Yifa
Chen‡
a,
Shenghan
Zhang‡
a,
Fan
Chen
a,
Sijia
Cao
a,
Ya
Cai
a,
Siqing
Li
a,
Hongwei
Ma
a,
Xiaojie
Ma
a,
Pengfei
Li
*ab,
Xianqiang
Huang
*c and
Bo
Wang
*a
aBeijing Key Laboratory of Photoelectronic/Electrophotonic Conversion Materials, Key Laboratory of Cluster Science, Ministry of Education, School of Chemistry, Beijing Institute of Technology, Beijing 100081, P. R. China. E-mail: bowang@bit.edu.cn
bAdvanced Research Institute of Multidisciplinary Science, Beijing Institute of Technology, Beijing 100081, P. R. China
cShandong Provincial Key Laboratory of Chemical Energy Storage and Novel Cell Technology, School of Chemistry & Chemical Engineering, Liaocheng University, Liaocheng, 252059, P. R. China
First published on 13th November 2017
By virtue of their structural periodicity, tunability, high porosity and rich functionality, metal–organic frameworks (MOFs) are of great interest in catalysis. However, MOF crystals are fragile and difficult to use as robust adsorbents or catalysts without processing into shapes. Precise control of particle size and catalytic sites for MOFs during the shaping procedures is also highly desired yet hard to realize. A versatile size control method for lanthanide MOFs, especially our newly designed Ce-MOF (BIT-58), is developed. The coordination and steric effects of various modulators are investigated. With size reduction from micrometers to nanometers (∼25 μm to ∼30 nm), more accessible metal sites of BIT-58 are exposed (10 times increased acid site amount; 7 times higher mesopore volume) and the catalytic performance is significantly improved. Furthermore, nano-sized BIT-58 can be processed into films or coatings with excellent catalytic activity, which holds great potential in batch or continuous-flow catalytic processes.
However, the brittle nature of MOFs, where MOFs easily break down into small particles or powders, hinders their long-term usage as catalysts. The catalyst loss of MOF catalysts is inevitable when MOF catalysts are applied in fluid reactions. Pipe clogging will also occur during long reaction cycles.5 To alleviate this problem, general processing methods for the fabrication of MOF crystals into pellets or beads under high pressure with high energy consumption are developed.6 However, these pellets or beads only slow down the pulverization process and the most accessible catalyst is confined to the surface with low MOF utilization. Hence, novel methods for the fabrication of MOFs into more robust forms are highly desirable. In particular, facile and versatile MOF coatings that can easily modify the inner surfaces of pipes or containers like tubes, autoclaves and beakers into highly active batch or continuous-flow reactors are long sought after.
In order to apply MOFs as robust coatings for efficient and diverse catalytic systems, the desired properties for MOF catalysts are proposed as follows: (1) small particle sizes (preferably in the nanometer range) to provide uniform dispersion;7 (2) unsaturated metal sites for high performance catalysis;3b (3) high stability that can endure harsh conditions.8 To date, it is still a challenge to combine most of the requirements together to make a nano-sized MOF with finely-tuned defects that are stable for industrial applications. MOFs with unsaturated/open metal sites, which generally lack chemical and/or thermal stability,9 still pose a challenge for size control and further processing. Moreover, the design of a suitable nano-sized MOF catalyst for batch or continuous-flow catalysis needs overall consideration: structural stability, catalytic site engineering, and more importantly, catalyst fabrication.
Herein, we report a coordination modulation method for lanthanide MOFs, and a highly efficient coating catalyst for Knoevenagel condensation based on a newly designed highly stable nano-sized Ce-MOF through defect engineering and electrospinning fabrication (Fig. 1). We design a Ce-BTB MOF (BIT-58, BIT stands for Beijing Institute of Technology) with Ce3+ as the metal center and 1,3,5-tris(4-carboxyphenyl)benzene (BTB) as the ligand to satisfy the above mentioned criteria. Ce3+ is widely used as a Lewis acid catalyst and has a versatile redox behavior with a high coordination number and large charge density, which provides the potential to keep high stability with open metal sites. The crystal size and defects of BIT-58 are controlled by a versatile coordination modulation method10 utilizing various nitrogenous heterocyclic modulators (e.g., 1-methylimidazole (1-mIM)). This method is also suitable for rare earth MOFs with distinct structures. Furthermore, a BIT-58 nanoparticle-based coating presenting high catalytic activity and excellent reusability is fabricated on the surface of a container through electrospinning for batch catalysis (Fig. 1).
![]() | ||
Fig. 1 The schematic representation of coordination modulation for lanthanide MOFs and the fabrication of a coating catalyst. |
Remarkably, BIT-58 exhibits exceptionally high chemical and thermal stability. A wide range of solvents are tested. For example, the integrity of BIT-58 remains unchanged in common organic solvents (e.g., chloroform) for more than three days (Fig. 2c). In addition, the BIT-58 remains intact in water at 25 °C or even at 100 °C for at least three days (Fig. 2c). Especially, BIT-58 is stable under highly acidic or basic conditions with a wide pH range from 1 to 12. Moreover, BIT-58 is stable at temperatures as high as 490 °C under N2 and 400 °C under air as shown by variable temperature PXRD (Fig. 2d and S3, ESI†) and thermogravimetric analyses (TGA) (Fig. S4, ESI†).
The crystal of nano-BIT-58 is imaged by transmission electron microscopy (TEM) and its crystal lattice is further measured by selected-area electron diffraction (SAED) analysis. The diffraction pattern is clearly visible with a spacing of 3.62 Å attributed to the (4 2 3) crystal plane (Fig. 3c). Elemental mapping analysis of nano-BIT-58 reveals that the Ce3+ ions in the particle are uniformly distributed (Fig. 3d). We further adjust the amount of 1-mIM added to the reaction. The average particle size shows a U-shaped curve by changing the amount of 1-mIM from 0 to 9 mL (volume ratios, 0 to 0.36) (Fig. 3g, h and S6, ESI†). The smallest particle size (about 30 nm) is achieved with 1.2 mL 1-mIM (volume ratio, 0.07). To prove the generality of this method, we further extend this method to different rare earth MOFs. In particular, the crystal sizes of Ce-NDC,15a Ce-BTC,15b,c Eu-BTC,15d Dy-BTC15d and La-BTB11 with different structures are also tuned using the same method with 1-mIM as the modulator (Fig. S11 and S12, ESI†).
With a stable nano-sized BIT-58 in hand, the exposed defects in the MOF nanocrystals are carefully characterized by NH3-temperature programmed desorption (NH3-TPD) (Fig. S16, ESI†). The TPD peak at about 100 °C reflects the physical sorption of NH3 on MOFs, and this peak is wider in nano-BIT-58 than that of BIT-58 crystals with a 1.53 times increase in desorbed NH3 amount (nano-BIT-58, 3.92 and BIT-58, 2.56) (Fig. 3e). TPD peaks higher than 200 °C attributed to different acid sites are either broader or more intense in nano-BIT-58 compared with BIT-58. NH3-TPD curves show that nano-BIT-58 presents a total acid site amount of 7.06 which is 10.5 times that of BIT-58 (0.67) due to the enhanced defects like more Lewis acid sites (e.g., unsaturated metal sites) and Brønsted acid sites (e.g. uncoordinated carboxyl groups) exposed.16
The largely exposed metal sites and drastically enhanced mesopore volume imply that the nano-BIT-58 is a superior catalyst.17 As a proof of concept, nano-BIT-58 with a particle size of about 30 nm exhibits higher catalytic efficiency than BIT-58 in a Knoevenagel condensation catalysis of benzaldehyde and malononitrile (Fig. 4a).18 After workup, the structural integrity of nano-BIT-58 is maintained (Fig. 4b). The conversion efficiency of nano-BIT-58 reaches 100% at 6 h, which is superior to that of BIT-58 (78%, 6 h) (entry 1, Table 1 and Fig. S17, ESI†). Moreover, we have extended the substrates to various benzaldehyde derivatives (i.e. 4-chlorobenzaldehyde, 4-bromobenzaldehyde, 4-methoxybenzaldehyde, 3,5-dimethoxybenzaldehyde, 1-naphthaldehyde and 9-anthraldehyde) with diverse molecule sizes. The catalytic performance improvement is shown by the efficiency ratio of the nano-BIT-58 catalyzed reaction to the BIT-58 catalyzed reaction, which is more significant in the catalysis of larger benzaldehyde derivatives with a similar substitution pattern. For example, 4-chlorobenzaldehyde (4.521 Å × 9.428 Å) and 4-bromobenzaldehyde (4.521 Å × 9.718 Å) have 2.9 and 1.9 times improvement in catalytic performances (entries 2 and 3, Table 1), respectively. 3,5-Dimethoxybenzaldehyde (7.248 Å × 8.074 Å) shows a 7.3 times increase compared with 3.2 times for 4-methoxybenzaldehyde (4.521 Å × 9.31 Å) (entries 4 and 5, Table 1). Furthermore, the difference in catalytic performances is more significant when the derivatives are 1-naphthaldehyde (7.240 Å × 7.417 Å) and 9-anthraldehyde (7.244 Å × 9.756 Å) with larger molecule sizes tested, in which nano-BIT-58 has 2.9 and 14.0 times improvement in conversion efficiency, respectively (entries 6 and 7, Table 1). Although the pore size distribution is broadened, nano-BIT-58 still shows substrate selectivity toward substrates with a suitable molecular size. The catalytic conversion efficiency with a molecular size smaller than 8 Å is almost quantitative compared to that with the larger reactants.
Entry | Substrates | BIT-58 | Nano-BIT-58a | Efficiency ratio (nano-BIT-58/BIT-58) |
---|---|---|---|---|
a Nano-BIT-58 represents 1-mIM modulated particles (∼30 nm). b The conversion efficiencies of the reaction for various substrates are collected at 6 h under the same conditions. | ||||
1 |
![]() |
78%b | 100% | 1.3 |
2 |
![]() |
24% | 45% | 1.9 |
3 |
![]() |
25% | 72% | 2.9 |
4 |
![]() |
8% | 26% | 3.2 |
5 |
![]() |
10% | 73% | 7.3 |
6 |
![]() |
31% | 90% | 2.9 |
7 |
![]() |
3% | 42% | 14.0 |
As the crystal size of nano-BIT-58 is controlled in the nanometer range, it affords perfect manufacturing properties. We successfully fabricated nano-BIT-58 into a film (70 wt% nano-BIT-58 in polyacrylonitrile (PAN)) with intact internal topology through electrospinning (Fig. 4e and S18, ESI†).19 The obtained film displays a nanofiber-interweaved network and nano-BIT-58 particles are uniformly dispersed on the nanofibers (about 200 nm) (Fig. 4c). The porosity of nano-BIT-58 in the film is accessible as demonstrated by the N2 sorption test with a SBET of 409 m2 g−1 (Fig. S19, ESI†). Besides, the film can hold 0.05 MPa pressure in a stretching resistance test (Fig. S20, ESI†). With high mechanical strength and readily accessible pores, this film is directly used in the condensation reaction. It presents 100% catalytic conversion efficiency in just 6 h and is easily recycled at least three times without losing its activity and stretching robustness (Fig. 4d, e, S20 and S21, ESI†). It is noteworthy that we successfully manufactured a large-scale film (14 cm × 15 cm) through position-controlled electrospinning (Fig. S22, ESI†). Furthermore, a portable electrospinning device is used to directly deposit this film on the surface of various substrates (i.e. beaker, aluminum foil, plastic mesh, nickel foam, glass cloth, non-woven fabric and cardboard) (Fig. 4f and S23, ESI†). The wet nanofibers after electrospinning with trace amounts of solvents are attached to the surface of the substrate with interfacial interactions.20 Taking a beaker for example, nano-BIT-58/PAN as a powerful catalyst coating directly turns a beaker with no activity into a highly active one and exhibits a 95% catalytic conversion efficiency in the reaction (Fig. 4f). After the catalysis, the product is easily separated by pouring out and the coated beaker can be directly used in the next cycle without loss of activity.
Footnotes |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c7ta09036f |
‡ These authors contributed equally to this work. |
This journal is © The Royal Society of Chemistry 2018 |