Wenhuan Dong‡
a,
Li Zhang‡a,
Chenhuan Wangb,
Cheng Feng*a,
Ningzhao Shanga,
Shutao Gaoa and
Chun Wang*a
aCollege of Sciences, Agricultural University of Hebei, Baoding 071001, Hebei Province, P. R. China. E-mail: fengchencctv@163.com; chunwang69@126.com
bCollege of Environmental and Chemical Engineering, Yanshan University, Qinhuangdao 066004, China. Fax: +86-312-7528292
First published on 8th April 2016
A nanoporous carbon (NPC) material was prepared by one-step direct carbonization of a metal–organic framework, MOF-5, without additional carbon precursors. Pd nanoparticles were immobilized on the MOF-5-derived NPC by an impregnation method coupled with subsequent reduction with NaBH4. The prepared catalyst was in-depth characterized by X-ray photoelectron spectroscopy, transmission electron microscopy, scanning electron microscopy, and N2 adsorption. The catalyst was used to catalyze the Suzuki–Miyaura coupling reactions and exhibited high catalytic efficiency with yields ranging from 90% to 99% under mild conditions. The results demonstrated the great application potential of MOF precursor-based metal nanoparticle composites in catalysis.
Several solid materials, such as active carbon,9 zeolites,10 mesoporous silica11 and polymers,12,13 have been used as heterogeneous catalyst supports for C–C coupling reactions. However, some of the supported catalysts involve disadvantages such as, uneven distribution of the active sites, tedious preparation of the catalyst, lower catalytic activity and so on. Therefore, the development of highly active and selective heterogeneous catalysts for catalyzing C–C coupling reactions under mild conditions is required for practical use.
Recently, nanoporous carbons (NPCs) materials, have been touted as ideal catalyst support for heterogeneous catalyst because of their high specific surface area and porosity14 in combination with high chemical (acid and base resistant), thermal (>1000 K) and excellent mechanical stability.15,16 Highly porous carbons can be prepared via a variety of methods, including direct pyrolysis of organic precursors, activation (physical or chemical) of carbon,17 hard-template or soft-template route,18 and nanocast method.19 However, these methods often encounter one or more shortcomings, such as the obtained carbon materials often contain disordered structures, the templates need to be removed after carbonization, the preparation process is tedious and so on. Therefore, the development of novel synthesis strategy based on facile, versatile, and reproducible method is highly desirable.
As an emerging class of highly porous material, metal–organic frameworks (MOFs) have gained particular attention in recent years mainly due to their ease of preparation, designable framework structures and multifunctional nature.20 MOFs with fascinating diverse structures, topologies, permanent nanoscale porosity, high surface area and uniform structured cavities, have been demonstrated to be ideal templates for fabricating nanoporous carbon. Highly nanoporous carbon can be fabricated by direct carbonization of different MOFs without the need of additional carbon precursors because MOFs was taken as both a sacrificial template and a secondary carbon precursor. Several MOFs, such as UiO-66,21 MIL-100,22 and Al-PCP,23 have recently been demonstrated as promising templates to construct porous carbons. Compared with the conventional nanocasting technique with several steps, the merit of this approach lies in that it is a facile, controllable, and single-step procedure method. NPCs derived from MOFs have found a wide range of applications in different fields, such as water treatment, contamination removal,24 separation, electrode materials,18 gas storage25 and carriers for drug delivery systems,26 due to their high specific surface area, large pore volume, high thermal stability and excellent electrochemical performance.
In continuation of our efforts in the development of a sustainable and active catalyst system,27–29 in this paper, porous carbon was fabricated by one-step direct carbonization of MOF-5 (Zn4O(H-BDC)3, BDC = 1,4-benzenedicarboxylate) without using any additional carbon precursors. The obtained MOF-5-derived NPC exhibited a high specific surface area and large pore volume. Pd nanoparticles were immobilized on MOF-5-derived NPC by an impregnation method coupled with subsequent reduction with NaBH4. To evaluate the performance the MOF-5-NPC-Pd, Suzuki–Miyaura reaction was selected as the model reaction. The results indicated that the MOF-5-NPC-Pd can catalyzed the Suzuki–Miyaura reaction efficiently under mild conditions.
X-ray photoelectron spectroscopy (XPS) was performed with a PHI 1600 spectroscope using Mg Kα X-ray source for excitation. Scanning electron microscopy (SEM) studies were conducted on a Hitachi (Model S4800) instrument. The size and morphology of the nanoparticles were observed by transmission electron microscopy (TEM) using a JEOL model JEM-2011 (HR) at 200 kV. The Brunauer–Emmett–Teller (BET) surface areas were determined from the N2 adsorption at 300 K using V-Sorb 2800P (China). The amount of Pd and Zn was determined by means of inductively coupled plasma atomic emission spectroscopy (ICP-AES) on Thermo Elemental IRIS Intrepid II.
To preparation of the Zn-free MOF-5-NPC-900-Pd, 50 mg of MOF-5-NPC-900 powder was dispersed in 20 mL of 10% HCl and standed for 6 h. And then the mixture was filtered and washed with distilled water. Finally, the MOF-5-NPC-900 without Zn or ZnO was obtained by vacuum drying at 60 °C for 2 hours.
The Zn-free MOF-5-NPC-900-Pd was prepared according to the same procedure mentioned above except that 50 mg MOF-5-NPC-900 was replaced by 50 mg Zn-free MOF-5-NPC-900.
The TEM investigations are carried out to observe the size, and the distribution of Pd nanoparticles embedded in Zn-free MOF-5-NPC-900-Pd. The highly existence of Pd nanoparticles, which embedded in Zn-free MOF-5-NPC-900 was clearly observed in Fig. 1A and B. The density of Pd nanoparticles in Zn-free MOF-5-NPC-900-Pd nanocatalyst is abundant and these nanoparticles did not form clusters. Fig. 1B and C showed the high-resolution TEM (HRTEM) image of the as-prepared catalyst, wherein the lattice spacing is 0.22 nm, which is just the lattice spacing of face centered cubic (fcc) Pd (0.22 nm), further indicating that is Pd nanoparticles. Besides, the mean diameter of the particles was just 2.7 nm and was almost similar to the pore diameter of the nanoporous carbon support. It also can be clearly seen from the SEM image (Fig. 1D) that some of the Pd NPs supported on the surface of the Zn-free MOF-5-NPC-900, and the most of them inserted into the cavities of Zn-free MOF-5-NPC-900. The element mapping images (Fig. S2†) clearly showed the uniform distribution of fine Pd nanoparticles throughout the Zn-free MOF-5-NPC-900-Pd composite.
The X-ray diffraction (XRD) pattern in Fig. 2 showed the crystalline structure of the Zn-free MOF-5-NPC-900-Pd samples. The wide diffraction peak at 2θ = 25° can be indexed to porous carbon.19 Besides, we characterized the XRD of the catalyst, the broadly peak appear at 40°, and the peaks at 47° and 68° were very poor, which suggests the well dispersion of Pd nanoparticles.31,32 The three peaks appear at 40°, 47° and 68° can be assigned to (111), (200) and (220) crystal planes of Pd0, respectively.
The XPS spectra (Fig. 3) demonstrated that the Pd species embedded in the sample Zn-free MOF-5-NPC-900 was present in metallic state rather than in oxidation state with the bond energies of 335.4 and 341.0 eV in the Pd 3d5/2 and 3d3/2 levels. As displayed in Fig. 3, the Pd 3d binding energy region was deconvoluted into four peaks with binding energies of 335.6, 337.1, 340.9 and 342.0 eV. The two minor peaks in the Pd 3d spectrum centered at 342.0 and 337.1 eV were assigned to Pd2+ 3d3/2 and Pd2+ 3d5/2, and the other two peaks centered at 340.9 and 335.6 eV are very sharp with a huge intensity. These peaks are assigned to Pd0 3d3/2 and Pd0 3d5/2, respectively.33,34
Entry | Catalysts | Yields/% |
---|---|---|
a n(K2CO3)![]() ![]() ![]() ![]() ![]() ![]() ![]() ![]() |
||
1 | MOF-5-NPC-700-Pd | 68 |
2 | MOF-5-NPC-800-Pd | 73 |
3 | MOF-5-NPC-900-Pd | 92.1 |
4 | MOF-5-NPC-1000-Pd | 90.3 |
5 | Zn-free MOF-5-NPC-900-Pd | 98.6 |
Aryl halide | Catalyst | Reaction conditions: solvent/temp./time/Pd loading | Yield/% | Ref. |
---|---|---|---|---|
Bromobenzene | MOF-5-NPC-900-Pd | EtOH–H2O/25 °C/1 h/0.1 mol% | 98.6 | This work |
Bromobenzene | Pd/MIL-53-NH2 | EtOH–H2O/40 °C/0.5 h/0.5 mol% | 94 | 35 |
Bromobenzene | Pd-MCM-41 | EtOH–H2O/80 °C/12 h/0.05 mol% | 90 | 36 |
Iodobenzene | Pd/G | EtOH–H2O/60 °C/02–24 h/0.3 mol% | 74 | 37 |
Iodobenzene | Pd/SBA-15 | EtOH–H2O/60 °C/2–24 h/0.3 mol% | 42 | 37 |
4-Bromophenyl acetaldehyde | Pd@p-SiO2 | DMF–H2O/200 °C/3 h/0.003 mol% | 65 | 38 |
Iodobenzene | Pd/CMK-3 | DMF–H2O/150 °C/10 min/0.02 mol% | 99 | 39 |
To standardize the reaction conditions, a series of reactions were performed using several bases, solvents, and different catalyst dosage to obtain the best possible combination. Initially, the experiment was performed using Suzuki–Miyaura cross-coupling reaction of bromobenzene with phenyl boronic acid. As we can see from Table 2, when the reaction was carried out in MeOH, EtOH, DMF and H2O under the same reaction conditions, the products were obtained in poor yields of 38–70% (Table 4, entries 1–4). However, when we adopted the organic/aqueous co-solvent, high yields of 78–98% were obtained (Table 4, entries 5–7). The merit of the co-solvent can be attributed to the good solubility of the organic reactants and the inorganic base, which can accelerate the transmetalation and contributed to fast overall coupling.40 The reaction conditions were also optimized with respect to the base. The reactions were carried out under similar conditions using different bases such as Na2CO3, KOH, NaOH and K2CO3 (Table 4, entries 7–12), it clearly indicated that K2CO3 was the optimal base for the reaction. No product was obtained without base (Table 4, entry13). We can also found that the amount of the catalyst has a great influence on the transformation (Table 4, entries 14–16). When the dosage of the catalyst was above 0.1 mol%, the yield of the product was nearly quantitative (Table 4, entry 14 and 15). And yield of the product was decreased to 77% (Table 3, entry 16) with 0.05 mol% Pd. No product was obtained in the absence of Pd NPs (Table 4, entry 17).
Entry | Solvents | Bases | Pd/mol% | Yield/% |
---|---|---|---|---|
a Reaction conditions: bromobenzene (0.5 mmol), phenylboronic acid (0.75 mmol), base (1.5 mmol), solvents (4 mL), room temperature. | ||||
Solvents effect | ||||
1 | MeOH | K2CO3 | 0.1 | 53 |
2 | EtOH | K2CO3 | 0.1 | 70.2 |
3 | DMF | K2CO3 | 0.1 | 68.1 |
4 | H2O | K2CO3 | 0.1 | 38 |
5 | EtOH/H2O (1![]() ![]() |
K2CO3 | 0.1 | 78.1 |
6 | EtOH/H2O (1![]() ![]() |
K2CO3 | 0.1 | 98.6 |
7 | EtOH/H2O (3![]() ![]() |
K2CO3 | 0.1 | 82.3 |
![]() |
||||
Bases effect | ||||
8 | EtOH/H2O (1![]() ![]() |
NaOH | 0.1 | 72.1 |
9 | EtOH/H2O (1![]() ![]() |
KOH | 0.1 | 78.4 |
10 | EtOH/H2O (1![]() ![]() |
Et3N | 0.1 | 65 |
11 | EtOH/H2O (1![]() ![]() |
Na2CO3 | 0.1 | 89.7 |
12 | EtOH/H2O (1![]() ![]() |
K2CO3 | 0.1 | 98.6 |
13 | EtOH/H2O (1![]() ![]() |
No base | 0.1 | Trace |
![]() |
||||
Pd mol% | ||||
14 | EtOH/H2O (1![]() ![]() |
K2CO3 | 0.15 | 99.5 |
15 | EtOH/H2O (1![]() ![]() |
K2CO3 | 0.1 | 98.6 |
16 | EtOH/H2O (1![]() ![]() |
K2CO3 | 0.05 | 77 |
17 | EtOH/H2O (1![]() ![]() |
K2CO3 | 0 | Trace |
To generalize the application of the Zn-free MOF-5-NPC-900-Pd catalyst, the reaction with a diverse range of arylboronic acids and aryl halides were carried out using 0.1 mol% Zn-free MOF-5-NPC-900-Pd as catalyst at room temperature (Table 5). It was seen that the catalytic system was applicable to various aryl bromides and tolerant to a broad range of functional groups and for most of the substrates, the reaction could be completed in 0.75–1.5 h with high yields, with the substrates having either electron-withdrawing groups (–OH, –COCH3, –CHO) or electron-donating groups (–OCH3, –H, –CH3). It was also found that the yield of reaction para- or meta-substituted aryl bromide is higher than those of ortho-position aryl bromides. To test the feasibility of the aforementioned protocol for challenging substrates, several aryl chlorides with phenylboronic acid were employed and the reaction time was extended to 5 h. And the desired products were obtained in moderate yields (Table 5, entries 13, 14, 15), this just owning to the strength of the C–Cl bond, whose bond dissociation energy was 96 kcal mol−1.41
Entry | X | Y | Z | t/min | Yieldc/% |
---|---|---|---|---|---|
a Reaction conditions: bromobenzene (0.5 mmol), phenyl boronic acid (0.6 mmol), K2CO3 (1.5 mmol), solvent: 2 mL ethanol + 2 mL H2O, catalyst: Zn-free MOF-5-NPC-900-Pd (0.1 mol%), room temperature.b Aryl chlorides (0.5 mmol), phenyl boronic acid (0.6 mmol), K2CO3 (1.5 mmol), solvent: 2 mL ethanol + 2 mL H2O, catalyst: Zn-free MOF-5-NPC-900-Pd (0.5 mol%), 78 °C.c Yield based on column chromatography. | |||||
1 | Br | H | H | 60 | 98.6 |
2 | Br | 4-OCH3 | H | 45 | 93.1 |
3 | Br | 4-OH | H | 45 | 95.4 |
4 | Br | 4-OH | 2-CH3 | 60 | 94.6 |
5 | Br | 2-CH3 | H | 90 | 91.3 |
6 | Br | 4-CH3 | 4-NO2 | 90 | 93.8 |
7 | Br | 4-OCH3 | 4-NO2 | 50 | 91 |
8 | Br | 4-COCH3 | H | 45 | 96.3 |
9 | Br | 4-OH | 3-CH3 | 60 | 96.2 |
10 | Br | 4-CHO | H | 45 | 96.1 |
11 | Br | 4-CHO | 4-NO2 | 50 | 93.8 |
12 | Br | 4-COCH3 | 4-NO2 | 50 | 95.3 |
13b | Cl | H | H | 300 | 74.2 |
14b | Cl | 4-OCH3 | H | 300 | 30.7 |
15b | Cl | 2-CH3 | H | 330 | 25.2 |
The recovery and reusability of the catalyst were performed, using the reaction of bromobenzene with benzeneboronic acid as the representative reactants, which catalyzed by 0.1 mol% of Zn-free MOF-5-NPC-900-Pd. The results demonstrated that Zn-free MOF-5-NPC-900-Pd can be reused 5 times without significant loss of catalytic activity (Fig. 4). The catalyst after 5 cycles was characterized by TEM (Fig. S3†) and XPS (Fig. S4†), which was similar with that of the fresh prepared catalyst. The amount of Pd in the catalyst after five cycles decreased from 4.85% to 4.4%, which might be the reason for the disability of the catalyst.
Footnotes |
† Electronic supplementary information (ESI) available: The nitrogen adsorption–desorption isotherms and element mappings of the catalyst, TEM and XPS images of the catalyst after 5 cycles, 1H NMR data of the products. See DOI: 10.1039/c6ra00378h |
‡ The authors contribute equally to this work. |
This journal is © The Royal Society of Chemistry 2016 |