High and selective CO2 uptake in a nitrogen-rich pillar-layered metal organic framework

Chao Chen*, Minfeng Jia, Gang Wang, Xiaoli Li and Shimin Li
College of Chemistry and Chemical Engineering, Xinyang Normal University, Xinyang 464000, Henan Province, China. E-mail: chenchao@xynu.edu.cn; Tel: +86 376 6393906

Received 22nd October 2015 , Accepted 1st December 2015

First published on 2nd December 2015


Abstract

A nitrogen-rich pillar-layered metal organic framework, Co(Imda)(4,4′-bpy), comprising cobalt(II) clusters interconnected by imidazole-4,5-dicarboxylic acid and 4,4′-bipyridyl groups was synthesized, and characterized by powder X-ray diffraction, N2 adsorption–desorption measurements, thermogravimetric analysis, and scanning electron microscopy. This material was firstly investigated for CO2 capture. It exhibited several outstanding attributes as a CO2 adsorbent: high CO2 uptake (135 mg g−1 at 298 K, 1 bar), good separation selectivity against N2 (CO2/N2 selectivity of ca. 18 at 298 K, 1 bar), fast adsorption kinetics (saturation within 10 min), easy regeneration (298 K, argon purge) and excellent stability in moisture and during consecutive adsorption–desorption cycles.


The gradually rising level of CO2 concentration in the atmosphere, largely caused from the combustion of fossil fuels, has raised serious public concerns about global warming. Carbon capture and sequestration schemes are one approach that hold high promise for reducing CO2 emissions in the short term.1 At present, large-scale CO2 capture and separation processes operating in power plants around the world are employing liquid phase amine absorption technology.2 On the other hand, CO2 adsorption and separation processes based on solid sorbents have also been actively investigated, which are considered to be more efficient for CO2 capture owing to their lower regeneration energy cost involved and good cyclic performances.3 Over the last decade, diverse metal organic frameworks (MOFs) in which metal ions or clusters are interconnected by organic linkers forming crystalline structures with well-ordered micropores have been prepared by solvothermal methods, and increasingly investigated as CO2 adsorbents.4 Their excellent structural and chemical properties, such as large surface areas and pore volumes, tunable pore sizes, coordinatively unsaturated metal sites, and surface properties easily adjustable by post-synthetic functionalization seem to make them highly promising as CO2 adsorbents.5,6

Pillar-layered MOFs are consisted of two-dimensional layers (formed by metal ions and organic linkers) that have ligating sites available for linkage with pillars (different organic species) to form three dimensional porous structures, and have been under growing attention recently due to the fact that the two different types of ligand employed allow higher flexibility to tune their structural and chemical properties than for common MOFs that are synthesized from a single ligand species only. So far, only limited groups have considered CO2 capture by the pillar-layered MOF materials.7–12 Nugent et al. reported a high gravimetric CO2 uptake by SIFSIX-2-Cu-i at 298 K and 1 bar (238 mg g−1),7 which is among the highest capture capacities reported yet among MOFs. Gao et al. synthesized a porous metal-triazolate framework, MTAF-3, which shows remarkable enhancement of CO2 uptake capacity compared to the parent MOF-508 through changing the pillar ligand, 4,4′-bipyridine in MOF-508 with 4,4′-(2H-1,2,3-triazole-2,4-diyl)dipyridine.9

In this work, a nitrogen-rich pillar-layered cobalt(II) metal organic framework, Co(Imda)(4,4′-bpy), was firstly investigated for CO2 capture. The material is a three dimensional non-interpenetrated microporous MOF structure, in which the layers based on imidazole-4,5-dicarboxylic acid (Imda) and the cobalt cluster are pillared by 4,4′-bipyridyl (4,4′-bpy). The CO2 capture performance of this material was evaluated in terms of its adsorption capacity and selectivity (towards N2), adsorption kinetics, regeneration, and stability in the adsorption–desorption recycles.

The XRD diffraction pattern of Co(Imda)(4,4′-bpy) (Fig. 1a) was in agreement with the one reported by Li et al.13 A comparison of XRD patterns of Co(Imda)(4,4′-bpy) with cobalt oxide and cobalt hydroxide (Fig. S1) indicate that the MOF product is 100% pure. N2 adsorption–desorption isotherms (Fig. 1b) showed a reversible type I isotherm, which indicated the microporous structure of this material. In the region P/P0 > 0.9, the isotherm began to increase sharply, indicating the presence of some textural mesopores caused by inter-particle voids.14 The BET surface area was estimated to be 572 m2 g−1 based on the N2 adsorption–desorption measurement. The TGA curve (Fig. 1c) indicated that the structural decomposition took place above ca. 250 °C, where the structure begins collapse and the coordinated ligands start to be released. SEM picture showed that the material exhibited particle morphology of hexagonal prism, with particles of ca. 0.5 to 3 μm in size (Fig. 1d).


image file: c5ra22144g-f1.tif
Fig. 1 (a) XRD pattern; (b) N2 adsorption–desorption isotherms; (c) TGA profile; and (d) SEM image of Co(Imda)(4,4′-bpy).

The static CO2 adsorption by Co(Imda)(4,4′-bpy) was examined at ambient conditions. Fig. 2a shows the corresponding CO2 adsorption isotherm. At 298 K, 1 bar, Co(Imda)(4,4′-bpy) exhibited a high CO2 adsorption capacity of 135 mg g−1, surpassing the values reported by other pillar-layered MOFs except SIFSIX-2-Cu-i (Table 1). In addition, the adsorbed CO2 amount increased rapidly at a lower pressure range near 0.15 bar and a CO2 adsorption capacity of ca. 76 mg g−1 was achieved, which accounts for nearly 56% of the total capacity established at 1 bar, which would be useful in a post-combustion CO2 capture system. In a post-combustion CO2 capture system, a high concentration of N2 (ca. 70%) exists in the flue gas, so high CO2 selectivity from the CO2/N2 mixture is desirable. Thus, N2 adsorption isotherm was independently measured at 298 K (Fig. 2a). Based on the amounts of respective gas adsorbed (mg g−1) at 1 bar, the CO2/N2 selectivity was estimated to be ca. 18, which is significantly higher than those of prototypical activated carbons,15 MOFs,16,17 and comparable to those reported for ZIFs.18 We also calculated the CO2/N2 adsorption selectivity using the Ideal Adsorbed Solution Theory (IAST) for CO2[thin space (1/6-em)]:[thin space (1/6-em)]N2 mixture in the ratio of 0.15[thin space (1/6-em)]:[thin space (1/6-em)]0.85 (Fig. S2).19,20 The IAST CO2/N2 selectivity at 1 bar was calculated to be 64.1 at 298 K. We attribute the high and selective CO2 uptake in Co(Imda)(4,4′-bpy) to the combined effects of its microporosity, and strong quadrupolar interactions of CO2 with nitrogen atoms present in the organic linkers (Fig. 2b).18


image file: c5ra22144g-f2.tif
Fig. 2 (a) CO2 and N2 adsorption isotherms of Co(Imda)(4,4′-bpy) at 298 K; (b) a single unit of coordinated molecular building blocks of Co(Imda)(4,4′-bpy): blue, red and grey balls represent cobalt, oxygen, and nitrogen atoms; (c) CO2 adsorption profile of Co(Imda)(4,4′-bpy) at 298 K by TGA, and (d) cyclic CO2 adsorption–desorption runs (high purity CO2) of Co(Imda)(4,4′-bpy).
Table 1 A comparison of CO2 capture capacities by reported pillar MOFs
Sample Temp. (K) CO2 uptakea (mg g−1) Reference
a CO2 uptake measured at 1 bar.
Co(Imda)(4,4′-bpy) 298 135 This work
SIFSIX-2-Cu-i 298 238 7
SIFSIX-3-Zn 298 112 7
UTSA-15a 296 61 8
MTAF-3 273 100 9
SNU-M11 298 92 10
MOOFOUR-1-Ni 298 108 11
Cu(TCMBT)(bpp)(μ3-OH) 298 88 12


The CO2 adsorption kinetics of Co(Imda)(4,4′-bpy) at 298 K was examined by TGA. As shown in Fig. 2c, the sample showed fast CO2 adsorption kinetics with practical CO2 adsorption equilibrium achieved within 10 min in both high purity CO2 and 15% CO2 (85% N2) condition; lower concentration of CO2 in the feed gas mixture led to slower adsorption kinetics. This is an advantage over other CO2 adsorbents that require a long time to reach adsorption equilibrium, such as polyethylenimine-impregnated mesoporous silica that requires more than 1 h for its adsorption equilibrium.21 To save energy in adsorbent regeneration, adsorbed CO2 should be desorbed easily from the adsorbent during a multi-cycle operation. As shown in Fig. 2d, CO2 could be easily desorbed at 298 K with only an argon gas purge in a TGA measurement. Furthermore, it showed a stable adsorption–desorption performance in 8 consecutive runs without noticeable deterioration of CO2 capture capacities. It is also worth mentioning that this material is stable in moisture condition as can be expected from its hydrothermal synthesis, which makes it a good candidate material in practical applications.

In summary, a nitrogen-rich pillar-layered metal organic framework, Co(Imda)(4,4′-bpy), exhibited an excellent CO2 capture performance, including high CO2 uptake, good CO2 selectivity against N2, fast CO2 adsorption kinetics, easy regeneration, and excellent stability in moisture and during consecutive adsorption–desorption cycles. These outstanding attributes make it a promising candidate for post combustion CO2 capture.

Acknowledgements

This study was supported by the Key Project of Scientific and Technological Research of Henan Provincial Committee of Education (13A150757).

Notes and references

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Footnote

Electronic supplementary information (ESI) available: Experimental details, such as material synthesis and characterization, CO2 or N2 adsorption–desorption measurements, CO2/N2 selectivity calculation. A comparison of XRD patterns of Co(Imda)(4,4′-bpy) with CoO and Co(OH)2 was shown in Fig. S1; CO2 and N2 adsorption isotherms fitted by dual-site Langmuir model and single-site Langmuir model respectively for IAST CO2/N2 selectivity calculation of Co(Imda)(4,4′-bpy) was shown in Fig. S2. See DOI: 10.1039/c5ra22144g

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