Suqin
Ci
ab,
Jianping
Zou
a,
Guisheng
Zeng
a,
Qiang
Peng
a,
Shenglian
Luo
*a and
Zhenhai
Wen
*ab
aKey Laboratory of Jiangxi Province for Ecological Diagnosis-Remediation and Pollution Control, Nanchang Hangkong University, Nanchang, 330063, Jiang Xi, China
bDepartment of Mechanical Engineering, University of Wisconsin-Milwaukee, 3200 North Cramer Street, Milwaukee, Wisconsin 53211, USA. E-mail: wenzhenhai@yahoo.cn; sllou@hnu.cn; Fax: 1-414-229-6958; Tel: 1-414-229 3370
First published on 27th March 2012
A facile strategy has been developed to realize the controllable synthesis of single crystalline NiO nanoflakes. According to the SEM, TEM and BET analysis, it was found that the m-NiO nanoflakes have a hexagonal structure with an average pore diameter of 4.4 nm, and exhibit a high surface area of 113.4 m2 g−1 and a pore volume around 0.142 cm3 g−1. The m-NiO nanoflakes exhibit a significantly improved electrochemical performance as an anode of lithium-ion batteries (LIBs) compared with bulk NiO based on cyclic voltammograms and galvanostatic measurement. Additionally, the m-NiO nanoflakes showed remarkable advanced activity for catalyzing oxygen reduction reaction (ORR ) relative to the bulk NiO electrode and the bare electrode. Further, rotating disk electrodes demonstrated that the m-NiO nanoflakes, as the support of the Pt nanoparticles, shows significantly improved activity for ORRs.
Nickel oxide (NiO), as an important transition metal oxide with a p-type semiconductor, has received large amounts of research interest and has been considered as one of the promising materials in fuel cells, advanced batteries, supercapacitors, dye-sensitized photocathodes, optics, and catalysis fields, etc.7–10 Therefore, it is highly desirable to develop a controllable and convenient method to fabricate unique NiO nanostructures and explore their functional properties.11–16 Previous studies on these NiO nanostructures suggest that the controlled growth of NiO nanocrystals usually leads to gradual changes in morphologies and crystal structures, and even alter the physical or chemical properties of the NiO nanocrystals.17,18 To get high quality nanocrystals and achieve porous nanostructures, one usually needs to modulate the growth dynamics of nanocrystals with a certain reaction system. For example, the synthesis of single crystalline NiO nanosheets could be prepared by hydrothermal treatment of nickel acetate and methylamine at a relatively low temperature. However, it is still a big challenge to realize the controlling of the morphology and porous structure if organic sources were not used in the system. 7
Herein, we reported a facile route to the controllable synthesis of single crystalline NiO mesoporous-flake nanostructures. The primary electrochemical measurement revealed that, in comparison with the bulk NiO, the mesoporous NiO (m-NiO) nanoflakes exhibited considerably improved electrochemical properties as both an anode of lithium ion batteries (LIBs) and as the electrocatalyst for oxygen reduction reaction (ORR).
The Pt nanoparticles were prepared using H2PtCl6 as the Pt source and ethylene glycol (EG) as the reducing agent. Typically, 10 mL 0.1 M H2PtCl6 was slowly dropped into 50 mL of EG under intense stirring. The mixed solution was refluxed in a flask at 110 °C under continuous stirring under a nitrogen atmosphere for 2 h. The Pt nanoparticles were then collected by centrifugation followed by washing with ethanol and deionized water, and drying 80 °C. For the synthesis of the m-NiO nanoflakes supported Pt nanoparticles (Pt/m-NiO nanoflakes), 40 mg m-NiO nanoflakes were dispersed in 1.0 mL ethanol solution under sonication, then 10 mg Pt nanoparticles were added to the mixture under vigorous stirring followed by sonicating for 1 h. Note: The mixture was used for preparing the Pt/m-NiO nanoflakes directly after adding 50 μL Nafion solution (5%).
Fig. 1 TEM images of the NiO series synthesized at different conditions. (a) 110 °C (0.01 M CTAB, 5 h); (b) 110 °C (0.02 M CTAB, 10 h); (c) 110 °C (0.01 M CTAB, 15 h); (d) 150 °C (0.02 M CTAB, 15 h), (e) 110 °C (0.03 M CTAB, 15 h); (f, g) 150 °C (0.03 M CTAB, 15 h); (h) SEM of the m-NiO nanoflakes; (i) SAED of the m-NiO nanoflakes. |
When the reaction temperature was tuned at 150 °C, the as-prepared NiO nanostructures were enlarged possibly due to the fast nucleation or growth processes induced by high temperature (Fig. 1d–f). The mixed morphologies (nanorods and nanoflakes) were also observed with low concentration of CTAB or short period of reaction time (Fig. 1d and 1e). Fig. 1f exhibits the TEM image of the products with “pure phase” m-NiO nanoflakes that obtained at 150 °C with 0.03 M CTAB for 15 h, suggesting that the m-NiO nanoflakes have a size range of 50–100 nm and uniform porous structures. Through the observation of magnified TEM image, it was found that most of the NiO nanoflakes possessed a hexagonal shape with crystalline size of around 5.8 nm and unspecified porous structure (Fig. 1g). Fig. 1h displays the SEM image of the m-NiO nanoflakes, further confirming that the as-prepared m-NiO nanoflakes have a uniform size and flake morphology. Selected area electron diffraction (SAED) proves that the mesoporous NiO nanoflakes had a single crystalline (Fig. 1i).
According to the controlled conditions experiments, a possible mechanism was proposed to explain the formation of m-NiO nanoflakes. At first, the hydrolysis of urea would slowly release OH− under solvothermal conditions; then, Ni(OH)2 would be formed when the Ni2+ met with the produced OH− from hydrolysis of urea through the organization between these ions and the surfactant CTAB. After heat treatment at 450 °C, the NiO nanoflakes with disordered porous structures were formed, attributing to the removal of CTAB and the dehydration reaction. All of the reactions involved during the processes are as following:
CO(NH2)2 + 3H2O → 2OH− + 2NH4+ + CO2 | (1) |
2OH− + Ni2+ →Ni(OH)2 | (2) |
Ni(OH)2 → NiO + H2O | (3) |
Fig. 2a shows the powder X-ray diffraction pattern of the m-NiO nanoflakes. Three broad peaks at 2θ = 37.2°, 43.2° and 62.6° can be assigned to (111), (200), (220) planes, respectively, which can be well indexed as the cubic structures of NiO with a cell parameter of a = 4.177 Å (JCPDS no. 47–1049). The NiO nanocrystalline size was evaluated to be 6.3 nm based on the Scherrer formula, which was basically consistent with the above TEM result. The low-angle XRD pattern (Fig. 2b) shows at least 2 diffraction peaks, one broad diffraction peak in the range of 0.7–1.0° (2θ) was present in the low-angle region, and another peak centered at around 1.5° (2θ), confirming that the m-NiO nanoflakes possess mesovoids without long-range orders. The nitrogen isotherm curve of the m-NiO nanoflakes through N2 adsorption measurements is shown in Fig. 2c, which exhibits the type IV isotherm with a distinct hysteresis loop in the range of 0.5 to 0.9 P/P0. According to the IUPAC nomenclature, such a characteristic indicates the different processes between adsorption and desorption from the mesopores. Based on the report of nitrogen adsorption–desorption, the m-NiO nanoflakes exhibit a BET surface area of 113.4 m2 g−1 and a total pore volume of 0.142 cm3 g−1. Pore size distribution was also investigated by using the BJH (Barrett–Joyner–Halenda) method to analyze the pore structures of the as-prepared m-NiO nanoflakes, as presented in Fig. 2d, the peak of the pore size were centered at around 4.4 nm, indicating that the m-NiO nanoflakes have an average pore diameter of 4.4 nm.
Fig. 2 X-ray diffraction patterns (a) and small angle X-ray diffraction patterns (b) of the m-NiO nanoflakes; nitrogen adsorption–desorption isotherms (c) and pore size distribution curve (d) of the m-NiO nanoflakes. |
Li-ion batteries (LIBs) have extensively been applied in portable electronic products due to their high energy density and excellent cycle life. 19–21 Nanomaterials could be a promising candidate as they exhibit higher capacity and improve rate capability, attributing to the short diffusion lengths of the lithium ions, large material/electrolyte contact area and good strain accommodation. 7,21–23 Therefore, it is highly interesting to investigate the electrochemical properties of the m-NiO nanoflakes for lithium storage. 15,24,25
Cyclic voltammograms (CVs) were firstly carried out to compare the electrochemical properties of the bulk NiO and m-NiO nanoflakes as an anode in LIBs. Fig. 3a and 3b display the initial two CVs for the bulk NiO and m-NiO nanoflakes, respectively. Generally, the CV curves are consistent with those reported previously. 11 On one hand, there are two cathodic peaks at around 2.0 V and below to 0.3 V in the first scan, corresponding to the formation of solid electrolyte interface (SEI) and the reduction of NiO to Ni, and during the anodic scan, there two anodic peaks appear at 2.25 V and 0.65 V that indicate the decomposition of Li2O and the electrolyte. On the other hand, there is a pronounced decrease of cathodic current between the first and the second CV in both electrodes, which was also observed in previous NiO-based anode and can be attributed to the irreversible reaction and the formation of SEI layer. Obviously, the m-NiO nanoflakes manifest smaller changes in comparison with the bulk NiO, implying that less capacity is lost in the initial two cycles. Eqn (4)–(5) below describe the possible reaction involved during the processes:
2Li+ + 2e− + NiO ↔ Li2O + Ni | (4) |
2Li ↔ 2Li+ + 2e− | (5) |
2Li + NiO ↔ Li2O + Ni | (6) |
Fig. 3 The initial two cyclic voltamograms of (a) bulk NiO, (b) m-NiO nanoflakes conducted at a sweep rate of 0.1 mV s−1. The first and second charge–discharge profiles for (c) bulk NiO and (d) m-NiO nanoflake LIB anodes at a current density of 50 mA g−1. |
The lithium storage capacity and cyclability were further examined by using galvanostatic charge/discharge cycling method at a current density of 200 mA g−1. As consistent with the CVs results, the initial two charge/discharge curve change significantly, both the potential of the plateau and the capacity show remarkable difference between the first and the second discharge curve (Fig. 3c, d).
Fig. 4 compares the cycling performance and rate capability of the bulk NiO and m-NiO nanoflakes. As expected, the m-NiO nanoflakes behave a significantly improved performance in terms of the capacity, rate capability and stability. First of all, the m-NiO nanoflakes display a capacity of 817.8 mA h g−1 in the first discharge process, this capacity is much higher than that of bulk NiO (647.6 mA h g−1). In addition, the initial capacity loss is about 10.8% in m-NiO nanoflakes, while the bulk NiO shows a distinct fade of discharge capacity in the initial two cycles (around 50% loss). Although the discharge capacity gradually decreased in the subsequent cycling, the m-NiO nanoflakes discharged a capacity of 411.6 mA h g−1 after 20 cycles, which is larger than the theoretical specific capacity of the commercial graphite anode material. However, for the bulk NiO only a capacity of 99.7 mA h g−1 was delivered after 20 cycles. The reversible capacity decreased slowly with increasing current density to 80 mA g−1. Even at a high rate of 100 mA g−1, the m-NiO nanoflakes still delivered a specific capacity above 300 mA h g−1. Moreover, when the current density was tuned back to 50 mA g−1, the m-NiO nanoflakes reached a reversible capacity of around 410 mA h g−1 and maintained this capacity in the following cycles.
Fig. 4 Cyclic performance of bulk NiO (black) and m-NiO nanoflakes (red) at a current density of 50 mA g−1, 80 mA g−1, and 100 mA g−1. |
Electrochemical impedance spectroscopy was performed after 20 cycles to understand the resistance associated with the bulk NiO and the m-NiO nanoflakes. Fig. 5 shows the Nyquist plots recorded for the bulk NiO and the m-NiO nanoflakes, which typically consists of a high frequency semicircle corresponding to the charge–transfer resistances (Rct). Nyquist data were then fitted to a hypothetical equivalent circuit (inset of Fig. 5) to evaluate the Rct and the resistance of the film formed on the electrode surface (Rf). It was revealed that Rct and Rf for the m-NiO nanoflakes was 21.78 Ω and 11.63 Ω, respectively, lower than the corresponding Rct (31.95) and Rf (12.01) of the bulk NiO electrode, indicating that the m-NiO nanoflakes can significantly decrease the total impedances, which might be one reason for the m-NiO nanoflakes achieving improved electrochemical performance.
Fig. 5 The Nyquist curve of the LIB with NiO (black) and m-NiO nanoflakes (red) as the working electrode. Inset is the equivalent circuit to the corresponding LIBs. |
The oxygen reduction reaction (ORR) has been of widespread attention due to its significant role in fuel-cell and metal–air battery systems. 26–28 Various strategies, especially exploring the non-precious or decreased precious metal catalysts, have been proposed for improving the sluggish kinetics of the ORR. 29–31 The preliminary results herein show that the m-NiO nanoflakes can somehow advance the catalytic activity of the ORR, as compared to the bare glassy carbon (GC) electrode and bulk NiO electrode. Furthermore, if loading Pt nanoparticles, the m-NiO nanoflakes make a remarkable improvement for catalyzing the ORR.
CVs were carried out to investigate the electrochemical properties for ORR on m-NiO nanoflakes, the bulk NiO and GC electrodes in 0.5 M KOH electrolyte. Fig. 6a shows CVs recorded from the above three electrodes in N2-saturated electrolyte, respectively. One can observe a significant difference between the NiO modified electrode and GC electrode. On the bare GC electrode, there is no obvious redox peak. For both m-NiO nanoflakes and bulk NiO electrodes, they exhibit a similar CV behavior, in which it was observed that a pair of reversible redox peaks at around 0.25 V was associated with the revisable redox reaction on NiO. Fig. 6b shows a voltammogram curve recorded in O2 saturated 0.5 M KOH solution at the three electrodes. An obvious cathodic peak positioned at about −0.3 V can be observed for the three electrodes, which can be ascribed to the electrochemical reduction of oxygen. Obviously, the cathodic peak current at the m-NiO nanoflakes electrode was much higher than that of the other two electrodes, actually, the peak current (85.6 μA) obtained from the m-NiO nanoflakes electrode was twice that of the bulk NiO electrode (41.4 μA), and four times higher than that of the GC electrode (16.6 μA), suggesting that the m-NiO shows higher activity than the other two electrodes.
Fig. 6 Cyclic voltammograms of the electrodes in N2 (a) and O2 (b) saturated aqueous solution of 0.5 M KOH at a scan rate of 50 mV s−1: m-NiO nanoflakes/GC (red), bulk NiO/GC (blue); bare GC (black) electrode. |
Fig. 7 shows typical current density–time responses for the ORR measured at a fixed potential of −0.30 V in O2 saturated 0.5 M KOH solution at the m-NiO nanoflakes, the bulk NiO and bare GC electrodes, respectively. As expected, the current at m-NiO nanoflakes electrode was evidently higher than the other two electrodes. In the steady state region, the m-NiO nanoflakes electrode presented the highest steady-state current (7.5 × 10−6 A). While the bulk NiO and GC electrode exhibited only a steady-state current of about 4.1 × 10−6 A and 2.6 × 10−6 A respectively. This result further demonstrated that the m-NiO nanoflakes had a higher activity and better stability when used as the electrode of ORRs.
Fig. 7 Current–time curves of (1) bare GC electrodes, (2) bulk NiO and (3) m-NiO nanoflakes in O2 saturated 0.05 M KOH at a fixed potential of −0.3 V. |
The m-NiO nanoflakes did show a promising route to advance the activity of the ORR, possibly due to its unique structure and large surface area. It should be noted that Pt nanoparticles in the Pt/Fe3O4 nanostructures were reported to show a significant increase in mass activity toward ORR compared with the single component Pt nanoparticles. 32
Fig. 8a,b shows the TEM images of the Pt nanoparticles and the Pt/m-NiO nanoflakes, respectively, one can observe the as-prepared Pt nanoparticles are in the range of 2–5 nm (Fig. 8a), and the Pt nanoparticles were well distributed on the surface of m-NiO nanoflakes (Fig. 8b). The electrochemically active surface area (EASA) was evaluated through the hydrogen adsorption region of CVs technique in 0.5 M KOH, it was found that the Pt/m-NiO flakes shows a slight higher EASA than pure Pt nanoparticles, the larger EASA for the former was possibly attributed to the highly dispersed Pt nanoparticles on m-NiO flakes.
Fig. 8 TEM images (a) Pt nanoparticles and (b) Pt/m-NiO nanoflakes. |
The electrochemical catalytic activity for ORR in Pt nanoparticles and Pt/m-NiO nanoflakes were then characterized by the rotating disk electrode measurement performed in 0.5 M KOH aqueous solution, as shown in Fig. 9a. Both electrodes exhibit similar polarization curves. Although the Pt mass loading at the Pt/m-NiO nanoflakes electrode is only one fifth of the Pt nanoparticle electrode, the former manifests a slightly higher limited current density, proving that the Pt/m-NiO nanoflakes show 5 fold increase in mass activity toward ORR, as compared with the Pt nanoparticles. Fig. 9b–c presents the RDE voltammograms and the corresponding Koutecky–Levich plots, respectively. The inverse current density (j−1) shows good linearity and parallelism as a function of the inverse of the square root of the rotation rate (ω−1/2) at different potentials, indicating consistent electron transfer and the first-order kinetics with respect to the ORR. Based on the Koutecky–Levich equation, the kinetic current density at −0.20 V was calculated to be 17.9 mA cm−2 based on the intercept of the Koutecky–Levich plots, which is 2 times higher than that of the Pt nanoparticle catalyst (7.20 mA cm−2), and is even higher than that of the Pt/C catalysts (14.20 mA cm−2).33 We further studied the ORR polarization curves for the Pt/m-NiO nanoflakes before and after 100 cycles to evaluate their stability for catalyzing the ORR. After 100 cycles, there was only a 6 mV negative-shift in the half-wave potential on the Pt/m-NiO nanoflakes (Fig. 9d), signifying that the m-NiO nanoflakes supports and also possesses excellent long-term stability. Since the m-NiO nanoflakes not only had a large surface area and showed improved kinetics for the ORR, the synergetic interactions between Pt and m-NiO may lead to higher electron population on Pt, resulting in more activity toward the ORR than the Pt nanoparticle catalyst. It is reasonable to envisage that an optimal catalytic performance for the ORR can be obtained after depositing the Pt nanoparticles on the surface of the m-NiO nanoflakes.
Fig. 9 The ORR curves for Pt and Pt/m-NiO nanoflakes through RDE measurements with a rotation speed of 1600 rpm and a scanning rate of 5 mV s−1 in 0.5 M KOH (a); the polarization curves of Pt/m-NiO nanoflakes ORR at different rotating rates (b); Koutecky–Levich (K–L) plot of current density versus w−1/2 at different potentials on the Pt/m-NiO nanoflakes electrode (c); The linear-sweep voltammograms recorded after 0 and 100 CVs cycles in O2 saturated 0.5 M KOH with 1600 rpm and a scan rate of 5 mV s−1 on the Pt/m-NiO nanoflakes, CVs range: −0.8 ∼ 0.4 V, scan rate, 0.1 V s−1 (d). |
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