| Literature DB >> 23653186 |
Lei Li1, Shenglin Xiang, Shuqi Cao, Jianyong Zhang, Gangfeng Ouyang, Liuping Chen, Cheng-Yong Su.
Abstract
Developing a synthetic methodology for the fabrication of hierarchically porous metal-organic monoliths that feature high surface area, low density and tunable porosity is imperative for mass transfer applications, including bulky molecule capture, heterogeneous catalysis and drug delivery. Here we report a versatile and facile synthetic route towards ultralight micro/mesoporous metal-organic aerogels based on the two-step gelation of metal-organic framework nanoparticles. Heating represents a key factor in the control of gelation versus crystallization of Al(III)-multicarboxylate systems. The porosity of the resulting metal-organic aerogels can be readily tuned, leading to the formation of well-ordered intraparticle micropores and aerogel-specific interparticle mesopores, thereby integrating the merits of both crystalline metal-organic frameworks and light aerogels. The hierarchical micro/mesoporosity of the Al-metal-organic aerogels is thoroughly evaluated by N₂ sorption. The good accessibility of the micro/mesopores is verified by vapour/dye uptake, and their potential for utilization as effective fibre-coating absorbents is tested in solid-phase microextraction analyses.Entities:
Year: 2013 PMID: 23653186 PMCID: PMC3644084 DOI: 10.1038/ncomms2757
Source DB: PubMed Journal: Nat Commun ISSN: 2041-1723 Impact factor: 14.919
Figure 1Schematic representation of the formation of MIL-53(Al) MOF versus AlBDC MOA.
MOF, metal-organic framework; MOFP, metal-organic framework particle; MOG, metal-organic gel; MOA, metal-organic aerogel.
Figure 2Physical characterization of the representative MOAs.
(a) SEM of AlBTC-1:1-0.40 (bar width=500 nm). (b) TEM of AlBTC-3:2-0.075 (scale bar, 100 nm; the insert shows digital photograph of gel before subcritical extraction). (c) PXRD patterns of AlBDC-3:2-0.15 wet gel obtained in EtOH at 353 K (I), AlBDC-3:2-0.15 aerogel (II), intermediate obtained from AlBDC-3:2-0.15 reaction systems in EtOH at 333 K (III) and 323 K (IV), and simulation from the single-crystal data of MIL-53(Al) in its LP form (V). (d) 27Al MAS NMR spectral ex situ monitoring of AlBDC-3:2-0.15 system at different gelation times in comparison with pure Al(NO3)3·9H2O, MIL-53(Al) solid in LP form and their mixtures.
Porosity properties of selected Al-MOAs based on H2BDC and H3BTC in ethanol.
| MOA | ||||||
|---|---|---|---|---|---|---|
| AlBDC-3:2-0.05 | 1,250±41 | 662±37 | 1.10±0.13 | 0.76±0.14 | 0.43±0.02 | 5.4±1.0/0.89±0.01 |
| AlBDC-3:2-0.075 | 1,283±45 | 733±47 | 1.28±0.08 | 0.92±0.07 | 0.45±0.02 | 7.8±0.7/0.89±0.01 |
| AlBDC-3:2-0.15 | 1,324±75 | 828±27 | 2.66±0.18 | 2.25±0.14 | 0.46±0.03 | 23.0±0.0/0.91±0.01 |
| AlBDC-3:2-0.20 | 1,560±38 | 919±31 | 6.27±1.17 | 5.41±1.09 | 0.55±0.01 | 87.8±6.2/0.89±0.04 |
| AlBTC-1:1-0.075 | 1,073±37 | 386±26 | 0.82±0.09 | 0.27±0.06 | 0.37±0.02 | 3.6±0.1/0.99±0.06 |
| AlBTC-1:1-0.15 | 1,058±95 | 487±45 | 1.05±0.05 | 0.63±0.04 | 0.36±0.03 | 5.4±2.0/1.00±0.10 |
| AlBTC-1:1-0.60 | 917±57 | 475±44 | 2.90±0.89 | 2.63±0.90 | 0.29±0.13 | 32.9±0.0/0.98±0.08 |
| AlBTC-3:2-0.05 | 1,448±6 | 442±12 | 1.78±0.03 | 1.34±0.10 | 0.41±0.01 | 6.7±0.7/1.00±0.06 |
| AlBTC-3:2-0.075 | 1,266±44 | 636±40 | 7.16±1.06 | 6.86±1.12 | 0.39±0.04 | 59.7±3.8/0.98±0.08 |
| AlBTC-3:2-0.15 | 1,189±6 | 295±27 | 3.69±0.59 | 3.27±0.62 | 0.40±0.01 | 19.9±4.0/1.12±0.04 |
| AlBTC-1:1-0.2-t1 | 1,292±35 | 295±58 | 1.05±0.05 | 0.46±0.08 | 0.44±0.01 | 3.7±0.1/1.00±0.06 |
| AlBTC-1:1-0.2-t2 | 1,443±41 | 457±16 | 1.17±0.08 | 0.66±0.04 | 0.42±0.01 | 3.7±0.0/1.08±0.06 |
| AlBTC-1:1-0.4-t2 | 1,638±58 | 578±80 | 6.26±1.02 | 5.91±1.03 | 0.46±0.01 | 26.2±4.6/1.06±0.04 |
| AlBTC-1:1-0.6-t2 | 1,619±90 | 543±19 | 6.28±0.52 | 5.93±0.46 | 0.44±0.03 | 33.1±0.1/1.06±0.07 |
All data are the average results with standard deviations calculated from the measurements of three independent samples of each MOA prepared in parallel batches. The sorption reliability was verified by repeating the measurement of a specific MOA sample three times, thus confirming the pore robustness against N2 uptake (see details in Supplementary Method and Supplementary Tables S9 and S10).
*The MOAs were obtained from corresponding MOGs with preparation details listed in Supplementary Table S3, gelating and aging at 353 K and subjecting to subcritical CO2(l) extraction.
†SBET is the BET-specific surface area.
‡Smicro is the t-plot-specific micropore surface area.
§Vt is the total specific pore volume.
||Vmeso is the specific mesopore volume calculated from adsorption isotherm using the BJH method.
¶Vmicro is the specific micropore volume calculated using the SF method.
#Dmeso is the mesopore diameter calculated from adsorption isotherm using the BJH method.
**Dmicro is the micropore diameter calculated using the SF method.
††t1 refers to template CTAB–TMB concentrations of 0.06–0.06 mol l−1.
‡‡t2 refers to template CTAB–TMB concentrations of 0.12–0.06 mol l−1.
Figure 3Representative N2 sorption data.
(a,b) The N2 adsorption–desorption isotherms of AlBDC-3:2 series MOAs at 77 K (the inserts show enlarged parts of isotherms). (c) The N2 adsorption–desorption isotherms of the templated MOAs at 77 K. (d) The SF micropore distribution of the AlBDC-3:2 series MOAs. (e) The BJH pore distribution of the AlBDC-3:2 series MOAs (vertical offsets). (f) The SF micropore distribution of the templated MOAs. (g) The BJH pore distribution of the templated MOAs.
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ctively regulate the surface areas and mesopore sizes. The BET surface areas of the MOAs significantly increase up to ~1,638 m2 g−1, and their mesopore sizes are narrowly distributed at ~3.7 nm (analysed using the BJH algorithm, Fig. 3g). Increasing the concentration causes a steady increase of the mesopore sizes, but the hysteresis loops show a small change upon reactant and template concentration variation.
Figure 4Gas uptake and separation data.
(a) The H2 adsorption–desorption isotherms at 77 and 87 K for the AlBTC-3:2-0.075 MOA. (b) The low-pressure CO2 adsorption–desorption isotherms of the various MOAs at 195 K. (c) The high-pressure CO2 adsorption–desorption isotherms of the selected MOAs at 298 K. (d) The CO2, CH4 and N2 adsorption isotherms of AlBTC-1:1-0.2-t2 MOA at 195 K.
Figure 5Dye uptake and SPEM data.
(a) The kinetic curves of the AlBDC-3:2-0.15 MOA (7.5 mg) in 50 ml of dyes solution (100 mg l−1) for congo red (circle) and brilliant blue R-250 (square). The inserts show pictures of the dye-polluted water (I, III) before and (II, IV) after dye adsorption. (b) A schematic demonstration of the SPME analyses of a volatile analyte using the MOA-coated fibres (SEM image). (c) The extraction contrast profiles with AlBTC-3:2-0.05 MOA-coated and PDMS fibres for 1 ppm BTEX compounds. (d) The extraction contrast profiles with AlBTC-3:2-0.05 MOA-coated and PA fibres for 1 ppm phenols. The conditions for BTEX: extraction temperature, 298 K; extraction time, 10 min (stirring); desorption time, 0.5 min. PDMS, polydimethylsiloxane; B, benzene; T, toluene; E, ethylbenzene; X, xylene. Conditions for phenols: extraction temperature, 298 K; extraction time, 20 min (stirring); desorption time, 1 min. PA, polyacrylate; C, 2-chlorophenol; M, 4-methylphenol; N, 2-nitrophenol; D, 2,4-dichlorophenol; T, 2,4,6-trichlorophenol.