF narrow channels (water molecules were omitted for clarity). B) Constitutive Al hydroxo‐chains built of trans‐cis edge sharing Al(OH)4O2 octahedra. C) Representation of one channel emphasizing its highly confined environment (represented by the yellow tube) due to dense network of µ 2‐OH and stacked phenyl rings of BTeC. Color code: Al(OH)4O2, gray polyhedra; C, gray; O, light red; H, white. In C), one of the chains is highlighted using purple polyhedra.
Figure 2
Figure 2
CO2 adsorption performances of MIL‐120(Al)‐HP and MIL‐120(Al)‐AP at 298 K. A) CO2 (in red and blue, respectively) and N2 (in gray) adsorption isotherms at 298 K. Enlargement on the step region is given in the inset. B) IAST selectivity at different compositions for MIL‐120(Al)‐AP using the Langmuir model. C) Isosteric enthalpy of adsorption versus CO2 uptake for MIL‐120(Al)‐AP. D) Comparison of volumetric and gravimetric CO2 uptakes at 0.1, 1 bar, at 298 K between MIL‐120(Al)‐AP and benchmark adsorbents including MOFs and zeolites. The volumetric uptake was calculated using the crystallographic density.
Figure 3
Figure 3
Variable temperature synchrotron SRPD data. Measurements performed under dynamic vacuum (activation step) for A) MIL‐120(Al)‐HP, showing no phase transition, while remaining monoclinic; and B) MIL‐120(Al)‐AP revealing phase transition, at ≈ 357 K, from monoclinic to triclinic phase. Heating rate is equal to 6 K min−1, up to 373 K in (A) and 400 K in (B).
Figure 4
Figure 4
Crystal structure of MIL‐120(Al)‐HP cooled down to 200 K and loaded with 1 bar of CO2. A) General view along [0 0 1]. B) Top view of a part of one channel, and C) a cut through a channel showing the arrays of alternated CO2 molecules and their interactions with the frameworks throughout µ 2‐OH (represented as green dashed lines) and phenyl groups (yellow dashed lines) of the BTeC, with the respective distances i): 3.6Å; ii): 3.3Å; iii): 3.6Å; iv): 3.7Å). Color code: Al(OH)4O2, gray polyhedra; C, gray; O, light red. H‐atoms were not localized.
Figure 5
Figure 5
Molecular simulations of MIL‐120(Al)‐AP structure and adsorption properties. A) Most stable DFT‐optimized structure of MIL‐120(Al). The unit cell parameter is not shown to highlight the different orientations of µ 2‐OH group in the channel. The most stable Str1 and Str2 structures correspond to distinct orientations of µ2‐OH groups [details in Supporting Information]. B) Calculated X‐ray diffraction patterns for the two most stable DFT‐optimized MIL‐120(Al)‐APs and the corresponding experimental data. C) GCMC‐simulated and experimental single‐component CO2 adsorption isotherms at 298 K. D) Illustrations of the DFT‐optimized CO2‐loaded MIL‐120(Al)‐AP‐Str1 and MIL‐120(Al)‐AP‐Str2 structures with different CO2 loading (one [top] and two [bottom] CO2 molecules per unit‐cell). The dashed line represents the interaction between the CO2 molecule (O) and the µ 2‐OH group (H) of the framework correspondingly. E) GCMC‐simulated 15CO2:85N2 binary mixture adsorption isotherm of MIL‐120(Al)‐AP‐Str1 at 298 K calculated by GCMC simulations, F) Corresponding snapshot (zoom in) showing the location of CO2/N2 in MIL‐120(Al)‐AP‐Str1 at 1 bar and 298 K from GCMC simulation (cf. full sharpshot in Figure S16, Supporting Information). Color code in A, D, and F: Al(OH)4O2, gray polyhedra; C, gray; O, light red; H, white (C‐H) and light yellow (O‐H); N, blue. Interactions between CO2 molecules and µ 2‐OH groups are represented as green dashed lines. All views are shown along [0 1 1].
Figure 6
Figure 6
CO2 adsorption uptakes of MIL‐120(Al)‐AP. A) CO2 adsorption isotherms at 298 K on different scale batch preparations. B) CO2 adsorption isotherms comparison between pure and structured samples with 10% Bentonite or Silica. C) Breakthrough curves for MIL‐120(Al)‐AP beads with 10% Si. D) Breakthrough results of MIL‐120(Al)‐AP beads with 10% bentonite. The activation condition for both samples was heating at 50 °C for 12 h under vacuum, run 1 refers to the measurement in dry conditions, run 2 refers to the measurement in dry conditions after exposure to humid conditions, while in between the sample was reactivated at 50 °C under vacuum.
Figure 7
Figure 7
Operando IR spectra. IR spectra in the ν(OH) and ν(C═O) region for MIL‐120(Al)‐AP with time on stream during the first minutes of CO2 adsorption in the presence of water (20% CO2 and 1% H2O in Ar flow at RT).
Figure 8
Figure 8
Sensitivity analysis of MIL‐120(Al)‐AP production costs. A) Effect of the ligand and energy costs; B) effect of the base equipment costs. The green dots over the lines represent the base economic scenario (2022 prices).

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