DOI:
10.1039/C4RA11798K
(Paper)
RSC Adv., 2015,
5, 9561-9564
Angstrom-scale vanadium carbide rods as Pt electrocatalyst support for efficient methanol oxidation reaction
Received
5th October 2014
, Accepted 23rd December 2014
First published on 5th January 2015
Abstract
Angstrom-scale vanadium carbide rods combined with carbon (denoted as C–V8C7 (rods)) are synthesized through an ion-exchange route. The angstrom-scale C–V8C7 (rods) show better promotion effect on Pt than the nanoscale C–V8C7 (particles) towards methanol oxidation reaction (MOR). Furthermore, Pt particle loading on C–V8C7 (rods) (denoted as Pt/C–V8C7 (rods)) show much higher MOR activity and stability than commercial Pt/C electrocatalyst. The present method is imagined to be adopted to easily synthesize other angstrom-scale materials.
1. Introduction
Transition metal carbides are efficient as promoters to improve the performances of noble metal based electrocatalysts due to synergistic effects.1–4 By introducing carbides, the use level of noble metals can be greatly reduced to achieve the same or higher activity.5–12 The literatures indicate that the interaction between carbide and noble metal increases with the decrease of carbide particle size.13–15 The larger carbide particles have lower specific surface area, resulting in poor dispersion of loaded noble metal nanoparticles. It is imagined that the mixing of carbide and noble metal at the atomic level would lead to full interaction.
The carbides that have been most extensively studied as electrocatalyst promoter are tungsten carbide (WC)16–23 and molybdenum carbides (MoC and Mo2C).24–28 The recent study indicated that vanadium carbide is more efficient29 in promoting the activity of platinum (Pt) than WC and Mo2C, which might make vanadium carbide a new research focus as catalyst promoter. However, the traditional synthesis methods of vanadium carbide (and also other carbides) lead to large particle sizes that are tens or hundreds of nanometers in diameter.30,31 Recently, in situ exchange routes to vanadium carbide with the diameter down to 2–10 nm (ref. 32–35) have been reported, great promotion effects of V8C7 on activities of Pt or Pd have been found.
Herein, we report a synthesis of angstrom-scale V8C7 with rod-shape. To the best of our knowledge, this is the first attempt to prepare such small V8C7 material. It is also found that Pt being loaded on the synthesized angstrom-scale V8C7 rods show excellent activity and stability towards MOR in acidic media.
2. Experimental
2.1 Synthesis of C–V8C7 composites
Typically, polyacrylic weak-base anion-exchange resin (10 g, D201×1 resin, Hebi Power Resin Factory, China) was impregnated in 100 mL sodium orthovanadate (SOV, Na3VO4·12H2O, A.R., Shanghai Ekear Biological Technology Co., Ltd., China) for 6 h, then the solid was separated and dried at 80 °C and heated at 800 °C for 1 h. After cooled down to room temperature, the sample was ground into powder to get the C–V8C7 composite. The samples with SOV concentrations of 0.02 and 0.002 mol L−1 were denoted as C–V8C7 (particles) and C–V8C7 (rods) respectively.
2.2 Preparation of electrocatalysts
Pt particles were loaded on the C–V8C7 to form Pt/C–V8C7 electrocatalyst. Typically, C–V8C7 (60 mg) was added into a mixture of 20 mL glycol (A.R., Tianjin Fuyu Fine Chemicals Co., Ltd, China) and chloroplatinic acid (H2PtCl6, containing 40 mg Pt, A. R., Sinopharm Chemical Reagent Co., Ltd) and dispersed to form a uniform ink in ultrasonic bath for 30 min. The pH of the mixture was adjusted to 10 by adding 1 mol L−1 NaOH/glycol solution. The sample was then put into a microwave oven (900 W) for heating at a 10 s on and 10 s off procedure for 12 times.36 Afterwards, the mixture was washed with deionized water and dried in vacuum at 50 °C for 24 h to get the Pt/C–V8C7 electrocatalyst. The Pt particles being loaded on C–V8C7 (particles) and C–V8C7 (rods) were denoted as Pt/C–V8C7 (particles) and Pt/C–V8C7 (rods), respectively. The Pt contents in the electrocatalysts were 40 wt% stoichiometricly.
2.3 Preparation of electrodes
Pt/C–V8C7 (5 mg) or commercial Pt/C (4 mg, 47.6 wt% Pt, TKK, Japan) were dispersed in mixture of 0.05 mL 5 wt% Nafion suspension (DuPont, USA) and 1.95 mL ethanol in ultrasonic bath to form the electrocatalyst ink. The ink (0.005 mL) was deposited on surface of a glass carbon electrode (0.25 cm2) and dried at room temperature. The total Pt loadings were 0.02 mg cm−2.
2.4 Electrochemical characterization
All electrochemical measurements were performed in a three-electrode cell on a potentiostat at 30 °C. A platinum foil (1.0 cm2) and saturated calomel electrode (SCE) were used as counter and reference electrodes, respectively. All chemicals were of analytical grade and used as received.
2.5 Physical characterization
The morphologies of the synthesized materials were characterized by transmission electron microscopy (TEM, JOEP JEM-2010, JEOL Ltd.) operating at 200 kV. The structures of the samples were determined on an X-ray diffractometer (XRD, D/Max-IIIA, RigakuCo., Japan, CuK1, λ = 1.54056 Å radiation).
3. Results and discussion
Fig. 1a is the TEM image of the C–V8C7 (rods), which shows the rods with the width of around 1 nm and length of several nanometers that are uniformly dispersed on carbon matrix. Fig. 1b is the magnified TEM image of C–V8C7 (rods), inset shows a rod with the width of 1.5 nm, length of 5.6 nm and lattice of V8C7 (222) facet. Fig. 1c displays the corresponding width distribution of the rods. From randomly selected 100 rods, the average width of the rods was calculated as 0.8 nm, being angstrom scale. Fig. 1d is the TEM image of C–V8C7 (particles), which shows obvious agglomerations, due to the high concentration of SOV in the preparation step.
 |
| Fig. 1 (a) TEM and (b) magnified TEM images of C–V8C7 (rods); (c) rods' width distribution of V8C7 (rods); (d) TEM image of C–V8C7 (particles). Inset of (b) is the TEM image of a V8C7 rod. | |
Fig. 2 shows the XRD patterns of C–V8C7 (particles) and C–V8C7 (rods) (solid lines). The diffraction peaks at 2θ of 37.4°, 43.4°, 63.0° and 75.6° correspond to (222), (400), (440) and (622) facets of V8C7 crystal respectively, confirming that the rods and particles in Fig. 1 are V8C7. The peak intensity of the V8C7 weakened with the decreasing concentration of SOV, which related to the V8C7 particle size.
 |
| Fig. 2 XRD patterns of C–V8C7 (rods), C–V8C7 (particles), Pt/C–V8C7 (rods) and Pt/C–V8C7 (particles). | |
The formation of V8C7 rods should be due to long-chain structure of the D201×1 resin. A proper concentration of SOV would lead to discontinuous chain of V8C7, i.e. V8C7 rods. However, a high concentration of SOV would lead to conglomerated chain, i.e. V8C7 particles.
The XRD patterns of Pt/C–V8C7 (rods) and Pt/C–V8C7 (particles) are also shown in Fig. 2 (dotted lines). The peaks at 39.8°, 46.2° and 67.5° correspond to the (111), (200) and (220) facets of Pt crystal respectively. And the V8C7 peaks and the Pt peaks are overlapped with each other.
Fig. 3 shows the TEM images of Pt/C–V8C7 (rods) and Pt/C–V8C7 (particles). Due to that the C–V8C7 composites have different V8C7 content (leading to different density), Pt particles on C–V8C7 (rods) are sparse (see Fig. 3a), and on C–V8C7 (particles) seem to be abundant (see Fig. 3b). Inset of Fig. 3a shows the EDS pattern of Pt/C–V8C7 (rods) with C, Cu, V, Pt and Cr elements (Cu and Cr come from sample bracket). And Fig. 3c shows the V8C7 (400) and Pt (111) lattices in Pt/C–V8C7 (rods). They all prove the coexistence of V8C7 and Pt.
 |
| Fig. 3 TEM images of (a) Pt/C–V8C7 (rods) and (b) Pt/C–V8C7 (particles); (c) HRTEM image of Pt/C–V8C7 (rods). Inset of (a) is the corresponding EDS pattern. | |
The MOR performances of the Pt/C–V8C7 electrocatalysts were tested and shown in Fig. 4. Fig. 4a shows the cyclic voltammograms of MOR on Pt/C–V8C7 (rods), Pt/C–V8C7 (particles) and commercial Pt/C electrocatalysts. It can be seen that the onset potential of these electrocatalysts is in the following order: Pt/C–V8C7 (rods) (+0.25 V) < Pt/C–V8C7 (particles) (+0.27 V) < commercial Pt/C (+0.39 V). The mass current densities are in the following order: Pt/C–V8C7 (rods) (1605 mA mgPt−1) > Pt/C–V8C7 (particles) (1377 mA mgPt−1) > commercial Pt/C (775 mA mgPt−1). And the corresponding mass current density ratio is 2.07
:
1.78
:
1. Significantly, the onset potential for methanol oxidation on Pt/C–V8C7 (rods) was negatively shifted for 140 mV compared with that on Pt/C. This is a great improvement since a direct methanol fuel cell gives only less than 0.5 V output at reasonable current density, leading to an expected 28% improvement in electric efficiency. Fig. 4b shows the electrochemical active surface areas (EASAs) of the electrodes. The EASA is in the following order: Pt/C–V8C7 (rods) (62.0 m2 g−1) > Pt/C–V8C7 (particles) (50.1 m2 g−1) > commercial Pt/C (44.7 m2 g−1). And the corresponding EASA ratio is 1.39
:
1.12
:
1. It can be seen that the mass current density ratio (2.07
:
1.78
:
1) is larger than the EASA ratio (1.39
:
1.12
:
1), that is to say, the EASA is not the sole factor to determine the catalytic performances. By comparing the ingredients of Pt/C–V8C7 and Pt/C, it can be deduced that the other factor to increase the catalytic activity of Pt/C–V8C7 should be the promotion effect of V8C7 on Pt. As to the higher activity of Pt/C–V8C7 (rods) than that of Pt/C–V8C7 (particles), it is related to the smaller size of V8C7 rods, which have higher specific surface area or more sites to interact with the Pt particles. Significantly, it is very energy-efficient that the Pt/C–V8C7 (rods) has only one-tenth V8C7 content that of the Pt/C–V8C7 (particles). More significantly, the enhancement of the current densities at lower potentials was much higher as shown in Fig. 4c, showing that the ratio of the current density on Pt/C–V8C7 (rods) over the current density on Pt/C exceeds 9 at 0.4 V.
 |
| Fig. 4 The cyclic voltammograms on Pt/C–V8C7 (rods), Pt/C–V8C7 (particles) and Pt/C electrocatalysts in (a) 0.5 mol L−1 H2SO4/1.0 mol L−1 methanol solution and (b) 0.5 mol L−1 H2SO4 solution, with the scan rate of 50 mV s−1 at 30 °C; (c) the plot of the ratio of the current density on Pt/C–V8C7 (rods) to that on Pt/C. | |
The stabilities of the Pt/C–V8C7 (rods) and Pt/C electrodes for MOR are shown in Fig. 5. The shadows in Fig. 5 are the cycling difference between the 1st cycle and the 2000th cycle. It is clear that the activity of the commercial Pt/C reduced 27.7% from 775 mA mgPt−1 to 560 mA mgPt−1 for MOR by comparing the peak current density. However, the activity of the Pt/C–V8C7 (rods) reduced 9.4% from 1605 mA mgPt−1 to 1470 mA mgPt−1. The results indicate that the Pt/C–V8C7 (rods) electrocatalyst is more stable than the commercial Pt/C.
 |
| Fig. 5 The cyclic voltammograms on Pt/C–V8C7 (rods) and Pt/C electrodes in (a) 0.5 mol L−1 H2SO4/1.0 mol L−1 methanol solution and (b) 0.5 mol L−1 H2SO4 solution, with the scan rate of 50 mV s−1 at 30 °C. The shadows show the difference between the 1st cycle and the 2000th cycle. | |
Literature reported that electron transfer (synergistic effect) exists between carbides and the loaded noble metals, which not only improves the oxidation of methanol and the intermediate poisons due to easy electron-transfer,1 but also increases the stability due to increased linkage strength between carbides and noble metals.24 The synergistic effect may account for the promotion effect of V8C7 on the excellent activity and stability of the Pt/C–V8C7 (rods) electrocatalyst.
4. Conclusions
Angstrom-scale V8C7 rods have been successfully synthesized through an ion-exchange route. The angstrom-scale C–V8C7 (rods) show higher promotion effect than nanoscale C–V8C7 (particles) on the performance of Pt electrocatalysts, although the former has only one-tenth V8C7 content that of the latter. Moreover, the Pt/C–V8C7 (rods) electrocatalyst shows much higher activity and stability than the commercial Pt/C for MOR.
Acknowledgements
This work was funded by National Natural Science Foundations of China (21306067), China Postdoctoral Science Foundation (2014T70481), Natural Science Foundation of Jiangsu (BK20130490, BK20140531), Industry High Technology Foundation of Jiangsu (BE2013090) and Zhenjiang Industry Supporting Plan (GY2013023).
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