Xing
Duan
*a,
Yuanjing
Cui
b,
Yu
Yang
b and
Guodong
Qian
*b
aCollege of Materials & Environmental Engineering, Hangzhou Dianzi University, Hangzhou, 310027, PR China. E-mail: star1987@hdu.edu.cn
bState Key Laboratory of Silicon Materials, Cyrus Tang Center for Sensor Materials and Applications, School of Materials Science and Engineering, Zhejiang University, Hangzhou, 310027, PR China. E-mail: gdqian@zju.edu.cn
First published on 28th December 2016
A methoxy-decorated novel metal–organic framework (MOF), Cu2(DTPD) (ZJU-12, H4DTPD = 5,5′-(2,6-dimethoxynaphthalene-1,5-diyl)diisophthalic acid) with optimized pore space and open metal sites, was solvothermally synthesized and structurally characterized. The activated ZJU-12a displays a moderately high BET (Brunauer–Emmett–Teller) surface area of 2316 m2 g−1. Due to the pore size of the crystal being consistent with the molecular size and kinetic diameters of C2H2 and CO2, ZJU-12a exhibits a high C2H2 storage capacity of 244 cm3 g−1 and CO2 capture capacity of 134 cm3 g−1 at room temperature.
To develop microporous metal organic framework materials with high gas adsorption performance, a series of strategies, such as improving the density of metal open sites, increasing the pore volume and surface areas, enhancing the quality of crystals and optimizing the activation conditions, taking advantage of framework catenation and interpenetration, adjusting the pore sizes and modifying the pore surfaces, has been extensively explored.6 Designing and synthesizing MOFs with open metal sites (OMSs) is one of the best strategies to enhance gas storage properties. The well-known MOF material HKUST-1 (ref. 7) with open copper coordination sites in a large cuboctahedral cage has a high acetylene adsorption capacity of 201 cm3 g−1. Xiang et al.8 reported a porous material with high densities of open metal sites, CoMOF-74, which exhibits a high volumetric acetylene storage capacity of 230 cm3 cm−3. However, high densities of open metal sites result in high adsorption enthalpy, which goes against the regeneration of crystal materials. On the other hand, pore size also plays an important role in the aspect of gas adsorption. For promoting the capability of capturing gas molecules, maximizing the guest–framework interaction by matching the pore space with the size of the gas molecules can be identified as an effective approach. To adjust the pore size, several strategies have been reported, such as inserting a symmetry-matching regulated secondary linker or anchoring a metal ion/cluster/functional groups at the cage/channel centers, which make the pore space of the primary framework partition into multiple domains.6d–j Zhao et al.6d introduced a tripyridyl-type linker into a MIL-88-type structure to obtain a family of CPM-33 materials which exhibit superior CO2 adsorption capacity. In particular, CPM-33b shows the highest CO2 adsorption value of 126.4 cm3 g−1 among MOFs without OMSs and is comparable to ZnMOF-74 and NiMOF-74.2b,9 Herein, with the purpose of improving the gas uptake capacity, we substitute benzene with dimethoxynaphthalene into terphenyl-3,3′,5,5′-tetracarboxylic acid to obtain a new tetracarboxylic organic linker H4DTPD (Scheme 1) and its corresponding first microporous MOF, [Cu2(DTPD)(H2O)2]·(DMF)5·(H2O)2 (ZJU-12; H4DTPD = 5,5′-(2,6-dimethoxynaphthalene-1,5-diyl)diisophthalic acid, ZJU = Zhejiang University), with optimized pore space and open metal sites. The activated ZJU-12a exhibits a moderately high BET (Brunauer–Emmett–Teller) surface area of 2316 m2 g−1 and a high C2H2 storage capacity of 244 cm3 g−1 and CO2 capture capacity of 134 cm3 g−1 at room temperature.
Dimethyl 5-amino-isophthalate (50 g) was added to 15% hydrobromic acid (900 mL) and cooled to 0 °C. A sodium nitrite solution (2.5 M, 120 mL) was added slowly with stirring to obtain a solution of diazonium bromide. The solution of diazonium bromide was slowly added to a solution including CuBr (49 g) and 15% hydrobromic acid (450 mL) under stirring, while the temperature was always kept under 0 °C. The mixture was kept stirring under room temperature overnight after the addition was completed. The solution was filtered, and the filter cake was dissolved in CCl2H2, dried with MgSO4, filtered and concentrated in a vacuum. The crude product was purified by column chromatography (silica gel, ethyl acetate/petroleum ether, 1:8 v/v) to obtain dimethyl 5-bromobenzene-1,3-dicarboxylate as a white powder. Yield: 85%. 1H-NMR (500 MHz, CDCl3): δ = 3.95 (s, 6H), 8.35 (d, 2H), 8.61 (s, 1H) ppm.
The dimethyl 5-bromobenzene-1,3-dicarboxylate (5.4 g), bis(pinacolato)diborane (6.0 g), Pd(dppf)2Cl2 (0.2 g) and potassium acetate (5.6 g) were added to 100 mL of dried 1,4-dioxane. The mixture was kept at 70 °C for 24 h under stirring. Afterwards, the resultant mixture was extracted with 50 mL of ethyl acetate. The organic layer was separated and dried with anhydrous MgSO4. Then, the solvent was concentrated in a vacuum after filtration. Finally, the crude product was purified by column chromatography (silica gel, ethyl acetate/petroleum ether, 1:8 v/v) to obtain pure dimethyl (5-pinacolboryl)isophthalate. Yield: 66%. 1H NMR (500 MHz, CDCl3): δ = 1.37 (m, 12H), 3.95 (s, 6H), 8.64 (d, 2H), 8.76 (s, 1H) ppm.
Naphthalene-2,6-diol (10 g) and K2CO3 (20 g) were dissolved in DMF (50 mL), then iodomethane (10 mL) was added, and the mixture was kept under 85 °C for 3 hours and afterwards was filtered after adding water (100 mL). The crude product was purified via recrystallization of CCl2H2 to obtain 2,6-dimethoxynaphthalene. Yield: 85%. 1H NMR (500 MHz, CDCl3): δ = 3.90 (s, 6H), 7.66 (d, 2H), 7.12 (s, 2H), 7.15 (d, 2H) ppm.
A solution of 2,6-dimethoxynaphthalene (5 g) in a 100 mL mixed solvent of CHCl3 and acetic acid (1:1) was added to NBS (9.6 g) under 0 °C. After the mixture reacted overnight at room temperature, the mixture was filtered. The solid was washed with water, saturated NaHCO3 solution, ethanol and CHCl3 to afford 1,5-dibromo-2,6-dimethoxynaphthalene as a white solid. Yield: 87%. 1H NMR (500 MHz, CDCl3): δ = 4.04 (s, 6H), 8.26 (d, 2H), 7.37 (d, 2H) ppm.
1,5-Dibromo-2,6-dimethoxynaphthalene (3 g), dimethyl (5-pinacolboryl)isophthalate (5.57 g) and K2CO3 (8 g) were added to 100 mL of anhydrous 1,4-dioxane, and the solution was deaerated under Ar for 15 min. Pd(PPh3)4 (0.47 g) was added to the reaction mixture with stirring, and the mixture was heated to 80 °C for 3 days under Ar. Afterwards, it was extracted with trichloromethane (150 mL). The organic layer was separated and was dried with anhydrous MgSO4 and the solvent was removed in a vacuum. The crude product was purified by column chromatography to obtain tetramethyl 5,5′-(2,6-dimethoxynaphthalene-1,5-diyl)diisophthalate. Yield: 59.2%. 1H-NMR (500 MHz, CDCl3): δ = 3.77 (s, 6H), 3.96 (s, 12H), 8.27 (s, 4H), 8.77 (s, 2H), 7.24 (d, 2H), 7.43 (d, 2H) ppm.
Tetramethyl 5,5′-(2,6-dimethoxynaphthalene-1,5-diyl)diisophthalate (5 g) was then suspended in 150 mL of NaOH (13.9 g) aqueous solution, and 1,4-dioxane (40 mL) was added. The mixture was stirred under reflux until clarification. Dilute HCl was added to the aqueous solution until the pH of the solution was 2. The solid was collected by filtration, washed with a lot of water, and dried to give 5,5′-(2,6-dimethoxynaphthalene-1,5-diyl)diisophthalic acid (H4DTPD, 96.7% yield). 1H-NMR (500 MHz, DMSO): δ = 3.76 (s, 6H), 7.38 (d, 2H), 7.50 (d, 2H), 8.09 (s, 4H), 8.56 (s, 2H), 13.39 (s, 4H) ppm.
The single crystal X-ray crystallography (SXRD) analysis proved that ZJU-12 crystallizes in the trigonal space group Rm. As expected, ZJU-12 is built from paddle-wheel Cu2(COO)4 secondary building units (SBUs) connected to H4DTPD linkers via carboxylate groups to have the well-known NbO topology (Fig. 1). The 3D framework of ZJU-12 has two types of cages along the c axis. The diameter of the spherical-like cage is about 6.4 Å, taking into account the van der Waals radii (Fig. 1a). Furthermore, the size of the irregular shuttle-shaped cage is approximately 3.2 × 20.6 Å2 (Fig. 1b). The kinetic diameter and molecular dimensional size of C2H2 (3.3 Å, 3.32 × 3.34 × 5.7 Å3) and CO2 (3.3 Å, 3.18 × 3.33 × 5.36 Å3) are a little lower than those of the cages, therefore these two gases can easily enter the cages of the crystal. Furthermore, due to the introduction of dimethoxynaphthalene, there are smaller sizes of windows along the a, b and c axes in ZJU-12 materials compared with the prototype framework NOTT-101. One, which has a value of about 1 Å, can be observed along the c axis (Fig. 1c) and the other two along the a axis are about 2 Å and 2.8 × 5.6 Å2 (Fig. 1d). The smaller window sizes can effectively prevent gas molecules from escaping from the pore space of framework materials. The calculated accessible free pore volume of ZJU-12a is 62% (7414 Å3 out of 11960.5 Å3), evaluated by the PLATON program.10
To estimate the permanent porosity, the dry acetone-exchanged ZJU-12 was activated under high vacuum to obtain the desolvated ZJU-12a. The N2 adsorption isotherm of ZJU-12a, which exhibits reversible type-I adsorption behaviour, was acquired at 77 K. The highest adsorbed amount of N2 for ZJU-12a is 606 cm3 g−1 and the corresponding pore volume is 0.938 cm3 g−1 (Fig. 2). The surface areas of ZJU-12a are evaluated to be 2316 m2 g−1 from Brunauer–Emmett–Teller (BET) (Fig. S3†) and 2567 m2 g−1 from Langmuir surface areas. The BET value is slightly lower than that for NOTT-101 (ref. 11a) (2805 m2 g−1) because of substitution of benzene with dimethoxynaphthalene, but is comparable to those for ZJU-25a11b (2124 m2 g−1), NOTT-109 (ref. 11a) (2110 m2 g−1), NJU-Bai-14 (ref. 11c) (2384 m2 g−1), ZJNU-54a11d (2134 m2 g−1) and ZJNU-44 (ref. 11e) (2314 m2 g−1). The pore size distribution calculated by the Horvath–Kawazoe model is in the range from 4 Å to 6 Å, which is consistent with the pore sizes from SXRD (Fig. S4†).
Fig. 2 N2 sorption isotherm of ZJU-12a at 77 K. Solid and open symbols represent adsorption and desorption, respectively. |
Acetylene is one of the important raw materials in industrial production, but the storage of acetylene is required to be under suitable low pressure, otherwise it has the possibility of explosion. Among all kinds of porous materials, MOF materials are considered to be the most promising ones for such an application. The optimized pore space and open metal sites within the framework of ZJU-12a encourage us to study its adsorption performance for acetylene and methane. We examine the acetylene adsorption of ZJU-12a. As shown in Fig. 3a, ZJU-12a can take up a large amount of acetylene. At 273 K and 298 K, the acetylene saturated adsorption capacity of ZJU-12a can reach 301 cm3 g−1 and 244 cm3 g−1, respectively. The gravimetric acetylene storage capacity of ZJU-12a at room temperature is significantly higher than those of examined porous MOF materials.2f,7,12 In fact, the gravimetric C2H2 adsorption capacity of 244 cm3 g−1 is the highest one ever reported (Table 1), indicating the promise of this novel microporous MOF material for practical acetylene storage applications. Taking the framework density of 0.799 g cm−3 without the coordinated waters into account, the volumetric capacities are 241 cm3 cm−3 and 195 cm3 cm−3 at 273 K and 298 K, respectively. The initial Qst of C2H2 adsorption in ZJU-12a is calculated to be 29 kJ mol−1 (Fig. 4), which is significantly lower than that for MOF-74 with high densities of open metal sites.
Fig. 3 Gas sorption isotherms of ZJU-12a for (a) C2H2 at 273 K and 298 K, and (b) CO2 at 273 K and 298 K. Solid symbols: adsorption, open symbols: desorption. |
MOFs | S BET (m2 g−1) | V P (cm3 g−1) | C2H2 uptake (cm3 g−1) | Ref. |
---|---|---|---|---|
ZJU-12a | 2316 | 0.938 | 244 | This work |
FJI-H8 | 2025 | 0.82 | 224 | 12e |
NJU-Bai17 | 2423 | 0.914 | 222.4 | 12g |
ZJU-40a | 2858 | 1.06 | 216 | 12o |
ZJNU-47 | 2638 | 1.031 | 213 | 12h |
ZJNU-54 | 2134 | 0.871 | 211 | 11d |
Cu 2 TPTC-OMe | 2278 | 1.039 | 204 | 12j |
Cu 2 TPTC-Me | 2405 | 0.9805 | 203 | 12j |
HKUST-1 | 1850 | 0.76 | 201 | 7 |
CoMOF-74 | 1504 | 0.63 | 197 | 12b |
ZJU-8a | 2501 | 1.0224 | 195 | 12k |
ZJU-5a | 2823 | 1.074 | 193 | 12f |
ZJU-9a | 2353 | 0.887 | 193 | 12l |
ZJU-70 | 1362 | 0.676 | 191 | 12c |
NOTT-101 | 2805 | 1.080 | 184 | 12d |
ZJU-7a | 2198 | 0.8945 | 180 | 12m |
PCN-16 | 2810 | 1.06 | 176 | 12a |
MOF-505 | 1139 | 0.67 | 148 | 7 |
NOTT-102 | 3342 | 1.280 | 146 | 12d |
ZJU-26a | 989 | 0.572 | 84 | 12n |
The excessive emission of carbon dioxide (CO2) is the major factor for the greenhouse effect. MOF materials are very promising solid porous adsorbents for CO2 capture on account of their intrinsic advantages. We investigate the CO2 adsorption performance, indicating that ZJU-12a exhibits a CO2 uptake of 243 cm3 g−1 at 273 K and 134 cm3 g−1 at 298 K at 1 bar (Fig. 3b). Remarkably, the gravimetric CO2 sorption capacity at room temperature is higher than those of MOF materials ZJNU-54a12i (120 cm3 g−1), PCN-124 (ref. 13a) (114 cm3 g−1), ZJNU-44 (ref. 13b) (116 cm3 g−1), NPC-6 (ref. 13c) (108 cm3 g−1), JLU-Liu21 (ref. 13d) (118 cm3 g−1), NJU-Bai21 (ref. 13e) (115 cm3 g−1) and NJU-Bai-14 (ref. 11c) (100 cm3 g−1). The high C2H2 and CO2 adsorption values demonstrate that open metal sites and optimized pore size can really enhance the interaction between the gas molecules and the framework. The initial adsorption enthalpy Qst for CO2 was calculated by the virial method and the value is 26.9 kJ mol−1 (Fig. 4). Such low C2H2 and CO2 adsorption enthalpy values meet the requirement of low energy consumption in the adsorbent recycling process.
Footnote |
† Electronic supplementary information (ESI) available. CCDC 1510153. For ESI and crystallographic data in CIF or other electronic format see DOI: 10.1039/c6ce02291j |
This journal is © The Royal Society of Chemistry 2017 |