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Article

Effects of Preparation Methods of Pd Supported on (001) Crystal Facets Exposed TiO2 Nanosheets for Toluene Catalytic Combustion

by
Guiyun Yu
1,*,
Chengyan Ge
1,2 and
Haiqin Wan
2,*
1
School of Chemistry and Chemical Engineering, Yancheng Institute of Technology, Yancheng 224000, China
2
Laboratory of Vehicle Emissions Control, School of the Environment, Jiangsu Key Nanjing University, Nanjing 210093, China
*
Authors to whom correspondence should be addressed.
Catalysts 2022, 12(11), 1406; https://doi.org/10.3390/catal12111406
Submission received: 17 September 2022 / Revised: 24 October 2022 / Accepted: 7 November 2022 / Published: 10 November 2022
(This article belongs to the Special Issue Advanced Nanostructured Materials for Modern Catalysis Applications)
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Abstract

:
A series of TiO2 nanosheets-supported Pd catalysts were individually prepared by impregnation, deposition–precipitation, photo-deposition and in situ reduction by NaBH4. For comparison, Pd supported on P25 was prepared by the impregnation method. The experimental results show that the catalytic efficiency of the catalyst prepared with titanium dioxide nano sheet as the support is higher than that of the catalyst supported with P25. Its excellent properties are as follows: The resulting sample indicates that TiO2 nanosheets-supported Pd catalyst display an improved activity than Pd/P25, whose temperature of 100% complete conversion of toluene decreased by 40 ℃ at the most. The Pd particles on the catalyst synthesized by the light deposition method and the NaBH4 reduction method are more obvious, while the Pd particles on the catalyst synthesized by the immersion method and the deposition–precipitation method are less obvious, which shows that the latter two methods are more conducive to the dispersion of Pd. The good catalytic activity may be due to the better exposed mirror and dispersion of titanium dioxide nanosheets. This is mainly related to the exposed crystal plane of the nanosheet TiO2 (001), which made it easier to form the oxygen vacancy. Moreover, among all of the TiO2 nanosheets-supported Pd catalysts, Pd/TiO2 NS (TiO2 NS means TiO2 nanosheets) prepared by the impregnation method show the highest catalytic activity. The XRD results show that Pd prepared by impregnation is more dispersed and smaller. This is due to PdO being dispersed more efficiently than the others, leading to more Pd active sites.

1. Introduction

Catalytic combustion is a high-efficiency controlling treatment for removing volatile organic compounds (VOCs), and the key issue is to design a suitable catalyst. Considering the crucial role of the support in a catalyst, the interaction between the carrier and the active substance affects its catalytic performance and the oxidation mode of the active species. In particular, these interactions may provide active sites for oxidizing VOCs. For example, CeO2, Nb2O5, La2O3, TiO2, etc., are conducive to the regulation of Pd to PdO [1,2,3,4]. Therefore, the form of the carrier and the preparation method of the catalysis are important ways to influence the catalytic performance of the catalyst. The TiO2 material was widely developed and used in the fields of thermal catalysis and photocatalysis owing to its unique properties, certain acid center, adjustable crystal shape and appropriate band gap width [5,6,7,8,9]. The interaction between the metal and the support was observed in TiO2-based catalyst toward the oxidation of the VOCs. Li et al. [10] prepared Ag @ Pd/TiO2 catalyst. Compared with Pd/TiO2, the Pd content (0.2%) was only about one-third of the Pd/TiO2, but showed higher toluene catalytic oxidation activity; T50 (T50: temperature for 50% conversion) was about 203 °C. Hosseini et al. [11] discussed the role of mesoporous TiO2 in the removal of toluene, and they found that 0.5% Pd-1% Au/TiO2 was an optimal catalyst, T50 was 219 °C, and the presence of highly porous structures was a crucial factor. Additionally, the existence of a strong interaction between TiO2 and Pd-Au played a vital role in improving the catalytic performance.
The crystal structure and exposed crystal facets of the support are the most important structural parameters affecting the metal–support interaction and its photocatalytic performance [12]. Sun et al. constructed the Pt-TiO2 film with exposed {0 0 1} facets and showed profoundly higher UV-light-driven photocatalytic activity and stability than that of pure TiO2 film with exposed {001} facets due to the synergistic effects of exposed {0 0 1} facets and the interaction between the two components [13]. Liu et al. [14] investigated the crystal-plane effect on the CO oxidation properties over the Au/TiO2 catalyst, showing the order of the catalytic activities as follows: Au/TiO2−{100} > Au/TiO2−{101} > Au/TiO2−{001}. Chen et al. [15] studied the morphology effect of an Au-TiO2 sample for C3H6 epoxidation with H2 and O2. There were strong interactions between Au nanoparticles and TiO2 supporters. The Auδ− and Auδ+ species exhibited the largest amount of Au/TiO2{0 0 1} and Au/TiO2{100}, respectively, leading to different catalytic activity and selectivity. It demonstrated that morphological engineering could act as an effective approach to optimize the catalytic performance and thus deeply understand the catalytic mechanism of oxides. The {101} crystal surface of anatase TiO2 is the most stable in thermodynamics, while the {001} crystal surface is the most active.
Since 2008, when anatase TiO2 dominated by a crystal surface of {001} was prepared by Yang et al., much attention has been focused on it, including morphology control, stable exposure of {001} crystal plane by HF and its application [16,17]. In addition to its highly photocatalytic performance [18,19,20], Deng et al. [21] also found that TiO2 NS dominated by the {001} crystal surface had higher catalytic properties than TiO2 nanoparticles in the NH3-SCR reaction for the catalyst MnOx/TiO2.
Therefore, a simple oxide with a clear crystal plane exposure as support is very useful for understanding the metal–support interaction.
In addition, three impregnation methods, including wet impregnation, stepwise impregnation and co-impregnation, were widely used to construct M/TiO2 samples, and wet impregnation attracted increasing attention in the view of practical operation. For example, Araya et al. adopted the co-impregnation method to investigate the effect of different supports (Al2O3, ZrO2 and SiO2) [22]. Yuan et al. prepared a series of Pt/TiO2 catalysts using NaBH4 as a reduction agent. The effects of loading amount of Pt and exposed crystal planes of TiO2 on the physical and chemical properties, and the catalytic performance in HCHO oxidation reaction were investigated [16]. The status of the metal component is related to the preparation methods. The surface configuration of as-synthesized catalysts could be regulated by various synthesis parameters, such as heating temperature, deposition amount, loading method or the impregnation order [23,24,25]. Su et al. revealed that the catalytic performance of NO reduction over Fe-Ag/Al2O3, including its selectivity and catalytic activity, was affected by the preparation method [26]. Furthermore, our group successfully synthesized CuO-CeO2/γ-Al2O3 and FeOx-CeO2/γ-Al2O3 catalysts, indicating that the impregnation order determined their dispersion state and catalytic activity [23,27].
The Pd-based catalysts are a common catalyst for VOCs’ combustion. The status of Pd and the metal–support interaction are two key issues for exploring the catalytic mechanism. In this study, Pd/TiO2 NS was selected as the model catalyst to study the effect of the preparation method on the catalytic activity of toluene. The metal–support interaction was investigated by tuning the prepared methods to obtain different Pd species. The main focuses were: (1) Ti(OC4H9)4 was used as the titanium source and HF as the etching agent to synthesize TiO2 nanosheets exposed {001} by the hydrothermal method; (2) TiO2 NS was used as the support to prepare the Pd/TiO2 NS catalyst different ways (the impregnation method, the deposition–precipitation method, the photo-deposition method, the NaBH4 reduction method), and the influence of the preparation method on the catalytic activity of toluene was studied; (3) The metal–support interaction of these catalysts was analyzed by the characterization techniques of BET, TEM, XRD, XPS and H2-TPR.

2. Results and Discussion

2.1. Catalytic Performance of Toluene Oxidation

The light-off curves of the catalytic combustion of toluene over the Pd/TiO2 catalysts are shown in Figure 1. Two results are observable in the figure. Firstly, the catalyst prepared by the immersion method had the highest catalytic activity when the temperature ranged from 170 to 210 °C. The temperature of the toluene complete conversion decreased by 40 °C at most (from 250 °C by Pd/TiO2 P25-IM to 210 °C by Pd/TiO2 NS-IM). This was due to the unique property of TiO2 NS. Some similar results were previously reported [28,29]. Secondly, the light-off curves of Pd/TiO2 NS were complicated. Among these results, Pd/TiO2 NS-IM showed the highest catalytic performance; 100% conversion of toluene was achieved at 210 °C. For Pd/TiO2 NS-DP and Pd/TiO2 NS-PD, their light-off curves were similar with that of Pd/TiO2 P25 before 210 °C, and Pd/TiO2 NS-DP reached 100% conversion at 230 °C while Pd/TiO2 NS-PD and Pd/TiO2 P25 were reached at 250 °C. For Pd/TiO2 NS-NaBH4, its activity was higher than Pd/TiO2-NS-DP before 210 °C, but its catalytic rate decreased thereafter and it reached the toluene 100% conversion at 270 °C. This result indicated that the status and metal–support interaction of Pd are different on each Pd/TiO2 NS catalyst, which was related to its catalytic performance. To understand the detailed reasons, the physicochemical properties of these Pd/TiO2 NS catalysts were analyzed.

2.2. BET and TEM Analysis

As displayed in Table 1, the specific surface area values of Pd/TiO2 catalysts prepared by the deposition–precipitation, photo-deposition, NaBH4 reduction and impregnation methods are 80 m2/g, 77 m2/g, 74 m2/g and 52 m2/g, respectively, which are all lower than that of TiO2 nanometer sheets (92 m2/g). At the same time, we also provided the pore size and pore volume of the samples, which should be stacking holes. It was observed that the pore volume of the catalyst decreased after Pd loading. The large specific surface area of the catalysts provided more active sites, resulting in the enhanced catalytic activity over TiO2 NS as compared with P25. After Pd loading onto TiO2 NS, the specific surface area values of all Pd/TiO2 catalysts were decreased with the lowest value for the Pd/TiO2 NS-IM sample due to its well-dispersion of Pd nanoparticles onto the TiO2 NS surface [30]. This was further demonstrated by the following TEM data, which may be one of the reasons for its improved activity.
Figure 2 shows the HRTEM and TEM images of the synthesized TiO2 nanometer sheet. From Figure 2a, the d spacing was 0.35 nm and 0.47 nm, corresponding to (101) and (002) of anatase TiO2, respectively, which were in line with the previous report [31]. As shown in Figure 2c,d, TiO2 (NS) clearly showed a uniform flake shape, with an average length of about 50 nm and an average thickness of about 7 nm. The TEM images of the Pd/TiO2 NS (Figure 3) catalysts prepared by the different methods, among which Figure 3a–d were the catalysts synthesized by photo-deposition, NaBH4 reduction, impregnation and deposition–precipitation, respectively. By comparing both Figure 2 and Figure 3, it can be easily seen that the flake shape of TiO2 NS was retained after the Pd was supported by any of the prepared methods, indicating that the structure of TiO2 NS was stable when prepared by HF etching. This is consistent with the literature [32]. Furthermore, the sizes of Pd particles were different from each other. The Pd particles were clearly observed in Pd/TiO2 NS-PD and Pd/TiO2 NS-DP. For the other catalysts, some ultrafine Pd particles were observed as marked by red circles. However, for Pd/TiO2 NS-IM it was difficult to find them on the TiO2 support (Figure 3c). In consideration of the highest catalytic activity over Pd/TiO2 NS-IM, the results indicated that the Pd species were highly dispersed on the TiO2 NS surface in Pd/TiO2 NS-IM. Combined with the TEM result in Figure 3, we can reasonably infer that the particle sizes of Pd are increased in the order of Pd/TiO2 NS-IM < Pd/TiO2 NS-NaBH4 < Pd/TiO2 NS-DP < Pd/TiO2 NS-PD. The reduction order of particle size was consistent with their specific surface areas for the catalysts, which further demonstrated that the Pd nanoparticles were deposited onto the supporter. The highest dispersion degree and smallest size of the Pd nanoparticles onto the Pd/TiO2 NS-IM surface resulted in excellent catalytic activity [30].

2.3. XRD Analysis

Figure 4 shows the characteristic X-ray diffraction peaks of TiO2 (NS), P25 and Pd/TiO2 (NS) samples prepared by various methods. Among the results were some characteristic diffraction peaks of rutile TiO2 besides anatase TiO2 in the P25 samples (JCPSD-89-4920) [33], while there were characteristic diffraction peaks of anatase TiO2 in all TiO2 NS-based samples (JCPDS-21-1272) [20]. The observed diffraction peak {004} ( and diffraction peak {200} on TiO2 NS as marked by red arrows were somewhat narrow compared with P25, which may be due to the anisotropic growth of the crystal along the direction of {100}, which was consistent with the results observed by Deng et al. [21]. In addition, the Pd/TiO2 catalysts prepared by different methods (the impregnation method, the deposition–precipitation method, the photo-deposition method, the NaBH4 reduction method) showed the consistency between anatase peak of TiO2 and TiO2 nanocrystalline sheets, indicating that these preparation methods did not change the crystal structure of the TiO2 nanocrystalline sheets. We did not find the characteristic diffraction peak of Pd in the XRD patterns, which may be due to the efficient dispersion of Pd or because the load was lower than the detection limit.

2.4. H2-TPR Analysis

Figure 5 shows the H2-TPR diagram of catalysts Pd/TiO2 NS. As shown in the figure, the reduction peaks below 100 °C were attributed to the reduction peaks of Pd species [34]. All of the Pd/TiO2 NS samples showed a reduction peak of Pd species at around 75 °C, while Pd/ P25 showed this peak at 84 °C [35]. Huan Chen et al. obtained similar results [36]. This is mainly due to nanosheet TiO2 having a more {001} exposed crystal surface, which is easy to reduce [37]. E. López et al. [38] developed a Pd/Al2O3 sample for the catalytic hydrodechlorination of chlorobenzene, exhibiting that the loading amount and size of the Pd nanoparticles onto the Al2O3 surface directly determined their catalytic performance. A strong metal–support interaction existed through the deposition of Pd metal nanoparticles with a small size, owing to its intrinsic size effect [34], while Pd particles with a large size were beneficial to the formation of β-PdH [39,40]. Notably, for all samples, the characteristic H2 consumption peaks imply that PdO species onto the TiO2 NS surface benefits the H2 reduction even below room temperature. Additionally, the supported Pd nanoparticles were susceptible to activating and storing H2, which is more conducive to improving the catalytic activity of p-toluene oxidation under mild ambient conditions. In the hydrogen atmosphere, more oxygen vacancy will be generated on the surface of Pd/TiO2 NS, which is conducive to improving the catalytic activity of p-toluene oxidation.

2.5. XPS Analysis

To investigate elemental compositions and chemical states, the XPS spectra of Pd/TiO2 NS-IM, Pd/TiO2 NS-DP, Pd/TiO2 NS-NaBH4 and Pd/TiO2 NS-PD are exhibited in Figure 6 [41,42,43]. Two signals at 336.4 eV and 341.6 eV corresponded to Pd 3d5/2 and Pd 3d3/2, respectively, indicating their chemical state of Pd2+ in the Pd/TiO2 samples. This result is similar to the reported Pd/A12O3 catalyst prepared by the impregnation method [44,45]. Similar to the Pd/TiO2 NS sample, the binding energies of Pd/Al2O3 and Pd/SiO2 are shifted to the lower energy due to the formation of low valence Pd0 species [46], which may be caused by a reductive environment. It also shows that the interaction is strong between the active substance of the catalyst and the support. The strong interaction between Pd nanoparticles could result in the deficiency of the electron of Pd in Pd/TiO2 NS, which may enable more toluene molecules to be adsorbed on the catalyst surface and improve the catalytic activity. This is consistent with our previous results [47].

3. Materials and Methods

3.1. Catalyst Preparation

  • Preparation of TiO2 Nanosheets (TiO2 NS)
A total of 20 mL Ti(OC4H9)4 was mixed with 3.2 mL of HF solution (50 wt.%) at room temperature, and then transferred to a 100 mL Teflon-lined autoclave for subsequent heating at 200 °C for 24 h. The obtained powder was collected and washed alternately with ethanol and distilled water more than 6 times to remove the remaining fluorine. The TiO2 NS was achieved by drying at 110 °C for 24 h.
  • Preparation of the Pd/TiO2 NS and Pd/P25 Catalysts
The impregnation method: A total of 1 g TiO2 NS powder was first added to the PdCl2 solution, and then heated at 80 °C and constantly stirred until the water was fully removed. The obtained sample was dried in an oven at 110°C for 12 h, and then ground and calcined at 400 °C for 4 h. The resulting catalyst was denoted as Pd/TiO2 NS-IM. To obtain the Pd/P25-IM catalyst, the previous steps were followed and TiO2 NS was replaced with P25.
The deposition–precipitation method: The PdCl2 solution was mixed with TiO2 NS powder, continuously stirred and pH was adjusted with 1 mol/L Na2CO3 to pH = 10.5. The mixed solution was stirred under magnetic power for 2 h. The material obtained was washed with distilled water until the pH value reached neutral, and then dried at 110 °C overnight. Finally, the obtained powder was calcined at 400 °C for 4 h. The resulting sample was Pd/TiO2 NS-DP.
The NaBH4 reduction method: The mixed solution of PVP and PdCl2 (Pd/PVP quality ratio = 1.0:1.5) was placed in the ice bath and stirred for 20 min before adding NaBH4 solution (Pd/NaBH4 mole ratio = 1.0:5.0). TiO2 NS powder was then dispersed in the above-mentioned mixture and stirred for 6 h. The solid obtained by filtration and cleaning was dried at 80 °C. Finally, the powder was calcined at 400 °C for 4 h and then collected as Pd/TiO2 NS-NaBH4.
The photo-deposition method: The mixture of TiO2 NS powder and PdCl2 solution was placed in the reactor in darkness and the ice bath and stirred for 20 min after adding 5 mL of methanol. The mixture was constantly stirred and nitrogen was pumped into it with a flow rate of 60 mL/min for 1 h. The mixture was placed under a 500 W high pressure UV mercury lamp and continuously illuminated for 4 h. The material obtained was washed with distilled water, dried at 110 °C and then ground powder was calcined at 400 °C for 4 h. The catalyst obtained was denoted as Pd/TiO2 NS-PD.
The mass proportion of the metal element Pd in all of the catalysts was 1%.

3.2. Catalyst Characterization

The X–ray diffraction (XRD) was performed on a Philips X’pert Pro diffraction meter using Cu Kα radiation (λ = 1.5408 Å) at 40 kV and 40 mA at room temperature. These data were collected at the scan rate of 5° min−1 between 10–80° (2q). The Brunauer–Emmett–Teller (BET) surface area determination and Barret–Joyner–Halenda (BJH) pore volume and size analysis were measured on an ASAP 2020 instrument at 77 K according to the N2 adsorption–desorption isotherms. Transmission electron microscopic (TEM) and higher-resolution transmission electron microscopy (HRTEM) images were collected by using a JEM-200CX at an acceleration voltage of 200 kV.
The binding energies of Pd of the synthetic material were measured by an X-ray photoelectron spectra (XPS), which was carried out by an ESCALAB250Xi photoelectron spectrometer with a monochromatic Al Kα source (hv = 1486.6 eV) and a charge neutralizer. The hydrogen temperature programmed reduction (H2-TPR) experiment was conducted on the Finesorb-3010 instrument, which was equipped with a thermal conductivity detector (TCD). During the experiment, 100 mg of the sample was first put into a quartz tube, preheated at 110 °C for 1 h under N2 atmosphere, and then cooled to room temperature. Then, a 10% H2/Ar gas mixture (50 mL min−1) was introduced into the sample tube and the sample was heated to 200 °C at the heating rate of 10 °C·min−1.

3.3. Catalytic Performance Test

Oxidation of toluene was conducted in a continuous down-flow fixed-bed micro reactor under atmospheric pressure. Briefly, a 100 mg sample (pressed and sieved through 40–60 mesh) was pretreated in a H2 stream (40 mL min−1) at 300 °C for 2 h, then cooled to 100 °C. Subsequently, the toluene with a constant-flow pump at a rate of 0.0104 mL h−1 was delivered into a mixed-flow gas, which contained 30% oxygen, 70% nitrogen, with a total flow of 40 mL min−1, for a space velocity of 24,000 mL gcat−1 h−1. The products were analyzed online by a gas chromatograph equipped with a Porapak Q-packed column and a thermal conductivity detector (TCD). To obtain accurate results, each experiment was performed three times in parallel with a sustained reaction duration of no less than 30 min. The average value was used as the activity at each temperature.

4. Conclusions

Although nano TiO2 have been widely used as photocatalysts and obtained good activity effects, their application is still limited by the short life of the photoexcited charge carriers and the wide band gap requiring ultraviolet (UV) radiation. In this study, the TiO2 NS was used as Pd-based carrier to prepare the Pd/TiO2 NS catalyst, which was applied to study the catalytic combustion performance of VOCs and was found to have very good catalytic activity.
Firstly, TiO2 nanocrystalline was synthesized by the hydrothermal synthesis method with HF as the etching agent, and then the single metal Pd/TiO2 NS catalyst was synthesized by different methods (the impregnation method, the deposition–precipitation method, the photo-deposition method and the NaBH4 reduction method). The relationship between the catalyst structure and the catalytic combustion activity of toluene was studied by combining with BET, TEM, XRD, H2-TPR and other characterization techniques. In the future, we will be committed to improving the reaction mechanism of TiO2 NS-supported Pd catalysts for VOCs’ combustion, reducing TiO2 NS support to form defects on its surface and reloading Pd and studying the effect of surface defects on catalyst performance. The conclusions obtained in this work are as follows:
(1)
Pd/TiO2 catalysts were synthesized by different methods to study the effects of different preparation methods on the catalytic combustion activity of toluene. Firstly, we compared the catalytic activity of toluene with that of ordinary commercial P25 and TiO2 nanometer tablets after impregnating the Pd. The results showed that Pd/TiO2 NS with {001} crystal surface as the exposed crystal surface was significantly better than Pd/P25, and the temperature of 100% complete transformation of toluene was 40 °C lower. This is mainly because the {001} crystal surface of nano-sheet TiO2 is easier to form oxygen vacancy;
(2)
According to the experimental results, the catalyst prepared by the impregnation method had smaller Pd particles and more active sites. The smaller the Pd particles, the better the catalytic performance. The 100% conversion of toluene was achieved at 210 °C on Pd/ TiO2-IM. The catalytic activity of Pd / TiO2 catalyst prepared by the illumination (Pd/TiO2-PD) and deposition–precipitation (Pd/ TiO2-DP) methods was lower than that of Pd / TiO2 catalyst prepared by immersion method. Compared with the other synthesis methods, Pd in the impregnation method may be dispersed better in the synthesis process and the particles are smaller, so that more Pd active sites can be spread on the TiO2 nano-sheet carrier.

Author Contributions

Conceptualization, H.W.; Formal analysis, G.Y. and C.G.; Investigation, G.Y. and C.G.; Methodology, G.Y., and C.G.; Project administration, H.W.; Writing—original draft, G.Y., and C.G.; Writing—review & editing, G.Y., C.G. and H.W.; All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the National Key Research and Development Program of China (Grant No.2016YFC0204301) and the National Natural Science Foundation of China (Grant No. 21976082, 21607122).

Data Availability Statement

Not applicable.

Conflicts of Interest

The authors declare no conflict of interest.

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Catalysts 12 01406 g001 550
Figure 1. Catalytic oxidation of toluene by Pd/TiO2 catalyst prepared by different methods.
Figure 1. Catalytic oxidation of toluene by Pd/TiO2 catalyst prepared by different methods.
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Catalysts 12 01406 g002 550
Figure 2. HRTEM (a,b) and TEM (c,d) diagrams of TiO2(NS).
Figure 2. HRTEM (a,b) and TEM (c,d) diagrams of TiO2(NS).
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Catalysts 12 01406 g003 550
Figure 3. TEM image of Pd/TiO2 catalyst prepared by different methods: (a) the photo-deposition method; (b) the deposition–precipitation method; (c) the impregnation method; (d) the NaBH4 reduction method.
Figure 3. TEM image of Pd/TiO2 catalyst prepared by different methods: (a) the photo-deposition method; (b) the deposition–precipitation method; (c) the impregnation method; (d) the NaBH4 reduction method.
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Catalysts 12 01406 g004 550
Figure 4. XRD patterns of Pd/TiO2 prepared by different methods.
Figure 4. XRD patterns of Pd/TiO2 prepared by different methods.
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Catalysts 12 01406 g005 550
Figure 5. H2-TPR diagram of the catalyst prepared by different preparation methods.
Figure 5. H2-TPR diagram of the catalyst prepared by different preparation methods.
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Figure 6. Pd 3d XPS spectra of different catalysts.
Figure 6. Pd 3d XPS spectra of different catalysts.
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Table
Table 1. The physical properties of the samples.
Table 1. The physical properties of the samples.
CatalystSurface Area
m2/g		Pore Volume
cm3/g		Pore Size
nm
P25500.421
TiO2 NS920.4318.1
Pd/TiO2 NS-DP800.3820.1
Pd/TiO2 NS-PD770.3817.9
Pd/TiO2 NS-NaBH4740.3720.1
Pd/TiO2 NS-IM520.2225.2
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Yu, G.; Ge, C.; Wan, H. Effects of Preparation Methods of Pd Supported on (001) Crystal Facets Exposed TiO2 Nanosheets for Toluene Catalytic Combustion. Catalysts 2022, 12, 1406. https://doi.org/10.3390/catal12111406

AMA Style

Yu G, Ge C, Wan H. Effects of Preparation Methods of Pd Supported on (001) Crystal Facets Exposed TiO2 Nanosheets for Toluene Catalytic Combustion. Catalysts. 2022; 12(11):1406. https://doi.org/10.3390/catal12111406

Chicago/Turabian Style

Yu, Guiyun, Chengyan Ge, and Haiqin Wan. 2022. "Effects of Preparation Methods of Pd Supported on (001) Crystal Facets Exposed TiO2 Nanosheets for Toluene Catalytic Combustion" Catalysts 12, no. 11: 1406. https://doi.org/10.3390/catal12111406

APA Style

Yu, G., Ge, C., & Wan, H. (2022). Effects of Preparation Methods of Pd Supported on (001) Crystal Facets Exposed TiO2 Nanosheets for Toluene Catalytic Combustion. Catalysts, 12(11), 1406. https://doi.org/10.3390/catal12111406

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