3-Dimensional TiO2 nanostructure supports and their improved electrochemical properties in methanol electrooxidation

Jae-Kyung Oh a, Young-Woo Lee a, Sang-Beom Han a, A-Ra Ko a, Do-Young Kim a, Hyun-Su Kim a, Si-Jin Kim a, Bumwook Roh b, Inchul Hwang b and Kyung-Won Park *a
aDepartment of Chemical and Environmental Engineering, Soongsil University, Seoul 156743, Republic of Korea. E-mail: kwpark@ssu.ac.kr; Fax: +82 (2) 813 0613; Tel: +82 (2) 812 5378
bHyundai Motor Company, Mabuk-Ri, Gyeonggi-Do, Republic of Korea

Received 23rd February 2011 , Accepted 7th April 2011

First published on 28th April 2011


Abstract

The TiO2 nanostructure support consists of backbones and branches of a rutile phase forming a 3-dimensional structure with high specific surface area. The Pt catalysts on the TiO2 nanostructure supports exhibit much improved electrocatalytic activity and stability toward methanol electrooxidation in comparison with conventional Pt/C.


Direct methanol fuel cells (DMFCs) have been of considerable interest because of a variety of merits such as low operating temperatures, high energy density of methanol, and applications to micro-sized fuel cells.1–3 However, the main issue in the DMFCs is to find catalysts and support materials suitable for excellent catalytic activity and stability. In general, carbon supported Pt-based catalysts have been widely used as a representative anode structure in DMFCs.

However, carbon support materials exhibit corrosion of carbon and weak interaction between catalysts and supports despite highly excellent electronic conductivity resulting in serious agglomeration of catalysts during electrochemical reactions.4 Thus, in particular, transition metal oxides such as TiO2, WO3, SnO2, RuO2, and Ta2O5 have been reported as alternatives to carbon supports to enhance the catalytic activity and stability for methanol electrooxidation.5 Among them, TiO2 has been potentially attractive as a candidate of support due to strong catalyst–support interaction, stability in the fuel cell operation atmosphere, and commercial availability.6

Recently, there have been many literatures of novel support materials with highly active surface areas such as meso-porous structures and 2-dimensional or 3-dimensional structures for high dispersion of catalysts on supports.7 Herein, we synthesized a 3-dimensional TiO2 nanostructure support by means of a seeding method with 1-dimensional TiO2 nanowires as a seed.8 The TiO2 nanostructure support can have high specific surface area and improved electronic transfer efficiency. The formation mechanism of the TiO2 nanostructure support is shown in Scheme S1, ESI. The order of growth rate of a rutile TiO2 structure is V〈110〉 < V〈100〉 < V〈101〉 < V〈001〉 < V〈111〉. Accordingly, the {001} and {111} facets disappear while {110}, {100}, and {101} facets are easily exposed during the growth process. As a result, the TiO2 nanobranch and nanowire with a rutile phase are exposed to {110} and {101} facets (Fig. 1(a) and (b)). The TiO2 nanobranch support exhibits a 3.23 times higher surface area (109 m2 g−1) than that of the TiO2 nanowire (34 m2 g−1) because of the 3-dimensional branch-type structure of the as-synthesized TiO2. To evaluate electrocatalytic properties of the electrode for the fuel cell, we prepared Pt catalyst on the branch-type TiO2 support (Pt/TiO2-NB) by polyol process using ethylene glycol with NaOH (Experimental section, ESI).


(a) TEM image of the TiO2-NB supports. (b) High-resolution TEM image of the TiO2-NB supports. [The inset indicates the FFT pattern of the TiO2-NB as backbone and branch.] (c) TEM image of the Pt nanoparticles deposited on the TiO2-NB supports. (d) Size distribution of deposited Pt nanoparticles. (e) High-resolution TEM images and FFT patterns of deposited Pt on the TiO2-NB supports.
Fig. 1 (a) TEM image of the TiO2-NB supports. (b) High-resolution TEM image of the TiO2-NB supports. [The inset indicates the FFT pattern of the TiO2-NB as backbone and branch.] (c) TEM image of the Pt nanoparticles deposited on the TiO2-NB supports. (d) Size distribution of deposited Pt nanoparticles. (e) High-resolution TEM images and FFT patterns of deposited Pt on the TiO2-NB supports.

Fig. 1(c) shows TEM image of as-synthesized Pt (40 wt%) nanoparticles (NPs) on the TiO2-NB supports. The average particle size of the Pt NPs is ∼3.49 nm (Fig. 1(d)). The Pt NPs are well dispersed on branches and backbones of the TiO2-NB supports. As shown in Fig. 1(e), the TiO2-NB (marked as 1 and 2) represents the {110} and {101} facets with d-spacings of 0.325 nm and 0.249 nm of the TiO2 rutile phase, respectively. The polycrystalline Pt NPs (marked as 3 and 4) represent the {111} facets with a d-spacing of 0.227 nm in the Pt metallic phase with a face-centered-cubic crystal structure.

Fig. 2 shows cyclic voltammograms (CVs) of the supported catalysts during 400 cycles between −0.2 to 1.0 V in 0.1 M HClO4. The electrochemical active surface areas (EASAs) of the Pt catalysts were measured by integrating hydrogen desorption regions (assuming 210 μC cm−2 of a polycrystalline Pt electrode) in 0.1 M HClO4 solution. In the case of the Pt/C, the EASAs after the stability test seriously decrease, that is, the reduction of 90.4% from the initial value. In contrast, the Pt/TiO2-NB displays the reduced EASAs of 54.1% after the durability test. This represents that the improved electrochemical properties of the Pt/TiO2-NB may be mainly due to the stability of the TiO2-NB support as compared to the carbon in the Pt/C.


(a) and (b) Cyclic voltammogram (CV) properties as a stability test from the initial cycle to 400 cycles of Pt/C (E-TEK) and Pt/TiO2-NB in 0.1 M HClO4 with a scan rate of 50 mV s−1 at 25 °C. (c) Reducing rates of electrochemical active surface areas (EASAs) of catalysts related to Pt catalytic surface area with the increased cycles.
Fig. 2 (a) and (b) Cyclic voltammogram (CV) properties as a stability test from the initial cycle to 400 cycles of Pt/C (E-TEK) and Pt/TiO2-NB in 0.1 M HClO4 with a scan rate of 50 mV s−1 at 25 °C. (c) Reducing rates of electrochemical active surface areas (EASAs) of catalysts related to Pt catalytic surface area with the increased cycles.

To compare electrochemical properties of the as-prepared catalysts toward methanol electrooxidation, CVs were obtained in 0.1 M HClO4 + 2.0 M CH3OH solution (Fig. 3). The onset potential of the Pt/NB-TiO2 (+0.11 V) is lower than that of the Pt/C (+0.14 V). In the forward scan, peak potentials in methanol electrooxidation are +0.72 and +0.76 V for the Pt/TiO2-NB and Pt/C, respectively. The more negative peak potential of the Pt/TiO2-NB indicates an excellent activity in comparison with the Pt/C. Also, the Pt/TiO2-NB for methanol electrooxidation shows a 2.17 times higher forward anodic peak current density (3.54 mA cm−2) than that of the Pt/C (1.63 mA cm−2). The Pt/TiO2-NB indicates an excellent electrocatalytic activity during methanol electrooxidation in comparison with the Pt/C. Furthermore, the Pt/TiO2-NB maintains higher catalytic activity than that of the Pt/C in methanol electrooxidation after the cycling test (Fig. 3). After the 400 cycles, the electrooxidation current density of the Pt/TiO2-NB (1.80 mA cm−2) at 0.6 V is still higher than that of the Pt/C (0.21 mA cm−2). Also, in the forward anodic peak after the cycling test, the Pt/TiO2-NB shows slightly reduced current density (27.7%) for methanol electrooxidation. In contrast, the Pt/C exhibits the abruptly reduced current density (80.9%) for methanol electrooxidation.



          Cyclic voltammograms (CVs) before and after the stability test of (a) Pt/TiO2-NB and (b) Pt/C in 0.1 M HClO4 + 2 M CH3OH with a scan rate of 50 mV s−1 at 25 °C. To evaluate electrochemical stability of the catalysts, the 400 cycle CVs of the catalysts were carried out in 0.1 M HClO4.
Fig. 3 Cyclic voltammograms (CVs) before and after the stability test of (a) Pt/TiO2-NB and (b) Pt/C in 0.1 M HClO4 + 2 M CH3OH with a scan rate of 50 mV s−1 at 25 °C. To evaluate electrochemical stability of the catalysts, the 400 cycle CVs of the catalysts were carried out in 0.1 M HClO4.

The Pt/C after the cycling test (Fig. 4(a) and (b)) shows a larger average size of 4.85 nm and wider size distribution than those of the Pt/C before the cycling test (Fig. S1, ESI) resulting in deteriorated electrocatalytic properties for methanol electrooxidation. On the other hand, the Pt/TiO2-NB maintains the size distribution and morphology of the catalysts after the cycling test (Fig. 4(c) and (d)) resulting in enhanced electrocatalytic properties. In particular, it has been reported that the rutile phase of TiO2 may exhibit an excellent durability and the existence of rutile TiO2 can be beneficial to the formation of the surface structures of metallic catalysts favorable for catalytic properties.9 Accordingly, the superior electrocatalytic activity and stability of the Pt/TiO2-NB for methanol electrooxidation may be due to the rutile phase and the 3-dimensional nanostructure of the TiO2-NB support. Thus, it is concluded that the TiO2-NB support may be a promising support for the DMFCs. However, the membrane–electrode-assembly (MEA) using the TiO2-NB supported catalysts will be applied to the DMFCs for our further works.



          TEM images and particle size distribution of Pt/C after the durability test (a), (b). [The inset indicates the FFT pattern of the Pt NP.] TEM images and particle size distribution of Pt/TiO2-NB after the durability test (c), (d). [The inset indicates the FFT pattern of the TiO2-NB support and Pt NP.]
Fig. 4 TEM images and particle size distribution of Pt/C after the durability test (a), (b). [The inset indicates the FFT pattern of the Pt NP.] TEM images and particle size distribution of Pt/TiO2-NB after the durability test (c), (d). [The inset indicates the FFT pattern of the TiO2-NB support and Pt NP.]

In summary, we have reported the TiO2 nanostructure material for electrocatalytic reactions. The as-synthesized TiO2 supports have exhibited relatively high surface area with a 3-dimensional branch-type structure. The Pt/TiO2-NB exhibits much improved electrocatalytic properties for methanol electrooxidation because of the stable TiO2 nanostructure supports.

This work was supported by New & Renewable Energy R&D program (2008-N-FC12-J-01-2-100) and the “program for CITG” support program supervised by the NIPA (National IT Industry Promotion Agency) (NIPA-2010-0004).

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Footnotes

Electronic supplementary information (ESI) available: Experimental section and supplementary data. See DOI: 10.1039/c1cy00060h
These authors contributed equally to this work.

This journal is © The Royal Society of Chemistry 2011