Jung Hee
Yoon
a,
Dongwook
Kim
a,
Xiaokai
Song
ab,
Seungwan
Han
a,
Jiho
Shin
c,
Suk Bong
Hong
*c and
Myoung Soo
Lah
*a
aInterdisciplinary School of Green Energy, Ulsan National Institute of Science & Technology, Ulsan, 689-798, Korea. E-mail: mslah@unist.ac.kr; Fax: +82 52 217 2019; Tel: +82 52 217 2931
bDepartment of Chemistry and Applied Chemistry, Hanyang University, Ansan, Kyunggi-do, 426-791, Korea
cDepartment of Chemical Engineering and School of Environmental Science and Engineering, POSTECH, Pohang, 790-784, Korea
First published on 19th October 2012
The excellent breakthrough separation performance of a new microporous MOF for CO2/N2 and CO2/CH4 gas mixtures results from the combination of different equilibrium uptake amounts depending on the adsorption enthalpies of the adsorbates and different uptake kinetics depending on their kinetic diameters.
On the other hand, the uptake capacity and pore properties of a microporous MOF can be relatively easily controlled by modulating the building components, metal ions and organic linkers. The selectivity of the MOF for adsorbates has so far been investigated by analyzing its sorption behaviors. Thermodynamic selectivity for adsorbates could be obtained by controlling pore surface properties with different adsorption enthalpies,4 and kinetic selectivity can also be achieved by adjusting portal dimensions for size-exclusive molecular sieving.5 Laboratory demonstrations of the real gas separation capabilities of microporous MOFs have been relatively easily evaluated by performing breakthrough experiments.6
Here, we report a new MOF with interlinked cages and narrow portal dimensions and demonstrate its sorption behaviors. The separation capabilities of the MOF for CO2/N2 and CO2/CH4 gas mixtures were evaluated using breakthrough experiments.
:
H2O = 10
:
2–3, v/v). The solution was sealed in a glass tube and heated to 120 °C for 1 d. Block-shaped purple crystals were collected and washed with DMA. Yield = 12.4 mg, 46.7%. EA for H1/3[(CoII13/2(BTB)4(OH)4/3(DMA)3]·2DMA·4H2O (C128H115.67N5O34.3Co6.5, fw = 2655.84 g mol−1), 1. Calc.: C, 57.89; H, 4.39; N, 2.64%. Found: C, 58.13; H, 4.35; N, 2.80%. IR (KBr, cm−1): 3606 (vw), 3436 (s, b), 3068 (vw), 3031 (vw), 2937 (vw), 1606 (s), 1587 (s), 1547 (s), 1508 (w), 1402 (s), 1311 (vw), 1263 (vw), 1244 (vw), 1187 (w), 1145 (vw), 1108 (vw), 1015 (m), 965 (vw), 891 (vw), 855 (s), 805 (m), 779 (s), 700 (m), 670 (m), 599 (vw), 591 (w), 572 (w), 493 (m). The activated sample, 1a, was prepared by soaking as-synthesized 1 in methylene chloride for 3 d, and then vacuum drying at 250 °C for 5 h. EA was done in air for H1/3[(CoII13/2(BTB)4(OH)4/3]·H2O (C108H63.67O26.3Co6.5, fw = 2165.71 g mol−1), 1a. Calc.: C, 59.90; H, 2.96; N, 0.00%. Found: C, 59.79; H, 3.25; N, 0.31%. IR (KBr, cm−1): 3445 (s, b), 3066 (vw), 3034 (vw), 2938 (vw), 2927 (vw), 1934 (vw), 1807 (vw), 1609 (s), 1582 (s), 1529 (s), 1508 (w), 1402 (s), 1305 (vw), 1247 (vw), 1179 (w), 1144 (vw), 1104 (vw), 1014 (m), 892 (vw), 851 (s), 808 (m), 775 (s), 703 (m), 667 (m), 565 (vw), 478 (m).
, a = b = 36.820(5) Å, c = 45.036(9) Å, V = 52876(15) Å3, Z = 18, μ (Mo-Kα, λ = 0.71073 Å) = 0.970 mm−1, dcalc = 1.369 mg cm−3, F(000) = 22293, 125
964 reflections were collected, 26
172 were unique [Rint = 0.0709]. R1 (wR2) = 0.0645 (0.1482) for 20,381 reflections [I > 2σ(I)], R1 (wR2) = 0.0807 (0.1542) for all reflections. The largest difference peak and hole were 1.315 and −0.749 e Å−3, respectively, see ESI.†
:
50 v/v) and CO2/CH4 (50
:
50 v/v) mixtures with a total gas flow rate of 20 cm3 min−1 at 195 and 298 K, by using a setup that was slightly modified from that reported previously (Fig. S2, ESI†).6a Approximately 1 g of the activated sample, 1a, was loaded in a vertical sample cell (0.64 cm inner diameter). The sample was further activated under flowing He at a flow rate of 50 cm3 min−1 at 523 K for 6 h, and then the reactor was slowly cooled to ambient temperature. The mass intensities of the mixture gases passing through the reactor were monitored on a Pfeiffer Prisma QMS 200 mass spectrometer detecting ion peaks at m/z+ = 4 (He+), 15 (CH3+), 28 (N2+), and 44 (CO2+). The 17.1% reduced relative intensity of CO2 coming from the fragmentation of CO2+ to CO+ was corrected based on preliminary mass measurements for a pure CO2 gas stream. The relative intensity of N2 in the breakthrough experiment for CO2/N2 mixture gases was also corrected for the additional CO+ fragment that has the same m/z+ = 28 as N2+. To avoid interference by the O+ (m/z+ = 16) fragment from CO2 in the intensity for CH4+ peak (m/z+ = 16), the m/z+ = 15-peak measurement was used for the intensity of CH4+. The amount of CH4 was estimated from the intensity of the CH3+ peak based on preliminary mass measurements of the CH4+ peak (52.8%) and its fragmented CH3+ peak (47.2%).
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| Fig. 1 The SBUs in the network of 1. (a) and (b) The two 8-connected SBUs of the 4-6-4 coordinate linear trinuclear cobalt cluster, Co3(COO)6. (c) The 4-connected SBU of the 4-6 coordinate dinuclear cobalt cluster, Co2(COO)3. (d) and (e) The two 3-connected μ3-OH groups linked to three different cobalt clusters. Color code: cobalt in the center of the linear trinuclear cobalt clusters, blue; the remaining cobalt, cyan; μ3-OH, green; oxygen, red; carbon, gray. Symmetry code: a = −y, 1 + x − y, z; b = −1 − x + y, −x, z. | ||
Examination of the network connectivity shows that these cobalt clusters are interconnected via four 3-connected BTB nodes and two 3-connected μ3-OH groups (Fig. 1d and e) to form a 3-D network with a complicated net topology. The assignment of the two μ3-O atoms as the OH residues was based on the geometry around the bridging oxygen atoms, such as the Co–O bond distances and the Co–O–Co bond angles. The one-third cationic charge per asymmetric unit needed for the charge balance of 1 was assumed to be from an unidentified proton attached to a lattice water molecule with one-third site occupancy. First, the two 8-connected SBUs and a 4-connected SBU are interconnected via two 3-connected μ3-OH nodes to form a corrugated two-dimensional (2-D) layer of a uninodal 3-connected hcb net topology (Fig. 2), where the 8c-SBUs could be considered as a ditopic linker and the 4c-SBU as a terminal residue with no further connectivity. The corrugated 2-D layers are stacked along the crystallographic c-axis in a staggered manner (Fig. 3a–d), and the stacked 2-D layers are further interconnected via four different 3-connected BTB ligands to form a three-dimensional (3-D) network with an unprecedented 3,3,3,3,3,3,4,8,8-connected net topology (Fig. 3e).12
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| Fig. 2 Ball-and-stick diagrams of a corrugated 2-D sheet consisting of the cobalt clusters, Co2(COO)3 and Co3(COO)6, connected via 3-connected μ3-OH groups in (a) top view and (b) side view. Schematic drawings of the 2-D network of an hcb net topology in (c) top view and (d) side view, where the SBUs were represented using the balls and the connectivity between the SBUs using the sticks. | ||
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| Fig. 3 Schematic drawings of two layers stacked in a staggered manner in (a) side and (b) top views, and of three stacked layers in (c) side and (d) top views. (e) The three stacked 2-D layers are connected via four different 3-connected BTB ligands, where the yellow balls represent the 3-connected BTBs. | ||
The complicated network of 1 contains three different cages: Cage A with (8c-SBU)6(BTB)6(μ3-OH)2; Cage B with (8c-SBU)7(4c-SBU)2(BTB)4(μ3-OH)4; and Cage C with ((8c-SBU)6(4c-SBU)2(BTB)3(μ3-OH)4(DMF)3)2 as structural components. Cage A, with a local S6 point symmetry, consists of six BTB ligands as edge components of the cage and the ligands are connected via six 8c-Co3 SBUs and two μ3-OH residues to form a cage with a pore diameter of ∼9 Å with six oval-shaped portals (Fig. 4).
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| Fig. 4 Ball-and-stick and space-filling models of Cage A with a local S6 point symmetry. Top view of (a) the ball-and-stick and (b) space-filling models. Side view of (c) the ball-and-stick and (d) space-filling models. Color code: BTB, blue; cobalt, dark blue; μ3-O, red; dummy ball representing the cavity of Cage A, green. | ||
Cage B, with a pseudo-C3 point symmetry, consists of four BTB ligands as triangular facial components of the tetrahedral cage and the three corners of the ligands are connected via seven 8c-SBUs, two 4c-SBUs, and four μ3-OH residues to form a cage with a pore diameter of ∼5.6 Å (Fig. 5).
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| Fig. 5 Ball-and-stick and space-filling models of Cage B with a pseudo-C3 point symmetry. Top view of (a) the ball-and-stick and (b) space-filling models. Side view of (c) the ball-and-stick and (d) space-filling models. Color code: BTB, blue and cyan; cobalt, dark blue; μ3-O, red; dummy ball representing the cavity of Cage B, violet. | ||
Cage A is surrounded by six Cage Bs to form an AB6 cage cluster (Fig. 6). All six portals of Cage A are shared with the six Cage B portals and the pore of Cage A is only accessible via the pores of the Cage Bs. Three edges of the tetrahedral cage are open as portals and the remaining three edges are closed. Cage C has the same local S6 point symmetry as Cage A, but is a dimeric cage of two one-face-open tetrahedra (Fig. 7). The one-face-open tetrahedron consists of three BTB ligands connected via six 8c-Co3 SBUs, two 4c-Co2 SBUs, and four μ3-OH residues. The pore diameter of cage C is ∼8.4 Å.
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| Fig. 6 Ball-and-stick model of the AB6 cage cluster, where Cage A is surrounded by six Cage Bs. Color code: BTB, blue and cyan; cobalt, dark blue; μ3-O, red; dummy balls representing the cavities of Cage A and Cage B, green and violet, respectively. | ||
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| Fig. 7 Ball-and-stick and space-filling models of Cage C with a pseudo-S6 point symmetry. Top view of (a) the ball-and-stick and (b) space-filling models of Cage C. Side view of (c) the ball-and-stick and (d) space-filling models. Color code: BTB, pink and dark cyan; cobalt, dark blue; μ3-O, red; dummy ball representing the cavity of Cage C, orange. | ||
In the packing of the cages, the AB6 cage clusters are arranged at the eight vertices of a hypothetical primitive unit cell and Cage C is at the body center of this unit cell (Fig. S3, ESI†). The cages, with their total pore volume (9383 Å3) corresponding to ∼18% of the total unit cell volume, are arranged as shown in Fig. 8. However, the portals of Cage C between the dimeric one-face-open tetrahedra are blocked by one ligated DMA molecule at the terminal dinuclear cobalt ions (Fig. S4, ESI†). In addition, the potential passages between the pores of Cage B and Cage C are also blocked via the other ligated DMA molecules at the terminal dinuclear cobalt ions (Fig. S5, ESI†).
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| Fig. 8 Packing diagram of 1 as a ball-and-stick model with three different types of cages, where the pores of the cages are represented using the green, violet, and orange dummy balls. | ||
The variable-temperature powder X-ray diffraction (VT-PXRD) patterns of 1 indicate that the framework structure is stable up to 150 °C (Fig. 9). The peak broadening starts at 175 °C, especially for the peaks at higher diffraction angles, while preserving the major diffraction peaks at lower diffraction angles. The sample finally loses its crystallinity completely at 350 °C. The removal of the water molecules in the pores up to 150 °C does not affect the structural integrity of 1 (Fig. S6, ESI†). The removal of the DMA molecules, especially the DMA molecules ligated to the cobalt center, up to 300 °C, inevitably alters the coordination geometry of the cobalt center. The alteration reduces the short-range ordering around the altered cobalt center in the crystal, while preserving the overall long-range ordering of the whole framework structure of 1.
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| Fig. 9 VT-PXRD patterns of as-synthesized 1. Peaks with crosses and stars represent Co3O4 and the α-Al2O3 of the high-temperature sample holder, respectively. | ||
To access the pores in the framework, the ligated DMA molecules blocking the portals of the pores must be removed from the framework. Activated sample 1a was prepared by soaking 1 in methylene chloride for 3 d, and then vacuum drying at 250 °C for 5 h. The thermal gravimetric analysis (TGA) data of activated 1a briefly exposed to air showed a 0.7% weight loss up to 160 °C, then no further weight loss before the decomposition of the framework structure at around 350 °C (Fig. S8, ESI†),‡ showing that all the DMA molecules, including the ligated ones, could be completely removed from the framework by vacuum drying at 250 °C. The elemental analysis result of 1a also supports the complete removal of the ligated DMA molecules.
However, at 195 K, the type I isotherms of the CO2 sorption on 1a with the adsorbed CO2 amount of ∼81 cm3 g−1 at 1 bar show that the portal dimensions of the cages are larger than the KD of CO2 (3.3 Å) and the accessible pores are microporous (Fig. 10). Unlike the N2 sorption at 77 K, the sorption isotherms at 195 K indicate a small amount of N2 sorption (∼14 cm3 g−1 at 1 bar) with hysteresis. The sorption kinetics of N2 on 1a at 195 K is extremely slow compared with that of CO2 sorption. The sorption behavior of CH4 and CO is also somewhat similar to that of N2. Both adsorbates show small adsorbed amounts with hysteresis and slow sorption kinetics. These results strongly suggest that the portal dimensions of the pores at 195 K are in the KD range of adsorbates (N2, 3.64; CO, 3.76; CH4, 3.8 Å). The smaller H2 may also access the pores at 195 K. However, it appears that the interaction of H2 with the pore surface is not strong enough to cause adsorption.
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| Fig. 10 Sorption isotherms of CO2 (green), CO (pink), CH4 (blue), N2 (black), and H2 (red) on 1a at 195 K. Solid and open shapes represent adsorption and desorption, respectively. | ||
The gas sorption isotherms on 1a at 273 and 293 K are basically similar to those at 195 K, except for the overall reduction of sorption amounts with no significant hysteresis during the adsorption and desorption processes (Fig. S11, S12, ESI†). The average adsorption enthalpy of CO2, −25.6 kJ mol−1, and the adsorption enthalpy at zero coverage, −27.2 kJ mol−1, calculated from the adsorption isotherms at 273 and 293 K, are within the expected range for MOFs with no specific interacting sites, where the adsorption enthalpy was calculated using a virial equation (Fig. 11).13 The average adsorption enthalpies of CH4 and CO, −21.9 and −18.5 kJ mol−1, and the corresponding adsorption enthalpies at zero coverage, 22.6 and −19.1 kJ mol−1, respectively, were also calculated from the adsorption isotherms at 273 and 293 K using the same method. It is noticeable that the adsorbed amount of CH4 at 195 K and 1 bar (19 cm3 g−1) is smaller than that of CO (28 cm3 g−1), even though the adsorption enthalpy of CH4 is slightly larger than that of CO (Fig. 10, 11d and 11f). The adsorption enthalpies of CO2 and CO calculated from the adsorption isotherms for three different temperatures, 195, 273, and 293 K, are similar to those from the adsorption isotherms for 273 and 293 K (Fig. 11b and f). However, the adsorption enthalpy of CH4 calculated from the adsorption isotherms for three different temperatures, 195, 273, and 293 K, (−13.0 kJ mol−1) is much smaller than that calculated from the adsorption isotherms for 273 and 293 K (−21.9 kJ mol−1) (Fig. 11d). CO2 and CO can access the pores of 1a over the whole temperature range. However, CH4 can access most pores of 1a at 273 and 293 K, but has only limited access to those pores at 195 K. The portal dimensions of the pores of 1a are temperature-dependent and CH4 can access only part of the pores, because the portal dimensions of some pores at 195 K are smaller than the KD of CH4.
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| Fig. 11 Sorption isotherms of (a) CO2, (c) CH4, and (e) CO on 1a at 195, 273, and 293 K, respectively, and the corresponding adsorption enthalpies of (b) CO2, (d) CH4, and (f) CO. Solid and open shapes in the sorption isotherms represent adsorption and desorption isotherms, respectively. The adsorption enthalpies calculated by using the two adsorption isotherms at 273 and 293 K are represented in black, and those calculated by using the three adsorption isotherms at 195, 273 and 293 K are marked in red. | ||
The ability of a material to separate gases by adsorption is dependent on the selectivity for gas mixtures. In addition to the equilibrium uptake amount, the uptake kinetics of adsorbates is also an important factor in gas separation applications. Breakthrough experiments were carried out to test the gas separation capabilities of activated 1a. Approximately 1 g of 1a was exposed to gas streams containing binary mixtures of CO2/N2 (50
:
50 v/v) and CO2/CH4 (50
:
50 v/v) at a flow rate of 20 cm3 min−1 at 195 and 298 K. The breakthrough profile for the CO2/N2 mixture on 1a at 195 K is like an idealized profile (Fig. 12a). The outlet gas composition consists of pure N2 for ∼200 s before the breakthrough of CO2. The plateau observed in the N2 breakthrough curve suggests that 1a does not adsorb N2 at all, probably because of the extremely slow adsorption kinetics at 195 K, as observed in the N2 sorption measurement. After the saturation of 1a by CO2, the composition of the outlet gases slowly approaches that of the feed gas. It is worth noting that the adsorbed CO2 on 1a could be removed easily by flowing He at a flow rate of 50 cm3 min−1 for 30 min at ambient temperature for the next cycle of the breakthrough experiment. The breakthrough profile for the CO2/CH4 mixture on 1a at 195 K is similar to that for the CO2/N2 mixture (Fig. 12a and b). The outlet gas composition consists of pure N2 for ∼150 s before the breakthrough of CO2. The simultaneous adsorption of CH4 on 1a with the adsorption of CO2 results in the reduced breakthrough time for CO2 in the profile for the CO2/CH4 mixture.
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Fig. 12 Breakthrough curves on 1a using (a, c) CO2/N2 (50 : 50 v/v) and (b, d) CO2/CH4 (50 : 50 v/v) mixture gases with a total gas flow rate of 20 cm3 min−1 at 195 and 298 K, respectively. | ||
The breakthrough profiles for the CO2/N2 and CO2/CH4 mixture on 1a at 298 K showed significantly reduced breakthrough times (Fig. 12c and d), mainly due to the reduced adsorption capacity of 1a for CO2 at this temperature (Fig. S14, ESI†).
The excellent breakthrough separation performance of 1a for CO2/N2 and CO2/CH4 gas mixtures is the result of the combined selectivity coming from both the different equilibrium uptake amounts depending on the adsorption enthalpies of the adsorbates and the different uptake kinetics depending on the KDs of the adsorbates. In addition, 1a could easily be regenerated for the next cycle of the breakthrough experiment by simply flowing He at ambient temperature. We believe that our work has important implications in the search for crystalline microporous materials that are more efficient in adsorptive CO2 separation.
Footnotes |
| † Electronic supplementary information (ESI) available: Structural drawings, TGA, PXRD, gas sorption data, and breakthrough experimental setup. CCDC reference number 894096. For ESI and crystallographic data in CIF or other electronic format see DOI: 10.1039/c2ra22118g |
| ‡ The 0.7% weight loss corresponds to water molecules that were readsorbed from the air when 1a was exposed to air during the sample preparation for the TGA experiment. |
| This journal is © The Royal Society of Chemistry 2012 |