Lanbo Di*a,
Weijie Xua,
Zhibin Zhana and
Xiuling Zhang*ab
aCollege of Physical Science and Technology, Dalian University, Dalian 116622, P. R. China. E-mail: dilanbo@163.com; xiulz@sina.com; Fax: +86-411-87402712; Tel: +86-411-87402712
bKey Laboratory for Non-traditional & Functional Materials Preparation of Education Department of Liaoning Province, Dalian University, Dalian 116622, P. R. China
First published on 19th August 2015
Supported Pd–Cu alloy nanoparticles have been successfully synthesized via a fast, facile and environmentally friendly method by simultaneous reduction of Pd(NO3)2 and Cu(NO3)2. The catalyst contains Pd–Cu nanoparticles with higher alloying degree, smaller particle size, higher ratio of Pd0, Cu+, and chemisorbed oxygen species, and therefore exhibits enhanced CO oxidation activity.
Compared with conventional methods, cold plasma method is an environmentally friendly and energy efficient method for preparing supported metal catalysts, and has been recently used for preparing supported Pd-based catalysts.14 The supported metal catalysts prepared by cold plasma exhibited smaller size and controllable structure of metal particles, and thereby exhibiting remarkably enhanced activity and properties. In previous studies, we developed a dielectric barrier discharge (DBD) cold plasma technology at atmospheric pressure for synthesizing supported catalysts and found that it is highly efficient for preparing high performance supported Pd catalysts.15 It will be an interesting work if high performance bimetallic catalysts can be fabricated by DBD cold plasma and the relationship between the structure and performance of bimetallic catalysts can be disclosed. However, to the best of our knowledge, no work has been conducted.
In this study, inert alumina supported high performance Pd–Cu alloy nanoparticles were successfully fabricated by the fast, facile and environmentally friendly DBD cold plasma method at atmospheric pressure, and the reasons for the high performance were analyzed.
The wide-angle XRD patterns of Al2O3, Pd/Al2O3–C (C: conventional thermal reduction), Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P (P: plasma reduction) samples are shown in Fig. 1. The Pd peaks at 40.1° and 46.6° for Pd/Al2O3–C sample are assigned to the (111) and (200) planes of face-centered cubic (fcc) structure of metallic Pd (JCPDS card, File no. 46-1043), respectively. Interestingly, from the XRD analysis, we can also see that the diffraction peaks of the Pd–Cu bimetallic nanoparticles in Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P display an fcc structure, which are similar to that of pure metallic Pd nanoparticles. However, the peaks shifted to higher 2theta values without forming any discrete Cu reflections, which indicates that the Pd–Cu nanoparticles are bimetallic alloy rather than a physical mixture of separately nucleated monometallic Pd and Cu nanoparticles.16
XPS spectra of (a) Pd3d, (b) Cu2p and (c) O1s in Pd/Al2O3–C, Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P were collected and shown in Fig. 2. XPS spectra of Pd3d (Fig. 2a) in Pd/Al2O3–C can be fitted with two peaks corresponding to metallic Pd and Pd2+, while a new peak corresponding to Pd4+ can be obtained in the Pd–Cu/Al2O3 samples due to the existence of Cu. From Fig. 2a, we can also see that binding energies (BE) of Pd3d core levels for Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P shift to higher BE. The obvious positively shifts may be ascribed to the strong electronic interaction between Pd and Cu atoms due to the formation of alloy,17,18 leading to downshift in the d-band center of Pd atom in the Pd–Cu/Al2O3 catalysts. This is consistent with the XRD results. Interestingly, the Pd3d core level for Pd–Cu/Al2O3–P shifts to a higher BE than that for Pd–Cu/Al2O3–C, which indicates that Pd–Cu nanoparticles exhibits a higher alloying degree.17,18 As shown in Fig. 2b, XPS spectra of Cu2p can be deconvoluted into three peaks at 932.4 eV, 932.5 eV and 934.1 eV, attributed to Cu0, Cu+19 and Cu2+.12 The compositions of Pd and Cu in the samples are summarized in Table 1. Pd predominantly exists in low oxidation state (Pd0 and Pd2+) and Cu in high oxidation states (Cu+ and Cu2+) for Pd–Cu/Al2O3–P.
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| Fig. 2 XPS spectra of (a) Pd3d, (b) O1s and (c) Cu2p in Al2O3, Pd/Al2O3–C, Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P. | ||
| Catalysts | DPd (nm) | The composition of Pd (%) | The composition of Cu (%) | Ochem (%) | T100 (oC) | Ea (kJ mol−1) | TOF155 °C × 103 (s−1) | ||||
|---|---|---|---|---|---|---|---|---|---|---|---|
| Pd0 | Pd2+ | Pd4+ | Cu0 | Cu+ | Cu2+ | ||||||
| Pd/Al2O3–C | 10.0 ± 3.2 | 79.7 | 20.3 | 0 | — | — | — | 9.8 | 175 | 211.3 ± 3.8 | 59.7 |
| Pd–Cu/Al2O3–C | 6.2 ± 1.5 | 54.5 | 28.3 | 17.2 | 16.9 | 16.9 | 66.2 | 11.6 | 160 | 170.3 ± 5.5 | 136.6 |
| Pd–Cu/Al2O3–P | 4.3 ± 0.9 | 56.9 | 29.9 | 13.2 | 10.0 | 22.1 | 67.9 | 31.1 | 155 | 119.3 ± 6.5 | 408.2 |
Fig. 2c presents the O1s spectra. For all samples, O1s spectra can be deconvoluted into three peaks at 530.4, 531.5 and 532.6 eV, ascribed to chemisorbed oxygen species,20 Al–O21 and OH,22 respectively. The ratios of chemisorbed oxygen species in O1s for the samples were also summarized in Table 1. More chemisorbed oxygen species are formed on the Al2O3 support for Pd–Cu/Al2O3–P than Pd/Al2O3–C and Pd–Cu/Al2O3–C. This is in line with the results of our previous work,15b which may be ascribed to the fact that the plasma reduction was a low-temperature and fast process (6 min).
For getting more insight into the metal–metal interaction, TPR profiles of the samples were characterized and illustrated in Fig. 3. Negative and positive peaks at around 70 and 470 °C in Pd/Al2O3–C correspond to desorption from surface metallic Pd of the H2 adsorbed at room temperature at the beginning of the analysis,23 and the reduction of the surface interacted PdO species,24 respectively. However, these peaks disappear and a positive peak is observed in Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P at around 200 °C, ascribed to the reduction of Pd and Cu from the mixed oxide (PdxCuyO) due to the formation of Pd–Cu alloy,25 and the reduction of chemisorbed oxygen species, respectively.26,27 Furthermore, the positive peak at around 200 °C for Pd–Cu/Al2O3–P is more broader than that for Pd/Al2O3–C and Pd–Cu/Al2O3–C due to the more chemisorbed oxygen species. These are consistent with the results of XRD and XPS.
Fig. 4 shows the TEM and HRTEM images of the samples, and the corresponding histograms of size distribution of the Pd nanoparticles. The average diameter of the Pd nanoparticles (Dmean) and the standard deviation (STD) were obtained by analyzing numerous TEM images. Pd nanoparticles are 10.0 ± 3.2, 6.2 ± 1.5 and 4.3 ± 0.9 nm, in diameter for Pd/Al2O3–C, Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P, respectively. The smaller size of the bimetallic Pd–Cu nanoparticles was attributed to the formation of high-melting-point Pd–Cu alloy.28 In addition, the size of Pd–Cu nanoparticles in Pd–Cu/Al2O3–P is smaller than that for Pd–Cu/Al2O3–C due to the low-temperature and fast reduction process. These are consistent with the results of XRD. The insert figures in Fig. 4 show high-resolution TEM (HRTEM) images of two individual particles in Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P, with spots in the Fourier transformed images at 0.22 nm, which is characteristic of a Pd–Cu alloy.29
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| Fig. 4 TEM images of (a) Pd/Al2O3–C, (b) Pd–Cu/Al2O3–C and (c) Pd–Cu/Al2O3–P, HRTEM images (given as insert), and the corresponding histograms of size distribution of the Pd nanoparticles. | ||
Fig. 5 presents the CO oxidation activity over Pd-based catalysts in the temperature range of 20–200 °C. Under the reaction conditions, the CO conversion increases gradually with the increase in temperature, and a sharp increase can be observed for the Pd catalysts when the temperature is close to T100 (100% CO conversion). T100 were achieved at 175 °C, 160 °C and 155 °C, respectively, over Pd/Al2O3–C, Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P.
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| Fig. 5 (a) Results of CO conversion over Al2O3, Pd/Al2O3–C, Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P, and (b) the corresponding apparent activation energies (Ea) and turnover frequencies (TOF) at 155 °C. | ||
Obviously, Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P exhibit enhanced CO oxidation activity with the addition of copper.
According to the data taken from Fig. 5a, the Arrhenius plots are shown in Fig. S2,† and good linear relationships are observed. The apparent activation energies (Ea) for Pd/Al2O3–C, Pd–Cu/Al2O3–C and Pd–Cu/Al2O3–P, which could be obtained from the slopes of the plots, were 211.3 ± 3.8, 170.3 ± 5.5 and 119.3 ± 6.5 kJ mol−1, respectively. To get insight into the intrinsic activities of the supported Pd catalysts, the turnover frequencies (TOF) normalized as the number of CO molecules reacting per active site per second were also calculated. The apparent activation energies (Ea) and turnover frequencies (TOF) at 155 °C of the samples are presented in Table 1.
The activation energy has been decreased with the addition of copper, and TOF of Pd–Cu/Al2O3–P and Pd–Cu/Al2O3–C for CO oxidation are about 6.8 times and 2.3 times as that of Pd/Al2O3–C, respectively. Low CO oxidation activity for monometallic Pd catalysts (Pd/Al2O3–C) was attributed to the fact that CO adsorption on the Pd surface is too strong, the active sites for oxygen adsorption and activation are blocked, namely, CO poison effect.30 Previous studies have shown that Cu can strongly modify the valence state of Pd by injecting charge into the sp sub-band.12 This electronic modification means that Pd–Cu alloys may facilitate CO dissociation relative to Pd by converting the nature of the CO interaction with Pd surface centers from covalent to a mixture with an ionic component. In addition, after injecting charge into the sp sub-band of Pd, active Cu+ ions will be formed, which may adsorb and activate oxygen.31
Interestingly, TOF of Pd–Cu/Al2O3–P is about 3.0 times as that of Pd–Cu/Al2O3–C, ascribed to the higher alloying degree (Fig. 2a), and smaller particle size of Pd–Cu nanoparticles (Fig. 4). The previous d-band center theory indicated that a change in the adsorbate chemisorption energy scales directly with the change in the metal center of the d-band: lowering of the d-band center (Fig. 2) results in the decrease in interaction strength of the various adsorbates to the substrate.17,18 In other words, CO adsorption on the Pd surface for Pd–Cu/Al2O3–P with higher alloying degree of Pd atom (Fig. 2a) will be not so strong as that for Pd–Cu/Al2O3–C. Consequently, there will be more active sites for oxygen adsorption on the Pd surface for Pd–Cu/Al2O3–P.
Furthermore, the valence states of Pd and Cu also play an important role in CO oxidation. The ratios of metallic Pd and Cu+ in Pd–Cu/Al2O3–P are 2.4% and 5.3% higher than that in Pd–Cu/Al2O3–C, respectively. Metallic Pd exhibits higher activity than that of PdO and PdO2, which are stable against reduction by CO.30 As for the valence states of copper, the propensity of Cu+ toward valence variations and thus its ability to seize or release surface lattice oxygen more readily enable Cu+ to exhibit higher activity than Cu0 and Cu2+.31 Finally, the ratios of chemisorbed oxygen species in Pd–Cu/Al2O3–P (31.1%) are much higher than that in Pd–Cu/Al2O3–C (11.6%). Chemisorbed oxygen species were thought to be liable to react with CO and may play an important role in CO oxidation.27 For these reasons, Pd–Cu/Al2O3–P shows higher CO oxidation activity than Pd–Cu/Al2O3–C.
In summary, we have reported a fast, facile and environmentally friendly method for synthesizing high performance supported Pd–Cu alloying nanoparticles on Al2O3 support. TOF of Pd–Cu/Al2O3–P for CO oxidation is about 3.0 times as that of Pd–Cu/Al2O3–C. This method can be regarded as a general approach for synthesizing other high performance supported bimetallic catalysts.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c5ra13813b |
| This journal is © The Royal Society of Chemistry 2015 |