Zhi-Cheng
Duan
,
Guanghua
Li
,
Ke-Chang
Li
and
Xiao-Bing
Cui
*
College of Chemistry and State Key Laboratory of Inorganic Synthesis and Preparative Chemistry, Jilin University, Changchun, Jilin 130023, P. R. China. E-mail: cuixb@mail.jlu.edu.cn
First published on 14th October 2024
Three novel organic–inorganic polyoxoniobate-based compounds modified with Cu(II) amine complexes were synthesized under hydrothermal conditions with the chemical formulas as follows: K0.5[Cu(enMe)2]4[K0.5SiNb12O40(VO)4.25](OH)1.5·9H2O (1), K0.5[Cu(enMe)2]4[K0.5H2PNb12O40(VO)2]·12.5H2O (2), and K0.5[Cu(enMe)2]4[K0.5H2VNb12O40(VO)2]·12.5H2O (3) (enMe = 1,2-diaminopropane). These compounds were characterized by single crystal X-ray diffraction, infrared spectroscopy (IR), UV-Vis spectroscopy, elemental analysis and powder X-ray diffraction (PXRD) analysis. Notably, while these three compounds exhibit identical cell parameters, they possess distinct stoichiometric compositions and differing polyoxometalate building block structures. Typically, compounds with the same cell parameters are classified as isostructural, sharing identical structures with only minor elemental variations in their compositions. To the best of our knowledge, compounds 1–3 represent the first instances of compounds that share the same cell parameters yet are not isostructural. In this study, we not only synthesized these three compounds and thoroughly examined the differences in their structures and properties, but also investigated their catalytic performances as catalysts for the oxidation of styrene.
In recent years, the chemistry of niobium polyoxoanions has undergone rapid development, and their cluster structure system has become increasingly larger.8 Initially, the synthesis of niobopolyacids was mostly centered around iso-polyoxoniobates (IPONbs), and some building blocks such as {Nb7O22},10 {Nb24O72},11 {Nb32O96},12 {Nb10O28},13 {Nb27O76},14 {Nb47O134},15etc., were constructed. Subsequently, the synthesis of heteropolyniobates (HPONbs) was achieved by modifying niobopolyacids at the atomic level through the introduction of heteroatoms (such as Si, P, V, etc.),16,17 and most of them were focused on the Nb-Keggin-type and capped Nb-Keggin-type derivatives. In 2002, Nyman's group reported the first heteropolyoxoniobate K12[Ti2O2][SiNb12O40]·16H2O.18 Following this, the same group has also reported additional similar Keggin-type HPONbs {TNb12O40}[T = Si, Ge].19 In subsequent studies, heteroatoms were also referenced to As, Te, and S atoms, resulting in the synthesis of {AsNb12},20 {Te2Nb24},21 and [SNb8].22 In the reported capped Nb-Keggin structures, Nb, Sb, Ti, and V atoms are generally introduced as capping atoms. Feng, Hill and others have further reported a variety of capped polyoxoniobates, such as [Nb2O2(H2O)2][SiNb12O40]10−,17 [Ti2O2][GeNb12O40]12−,23 {[Sb2O2][XNb12O40]}n− (X = Si, Ge, V, P, As),24 {VNb12O40(VO)2},25 {PNb12O40(VO)6}26 and so on.
In the context of niobium polyoxometalate synthesis, a number of polyoxoniobates with the same cell parameters and isostructural characteristics have been documented. Notably, In 2012, Nyman's group first introduced third main group elements into heteropolyniobates, and obtained two isostructural examples of poly-niobate anions, specifically [Al/GaNb18O54]15−.27 Subsequently, in 2015, Peng's group reported the synthesis of {[Sb2O2][XNb12O40]}n− (X = Si, Ge, V, P, As),24 which included five isostructural examples of crystals sharing the same cell parameters. However, in the present work, we synthesized three crystals that possess identical cell parameters as examples, and among these, compounds 2 and 3 are confirmed to be isostructural to each other; however, compound 1 shows an unprecedented feature. Although compound 1 shows the same cell parameters as compounds 2 and 3, it is not thoroughly isostructural to those two compounds, but presents significant structural differences between the structures of compounds 2 and 3. To the best of our knowledge, such a difference between similar structures has not been previously reported. The compounds under investigation include K0.5[Cu(enMe)2]4[K0.5SiNb12O40(VO)4.25](OH)1.59H2O (1), K0.5[Cu(enMe)2]4[K0.5H2PNb12O40(VO)2]·12.5H2O (2), and K0.5[Cu(enMe)2]4[K0.5H2VNb12O40(VO)2]·12.5H2O (3) (enMe = 1,2-diaminopropane). The Keggin anion clusters in compounds 1, 2, and 3 are centered on Si, P and V, respectively. The Keggin clusters feature six square windows within the {XNb12O40} (X = Si, P and V) Keggin framework; for {SiNb12O40(VO)4.25} in compound 1, five of the six square windows were capped by four 100% occupied {VO} groups and one 25% occupied {VO} group. With respect to compounds 2 and 3, there are only four half-occupied vanadium atoms capping the four equatorial windows within the Keggin core. Furthermore, we employed compounds 1–3 as catalysts for the catalytic oxidation reaction of olefins and evaluated the catalytic performances of these three compounds for styrene oxidation to styrene oxide. In addition, we also carefully discussed the influence of the subtle difference of the structures on the catalytic efficiencies.
The [SiNb12O40(VO)4.25]7.5− clusters have three types of oxygens, including 16 and 1/4 terminal oxygens (Ot), 24 bridging oxygens (Ob) and four central oxygens (Oc). The lengths of the V–Ot, and V–Ob bonds are 1.57(4)–2.312(16) Å and 1.603(11)–2.127(9) Å, respectively. The lengths of the Nb–Ot, Nb–Oc, and Nb–Ob bonds are 1.753(10)–2.004(7) Å, 1.755(7)–2.450(6) Å, and 1.777(13)–2.413(11) Å, respectively.
In the two-dimensional framework, each [SiNb12O40(VO)4.25]7.5− is connected to four [Cu(enMe)2]2+ segments via the interactions between the copper centre of the complex and the terminal oxygens of the {NbO6} octahedron of the cluster. Subsequently, four neighbouring [Cu(enMe)2]2+ complexes are then connected to a potassium atom via eight K–N bonds with a length of 3.387 Å, resulting in the formation of a windmill shaped unit, where the [Cu(enMe)2]2+ complexes function as blades. Each CuII cation adopts a tetra-coordination, defined by four N atoms from two enMe organic ligands and a terminal oxygen from [SiNb12O40(VO)4.25]7.5−. One pineapple cluster is linked to two windmill units, while a single windmill unit joins four pineapple clusters, therefore, establishing a two-dimensional framework structure (Fig. 1d). It should be noted that the orientations of the four pineapple clusters around the windmill exhibit intriguing characteristics; the four orientations of the four pineapple clusters around one windmill points to the clockwise direction, whereas the four orientations of the four pineapple clusters around the adjacent windmill point to the counterclockwise direction.
Despite differing in their central heteroatoms, compounds 2 and 3 have the same cluster structures and are isostructural to each other but both are not isostructural to compound 1. Here we chose compound 2 as the representative to specify their structure. The [PNb12O40(VO)2] cluster in compound 2 can be described as a modified Keggin unit, wherein one phosphorus atom is the heteroatom centre and four half vanadium atoms cover its four equatorial pits. The Keggin core is consistent with that in compound 1 with the same six square windows; however, there are only four half-vanadium atoms capping the four equatorial windows of the Keggin core, which markedly contrasts with the capped cluster observed in compound 1. The primary capped Keggin structure of compound 1 is thoroughly distinct from those of compounds 2 and 3. Nevertheless, the secondary extended structure of compound 1 closely resembles those of compounds 2 and 3, resulting in the three compounds exhibiting nearly identical cell parameters.
The synthesized compounds 1, 2 and 3 provide compelling examples of compounds with nearly identical secondary structures but different stoichiometric compositions. Consequently, compounds 2 and 3 are isostructural to each other, but the two are not isostructural to compound 1.
There are four and a 0.25 vanadium covering the five pits of the six ones of the Keggin core in compound 1. In contrast, there are only four 0.5 vanadiums capping the four pits of the six ones of the Keggin core in compounds 2 and 3. A notable distinction between the cluster structures of compound 1 and compounds 2 and 3 is that the apical position of the Keggin core in compound 1 is capped by a 0.25 vanadium, whereas the corresponding apical cluster windows of the Keggin core in compounds 2 and 3 remain uncapped. Additionally, the four sites of the equatorial Keggin windows in compound 1 are occupied by four vanadium atoms with an occupancy factor of 1, while the four corresponding sites are occupied by four half-occupied vanadiums in compounds 2 and 3. BVS calculations reveal (Table S2†) that the oxidation states of all the niobium atoms in the three compounds are +5. In contrast, all capped vanadium atoms exhibit a +4 oxidation state, while the central vanadium atom in compound 3 is characterized by a +5 oxidation state.33
The diameter of the capped Keggin core, measured from one terminal oxygen from a capped vanadium to the most distant terminal oxygen from a centre-symmetrically related capped vanadium, is approximately 11.35 Å. In comparison, the distance between the two most distant terminal oxygens from two equatorial niobium atoms within the Keggin core is 10.89 Å, meaning that the capping of the vanadiums on the windows of the Keggin core does not significantly alter the overall shape of the Keggin cluster. Therefore, while the primary structures of compound 1 and compounds 2 and 3 are stoichiometrically different, their secondary structures based on these different primary structures are almost identical; hence the three have almost the same cell parameters but are not isostructural.
Recently, a compound closely resembling compound 1 was reported by Dang's group.32 The primary cluster structure of the Dang's compound exhibits significant similarities to that of compound 1, characterized by the presence of 4.25 vanadium atoms capping the Keggin core. However, it is noteworthy that the sixth cluster window in Dang's compound is not capped by a potassium atom in contrast to compound 1. The bicapped polyoxoniobate was first synthesized (Fig. 2b and c),17,22–25 some years later, tetracapped polyoxoniobate was synthesized (Fig. 2d),20,32 and the hexacapped ones (Fig. 2e) also were synthesized.26 Although the primary building cluster structures of these compounds seem to have close relationship with each other, the secondary structures of these compounds are markedly different, complicating the determination of whether these clusters are intermediates between the Keggin and hexacapped Keggin ones. The synthesis of compounds 1–3 gives solid evidence that both the bicapped and tetracapped (or pentacapped) variants function as intermediates between the Keggin and hexacapped Keggin clusters, as their secondary structures are almost identical despite differences in their primary cluster structures. This means that the cluster differences of these series intermediates will not significantly influence their stacking extended structures. Thus, compounds 2 and 3, along with the Dang's compound32 and compound 1 can be viewed as four intermediates situated between the Keggin core and the hexacapped Keggin core reported by Wang et al. (Fig. 2).26
Fig. 2 (a) Ellipsoid representation of the Keggin cluster; (b) the bicapped Keggin cluster reported by Hu's group;25 (c) the bicapped Keggin cluster in compound 2; (d) the Keggin cluster capped by 4.25 vanadiums in compound 1; and (e) the hexacapped Keggin cluster reported by Wang’ group.26 |
FT-IR spectroscopy is a very powerful analytical technique, and can also be used to discern the subtle structural differences between the three compounds. In the IR spectrum of compound 1, a strong characteristic band at 917 cm−1 is attributed to ν(Si–Oc) frequency, and it should be noted that this particular band only can be observed in the spectrum of compound 1, as the heteroatom of the Keggin core of compound 1 is Si.35 In contrast, the IR spectrum compound 2 reveals a strong band at 1020 cm−1, which can be attributed to the superposition of two overlapping components: one associated with ν(P–Oc) and the other linked to the enMe organic ligands like those in compounds 1 and 3. Therefore, the peak intensity of this band in compound 2 is significantly greater than those observed in compounds 1 and 3. The relative peak intensity ratio of the band at around 1020 cm−1 and the highest peak in the IR spectrum of compound 2 is approximately 1:1.7, whereas the corresponding intensity ratios for compounds 1 and 3 are 1:3.2 and 1:4, respectively, indicating that the band around 1020 cm−1 in compound 2 originates from both the vibrations of P–O bonds and enMe organic ligands.
The IR spectrum of compound 3 displays a peak at 934 cm−1, which is attributed to the presence of vanadium in the +5-oxidation state (V5+), a feature not observed in the spectra of both compounds 1 and 2. This absence can be explained by the fact that only compound 3 incorporates vanadium(V) as the heteroatom in its Keggin core.
The X-ray powder diffractograms of compounds 1–3 agree well with the simulated XRD patterns, thereby confirming the phase purity of all the compounds (Fig. S1†). Variations in reflection intensity may be due to the preferred orientation in the powder samples of these compounds.
The UV-vis spectra of compounds 1–3 are shown in Fig. S2(a–c)† in the wavelength range of 200–500 nm. The UV-vis spectra of compounds 1–3 are more similar. The spectra of these compounds exhibit notable similarities. Specifically, the UV-vis spectra of compounds 1–3 demonstrate a pronounced absorption peak accompanied by a distinct shoulder at approximately 203 nm and 247 nm for compound 1, 204 nm and 245 nm for compound 2, and 204 nm and 250 nm for compound 3. These features are likely attributed to the charge transfer absorption peaks associated with O → Nb in the three compounds.
The oxidation of styrene has long been an important process since styrene oxide has been an important synthetic intermediate in the synthesis of fragrances, epoxy resins, plasticizers, pharmaceuticals, sweeteners and fine chemicals.39 Numerous different research groups from all over the world have devoted themselves to the development of the oxidation of styrene using various different traditional POMs, POM derivatives and composites formed by heterogenizing homogeneous POMs onto diverse solid supports.40–56 Unfortunately, it is noteworthy that the majority of previously reported POM catalysts or POM-based composite catalysts preferentially convert styrene to benzaldehyde rather than styrene oxide.40–56 This preference can be attributed to the mechanism pathway of styrene oxidation, which involves the formation of a styrene oxide as an intermediate, and acidic conditions tend to promote the hydrolysis of styrene oxide, leading to the production of benzaldehyde.57 Given that most traditional POMs are synthesized under acidic conditions or almost all the traditional POMs show strongly acidic properties,58 their use as catalysts for styrene oxidation will inevitably result in the formation of benzaldehyde.40–56
Only a few research studies utilizing such POM catalysts have successfully yielded styrene oxide as the main product; however, these studies typically employed short reaction times, resulting in lower conversions in exchange for higher selectivity towards styrene oxide.59 Consequently, catalytic systems based on traditional POMs are unsuitable for the production of acid sensitive epoxides because epoxide ring-opening occurs under acidic conditions.60 So, finding a suitable POM catalytic system for the production of epoxides is considerably challenging.
However, the PONb POMs, synthesized under strongly alkaline conditions, show much stronger basic properties compared to traditional acidic POMs.7–9 Therefore, the unique basic characteristics of PONbs enable them to inhibit acid-catalyzed epoxide hydrolysis, leading to the production of styrene oxides.57
Based on the aforementioned points, we employed PONbs as catalysts for the catalytic epoxidation of styrene, which provides an environmentally sustainable route for the production of styrene oxide. In this paper, we performed experiments to test the catalytic ability of tert-butyl hydroperoxide (TBHP) aqueous solution as an oxidizing agent and compounds 1–3 as catalysts to oxidize styrene in an intermittent reactor. In a typical run, the catalyst (2 mg), tert-butyl hydroperoxide (274 μL, 2 mmol), styrene as the substrate (114 μL, 1 mmol), and acetonitrile as solvent (2 mL) were transferred to a (5 mL) double-necked round-bottom flask. The mixture was stirred in an oil bath and heated to 40 °C, 60 °C or 80 °C. The content of the mixture was quantified using a gas chromatograph (Shimadzu, GC-8A) equipped with an FID detector and a capillary column (SE-54, 30 m × 0.53 mm × 1.0 μm) and identified by comparison with authentic samples and GC-MS coupling. In addition, the conversion and selectivity of reactions were analysed by gas chromatography and the area normalization method.
In the olefin oxidation reactions we used compound 1 as a catalyst in order to achieve the optimum reaction conditions, and the effects of various factors, including catalyst dosage, solvent type, reaction temperature and other factors, on the catalysis results were systematically explored. Initially, the optimum dosage of the catalyst optimized for this reaction was evaluated (Table 1, entries 2–4). It was observed that increasing the dosage of compound 1 from 1 mg to 2 mg resulted in an enhancement of the conversion rate from 88.4% to 95.2% and an increase in selectivity towards styrene oxide from 14.1% to 57.6%. However, upon further increasing the catalyst dosage to 3 mg, the conversion rate exhibited only a marginal increase to 95.9%, while the selectivity for styrene oxide declined to 37.3%. This indicated that a catalyst dosage of 2.0 mg was a better choice, so we chose 2.0 mg for subsequent experiments. Following this, the type of solvent used for this reaction was optimized. Here, acetonitrile, methanol, ethanol, and n-hexane were selected for their effectiveness (Table 1, entries 3 and 5–7). By screening the solvents, it is clearly observed that acetonitrile as a solvent shows good performance in terms of conversion and selectivity. Therefore, acetonitrile was selected as the solvent for further experiments.
Entry | Catalyst | Solvent | Dosage | Conv. (%) | Sel. (%) | ||
---|---|---|---|---|---|---|---|
So | Bza | Other | |||||
Reaction conditions: TBHP (2 mM, 274 μL), styrene (1 mM, 114 μL), solvent (2 mL), 80 °C, and 8 h reaction time. Bza, benzaldehyde; So, styrene oxide; and others, including benzoic acid and phenylacetaldehyde. | |||||||
1 | Blank | CH3CN | 0 mg | 33.4 | 29.0 | 59.5 | 11.5 |
2 | Compound 1 | CH3CN | 1 mg | 88.4 | 14.1 | 77.7 | 8.2 |
3 | Compound 1 | CH3CN | 2 mg | 95.2 | 57.6 | 36.0 | 6.4 |
4 | Compound 1 | CH3CN | 3 mg | 95.9 | 37.3 | 39.5 | 23.2 |
5 | Compound 1 | MeOH | 2 mg | 28.8 | 95.7 | 4.2 | 0.1 |
6 | Compound 1 | EtOH | 2 mg | 27.8 | 16.7 | 74.0 | 9.3 |
7 | Compound 1 | n-Hexane | 2 mg | 62.9 | 86.2 | 4.6 | 9.2 |
In order to investigate the influence of temperature on the reaction, catalytic experiments were conducted at 40, 60 and 80 °C, respectively. As shown in Table 2, for compound 1, both the conversion and selectivity of styrene oxide exhibited a notable increase, rising from 73% (40 °C) to 95.2% (80 °C) and 31.9% (40 °C) to 57.6% (80 °C), respectively. Therefore, 80 °C was selected as the optimum reaction temperature.
Entry | Temp (°C) | Conv. (%) | Sel. (%) | K (min−1) | ||
---|---|---|---|---|---|---|
So | Bza | Other | ||||
Reaction conditions: catalyst (2 mg), TBHP (2 mM, 274 μL), styrene (1 mM, 114 μL), CH3CN (2 mL), and 8 h reaction time. | ||||||
1 | 40 | 73.0 | 31.9 | 66.7 | 1.4 | 0.00130 |
2 | 60 | 92.9 | 13.0 | 84.7 | 2.3 | 0.00396 |
3 | 80 | 95.2 | 57.6 | 36.0 | 6.4 | 0.00886 |
The kinetic behaviour of the reaction was analysed from the catalysis data obtained during the 1st hour of the reaction at different temperatures of 40, 60 and 80 °C. As can be seen from Fig. 4, compound 1 shows a linear relationship between ln(Ct/C0) and reaction time at 80 °C, 60 °C and 40 °C. Analysis of the results from the figures shows that the catalytic reaction data are consistent with the kinetic characteristics of the first order reaction.
(1) |
(2) |
(3) |
Fig. 4 (a–c) The kinetic profiles of oxidation of styrene catalyzed by compound 1 at 40 °C, 60 °C, and 80 °C; (d) Arrhenius plots of compound 1 according to k at different temperatures. |
The kinetic behaviour of compound 1 as a catalyst can be studied using the Arrhenius equation. In this context, eqn (1)–(3) define Ct, C0, k, and t as the concentration at time t, the initial concentration at the beginning of the reaction, the reaction rate constant, and the reaction time, respectively. According to eqn (1) and (2), the slope of the resulting graph represents the reaction rate constant, allowing for the calculation of the value of k. The observed slopes for compound 1 were 0.0013 min−1 at 40 °C, 0.00396 min−1 at 60 °C and 0.00886 min−1 at 80 °C (Fig. 4a, b and c). Furthermore, the apparent activation energy Ea of the oxidative reaction was calculated to be 44.6 kJ mol−1 according to eqn (3) (Fig. 4d).
Based on the above experimental results, we obtained the optimal reaction conditions as follows: CH3CN (2 mL), catalyst (2 mg), TBHP (2 mmol, 274 μl), styrene (1 mmol, 114 μl), a reaction temperature of 80 °C, and a reaction time of 8 h. The catalytic reactions of compounds 2 and 3 were carried out under the optimum reaction conditions to explore their catalytic activities. As shown in Table 4, the 8 h conversions of compounds 2 and 3 were 94.2% and 92.5%, respectively, and the selectivities for styrene oxides were 58.6% and 76.3%, respectively (Table 4, entries 2 and 3). A comparison of the catalytic data of the three compounds showed that there was little difference in the catalytic oxidation conversion rates of styrene among the three compounds, but the selectivities of the three compounds varied considerably with 58.6% for compound 1, 58.6% for compound 2 and 76.3% for compound 3, respectively. This indicates that the vanadium atom-centered polyoxoniobates are more selective for the catalytic oxidation of styrene compared to those centered on Si and P atoms. The presence of a heteroatom has fatal influence to the acidic property of its parent cluster, and a famous example is that {PW12O40} is more stable than {SiW12O40} under less basic conditions (pH ∼ 1.5 vs. pH ∼ 4.5) and the P heteroatom is more acidic relative to the Si heteroatom.58 Furthermore, since the V heteroatom is more basic than both Si and P heteroatoms, the V-centered cluster is expected to show more basic properties, resulting in a higher selectivity in the production of styrene oxides.60
To explore the catalytic centers, K7HNb6O19, CuCl2, CuCl2 + enMe, and VOSO4 were also introduced as catalysts into the reaction system (Table 3, entries 4–7). The results showed that the conversion of copper salts was greatly improved, reaching 85.4%, but the contribution to the selectivity of styrene oxide was small, which is only 42.2% (Table 3, entry 5). When a mixture of 1,2-diaminopropane physically combined with the copper salts is used as a catalyst, the conversion decreased to 73.4%. This reduction may be due to the site-blocking effect of the ligand (Table 3, entry 6). Comparing the catalytic results of compounds 1–3 with those of copper salts, as well as the physical mixtures of copper salts and ligands, alongside K7HNb6O19 and VOSO4 as catalysts, revealed that the main catalytic centers of compounds 1–3 are both the copper atoms and the capped polyoxometalates. These results suggest that compounds 1–3 effectively combine the advantages of clusters and transition metal complexes into a more efficient catalyst, showing a synergistic interaction for high catalytic efficiency. It should be noted that the three compounds are nearly identical to each other; however, the subtle differences of the three compounds in their structures and their stoichiometric compositions will have fatal impact on their catalytic performance. Compound 1 possesses more capping vanadiums compared to compounds 2 and 3, yet this difference seems to have almost no significant influence on the catalytic performances of the two catalysts. Obviously, both the metal of the metal complexes and the addendum metal of the clusters can act as the catalytic centers of the reaction. Given that the capping vanadium and the addendum niobium atoms belong to the same main group, it is plausible that they exhibit similar catalytic influence on the reaction.61,62 Thus, we propose that the catalytic similarity between vanadium and niobium is a primary factor underlying the comparable catalytic performances of the three compounds.
Entry | Catalysts | Conv. (%) | Product selectivity (mol%) | ||
---|---|---|---|---|---|
So | Bza | Others | |||
Reaction conditions: catalyst (2 mg), for compound 1: 0.654 μmol, TBHP (2 mM, 274 μL), styrene (1 mM, 114 μL), CH3CN (2 mL), 80 °C, and 8 h reaction time. | |||||
1 | Compound 1 | 95.2 | 57.7 | 36.0 | 6.3 |
2 | Compound 2 | 94.2 | 58.6 | 36.2 | 5.2 |
3 | Compound 3 | 92.3 | 76.3 | 18.5 | 5.2 |
4 | K7HNb6O19 (1.6 mg) | 64.5 | 41.5 | 55.7 | 2.8 |
5 | CuCl2 (0.6 mg) | 85.4 | 42.2 | 46.6 | 11.2 |
6 | CuCl2 (0.5 mg) + enMe (10 μL) | 73.4 | 61.9 | 32.9 | 5.2 |
7 | VOSO4 (0.5 mg) | 39.4 | 6.0 | 81.7 | 12.3 |
In addition, thermal filtration experiments were carried out to study the homogeneity or heterogeneity of the catalyst. Compound 1 was selected and subjected to the filtration experiments. After 4 hours, the solution was filtered through a filtration membrane three times to remove the catalyst, after which the filtrate was allowed to proceed with the reaction for another 4 hours. The data showed that the reaction did not stop even without the catalyst within the catalytic system, which means that compound 1 was partially dissolved in the solution (Fig. S3†). The ratio ΔFilt/ΔCat serves as a critical parameter for assessing the reaction system, where ΔFilt is the increment in the conversion after the catalyst is filtered out, and ΔCat is the increment in the unfiltered conversion during the same time interval. ΔFilt/ΔCat ≈ 1 indicates that the catalyst is a homogeneous catalyst. The ΔFilt/ΔCat of compound 1 was 0.80, indicating that the catalytic activity of compound 1 was predominantly based on the homogeneous system.
Compound 1 did not fully dissolve within the reaction system, and subsequently, we explored the cycling stability of compound 1 and performed cycling performance experiments. After each cycling experiment, the solids present in the system were isolated via centrifugation and subsequently washed with acetonitrile. After complete drying at room temperature, the recovered catalyst was utilized in the subsequent catalytic oxidation experiment. As can be seen in Table 4, after four cycles, the reaction conversion slightly decreased from 95.2% to 86.8% and the selectivity for styrene oxide marginally increased. These results indicate that compound 1 exhibited stable catalytic activity over at least 4 cycles. The observed decrease in the conversion may be related to the loss of the catalyst during the cycling process. The infrared (IR) spectra of the catalysts before and after the 4 cycles were compared (Fig. S4†), and it was found that some principal peaks remained unchanged, while some principal peaks disappeared, thereby indicating that a portion of compound 1 had decomposed. The comparison of the XRD spectra of the catalysts was conducted both prior to and following the completion of four cycles. The analysis demonstrates that a portion of compound 1 had lost its crystallinity, confirming the results of its IR spectra.
Entry | Cycle | Conv. (%) | Product selectivity (mol%) | ||
---|---|---|---|---|---|
So | Bza | Others | |||
Reaction conditions: catalyst (2 mg), for compound 1: 0.654 μmol, TBHP (2 mM, 274 μL), styrene (1 mM, 114 μL), CH3CN (2 mL), 80 °C, and 8 h reaction time. | |||||
1 | Fresh | 95.2 | 57.7 | 36.0 | 6.3 |
2 | 1st | 94.0 | 52.7 | 42.0 | 5.3 |
3 | 2nd | 93.6 | 67.8 | 27.2 | 5.0 |
4 | 3rd | 93.0 | 60.9 | 35.5 | 3.6 |
5 | 4th | 86.8 | 62.8 | 32.0 | 5.2 |
Moreover, in light of the excellent catalytic efficacy of compound 1 for the oxidation of styrene, we proceeded towards exploring the general applicability of some other olefinic compounds using them as substrates (Table S3†) with toluene as an internal standard for the reactions. Compound 1 showed high catalytic oxidative conversions of cyclohexene and 1-octene of 95.7% and 90.5%, respectively, while demonstrating a moderate conversion of 76.2% for cyclooctene. However, the oxidation of these substrates resulted in lower selectivities towards the peroxide products of the substrate. Such a phenomenon has already been documented in analogous oxidation of alkenes catalyzed by [ZnWRu2(Zn2W9O34)]11, using tert-butyl hydroperoxide as an oxidant.63
In order to explore the mechanisms of compounds 1, 2 and 3 as catalysts to catalyze the oxidation of styrene, we conducted free radical trapping experiments using compound 1 as a representative example. Under the optimal reaction conditions and systems obtained above, molar carbon radical scavengers, such as CBrCl3 and TEMPO (2,2,6,6-tetramethylpiperidine oxide), and the oxygen radical scavenger Ph2NH (diphenylamine) were added.64 The experimental results, as shown in Table 5, indicate that all three radical traps have inhibitory effects on the reaction. Specifically, the addition of carbon radical traps (CBrCl3 and TEMPO) had limited inhibition effects on the catalytic oxidation reaction, with inhibition rates of 55.6% and 42.4%, respectively. In contrast, Ph2NH had the best inhibition effect on the conversion rate of the reaction, achieving a high inhibition rate of 97.7% (Table 5). Collectively, all the above experimental results indicate that the catalytic oxidation of styrene proceeds through the formation of oxygen radical intermediates.
Entry | Rad. trap | n (rad. trap)/n (styrene) | Conv. (%) | Conv. drop (%) |
---|---|---|---|---|
Reaction conditions: catalyst (0.0055 mM, 1.0 mg), TBHP (2 mM, 274 μL), styrene (1 mM, 114 μL), acetonitrile (2 mL), radical trap (1 mM), 80 °C, and 8 h reaction time. | ||||
1 | — | — | 95.2 | 0 |
2 | CBrCl3 | 1:1 | 42.2 | 55.7 |
3 | TEMPO | 1:1 | 54.8 | 42.4 |
4 | Ph2NH | 1:1 | 2.19 | 97.7 |
In this context, the most important function of Cu(II) is to decompose the stable hydroperoxide and trigger a radical mechanism.65 It has been reported that metal ions can decompose TBHP into tert-butyl peroxyl radicals via a one-electron transfer, where Cu(II) gets reduced to Cu(I) and the electron that is released initiates the radical chain by reacting with TBHP to give tert-butyl peroxyl radicals.66 In the present case, we also believe that the formation of radicals occurs via the reduction of Cu(II) to Cu(I). While we propose that the reduction of Cu(II) to Cu(I) in the catalyst leads to the radical initiation process, we must say that the PONbs, synthesized under strongly alkaline conditions and showing very strong basic properties as mentioned above, are very important to suppress the acid-catalyzed epoxide hydrolysis, thus facilitating the formation of styrene oxides.57 It is widely accepted that hydroperoxo species from polyoxotungstate and polyoxomolybdate are the main catalytic centers for the epoxidation of alkenes using hydrogen peroxide as an oxidant.67 Polyoxovanadate and polyoxoniobate can also both form similar hydroperoxo species just like those formed from polyoxotungstate and polyoxomolybdate.61,62 However, in the catalytic system using TBHP as an oxidant, the formation of peroxo radicals from polyoxovanadate and polyoxoniobate in conjunction with TBHP cannot be ruled out, as this may occur through a similar homolytic activation mechanism analogous to that of copper atoms to form a radical species.68 Based on the aforementioned control experiments and free radical trapping studies, we suggest that perhaps both the copper and vanadium atoms as well as niobium atoms are competitive catalytic centers. Based on the exploration of the catalyst active centres in this study, the following one possible mechanism is proposed69 (Fig. 5). The active metal cation reacts with TBHP to generate a hydroperoxy compound (2), species 2 loses a t-butanol molecule to render species 3, which reacts with the double-bonded carbon atoms of styrene to form a metalloepoxy intermediate (species 4), and then species 4 decomposes to the intermediate product and regenerates the catalyst. The species 5 can be further oxidized to yield benzaldehyde, phenyl acetaldehyde, benzoic acid and so on (Fig. S5†).
Footnote |
† Electronic supplementary information (ESI) available. CCDC 2378667 for compound 1, 2378668 for compound 2, and 2378669 for compound 3. For ESI and crystallographic data in CIF or other electronic format see DOI: https://doi.org/10.1039/d4dt02544j |
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