Journal of Chemistry
Volume 2016 (2016), Article ID 4563832, 9 pages
http://dx.doi.org/10.1155/2016/4563832

Research Article

Effect of Carbon Supported Pt Catalysts on Selective Hydrogenation of Cinnamaldehyde

Qing Han, Yunfei Liu, Dong Wang, Fulong Yuan, Xiaoyu Niu, and Yujun Zhu

Key Laboratory of Functional Inorganic Material Chemistry, School of Chemistry and Materials, Heilongjiang University, Ministry of Education, Harbin 150080, China

Received 4 May 2016; Accepted 28 July 2016

Academic Editor: Ioannis D. Kostas

Copyright © 2016 Qing Han et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Abstract.

Selective hydrogenation of cinnamaldehyde (CAL) to cinnamyl alcohol (COL) is of both fundamental and industrial interest. It is of great significance to evaluate the possible differences between different supports arising from metal dispersion and electronic effects, in terms of activity and selectivity. Herein, Pt catalysts on different carbon supports including carbon nanotubes (CNTs) and reduced graphene oxides (RGO) were developed by a simple wet impregnation method. The resultant catalysts were well characterized by XRD, Raman, N₂ physisorption, TEM, and XPS analysis. Applied in the hydrogenation of cinnamaldehyde, 3.5 wt% Pt/CNT shows much higher selectivity towards cinnamyl alcohol (62%) than 3.5 wt% Pt/RGO@SiO₂ (48%). The enhanced activity can be ascribed to the high graphitization degree of CNTs and high density of dispersed Pt electron cloud.

1. Introduction

With the rapid development of catalytic science, controlling the reaction selectivity is particularly significant [1, 2]. As a typical example, selective hydrogenation of α,β-unsaturated aldehydes is of both fundamental and industrial importance [3–5]. For instance, the hydrogenation of cinnamaldehyde (CAL) can produce cinnamyl alcohol (COL), hydrocinnamaldehyde (HALD), and hydrocinnamyl alcohol (HALC) (Scheme 1) [6–8]. COL is generally considered to be the most challenging product to obtain and is a type of important organic intermediates for chemical synthesis, which has been widely used in perfume, cosmetics, medicines, and fungicides industries [3, 4]. However, the selective production of COL is difficult because the hydrogenation of the C=C bond is thermodynamically favored over that of the C=O group. Therefore, the development of catalysts for this class of reactions is still challenging and highly desired.

Scheme 1: Reaction pathways for cinnamaldehyde hydrogenation.

Recently, a large number of homogeneous catalysts such as metal hydrides, aluminium isopropoxide, and others have been developed for selective hydrogenation of cinnamaldehyde to cinnamic alcohol [9, 10]; however, efficient separation and recovery of these advanced catalysts from reaction vessel are still a challenge, which prevents their widespread applications [11]. To this end, the development of heterogeneous catalysts on various supports provides a promising solution because of its environment-friendly property, ability to selectively hydrogenate, and simple method to recover [5, 9]. A number of noble metal (e.g., Pt, Pd, Ir, and Ru) and nonnoble metal (e.g., Fe, Co, Ni, and Cu) nanoparticles have been demonstrated as effective phase for this catalytic reaction [12–21]. A great deal of parameters, such as the nature of the active metal, its surface structures, particle sizes, contents, the methods of catalyst preparation, and the reaction conditions could influence the activity and selectivity [3, 6, 22–24]. Among them, the support, which maximizes the active surface area of metal catalysts by dispersing them over its surface, plays a key role in both the activity and the selectivity in the targeted selective hydrogenation due to the interaction between the support and nanoparticles [25]. For example, various reducible oxides such as CeO₂ [26], MnO₂ [27], SnO₂ [28], TiO₂ [29, 30], and ZnO [31] have been used as the supports and were found to be able to improve the selectivity toward COL production because of strong metal-support interactions, which can influence the degree of reduction, metal dispersion, and evolution of the active phase.

In addition to metal oxides, owning to the unique structures and properties, various carbon materials such as carbon nanofibers, carbon nanotubes (CNT), and reduced graphene oxides (RGO) have also been studied as effective supports for metal nanoparticles toward hydrogenation of unsaturated aldehyde [32–36]. We have found that graphene-supported Pt catalysts exhibit excellent catalytic performances in terms of selectivity for the hydrogenation of unsaturated aldehydes [37]. Unfortunately, the key factor of different carbon supports controlling the activity and selectivity still remains unclear.

Indeed, CNTs, which are the one-dimensional (1D) tubular structure of graphite, are totally different from graphene (2D planar structure). Therefore, it would be interesting to evaluate the possible differences between different carbon materials arising from metal dispersion and electronic effects, in terms of activity and selectivity. Herein, we have attempted to address this issue through investigating Pt catalysts on different carbon supports including CNTs and RGO, which were evaluated for the selective hydrogenation of CAL. 3.5 wt% Pt nanoparticles deposited on CNTs and RGO were prepared by the same wet impregnation method and were denoted as 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂, respectively. It was found that the selectivity of COL is different for the Pt supported on different carbon. 3.5 wt% Pt/CNT shows much higher selectivity towards cinnamyl alcohol (62%) than 3.5 wt% Pt/RGO@SiO₂ (48%). The effects of CNTs and RGO on the properties of catalysts were investigated, indicating the graphitization degree of support plays an important role in the sorption of CAL and Pt species.

2. Material and Methods

2.1. Synthesis of RGO@SiO₂ Supports

(3-Aminopropyl) Triethoxysilane (APTES) Modified Silica Gel (Aladdin 200 m ²/g). In a typical process, after vacuum drying at 110°C for 24 h, 5.0 g silica gel was added into APTES/toluene solution. The mole ratio of APTES to silica gel was maintained at 1 : 2. The mixed solution was stirred at 100°C for 24 h. After cooling to room temperature, the product was washed by using toluene 4 times (100 mL/times) and chloroform 4 times (100 mL/time), respectively. Next, the product was soaked in methanol/water solution (1 : 10, v/v) for 2 h and it was repeated 4 times to remove the organic residues in the process of modification. The resultant product was dried at 100°C for 24 h, marked as APTES-SiO₂.

RGO@SiO ₂ Supports. In a typical process, APTES-SiO₂ was added into graphene oxide solution. The quality ratio of graphene oxide to APTES-SiO₂ was kept at 1 : 9. The pH value of the mixture solution was adjusted to 4.0 by NaOH (0.1 mol/L) solution. After stirring for 1 h, FeCl₂ solution was slowly added to the reaction vessel. Subsequently, NaBH₄ solution (1 mol/L) was added to the mixture and stirred for 10 min. Next, HCl aqueous solution was added to remove the excess iron powders. The resultant sample was thoroughly washed by water to remove chloride ions, which was checked by AgNO₃ solution (1 mol/L). Then, the product was washed by ethanol and dried at 80°C for 10 h under vacuum drying, which is denoted as RGO@SiO₂.

2.2. Preparation of 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs

3.5 wt% Pt/RGO@SiO₂ was prepared in a typical process and the RGO@SiO₂ supports (0.5 g) were first suspended in deionized water (50 mL) and ultrasonicated for 0.5 h. Then, H₂PtCl₆ (19.3 mmol/L) solution was added to the slurry. Next, the mixture solution was put into ice bath and stirred vigorously for 0.5 h. The temperature of ice bath was kept at 2–4°C and the pH value of the mixture solution was adjusted to 8.0 by NaOH (0.1 mol/L) solution. Afterwards, an excess of NaBH₄ (0.4 mol/L) solution was added to the mixture under vigorous stirring. After 3 h, the mixture was statically placed in the ice bath for 10 h. Finally, the product (3.5 wt% Pt/RGO@SiO₂ catalysts) was obtained after filtrating, washing with deionized water until no chloride was detected, washing with ethanol, and drying at 60°C for 10 h. The 3.5 wt% Pt/CNTs catalyst was prepared by following the same method.

2.3. Catalyst Characterization

X-ray diffraction (XRD) patterns were obtained with a Rigaku D/max-IIIB diffractometer by using Cu-Kα (λ = 1.5406 Å) radiation. The accelerating voltage and the applied current were 40 kV and 20 mA, respectively. Raman spectra were recorded with a Jobin Yvon HR 800 micro-Raman spectrometer at 457.9 nm. The laser beam was focused on the sample with a 50x objective. Transmission electron microscopy (TEM) experiments were carried out with a JOEL model JEM-2100 electron microscope working at an acceleration voltage of 200 kV. The samples for the TEM measurements were suspended in ethanol and supported onto a holey carbon film on a Cu grid. X-ray photoemission spectroscopy (XPS) studies were carried out on a Kratos-AXIS ULTRA DLD with an Al-Kα radiation source. Nitrogen adsorption and desorption isotherms were measured at 77 K with a Micromeritics Tristar II 3020 analyzer. The sample was degassed under vacuum at 423 K for 4 h prior to measurements. The Brunauer-Emmett-Teller (BET) method was utilized to calculate the specific surface areas using adsorption data in a relative pressure range from 0.05 to 0.25.

2.4. Catalytic Performance Measurements

The catalytic performances of 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs toward the hydrogenation of cinnamaldehyde were carried out in a 100 mL stirred autoclave. In briefly, catalyst (50 mg) was immersed into 15 mL of isopropanol. The trace of dissolved oxygen was removed by flushing with nitrogen at 5 bar for 3 times and subsequently with hydrogen at 5 bar for 3 times. Then, the temperature was raised to 110°C under 10 bar of hydrogen for 1 h, to reactivate the catalysts. Then, a mixture of cinnamaldehyde (1.0 g) and isopropanol (15 mL) was added into the autoclave. After flushing with nitrogen at 5 bar for 3 times and subsequently with hydrogen at 5 bar for 3 times, the reaction was allowed to proceed at 60°C under 10 bar of hydrogen. The products were analyzed on a gas chromatography (Agilent 7820A) equipped with an FID detector and an HP-5 capillary column (30 m × 0.32 mm × 0.25 μm). The products were further identified by GC-MS (Agilent 6890/5973N).

3. Results and Discussion

Due to the poor dispersion of RGO support, RGO was dispersed on SiO₂ to obtain the RGO@SiO₂ support. Thus, 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs were prepared by reduction of H₂PtCl₆ using NaBH₄ and used to research the effect of different carbon supported Pt catalysts on selective hydrogenation of cinnamaldehyde.

3.1. XRD Analysis

A sharp and strong diffraction peak at 27° in 3.5 wt% Pt/CNTs was assigned to (002) facet of graphite, suggesting the ordered structure and high graphite degree of CNTs support (Figure 1). A weak and broad peak at 22.1° in 3.5 wt% Pt/RGO@SiO₂ can be assigned to the characteristic structure of RGO due to restacking effects, indicating the graphene oxide has been reduced to a certain degree. The results illustrate that the CNTs support has a higher graphitization degree than RGO@SiO₂ support. Additional diffraction peaks were observed in the patterns of both catalysts at 39.7, 46.4, and 67.5°, which correspond to the (111), (200), and (220) crystalline planes of the face-centered cubic (fcc) Pt, respectively [38]. The average particle sizes of Pt nanoparticles are about 4.0 and 4.4 nm for 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% of Pt/CNTs, respectively, which are calculated by using the full width at half maximum of Pt (111) reflection based on Scherrer’s equation [39].

Figure 1: XRD patterns of (a) 3.5 wt% Pt/RGO@SiO₂ and (b) 3.5 wt% Pt/CNTs.

3.2. Raman Spectroscopy

Raman is one of the useful tools for providing detailed structures of carbon materials, such as disorder and defect structure. Figure 2 shows the Raman spectra of 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs. In the Raman spectroscopy of both catalysts, the appearance of two prominent peaks, D (1368 cm⁻¹) and G (1590 cm⁻¹) bands, is usually assigned to the breathing mode of κ-point phonons of symmetry and the phonons of sp² carbon atoms, respectively [40, 41]. It is well known that the increase in the intensity ratio of D/G () accounts for a low crystalline degree of graphite materials. The values of 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs are 1.2 and 0.82, respectively (Table 1). It indicates that CNTs have a higher degree of graphitization than RGO support, which is in agreement with the XRD analysis. The ratio of 3.5 wt% Pt/CNTs is 0.70, suggesting that the tube wall of CNTs support is thin. In contrast, the intensity of 2D peak of 3.5 wt% Pt/RGO@SiO₂ catalyst is relatively weak, which is possibly caused by the reunion of RGO.

Table 1: Physicochemical properties of 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂.

Catalysts
(m²/g)
Pt size (nm)

C1s content (%)
Pt species content (%)/BE (eV)

C-C
C=O
-COO
Pt⁰/BE
Pt/BE
Pt/BE

3.5 wt% Pt/CNTs
147
4.0
0.82
64.2
28.1
7.7
58.6/71.6
25.9/72.8
15.5/75.1

3.5 wt% Pt/RGO@SiO₂
152
4.4
1.2
16.5
69.7
11.7
19.0/71.4
65.6/72.4
15.4/74.9

Values calculated from catalysts corrected mass (i.e., without mass induced by metal loading).

Pt particle sizes were calculated from XRD patterns based on Scherrer’s equation, respectively.

Calculated from the Raman results using the intensities of D and G peaks.

Caculated from the XPS results.

Figure 2: Raman spectra of 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs.

3.3. TEM Analysis

The morphology of 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs was investigated by TEM measurements, as shown in Figure 3. The structure of different carbon supports can be clearly distinguished. TEM images of 3.5 wt% Pt/RGO@SiO₂ and 3.5 wt% Pt/CNTs catalysts show that a number of Pt nanoparticles were well dispersed on 1D intertwined CNTs and 2D planar RGO support, respectively (Figures 3(a) and 3(c)). Figures 3(e) and 3(f) show the particle size distribution of Pt nanoparticles, respectively. The mean particle size of Pt nanoparticles for the 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ is around 3.8 nm and 3.1 nm, respectively. The results match well with the XRD analysis. Figures 3(b) and 3(d) are the corresponding high-resolution TEM (HRTEM) images. HRTEM images of Pt nanoparticles in both 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ catalysts display the well-defined lattice fringes.

(a)

(b)

(c)

(d)

(e)

(f)

Figure 3: TEM images of (a, b) 3.5 wt% Pt/CNTs and (c, d) 3.5 wt% Pt/RGO@SiO₂ catalysts; Pt particle size distributions of (e) 3.5 wt% Pt/CNTs and (f) 3.5 wt% Pt/RGO@SiO₂; the insets in panel (b and d) are the corresponding HRTEM images of CNT, Pt nanoparticle, and reduced graphene oxides (RGO).

The measured lattice spacing values from the insertion of HRTEM images are 0.233 nm and 0.253 nm, which can be well assigned to the (111) planes of the face-centered cubic Pt. HRTEM image of CNTs displays the (002) graphite planes with interlayer spacing of 0.34 nm mostly parallel to the tube axis (Figure 3(e)). In addition, Figure 3(f) also shows the well-defined lattice fringes of RGO. The lattice spacing values were calculated to be 0.287 nm, which is corresponding to the (002) planes of graphite.

3.4. X-Ray Photoelectron Spectroscopy

XPS was used to study the surface nature and structure of 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ (Figure 4). The high-resolution C1s spectra of the 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ could be deconvolved into three peaks at 284.6, 287.3, and 290.2 eV, which were assigned to the C element in C-C, C=O, and -COO groups, respectively, as shown in Figures 4(a) and 4(c). The content of C-C bond in 3.5 wt% Pt/CNTs reached 64.2%, and the half peak width is 0.62 eV, indicating that the CNTs have better graphitization degree, which is in agreement with the Raman and XRD results. In contrast, 3.5 wt% Pt/RGO@SiO₂ displays a weak sharp peak at 284.6 eV that only accounted for 16.5% of total carbon. And the half peak width is 0.79 eV, much wider than that of 3.5 wt% Pt/CNTs catalyst. These results suggest that the graphene oxide can be partly reduced into RGO. The more content of C=O and -COO bonds in 3.5 wt% Pt/RGO@SiO₂ may be resulting from the SiO₂ substrate, which decrease the reducibility of graphene oxide. The Pt4f XPS spectra of 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ are shown in Figures 4(b) and 4(d), respectively, together with their deconvolution into three spin-split states [42–44], as summarized in Table 1.

(a)

(b)

(c)

(d)

Figure 4: C 1s (a, c) and Pt 4f (b, d) high-resolution XPS spectra of (a, b) 3.5 wt% Pt/CNTs and (c, d) 3.5 wt% Pt/RGO@SiO₂.

In terms of quantitation of the composition of the Pt nanoparticles, the contents of the surface , , and species in 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ catalysts were estimated to be 58.6/25.9/15.5% and 19.0/65.6/15.4%, respectively. Interestingly, the amount of in 3.5 wt% Pt/CNTs catalyst (58.6%) is much higher than that of 3.5 wt% Pt/RGO@SiO₂ (19.1%).

3.5. Catalytic Performances

The effect of different carbon supports for Pt nanoparticles on the selective hydrogenation of CAL was investigated and the results were summarized in Table 2. When the reaction time is 2 h, the conversion of CAL is 39% over 3.5 wt% Pt/CNTs, which is comparable to that of 3.5 wt% Pt/RGO@SiO₂ (38%). The selectivity to COL for 3.5 wt% Pt/CNTs is 62%, which is much better than that of 3.5 wt% Pt/RGO@SiO₂ (48%). The selectivity to HALD and HALC is 35% and 11% over 3.5 wt% Pt/RGO@SiO₂, respectively, which is corresponding to 23% and 9% for 3.5 wt% Pt/CNTs. It indicates that 3.5 wt% Pt/CNT is more favor of the hydrogenation of C=O bond of cinnamaldehyde. In both cases, a minor quantity of acetal by-product was detected.

Table 2: The catalytic performances of various catalysts toward the hydrogenation of cinnamaldehyde.

Catalysts
Conversion (%)
Selectivity (%)

HALD
HALC
COL
Others

3.5 wt% Pt/CNTs
39
23
9
62
6

3.5 wt% Pt/RGO@
38
35
11
48
6

3.5 wt% Pt/graphene [37]
73
8
6
82
4

includes 1-(3-propoxyprop-1-enyl)benzene, cinnamyl formate, cinnamic acid, benzyl, cinnamate, 4,4-diphenylcyclohexa-1,5-dienyl acetate, and other condensation products that could not be identified by GC-MS because of their large molecular weights.

Reaction conditions: 10 bar H₂, 60°C, and 2 h.

The recycling experiments were carried out over 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ catalysts and shown in Figures 5 and 6, respectively. The catalysts were reused directly without any treatment after being precipitated and separated from the reaction solution. After four cycles, the activity of 3.5 wt% Pt/CNTs was a slight decrease, the conversion of CAL declined only from 39% to 32%, and the selectivity to COL decreased from 62% to 53% (Figure 5). And, for 3.5 wt% Pt/RGO@SiO₂ catalyst, the conversion to CAL and selectivity to COL after four catalytic cycles decreased to 26% and 34%, respectively (Figure 6). In general, the catalytic stability of 3.5 wt% Pt/CNTs is higher than that of 3.5 wt% Pt/RGO@SiO₂ catalyst.

Figure 5: Stability test for 3.5 wt% Pt/CNTs shown as performance versus number of recycling runs. Reaction conditions: 50 mg 3.5 wt% Pt/CNTs, 1.00 g CAL, 30 mL isopropanol, 10 bar H₂, 60°C, and 2 h.

Figure 6: Stability test for 3.5 wt% Pt/RGO@SiO₂ shown as performance versus number of recycling runs. Reaction conditions: 50 mg 3.5 wt% Pt/RGO@SiO₂, 1.00 g CAL, 30 mL isopropanol, 10 bar H₂, 60°C, and 2 h.

The difference in selectivity for 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ with same conversion may be attributed to the Pt species and supports. According to above characterization results, similar mean particle size values were obtained for 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ synthesized here, but high selectivity was seen only with the 3.5 wt% Pt/CNTs sample. It is seen that other factors may account for the good selectivity to COL with the 3.5 wt% Pt/CNTs catalyst. Firstly, there is the effect of the Pt electron structure. In our previous reports [37, 45–47], it has been found that the species plays a key role in the selectivity to COL in the selective hydrogenation of cinnamaldehyde, and there is a linear correlation between the amount of and the selectivity. The more the surface content catalyst has, the higher selectivity to COL it exhibits. We have brought out that there is the special effect of carbon support on the amount of species [37]. Here, the amount of Pt⁰ species is 58.6% and 19.0% on the surface of 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ (Figure 4, Table 1), respectively, which responds to the selectivity of COL (Table 2). The amount of species on the surface of 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂ is the important reason for the selectivity of COL. Furthermore, it is noticed that the amount of species for 3.5 wt% Pt/CNTs is similar to that of 3.5 wt% Pt/graphene (61%) [37]; however, the selectivity to COL is much lower compared with 3.5 wt% Pt/graphene (82%) [37]. It is obvious that there is not a linear correlation between selectivity to COL and species for 3.5 wt% Pt/CNTs, 3.5 wt% Pt/RGO@SiO₂, and 3.5 wt% Pt/graphene. Thus, we think that the carbon support itself plays other roles besides effect on the formation of species in the selective hydrogenation of CAL. The Raman results shown in Table 1 indicate that the value of is 0.82 and 1.2 for 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂, respectively, which is much higher than that of 3.5 wt% Pt/graphene (0.29) [37]. It suggests that the graphitization degree of support is listed as follows: graphene > CNTs > RGO@SiO₂, meaning there are more amounts of the disordered sp²-bonded carbon such as various -COH and -COOH groups, on the surface of 3.5 wt% Pt/CNTs and 3.5 wt% Pt/RGO@SiO₂. These groups derived from the low crystallinity degree of the carbon support. Secondly, property of supports can influence the sorption of CAL. According to literatures [9], the worse the crystallinity degree of the carbon support is, the weaker the adsorption of CAL is on its surface. The much lower graphitization degree of support is disadvantage for the weak π-π interactions between CAL and the surface sp²-bonded carbon support, which results in the low conversion of CAL. Moreover, the weak π-π interactions can favor the contact of C=C with Pt species due to CAL structure, which leads to the decrease in selectivity to COL and increase in selectivity to HALD. The graphitization degree of 3.5 wt% Pt/CNTs is much higher than that of 3.5 wt% Pt/RGO@SiO₂; thus, the high selectivity to COL may be partly attributed to the better graphitization degree. The better the graphitized degree carbon support is, the higher the adsorption capacity for CAL it shows on its surface. But the graphitization degree of 3.5 wt% Pt/CNTs is low compared with 3.5 wt% Pt/graphene. On the whole, 3.5 wt% Pt/CNT shows low conversion and selectivity which can be ascribed to the weak graphitization degree being not conducive to adsorption of CAL compared with 3.5 wt% Pt/graphene, although it also possesses high amount. So it can be seen clearly that the graphitization degree of carbon support plays an important role in the selective hydrogenation of CAL.

4. Conclusion

In summary, different carbon materials including CNTs and RGO were evaluated as support for Pt nanoparticles. TEM images showed that Pt nanoparticles dispersed well on CNTs and RGO surface with a size of about 4 nm. Compared with 3.5 wt% Pt/RGO@SiO₂, 3.5 wt% Pt/CNT shows better selectivity for the hydrogenation of C=O bonds. The unique catalytic performance can be attributed to not only the high graphitization degree of CNTs, which facilitate the adsorption of CAL and improve the selectivity of COL, but also the high density of dispersed Pt electron cloud, which benefit for the COL production.

Competing Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

Acknowledgments

This work was supported by Natural Sciences Fund of Heilongjiang Province (B2015009), Postdoctoral Science-Research Developmental Foundation of Heilongjiang Province of China (LBH-Q12022), the Scientific Research Foundation for the Returned Overseas Chinese Scholars, State Education Ministry (2013-1792), and Ministry of Human Resources and Social Security (2013-277).

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