The selective oxidation of alcohols to the corresponding carbonyl compounds is an important functional group transformation in organic synthesis     . Noble metals, especially Pd as the active components of heterogeneous catalysts, have been extensively investigated in recent years due to their effective catalytic abilities for the functional group transformation as good as their homogeneous counterparts     .
Among heterogeneous Pd catalysts, Pd catalysts supported on carbon materials such as Pd/XC-72 and Pd/graphite have been widely used for oxidation in the field of fine chemicals  . They have been proven to have many advantages as high efficiency catalysts due to their specific properties, such as acid and base resistance, porosity, and the possibility of recovering the metals by combustion of the supports     . Hence, preparation of supported Pd catalyst with small Pd size and high catalytic activity is always an interesting topic. Previous research findings showed that sizes and morphology, and thus properties of heterogeneous Pd catalysts synthesized in solution, were influenced by Pd precursors  , reaction temperature  and synthetic methods of catalysts      . Especially, an appropriate choice of the solvents as reducing agent is important in controlling the Pd particle size, because the reduction rate of [PdCl4]2− to Pd0 is greatly affected by the kind and the concentration of the reducing agent. Alba et al.  mentioned that glycerol as solvent and reducing agent for metal nanoparticles formation is clearly more convenient because of its lower cost and toxicity. Wool folk et al.  recently found that the NiWS catalyst activity could be improved upon the election of the solvents with different polar properties. However, the research about effects of alcohols as solvents on Pd/C catalysts for solvent-free selective oxidation of benzyl alcohol is scare.
Therefore, the objective of this study is to compare the effect of solvents with different numbers of hydroxyl groups used for catalyst preparation on the properties of Pd/XC-72 catalysts, in particular on the catalytic activity and selectivity for solvent-free selective oxidation of benzyl alcohol. Eventually, among the three solvents studied, i.e., ethanol, ethylene glycol and glycerine, the most appropriate solvent would be determined. It is expected that this research may be of significance to synthesize Pd nanocatalysts with an appropriate solvent to improve their physicochemical properties and catalytic activities in solvent-free selective oxidation of alcohols with molecular oxygen.
Palladium chloride (PdCl2) was purchased from E. Merck AG Darmstadt. Other chemicals, including XC-72, ethanol (C2H6O, EA), ethylene glycol (C2H6O2, EG), glycerine (C3H8O3, GI) and sodium hydroxide (NaOH), were purchased from the China National Pharmaceutical Group Corp. All the chemicals were analytical grade and used without further purification. Double distilled water (DD water) was used throughout the experiments.
2.2. Catalyst Preparation
Synthesis of Pd/XC-72 catalysts with different solvents can be described as follows: an aqueous solution of PdCl2 (2 mg∙mL−1, 2 mL) was added in 25 mL of solvent. The pH of the system was adjusted to ca.11 by adding dropwise an 8 wt% NaOH-solvent solution under vigorous stirring for 30 min. Subsequently, 200 mg of pristine Vulcan XC-72 (Cabot Corporation 200.6 m2∙g−1) were added, and the solution was ultrasonicated and stirred for 2 h to obtain a homogeneous suspension. Upon completion, the suspension was transferred into a 50 mL Teflon-lined stainless-steel autoclave. The autoclave was sealed, heated at 403 K for 3 h, and air-cooled to room temperature. Then, the product was collected by filtration and washed several times with doubly distilled water. Finally, the obtained solid was dried at 313 K under vacuum for 8 h. According to the solvents used, the samples were respectively named: Pd/XC-72(EA), Pd/XC-72(EG) and Pd/XC-72(GI).
TEM (Transmission Electron Microscope) images were obtained using a JEOL JEM-2100 operated at 200 kV. The samples were suspended in ethanol and dispersed on a holey carbon-coated Cu gird. The XRD (X-ray Diffraction) patterns were recorded on a Bruker D8 Advance diffractometer under ambient conditions using filtered Cu-Κα radiation (λ = 0.15406 nm) operated at 40 kV and 40 mA, and a scanning rate of 0.051 s−1 was applied to collect diffraction data from 15˚ to 90˚. The TGA (Thermal Gravity Analysis) were performed on an EXSTAR TG/DTA 6300 system at a heating rate of 10˚ min−1 from 293 K to 1173 K. The compositions of the Pd/XC-72 catalysts were evaluated by ICP-MS (Inductively Coupled Plasma-Mass Spectrometry) analysis after the sample was dissolved in a nitrohydrochloric acid solution. Multipoint nitrogen adsorption-desorption experiments were carried out by means of an automatic Micromeritics ASAP 2020 analyzer using the Brunauer-Emmett-Teller (BET) gas adsorption method.
2.4. Alcohol Catalytic Oxidation
The catalytic oxidation of benzyl alcohol was carried out using the following procedures. 0.1 g catalyst was added into the alcohol, and the mixture was then heated to the reaction temperature with vigorous stirring. Then an O2 gas flow was bubbled into the mixture to start the reaction. After the reaction, the solid catalyst was filtered off and the liquid products were analyzed after the addition of an internal standard by an Agilent gas chromatograph (GC) 6890 equipped with a flame ionization detector and a DB-5 capillary column (30 m long and 0.25 mm in diameter).
3. Results and Discussion
In the current study, the structure and crystallographic planes of the catalysts were analyzed by XRD. Figure 1 shows the XRD patterns of the as-prepared catalysts. All samples show three peaks at 2θ = 40.1˚, 46.7˚, and 68.1˚, which can be assigned to (111), (200) and (220) planes of face-centered-cubic Pd (JCPDS card no: 46-1043), respectively. We noted that the Pd (111) reflection of Pd/XC-72(GI)
Figure 1. XRD patterns of (a) Pd/XC-72(EA); (b) Pd/XC-72(EG) and (c) Pd/XC-72(GI). The upright black lines represent respective standard peaks (JCPDS card no: 46-1043).
(curve c) showed broader and weaker diffraction than that of Pd/XC-72(EA) (curve a) and Pd/XC-72(EG) (curve b), which suggested that smaller Pd nanoparticles are prepared in a highly dispersed state with the addition of glycerine. This statement can be supported by the data extracted from XRD analysis in Table 1. We know that Scherrer’s equation that relies on the FWHM (full width at half maximum) of the diffraction peaks can be helpful in gaining an estimation of the nanoparticle size. So, the calculation results according to Scherrer’s equation generally indicate that Pd nanoparticles of Pd/XC-72(GI) has the smallest particle size, which have similar results to that obtained from the TEM images (Figure 2).
Figure 2 shows the typical TEM images of Pd/XC-72 samples fabricated using different solvents. The corresponding particle size distributions derived from the TEM micrographs by counting ca. 100 particles are also shown in Figure 2. Figure 2(a) displays the TEM image of Pd/XC-72(EA). It can be found that the Pd nanoparticles of Pd/XC-72(EA) were big and aggregated in certain regions of the support. Moreover, the large and irregular particles with the average size of 13.2 nm were obtained in the presence of EA (Figure 2(b)). Figure 2(c) shows the TEM image of Pd/XC-72(EG). It shows that Pd nanoparticles with the average diameter of about 7.6 nm (shown in Figure 2(d)) were not evenly dispersed on the entire surface of XC-72. For the catalyst Pd/XC-72(GI) (Figure 2(e)), small Pd nanoparticles with the average size of 4.9 nm (see Figure 2(f)) were uniformly dispersed on the surface of the XC-72 support in the presence of glycerine. These results indicate that the size and dispersion of Pd nanoparticles on XC-72 can indeed affected by the solvents when using the same Pd precursor under the identical preparation condition. From the viewpoint of the kind of alcohol, the particle size become smaller in the order of ethanol > ethylene glycol > glycerine; this tendency corresponds to their increasing boiling points. Thus, it is suggested
Table 1. Structural data extracted from XRD analysis.
Figure 2. TEM images and particle size distributions of (a); (b) Pd/XC-72(EA); (c) (d) Pd/XC-72(EG); and (e) (f) Pd/XC-72(GI).
that the reduction of [PdCl4]2− by the alcohol with higher boiling point produces more Pd nuclei in a shorter period and suppresses the growth of Pd nanoparticles, that is, a faster reduction rate of [PdCl4]2− is needed to generate the smaller Pd nanoparticles with narrower distribution  .
All samples were characterized by TGA under a N2 atmosphere (Figure 3) to demonstrate whether the catalysts contained residual solvents. As shown in curve a, there is no significant mass loss in XC-72 from 293 K to 1173 K, suggesting that there are nearly no other additives on the XC-72 support. However, a mass loss of about 1.2% (curve b), 3.7% (curve c), and 4.3% (curve d), can be respectively observed in Pd/XC-72(EA), Pd/XC-72(EG) and Pd/XC-72(GI) from 293 K to 1173 K. According to the solvents boiling points, it can be presumed that the mass loss may be attributed to the decomposition of residual solvents (293 K to 563 K) and traces of inorganic salts (563 K to 1173 K).
The BET surface areas of the Pd-based catalysts together with pure Vulcan XC-72 are summarized in Table 2. Compared with Vulcan XC-72, the surface area of all the catalysts obviously decreased, which might be attributed to the deposition of Pd nanoparticles on the outer surface of the support fills the pores of the XC-72.
Figure 3. TGA curves of (a) XC-72; (b) Pd/XC-72(EA); (c) Pd/XC-72(EG); and (d) Pd/XC-72(GI). All the experiments were conducted under a N2 atmosphere.
Table 2. BET surface areas for different catalysts.
The change of BET surface area of Pd/XC-72(EA) is not significant probably because of its low Pd loading and large Pd particle size. For the Pd/XC-72(GI) catalyst, its BET surface area significantly dropped from 200.6 m2∙g−1 to 101.7 m2∙g−1. This result can be due to two reasons: 1) the pores in the XC-72 are partially filled by the small Pd nanoparticles with the average size of 4.9 nm; 2) the solvent glycerine may affect the surface properties of the support and probably fill its pore of Vulcan XC-72. The adsorption and desorption of reactants and products respectively, and the diffusion process will influence the catalytic properties. Consequently, the surface area and pore volume significantly affect catalytic properties  .
The catalytic performance of different Pd/XC-72 catalysts was investigated and the results are shown in Table 3. Irrespective of the different solvents, all the catalysts show rather high selectivity to benzaldehyde (99%). However, the catalytic activities are influenced by using different solvents during catalysts preparation. For the Pd/XC-72(EA), only about 20.7% of benzyl alcohol conversion was obtained, and it had the lowest TOF value (368 h−1). A higher TOF value (566 h−1) could be achieved over Pd/XC-72(EG). The Pd/XC-72(GI) catalyst showed the highest conversion of benzyl alcohol (almost 90 %) and TOF value (796 h−1). It is reported that smaller Pd particles with high dispersion containing more coordinately unsaturated Pd sites are generally believed to be more active for many
Table 3. Physico-chemical and catalytic properties of the Pd/XC-72 catalystsa.
a: Reaction conditions: catalyst = 0.1 g; benzyl alcohol = 5 mL; O2 flow rate = 20 mL∙min−1; T = 403 K; reaction time = 3 h. b: Atomic ratios of Pd to Cu determined by ICP-MS. c: Average particle sizes estimated by TEM images. d: TOF = turn-over frequency.
Pd catalyzed organic reactions  . For the aerobic oxidation of alcohols over palladium-based catalyst, the particle size of palladium is also a key factor to influence its catalytic activity. Wang et al.  studied the palladium catalyst with tunable size in a range of 2 - 5 nm possess good catalytic activities for the oxidation of alcohols. Therefore, the good catalytic performance of Pd/XC-72(GI) for the oxidation of alcohol can be attributed to the small size and the good dispersion on the support.
To better understand the formation of Pd/XC-72 catalysts, a possible mechanism was presented for the preparation of Pd nanoparticles supported on XC-72 by the facile solvothermal method in Scheme 1. Firstly, three different kinds of alcohols, as both solvents and mild reducing agents, were mixed with Pd2+ respectively. Subsequently, these Pd2+ ions were reduced by alcohols during the solvothermal reaction to form Pd nanoparticles. Based on the TEM data, one can draw a conclusion that the synthesis of highly stable small monodisperse populations of palladium nanoparticles with 4.9 nm in size was achieved via glycerine. Because the reduction of [PdCl4]2− by the alcohol with higher boiling point produces more Pd nuclei in a shorter period and suppresses the growth of Pd nanoparticles. Moreover, according to the results of TGA and ICP-MS, the final molar ratio of Pd nanoparticles and residual solvent in the respective Pd/XC-72 catalysts is the same. Therefore, glycerine molecules with three hydroxyl groups and high boiling point might be beneficial to stabilize the palladium nanoparticles over a long period, prompting the formation of small Pd nanoparticles with good dispersion and fine homogeneity.
A series of Pd/XC-72 catalysts were synthesized by a one-step solvothermal method using different solvents including ethanol, ethylene glycol, and glycerine. Catalysts were evaluated by solvent-free selective oxidation of benzyl alcohol at 403 K, and showed different catalytic activities. Among three catalysts, Pd/XC-72 (GI) with good dispersion and small Pd nanoparticles size has highly efficient in the solvent-free oxidation of benzyl alcohol with molecular oxygen. It is considered that the solvents, which are applied to dissolve Pd precursors, remarkably influence the interaction between the Pd nanoparticles and the supports. Meanwhile, the groups from solvents may prohibit the sintering of supported Pd during the
Scheme 1. Possible formation mechanisms of the as-prepared Pd/XC-72 catalysts.
catalyst synthesis process, which can influence the size, shape and dispersity of Pd nanoparticles. These results may improve our understanding of solvent effects during the preparation of Pd-based catalysts, and help us explore new ways in practical demands in many industries and labs as well as academic research interesting for design Pd-based nanocatalysts with increased effectiveness and relatively low cost.
This work was financially supported by the Doctoral Scientific Research Foundation of Henan Normal University (5101039170128), the National Science Foundation of China (grant no. 21171051), the National Science Foundation of China (grant no. 21271066); and the NFSC―Henan Talent Training United Fund (grant no. U1204519).
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