Shun-Shun
Qin
a,
Ze-Kun
Wang
a,
Lei
Hu
a,
Xing-Hao
Du
a,
Zheng
Wu
a,
Maria
Strømme
b,
Qian-Feng
Zhang
a and
Chao
Xu
*ab
aInstitute of Molecular Engineering and Applied Chemistry, Anhui University of Technology, Ma'anshan, 243002, P. R. China
bDepartment of Materials Science and Engineering, Uppsala University, The Ångström Laboratory, Box 35, 751 03 Uppsala, Sweden. E-mail: chao.xu@angstrom.uu.se; chao.xu0203@outlook.com
First published on 8th February 2021
Porous organic frameworks (POFs) with predesigned structures and tunable porosities have been widely studied in adsorption and heterogeneous catalysis. Introducing ionic structure into the framework endows POFs with new functionalities that may extend their applications. Here, we report new applications for a guanidinium-based ionic POF (IPOF-Cl) in palladium scavenging and heterogeneous catalysis. Due to the ionic framework and the porous structure, the IPOF-Cl displays fast adsorption kinetics and high adsorption capacities (up to 754 mg g−1) of Na2PdCl4 in aqueous solutions via a chemisorption (ion exchange) process. Significantly, it shows excellent scavenging activity towards trace amount of [PdCl4]2− in aqueous solution. More importantly, the loaded [PdCl4]2− species on the IPOF substrate are further reduced into ultrafine Pd nanoparticles with size of ∼2–5 nm. The obtained IPOF-Pd(0) nanocomposite containing uniformly distributed Pd nanoparticles and hierarchical porous structure demonstrates high activity in catalyzing a range of Suzuki coupling reactions. This study provides new routes for the development of ionic porous organic materials for applications in metal scavenging and catalysis.
Recently, a few examples of POFs consisting of ionic frameworks and counter-ions have been reported.22–26 Although the ionic POFs (IPOFs) usually have moderate surface areas due to the pore-blocking effect by the counter-ions, they demonstrate several unique advantages compared to their neutral analogs.27 For example, the ionic structure of IPOFs enables ion exchange which allows the pore size to be finely controlled by adjusting the size of counter-ions.28 Such IPOFs with controlled pore sizes demonstrated promising applications in size-selective adsorption and catalysis.25 In addition, the ionic interface in IPOFs triggers electrostatic interactions with guest molecules or ions that could enhance their performances in CO2 capture and in trapping ionic pollutants.26,29–32 Therefore, the design of IPOFs with tunable nanostructures, compositions and properties could further extend their applications in adsorption and catalysis.
Palladium catalysts (e.g., inorganic palladium salts, organopalladium, palladium nanoparticles) are widely used in a range of important organic transformations such as C–C coupling, hydrogenation, dehydrogenation.33 However, traditional homogeneous palladium catalysts usually suffer from significant recovery problems, which not only cause a waste of precious metal resource but also lead to heavy metal contamination in the products. In order to overcome these problems, it is highly desirable to develop efficient palladium scavengers and heterogeneous palladium catalysts.34–40 Given the ionic and porous structure, we envisioned that IPOFs may find applications in scavenging ionic palladium residues from solution via ion exchange and/or physical adsorption. In addition, immobilizing the palladium species in the porous channels of IPOFs offers a new route for the development of heterogeneous catalyst. Herein, we synthesize a dual functional IPOF-Cl composed of cationic guanidinium-based framework and chloride ions as charge-balance ions. The IPOF shows high adsorption uptake of tetrachloropalladate ions ([PdCl4]2−) in aqueous solutions. In addition, the adsorbed [PdCl4]2− ions in the porous channels are further reduced into ultrafine Pd nanoparticles (Scheme 1). As a result, the Pd nanoparticles immobilized IPOF shows high efficiency for catalytic conversion of a range of Suzuki coupling reactions.
Scheme 1 (a) Schematic reaction of ion exchange of IPOF-Cl with Na2PdCl4; (b) reduction of IPOF-PdCl4 by NaBH4 into IPOF-Pd(0). |
As displayed in various ionic porous materials (e.g. zeolites,45 ionic porous organic polymers,46 ionic metal–organic frameworks47), the ionic structure could endow IPOF-Cl with ion exchange ability that can potentially be used as a scavenger for anionic metal complexes. In this context, we studied the capture capability of IPOF-Cl towards [PdCl4]2−, a widely used homogeneous catalyst in a range of organic reactions.48,49 Firstly, we studied the kinetic of [PdCl4]2− capture from an aqueous solution by using IPOF-Cl. Specifically, an aqueous solution of Na2PdCl4 (33 mL, 0.6 mg mL−1) was mixed and stirred with grinded IPOF-Cl (20 mg) at room temperature. The Pd content in the solution at different intervals was determined by Inductively Coupled Plasma-Atomic Emission Spectrometer (ICP-AES). Obviously, the concentration of Na2PdCl4 in the solution decreased rapidly and more than 75% of the uptake was reached within the initial 10 min. The capture kinetic curve fits well with the pseudo-second-order kinetic model, indicating that the capture process was dominated by an ion exchange (or chemisorption) process (Fig. 2a and S3†).50 In addition, the adsorption isotherm was recorded to study the effect of Na2PdCl4 concentration on the capture process. As shown in Fig. 2c and S4,† the adsorption isotherm fits well with the Langmuir adsorption model. The maximum capture capacity is calculated to be 852 mg g−1. The value is much higher than the theoretical capacity of 572 mg g−1 based on ion exchange, which can be attributed to a synergetic effect of ion exchange and physisorption of Na2PdCl4 in the IPOF. When it reached adsorption equilibration in the aqueous solution of Na2PdCl4 (0.8 mg mL−1), the adsorbent was collected and its porosity was characterized by N2 sorption measurement (Fig. S5†). Since [PdCl4]2− ions possess a larger molecular weight and size than the original counter-ions of Cl−, the replacement of Cl− with [PdCl4]2− in IPOF-Cl not only increases the bulk density and but also partially blocks the pores of the material. As a result, the surface area and the total pore volume of the sorbent are significantly reduced from 163 m2 g−1 and 0.352 cm3 g−1 for IPOF-Cl to 48 m2 g−1 and 0.109 cm3 g−1 for IPOF-PdCl4, respectively. The reduced porosity also demonstrates the efficient capturing ability of IPOF-Cl towards [PdCl4]2−.
Given the high uptake and the fast kinetic of the capture process, we anticipated that it can be used as an efficient scavenger for removing trace amount of Na2PdCl4 from aqueous solutions. Remarkably, the use of 10 mg of IPOF-Cl reduced the concentration of aqueous Na2PdCl4 solution (9 mL) from 100 ppm to <1 ppm in 60 min (Fig. 2c). In addition, the UV–vis spectra and the optical images of the solution clearly show the efficient removal of Na2PdCl4 in the solution by the use of IPOF-Cl (Fig. 2d).
The hierarchical porous structure of IPOF-Cl and its high loading capacity of [PdCl4]2− further inspired us to investigate the potential of IPOF-Cl in heterogeneous catalysis. After capturing [PdCl4]2− from the aqueous solution, the solid was collected by centrifugation and then thoroughly washed by water. The obtained complex of IPOF-PdCl4 was redispersed in water, followed by adding NaBH4 to reduce the Pd(II) species into Pd(0) nanoparticles that gave IPOF-Pd(0). The composition of IPOF-Pd(0) was examined by XRD analysis. The intensive diffraction peaks at 2θ = ∼40.1, 46.5 and 68.0° can be attributed to the 110, 200, and 220 reflections of Pd(0), respectively. The broad diffraction peak at 2θ = ∼26.8° suggests that the crystalline structure of the IPOF substrate mainly remained intact (Fig. 3a). In addition, no significant change is observed in the infrared spectra (Fig. S6 and S7†). These results demonstrate the high chemical and structural stability of the IPOF. Such high stability for ketoenamine-linked porous organic materials has also been observed in previous studies.41,51,52 The high-resolution X-ray photoelectron spectroscopy (XPS) spectrum of IPOF-Pd(0) shows two sets of peaks: 338.48 and 335.25 eV in the Pd 3d5/2 region and 343.6 and 340.5 eV in the Pd 3d3/2 region, indicating the existence of both Pd(II) and Pd(0) in the composite (Fig. 3b and S8†). The deconvolution analysis of the spectrum suggests that it contains 74 wt% of Pd(0) and 26 wt% of Pd(II) species, respectively. The surface Pd content in the composite is calculated to be 31.4 wt% from the XPS analysis, which is slightly higher than the bulk Pd content (25.4 wt%) derived from the thermogravimetric analysis of the composite in an air atmosphere (Fig. S9†). Transmission electron microscopy (TEM) images reveal the formation of ultrafine Pd nanoparticles with a narrow size distribution of ∼2–5 nm in the nanocomposites (Fig. 3c and d). The nanoparticles are uniformly dispersed in the POF substrate and no significant aggregation of the nanoparticles is observed. It appears that the templating effect of IPOF with ordered porous structure plays a key role in the formation of such narrowly distributed ultrafine Pd nanoparticles.52 In addition, the interactions between the Pd nanoparticles and the amine groups in the organic framework could also assist the stabilization of the nanoparticles.53,54 As expected, the surface area of the composites is reduced to 27 m2 g−1. Importantly, the pore size distribution analysis of the N2 adsorption isotherm confirms that the hierarchical porous structure of the IPOF substrate remained after loading the Pd nanoparticles (Fig. 3e–f).
The catalytic activity of the IPOF-Pd(0) was evaluated in Suzuki coupling reactions of aryl halides and arylboronic acids in the presence of inorganic base. One of the advantages of the Suzuki coupling reaction is that the reaction can be conducted in various solvents including alcohol and water. Obviously, the high solubility of the arylboronic acid and the inorganic base in water could greatly promote the coupling reaction. More importantly, the use of water as the solvent provides a green and sustainable route for the organic synthesis. However, porous organic materials usually suffer from hydrolytic instability and/or hydrophobic nature preventing their applications in aqueous environments.55,56 Remarkably, the covalent nature and the ionic structure of the IPOF substrate endow high water stability and hydrophilicity of the catalyst, respectively, which greatly facilitate its catalytic application in aqueous solution. Therefore, we applied the catalytic reactions in a mixed solvent of water/ethanol (v:v = 2:3). As expected, the catalyst showed high catalytic activity for a range of Suzuki coupling reactions (Table 1). The coupling reaction between iodobenzene and phenylboronic acid catalyzed by IPOF-Pd(0) (1 mol%) gave a high yield of 97% in 2 h (entry 1). The use of bromobenzene resulted in a slightly lower yield of 93% under the same condition (entry 2). Compared to iodobenzene and bromobenzene, chlorobenzene is an ideal starting material for various organic reactions because of its low cost. However, the low reactivity of chlorobenzene usually results in low yields largely limiting its practical uses in coupling reactions.57 Noteworthy, IPOF-Pd(0) showed high catalytic activity in the coupling reaction between phenylboronic acid and chlorobenzene. By increasing the catalyst amount to 2 mol% and prolonging the reaction time to 6 h, a relatively high yield of 83% can be achieved (entry 4). We also evaluated the scope of the reaction by varying the substituent group of the aryl halides and arylboronic acids. Having electron-withdrawing groups (–CF3, –F) or electron-donating groups (–CH3) on the organic substrates did not significantly affect the efficiency of the catalyst, which gave high yields of 82–95% (entries 5–11). A hot filtration experiment was also conducted and we found that no further conversion of the raw materials to the products was observed once the catalyst had been removed. This result suggested that no significant Pd leaching from the IPOF-Pd(0) occurred during the catalysis process due to the high physiochemical stability of the catalyst. In addition, the catalyst showed good recyclability and it can be recycled and used at least 5 times without significant loss of the catalytic activity (Fig. S10†). More importantly, the catalyst showed good chemical and structural stability during the catalytic conversions (Fig. S11†). The excellent catalytic performance of the IPOF-Pd(0) in Suzuki coupling reactions can be attributed to the synergetic results of (i) the uniform distribution of ultrafine Pd nanoparticles endowing high catalytic activity of the catalyst; (ii) the hierarchical porous structure of the IPOF substrate allowing for fast mass transport during the catalytic transformations; and (iii) the ionic structure and the resulted good water-dispersibility of the IPOF substrate increasing the compatibility between the starting materials and the catalyst.
Entrya | Ar1-X | Ar2-B(OH)2 | Product | Yieldb (%) |
---|---|---|---|---|
a Reaction conditions: IPOF-Pd(0) (1 mol%), aryl halide (2.0 mmol, 1.0 equiv.), aryl boronic acid (2.4 mmol, 1.2 equiv.), K3PO4 (6.0 mmol, 3.0 equiv.), H2O (2.0 mL)/EtOH (3 mL), 85 °C, 2 h. b Yield of purified product after silica chromatography. c IPOF-Pd(0) (2 mol%), 6 h. | ||||
1 | 97 | |||
2 | 94 | |||
3 | 61 | |||
4c | 83 | |||
5 | 94 | |||
6 | 86 | |||
7 | 95 | |||
8 | 92 | |||
9 | 93 | |||
10 | 85 | |||
11 | 82 |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/d1nr00172h |
This journal is © The Royal Society of Chemistry 2021 |