Lieyuan Huangb,
Xingbo Ge*ab and
Shuai Dongb
aState Key Laboratory of Oil and Gas Reservoir Geology and Exploitation, Southwest Petroleum University, Chengdu 610500, P. R. China. E-mail: xbge@swpu.edu.cn; Tel: +86-28-83037337
bThe Center of New Energy Materials and Technology, School of Chemistry and Chemical Engineering, Southwest Petroleum University, Chengdu 610500, China
First published on 27th June 2017
Cost-efficient, active, and durable electrocatalysts are highly desired to facilitate the oxygen evolution reaction (OER) for water splitting. On the basis of a Ni hexacyanoferrate (NiHCF) Prussian blue-type coordination polymer, a facile route was developed to fabricate robust Ni/Fe composites for the OER in alkaline electrolyte. The obtained catalysts were characterized by SEM, XRD, FTIR, EDS and XPS methods, and the catalytic activity was evaluated by the electrochemical technique. The Ni/Fe catalyst, which was identified as mixed Ni/Fe oxides, afforded an OER onset overpotential of 310 mV and a Tafel slope of ∼44 mV per decade in alkaline medium. The Ni/Fe composite also exhibits excellent durability in the electrocatalysis process. No obvious degradation of the OER catalytic density was observed during the cyclic voltammetry (CV) process.
Ni/Fe-based composites have been known as active OER catalysts since 1980s,11 and renewed interest has been witnessed in recent years on developing Ni/Fe-based materials for better activity and stability.12–16 Many approaches, including electrodeposition, hydrothermal synthesis method, and photochemical metal–organic deposition etc., have been exploited to construct Ni/Fe oxides/or hydroxides as advanced OER catalysts. For example, the cathodically electrodeposited Ni/Fe alloy films, would be oxidized to oxides/or hydroxides layers under the OER condition (or just in the air), serving as OER active electrodes.12,17–19 Adopting this electrodeposition strategy, McCrory et al. evaluated the OER activity of a series of heterogeneous electrocatalysts and found Ni/Fe-based composites stood out among all non-precious metal catalysts in concentrated alkaline conditions.8,20 The chemical-hydrothermal or co-deposition method was also extensively reported to synthesize Ni/Fe oxides films,21 nanoparticles,22–24 Ni/Fe double hydroxide hybrids,25–29 and their high OER activity have been demonstrated. Recently, by combining photochemical metal–organic deposition and post annealing treatment, Smith et al. has successfully prepared amorphous Ni/Fe oxide thin films, exhibiting a superior OER activity compared to other Ni or Fe based electrocatalysts.30,31 Qiao et al. have in situ grown the nitrogen doped NiFe double layered hydroxide nanolayers on 3D nickel foam, thus achieved an extremely high OER catalytic activity.32 In spite of these progress, new catalysts and synthetic methods should be explored to fabricate more candidates for OER.
Prussian blue-type coordination polymers (PBs) are a type of versatile materials, which were extensively applied in magnetism,33,34 electrochromism,35 biosensors,36 catalysis37,38 and sodium-ion batteries.39,40 Due to its porosity, well-controlled morphology and compositions, PBs can be recognized as promising candidates for water oxidation catalysts. Very recently, PBs were served as precursors to prepare nanoporous metal oxide materials, which exhibited promising water oxidation activity in both neutral and basic media.41–43 Since PBs have three-dimensional open architecture, and taking account of the high activity of Ni/Fe composites, it would be worth addressing a detailed research on Ni hexacyanoferrates (NiHCF) as new efficient OER catalyst.
Herein, on the basis of NiHCF, we reported a facile route to fabricate active Ni/Fe composite as efficient OER electrocatalyst in alkaline medium. It was found that the structure and properties of the Ni/Fe composite could be tuned by varying the annealing condition. The optimized Ni/Fe composites exhibit enhanced activity and durability for OER.
The fabrication of Ni/Fe composites was realized by annealing the NiHCF precursor under various temperatures, ranging from 150 to 600 °C. All of the precursors were annealed under the selected temperature for 2 h with a ramp of 10 °C min−1. Hereafter, the samples made by annealing treatment would be named as “involved metals + heated temperature”. For instance, NiHCF annealed at 300 °C would be expressed as “Ni/Fe-300”.
The turnover frequency (TOF) was calculated according to equation: TOF = j × A/(4 × F × m), where j is the current density obtained at overpotential of 400 mV in A cm−2, A is the surface area of the electrode, F is the Faraday efficiency (96485 C mol−1) and m is the number of moles of the Ni2+ deposited onto the electrodes.
Fig. 1 XRD patterns of the as-prepared Ni hexacyanoferrate (NiHCF) and the annealed samples. The peaks beneath “*” attribute to Fe3O4 (JCPDF 28-0491). |
The chemical evolution of Ni/Fe samples were detected by FTIR spectroscopy, as shown in Fig. 2. Two absorption bands at 2165 cm−1 and 2097 cm−1 for both NiHCF and Ni/Fe-150 samples could be indexed to the CN stretching mode (Fe–CN–Ni) and the typical cyanide linkage isomerism pattern of NiHCF, respectively.33,37 These two absorption bands disappear at 300 °C, suggesting the decomposition of NiHCF. This observation is in line with the XRD results. Besides, the bending vibration appears at 1610 cm−1 could be ascribed to water molecular, and the bands ranging at 1000–1400 cm−1 can be assigned to M–O mode.44
The morphology and microstructure of the prepared catalysts were observed by SEM. Fig. 3 shows the SEM images of NiHCF, Ni/Fe-300 and Ni/Fe-600. All of the samples show an agglomerate of nanoparticles with diameter of 50–200 nm. EDS results suggest the atom ratio of Ni/Fe in the Ni/Fe composites is ca. 1.2, slightly higher than the initial ratio of Ni2+/[Fe(CN)6]3− (1:1).
Fig. 3 SEM images of the (a) as-prepared NiHCF, (b) NiHCF annealed at 300 °C and (c) 600 °C. The scale bars are 500 nm. |
The chemical and electronic states of Ni/Fe composites were investigated by XPS (Fig. 4). The XPS survey spectra (Fig. 4a) show the expected photoelectron peaks due to Ni, Fe, and O elements in three samples. The N 1s peak is only detected in NiHCF, which could be ascribed to Fe–CN–Ni group (FTIR).
Fig. 4 XPS spectra of the as-prepared NiHCF and the annealed samples: (a) survey, (b) Ni 2p, (c) Fe 2p and (d) O 1s. |
Additionally, the Ni 2p (Fig. 4b) and Fe 2p (Fig. 4c) spectra of NiHCF could be assigned to Ni hexacyanoferrate,45 thus confirmed the synthesis of Ni–Fe Prussian blue analogue. The two fitted peaks located at 855.2 eV and 856.5 eV for Ni 2p3/2 of Ni/Fe-300 (Fig. 4b) could be assigned to Ni2+ in NiFe2O4 and NiO, respectively,46,47 which consistent with the XRD results. For Ni/Fe-600 sample, the Ni 2p3/2 peaks shift to 856.1 eV and 857.8 eV, indicating the change of surface electronic state. The Fe 2p spectrum (Fig. 4c) of Ni/Fe-300 presented two peaks at the binding energy of 711.2 eV and 724.4 eV, which belong to the Fe 2p3/2 and Fe 2p1/2 of Fe3+.48 These Fe 2p3/2 and Fe 2p1/2 peaks have positively shifted in Ni/F-600 sample. The shift of Ni 2p and Fe 2p peaks in Ni/Fe-600 sample might be relevant to the appearance of O vacancy in the composites, which could be identified by the O 1s XPS spectra. As shown in O 1s spectra (Fig. 4d), the symmetrical O 1s peak for NiHCF at binding energy of 532.4 eV could be assigned to chemisorbed oxygen species. The O 1s region of Ni/Fe-300 catalyst could be fitted to two individual peaks. The O 1s at 530.2 eV is typically for metal–oxygen bonds, and the 531.8 eV peak can be attributed to OH adsorbed groups. For Ni/Fe-600 sample, the O 1s peaks at the binding energy of 529.6 eV and 530.9 eV could be assigned to the lattice oxygen and oxygen vacancy, respectively.49,50 The difference of relative intensity of the two peaks in two samples indicates the changes of the structure and surface properties with the variation of the annealing temperature.
To evaluate the OER activity of the as-prepared catalysts, the Ni/Fe composites were loaded onto ITO electrodes and investigated using electrochemical CV technique in 0.1 M KOH (pH 13) electrolyte at a constant scan rate of 20 mV s−1. Fig. 5a show a group of iR-compensated CV curves of Ni/Fe catalysts. While bare ITO electrode is inactive towards OER, all the samples show obvious OER activity. For NiHCF, a pair of redox peaks clearly shows up at 1.16–1.23 V, which could be assigned to [Fe(CN)6]3−/[Fe(CN)6]4− couple in the coordination polymer. These redox peaks decrease in intensity with the annealing temperature, and disappear at Ni/Fe-300 sample, further verify the complete decomposition of the NiHCF polymer. Although annealing at 150 °C did not change the crystalline structure of NiHCF, Ni/Fe-150 sample exhibits enhanced OER activity. The highest electrocatalytic activity was observed on Ni/Fe-300, with an onset overpotential as low as 310 mV, and a further increase of the annealing temperature inversely results in a decrease of the OER activity. The potentials required for the current of 1 mA cm−2, 5 mA cm−2 and 10 mA cm−2 were used to further elaborate the OER catalytic activity of Ni/Fe catalysts. The Ni/Fe-300 achieves a small overpotential of 355 mV, 416 mV and 462 at 1 mA cm−2, 5 mA cm−2 and 10 mA cm−2, respectively. TOF was calculated to illustrate the intrinsic activity of Ni/Fe catalysts (Table 1). We have calculated TOF using the catalyst mass and composition. The TOF of Ni/Fe-300 at overpotential of 400 mV is 0.05 s−1, higher than other annealed samples and comparable to the N–Ni/Fe LDH reported previously.32 The significant improvement in the OER kinetics on Ni/Fe-300 is also demonstrated by the lower Tafel slope of 44 mV dec−1 at low overpotential compared to other samples (Fig. 5b). It is well accepted that a Tafel slope of ∼40 mV dec−1 indicating the rate-determining step (RDS) of the OER reaction is the second electron transfer step from the hydroxylated active site to form the oxide: M–OH + OH− = M–O + H2O + e−, where “M” denotes the active site. While a slope of 60 mV dec−1 indicates that the RDS is a chemical evolution of the unstable M–OH* to form more stable M–OH.51–53 The distinction of Tafel slope between NiHCF and Ni/Fe oxides suggests a different catalytic mechanism.
Fig. 5 (a) iR-compensated CV curves and (b) Tafel plots of the as-prepared NiHCF and the annealed samples in 0.1 M KOH, the inset in (a) is a magnification of CVs from 0.96 V to 1.6 V (vs. RHE). |
Sample | Electrolyte | η onset potential [mV] | η at 1 mA cm−2 [mV] | η at 5 mA cm−2 [mV] | η at 10 mA cm−2 [mV] | Turnover frequency (TOF) at η = 400 mV | Tafel slope [mV dec−1] | Reference |
---|---|---|---|---|---|---|---|---|
NiHCF/ITO | 0.1 M KOH | 364 | 453 | 572 | — | — | 50 | This work |
Ni/Fe-150/ITO | 0.1 M KOH | 341 | 375 | 432 | 476 | 0.03 | 68 | This work |
Ni/Fe-300/ITO | 0.1 M KOH | 310 | 355 | 416 | 462 | 0.05 | 44 | This work |
Ni/Fe-450/ITO | 0.1 M KOH | 342 | 395 | 457 | 507 | 0.02 | 57 | This work |
Ni/Fe-600/ITO | 0.1 M KOH | 370 | 413 | 478 | 532 | 0.01 | 69 | This work |
MWCNTs/Ni(OH)2 | 0.1 M KOH | 322 | 373 | 435 | 474 | — | 87 | 54 |
HU-NiCo2O4/GC | 0.1 M KOH | 316 | — | — | — | — | 51 | 55 |
N–NiFe LDH | 0.1 M KOH | 210 | — | — | 230 | 0.05 | 35 | 32 |
IrO2 | 0.1 M KOH | 300 | — | — | 350 | 0.03 | 23 | 32 |
2D N–NiFe LDH | 0.1 M KOH | 310 | — | — | 390 | 165 | 32 | |
Co, N doped carbon | 0.1 M KOH | — | — | — | 350 | — | 83.3 | 56 |
NG-NiCo | 0.1 M KOH | 350 | — | — | — | — | 614 | 57 |
Fe6Ni10Ox | 1 M KOH | — | — | — | 286 | — | 48 | 22 |
Ni0.69Fe0.31Ox/C | 1 M KOH | — | — | — | 280 | — | 30 | 24 |
Ni2/3Fe1/3–GO | 1 M KOH | — | — | — | 230 | 42 | 28 | |
CQD/NiFe-LDH | 1 M KOH | — | — | — | 235 | — | — | 29 |
Ni–Co PBA | 1 M KOH | — | — | — | 380 | — | 50 | 43 |
The aforementioned results indicate that NiHCF could serve as a promising composite to fabricate active OER catalysts. The as-prepared Ni/Fe-300 afforded superior activity as an OER catalyst, with a lower onset overpotential and Tafel slope than that of the reported MWCNTs/Ni(OH)2 (ref. 54) and hollow urchin-like NiCo2O4 nanoparticle (Table 1).55 Actually, it's difficult to compare the activity of the catalysts prepared by diverse methods directly because of the distinct structure and thus the active surface area. Although the fabricated Ni/Fe catalyst is not as good as same well-studied Ni/Fe catalysts at current density of 10 mA cm−2, it could be compensated by further tailing the catalyst structure or using 3D porous substrate.
In order to compare the intrinsic activity of the Ni/Fe-300 catalyst with the reported results, the OER activity was also measured in 1 M KOH solution. The electrochemically active surface area (ECSA) was used to normalize the catalytic current density. The ECSA is estimated by determining the double-layer capacitance from CV according to the previous reports.8,20 Briefly, the potential is scanned in a nonfaradaic potential window (here is 1.266 V to 1.366 V vs. RHE) at varying scan rates (Fig. 6a). The obtained current plotted against the scan rate at 1.316 V (vs. RHE) gives a straight line (Fig. 6b). The slope of the line is assigned to the electrochemical double layer capacitance (Cdl). Herein, the Cdl adopted the average value of the slope of anodic and cathodic lines, and the ECSA is obtained by dividing Cdl with specific capacitance Cs (0.040 mF cm−2), which is found to be ∼0.1775 cm2. The ECSA normalized CV of Ni/Fe-300 is shown in Fig. 6c, the current density at η = 0.35 V for OER is ∼0.38 mA cm−2, which is superior to the NiOx (0.12 mA cm−2), NiCeOx (0.11 mA cm−2), NiCoOx (0.2 mA cm−2), NiCuOx (0.15 mA cm−2) and comparable to that of IrOx (0.4 mA cm−2).8 More benchmarking parameters of the recently reported catalysts could be found in Table 2. Further improvement of activity might be realized by using ideal supports such as graphene to well disperse the as-prepared catalysts.
The long-term stability of the Ni/Fe-300 catalyst towards the OER was also examined by the cycling and potentiostatic in 0.1 M KOH solution, Fig. 7 shows the OER polarization tests curves measured before and after 1000 CV cycles at a scan rate of 20 mV s−1. After the 1000 cycles, the Ni/Fe-300 catalyst shows a slight loss of current density compared with the initial cycle, indicating the Ni/Fe-300 catalyst is highly stable in a long-term electrochemical OER process. Besides, when biased potentiostatically at a overpotential of 334 mV on the electrode, the Ni/Fe-300 catalyst also afforded a relatively stable catalytic current density for 10 h consecutive electrolysis.
Fig. 7 Durability test for the Ni/Fe-300 (NiHCF annealed at 300 °C) sample by CVs before and after 1000 cycles and the i–t curve (inset) at the overpotential of 334 mV in 0.1 M KOH solution. |
Based on the above experimental results and analysis, we could reasonably discuss the origin of the superior OER activity of the Ni/Fe-300 sample. As confirmed by XRD, FTIR and XPS spectra, the NiHCF is gradually decomposed into Ni/Fe oxides at high temperature, and the Ni/Fe-300 catalyst mainly consists of NiFe2O4 and NiO. Studies suggested that spinel nickel ferrite (NiFe2O4) with Ni2+ occupying the tetrahedral holes and Fe3+ occupying the octahedral holes plays a significant role in improving the oxygen evolution activity of the mixed metal oxide systems.58–60 Therefore, the enhancement of the OER catalytic activity of Ni/Fe-300 could be attributed to the formation of mixed NiFe2O4 dominated phase and the synergistic effect involved in the hybrids. Otherwise, the higher annealing temperature leads to higher resistance (Fig. 6d), which would hamper the electrontransfer and thus cause the inferior OER activity. The interaction effects between the Ni and Fe in the mixed metal oxides still in controversy and could be thoroughly investigated. Profoundly, the OER activity Ni/Fe binary and Ni/Fe/M ternary metal compounds and incorporating with supporting materials (such as nitrogen-doped carbon nanotubes and 3D graphene) are worthy of exploring in future researches.
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