Xinghong Cuia,
Yanfang Zhua,
Fei Lic,
Daijun Liua,
Jianjun Chena,
Yuxin Zhangc,
Li Li Zhang*b and
Junyi Ji*a
aCollege of Chemical Engineering, Sichuan University, Chengdu, Sichuan 610065, China. E-mail: junyiji@scu.edu.cn
bInstitute of Chemical and Engineering Sciences, A*STAR, 1 Pesek Road, Jurong Island 627833, Singapore. E-mail: zhang_lili@ices.a-star.edu.sg
cCollege of Material Science and Engineering, Chongqing University, Chongqing, 400044, China
First published on 15th January 2016
We report a liquid–solid-solution assemble strategy to fabricate Fe2O3@graphene (Fe2O3@rGO) composites at the oil/water interface, where the Fe2O3 nanoplates with thickness of about 100 nm are anchored on crumpled graphene sheets. The in situ nucleation and growth process can ensure intimate contact between Fe2O3 nanoplates and graphene sheets, while the oil shell on Fe2O3 can prevent the aggregation of the Fe2O3@rGO composite. The crumpled structure and the relatively thin Fe2O3 nanoplates can shorten the electron diffusion path and enhanced the utilization rate of the active material. When used as the anode material, the Fe2O3@rGO anode shows a high reversible capacity of 1160 mA h g−1 at 0.2 A g−1 after 100 cycles, as well as a high cycling stability (101.3% capacity retention after 300 cycles at 1 A g−1). Moreover, with ∼156 s charging time (at a current density of 12.8 A g−1), the anode can deliver a significant capacity of 552 mA h g−1, indicating its promising application as a high-rate lithium ion battery anode.
Various strategies have proposed to avoid the pulverization and thereby enhance the structural stability and rate performance of the Fe2O3. One strategy is to construct nanosized architecture, such as nanorods,13 nanofibers,14 hollow-structures,15 nanoplates,16 which can shorten the diffusion paths of Li+ and electrons, and release the strain caused by the volume change. Another one is to hybridize the nanosized active materials with conductive materials to enhance the conductivity of the composites, such as activated carbon,17 carbon nanotube,18 graphene,19–21 conductive polymer22 et al. Among them, graphene with high conductivity, two dimensional structure and good mechanical property, has become the first choice to fabricate advanced electrodes. Graphene sheets in the electrodes can not only facilitate the electron transfer to the active materials, the superior mechanical property and flexibility can also buffer the volume change of host material during discharge/charge process. Though the study of Fe2O3/graphene hybrids has made great progress,9,23 anodes with high rate performance as well as high stability is still urgently demanded.
Here, we report a liquid–solid-solution assemble strategy to fabricate Fe2O3@graphene (short for Fe2O3@rGO) composite, where the Fe2O3 nanoplates with average diameter of about 500 nm in width and 100 nm in thickness are anchored on graphene sheets. The crumpled structure and the relatively thin Fe2O3 nanoplates can shorten the electron diffusion path and enhanced the utilization rate of the active material, while the intimate contact can facilitate the electron transfer from the conductive graphene sheets to Fe2O3. With such a structure, the Fe2O3@rGO anode shows a high reversible capacity of 1160 mA h g−1 at 0.2 A g−1 after 100 cycles, as well as a high cycling stability (101.3% capacity retention after 300 cycles at 1 A g−1). With ∼156 s charging time (at a current density of 12.8 A g−1), the anode can deliver a significant capacity of 552 mA h g−1, which is comparable to most of the state-of-the-art anodes, indicating its promising application as a high-rate LIB anode.
:
3) was fabricated through a liquid–solid-solution (LSS) process. Briefly, (NH4)2Fe(SO4)2·6H2O (0.24 g) was dissolved in GO aqueous solution (∼1 mg mL−1, 20 mL) to form a Fe2+ solution under ultrasonic (solution A, Fe2O3/GO experimental designed weight ratio of 7
:
3). Then, NaOH (1.50 g), DI water (10 mL), ethanol (20 mL) and oleic acid (10 mL) were mixed orderly under vigorous stir to form a clear solution (solution B). After addition of solution A dropwise to solution B under vigorous stir, the color of the mixture changed from black-brown to black. After stir for another 30 min, the mixture was transferred into a 100 mL Teflon-lined stainless steel autoclave, and treated at 180 °C for 10 h. After cooling to room temperature naturally, the black precipitates were separated by centrifugation, washed with ethanol and DI water for several times, respectively. The product was obtained after frozen drying and thermal treatment at 500 °C for 4 h under N2 atmosphere. For comparison, other composites (Fe2O3/GO experimental designed weight ratio of 5
:
5 and 9
:
1) were prepared using the same process with different Fe2O3/GO ratio as the contrast samples.
:
1
:
1 in weight) in N-methyl pyrrolidone to form a slurry, then coated onto a copper disc and dried under vacuum at 120 °C for 12 h. The mass loading of each electrodes (including active materials and additives) was ∼1 mg cm−2. Pure Li foil and polypropylene membrane (Celgard 2400) was used as the counter electrode and the separator, respectively, and 1 M LiPF6 in a mixture of ethylene carbonate and diethyl carbonate (1
:
1 by volume) was used as the electrolyte. Cell assembly was carried out in an Ar protected glovebox. The galvanostatic charge–discharge measurements (0.01–3 V) were performed on a LANHE (CT2001A) battery test system. Cyclic voltammetry (CV) was performed on a LK9805 electrochemical analyser under a scan rate of 0.1 mV s−1. Electrochemical impedance spectroscopy (EIS) was carried out on a Zahner electrochemical workstation in a frequency range of 0.01 Hz to 100 kHz with an amplitude of 10 mV. The specific capacity is calculated based upon the total active materials (Fe2O3 and rGO).
The obtained composites before and after heat treatment are characterized by X-ray diffraction (XRD) to trace the crystal transition. Fig. 2a shows all peaks of products are in good agreement with α-Fe2O3 (PDF #33-1346), α-FeOOH (PDF #29-2713) and γ-Fe2O3 (PDF #39-1346). This result reveals that the as-prepared composite is composed of hematite (α-Fe2O3) and goethite (α-FeOOH), while they are converted to γ-Fe2O3 during heat treatment via a dissolution–crystallization and dehydration–rearrangement process, respectively.28 Furthermore, since the XRD patterns of Fe3O4 (PDF #19-0629) and the γ-Fe2O3 are similar, X-ray photoelectron spectroscopy (XPS) measurement has been carried out to verify the Fe2+ and Fe3+ cations (Fig. 2b). The full spectrum indicates the presence of carbon, oxygen, and iron element, while the inset Fe 2p spectrum reveals two broad peaks and a satellite peak of Fe3+ around 710.9, 724.3 and 719.8 eV, respectively, all of which indicates the formation of γ-Fe2O3.15 Thermogravimetric analysis (TGA) of Fe2O3@rGO (Fig. 2c) reveals that the content of Fe2O3 in the composites are 70.9%, 81.4% and 92.9%, respectively (corresponds to Fe2O3@rGO (5
:
5), Fe2O3@rGO (7
:
3) and Fe2O3@rGO (9
:
1)), indicates the gradually increase of initial GO content can increase the mass content of rGO in the composites. The difference between the actual content and the experimentally designed value may be due to the deoxidization of GO sheets and the incomplete transfer of Fe ions. The Raman spectrums of Fe2O3@rGO (Fig. 2d) reveals the G bands of the Fe2O3@rGO (5
:
5), Fe2O3@rGO (7
:
3) composite shift from 1575 cm−1 to 1588 cm−1 and 1593 cm−1, respectively. The blue shift of the G band may introduced by the interaction between the graphene sheets and Fe2O3 nanoplates.29
Scanning electron microscopy (SEM) and high resolution transmission electron microscopy (HRTEM) are taken to investigate the morphology and structure evolution of the Fe2O3@rGO composites. Fig. 3a and b present the structure of the composite before heat treatment (Fe2O3/FeOOH@rGO). The composite reveals a highly crumpled graphene sheet, and the Fe2O3/FeOOH nanoplates are uniformly anchored on graphene sheets without apparent aggregation, which may benefit by oil film protection during the LSS assembly. After heat treatment, the morphology of the obtained Fe2O3@rGO (7
:
3) composite does not change significantly (Fig. 3c and d).
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Fig. 3 SEM images of (a, b) Fe2O3/α-FeOOH@rGO (7 : 3) and (c, d) Fe2O3@rGO (7 : 3) at different magnifications, and (e, f) TEM images of Fe2O3@rGO (7 : 3) at different magnifications. | ||
Fe2O3 nanoplates uniformly anchored on crumpled graphene sheets are observed. The Fe2O3 nanoplates are about 500 nm in width and 100 nm in thickness (Fig. 3e and f). Such thin nanoplates can shorten the electron diffusion path and enhanced the utilization rate of the active material. Furthermore, the composite structure can be retained after sonication, indicating good interaction between the graphene sheets and Fe2O3 nanoplates. On the contrary, the Fe2O3@rGO (5
:
5) composites show similar structure but with thicker graphene sheets, while the Fe2O3@rGO (9
:
1) shows highly aggregation of the Fe2O3 nanoplates on graphene sheets (Fig. S1, see ESI†). Moreover, the size of the Fe2O3 nanoplates show decrease trend with the decrease of the graphene content in the composites. This may be due to the different graphene content. The nucleus can be formed both on GO surface and in solution with insufficient GO sheets, which results in smaller Fe2O3 crystal size. The Fe2O3 nanoparticles suspended in solution trend to aggregation with Fe2O3@graphene composite to reduce the surface energy. In general, this crumpled Fe2O3@rGO composite may act as a high performance anode: the crumpled structure and the relatively thin Fe2O3 nanoplates can shorten the electrolyte ions diffusion pathway inside the electrode, while the intimate contact can facilitate the electron transfer rate from the conductive graphene sheets to active material (Fe2O3). Furthermore, the graphene sheets with high mechanical property can also buffer the stress from the volume expansion of the Fe2O3 nanoplates during cycling.
The electrochemical measurements of Fe2O3@rGO composites are firstly evaluated by cyclic voltammetry (CV). Fig. 4a shows the CV curves of Fe2O3@rGO (7
:
3) electrode for the initial five cycles. During the first discharge cycle, the minor peaks at 1.58 and 1.18 V correspond to the initial lithiation reaction to form LixFe2O3.16 The shoulder peak at 0.90 V is related to the phase change from hexagonal LixFe2O3 to cubic Li2Fe2O3 for further Li-insertion.16 The sharp peak at 0.66 V is caused by the reduction of Fe(III) to Fe(0) as well as the formation of solid electrolyte interface (SEI). During the charge cycle, the anodic peaks at 1.62 and 1.81 V are associated with the gradual oxidation of Fe(0) to FeO and then to Fe2O3.12 In the following cycles, the center and the strength of the peaks remain the same, which reveals a high reversibility of the composite. This reversibility and stability can also be observed by the galvanostatic charge/discharge test. Fig. 4b exhibits the charge/discharge curves of Fe2O3@rGO (7
:
3) at current density of 0.2 A g−1. After the first cycle, the charge/discharge curves of the 5th, 10th and 50th cycle show similar plateau voltage, as well as the specific capacity, indicating high stability and reversibility of the Fe2O3@rGO (7
:
3) electrodes.
The cycling and rate performance of the Fe2O3@rGO (7
:
3) electrodes are investigated. As shown in Fig. 4c, an initial reversible specific capacity of 969 mA h g−1 is obtained, which is comparable to most of the iron-based electrodes.14,30–33 After the slight decrease in the subsequent several cycles, the reversible specific capacity of Fe2O3@rGO (7
:
3) increases gradually, and reaches a high value of 1160 mA h g−1 after 100 cycles. This increase tendency and higher than theoretical specific capacity may be attributed to the gradual activation of Fe2O3, the synergistic effect of graphene and Fe2O3, as well as the pseudo-capacitive and the electron double layer capacitance (EDLC) of oxygen-containing graphene sheets.16,20,30 Furthermore, the Fe2O3@rGO (7
:
3) electrodes exhibit a high rate performance, the specific capacity decreases slightly with the increase of current density (Fig. 4d). The discharge capacities are 994.7, 950.3, 883.4, 837.2, 763.2 and 655.2 mA h g−1 at the current densities of 0.2, 0.4, 0.8, 1.6, 3.2 and 6.4 A g−1, respectively. When the current density increases to as high as 12.8 A g−1 (corresponds to a charge time of 156 s), the specific capacity still reaches a high value of 552 mA h g−1, indicating its potential as a high rate anode. Moreover, the reversible capacity can recover and keep the increase tendency once the current density is restored to 0.2 A g−1, implying good reversibility of the anode.
In order to evaluate the cyclic stability under different charge rate, the Fe2O3@rGO (7
:
3) electrode tested under different current densities are also evaluated. The electrode show good long-term cycling stability (Fig. 4e), at a current density of 1 A g−1, the anode maintains a high capacity of 838.2 mA h g−1 (101.3% capacity retention) after 300 cycles with a coulombic efficiency of almost 100%. When the current densities are up to 6.4 and 12.8 A g−1, the discharge capacities are 636.4 and 419.8 mA h g−1 after 400 cycles and with a capacity retention of the about 107% and 81%, respectively, indicates the stable structure and high-rate performance of the Fe2O3@rGO 7
:
3 composite.
For comparison, the electrochemical performance of the Fe2O3@rGO (5
:
5) and Fe2O3@rGO (9
:
1) electrodes are also investigated (Fig. 4c and d), both of them show inferior cycling and rate performance than the Fe2O3@rGO (7
:
3) electrode. The Fe2O3@rGO (5
:
5) electrode shows lower specific capacity value in cycling test and quick decrease during rate performance. The lower content of the active materials (Fe2O3), as well as the relatively larger Fe2O3 particle size and thicker graphene layer of the Fe2O3@rGO (5
:
5) electrode may hinder the electrolyte ions diffusion inside the electrode. On the other hand, the Fe2O3@rGO (9
:
1) composite show a high specific capacity in the beginning, then the values drop quickly in both the cycling and rate performance test. This may due to the lack of contact between graphene sheets and aggregated Fe2O3 nanoparticles, which can cause a high electron transfer resistance. To further understand the superior electrochemical performance of the Fe2O3@rGO (7
:
3) electrode, electrochemical impedance spectroscopy (EIS) measurements of these anodes are performed after 20 cycles activation. The Nyquist plots (Fig. S2, see ESI†) display that the diameter of the semicircle for Fe2O3@rGO (7
:
3) electrode in the high frequency region is smaller than the other two anodes, indicating lower ions and electrons diffusion resistance.34 This result indicates that Fe2O3@rGO (7
:
3) electrode possesses the most balanced performance between the electron transfer and the electrolyte ions diffusion resistance, and explains its best electrochemical performance.
Besides the electrodes with different graphene content, some latest literature works on iron-based high-rate LIBs anodes are also taken into comparison. As shown in Fig. 4f, the rate performance of the Fe2O3@rGO (7
:
3) electrode is comparable or higher than most of the state-of-the-art electrodes (including carbon-based anodes, and other metal oxide based anodes), especially under high current densities.8,9,13–16,35–42 This improved rate performance of the Fe2O3@rGO (7
:
3) anode is attributed to its well designed structure: the electrical conductive graphene network and the good interaction between Fe2O3 and rGO ensures good electrical contacts and small charge transfer resistance; meanwhile, the graphene sheets can effectively relieve the stress of volume expansion upon material conversion process, reduces the pulverization and agglomeration of the electrode material. Considering the simple and scalable preparation method and low cost, this composite shows promise for application as high rate LIB anodes.
Footnote |
| † Electronic supplementary information (ESI) available: Additional characterization data of SEM images, electrochemical impedance spectroscopy (EIS) measurements are presented. See DOI: 10.1039/c5ra22408j |
| This journal is © The Royal Society of Chemistry 2016 |