Madhurya Chandel,
Debabrata Moitra,
Priyanka Makkar,
Harshit Sinha,
Harshdeep Singh Hora and
Narendra Nath Ghosh*
Nano-materials Lab, Department of Chemistry, Birla Institute of Technology and Science, Pilani K K Birla Goa Campus, Goa-403726, India. E-mail: naren70@yahoo.com; Fax: +91 832 2557033; Tel: +91 832 2580318
First published on 3rd August 2018
Here, we report an ‘in situ’ co-precipitation reduction based synthetic methodology to prepare CuFe2O4 nanoparticle–reduced graphene oxide (CuFe2O4–RGO) nanocomposites. First principles calculations based on Density Functional Theory (DFT) were performed to obtain the electronic structures and properties of CuFe2O4, graphene and CuFe2O4–graphene composites, and to understand the interfacial interaction between CuFe2O4 and graphene in the composite. The synergistic effect, which resulted from the combination of the unique properties of RGO and CuFe2O4 nanoparticles, was exploited to design a magnetically separable catalyst and high performance supercapacitor. It has been demonstrated that the incorporation of RGO in the composite enhanced its catalytic properties as well as supercapacitance performance compared with pure CuFe2O4. The nanocomposite with 96 wt% CuFe2O4 and 4 wt% RGO (96CuFe2O4–4RGO) exhibited high catalytic efficiency towards (i) reduction of 4-nitrophenol to 4-aminophenol, and (ii) epoxidation of styrene to styrene oxide. For both of these reactions, the catalytic efficiency of 96CuFe2O4–4RGO was significantly higher than that of pure CuFe2O4. The easy magnetic separation of 96CuFe2O4–4RGO from the reaction mixture and good reusability of the recovered catalyst also showed here. 96CuFe2O4–4RGO also demonstrated better supercapacitance performance than pure CuFe2O4. 96CuFe2O4–4RGO showed specific capacitance of 797 F g−1 at a current density of 2 A g−1, along with ∼92% retention for up to 2000 cycles. To the best of our knowledge, this is the first investigation on the catalytic properties of CuFe2O4–RGO towards the reduction of 4-nitrophenol and the epoxidation reaction, and DFT calculations on the CuFe2O4–graphene composite have been reported.
In this paper, we are reporting the synthesis of nanocomposites composed of CuFe2O4 nanoparticles and reduced graphene oxide (RGO). The synthesized nanocomposites displayed their applications in two different but important fields, (i) as a magnetically separable catalyst for two reactions, and (ii) as an active material to fabricate high performing supercapacitor. To evaluate the catalytic activities of CuFe2O4–RGO nanocomposites, we have chosen two reactions (i) reduction of 4-nitrophenol (4-NP) to 4-aminophenol (4-AP) in presence of excess NaBH4 in an aqueous medium, and (ii) epoxidation of styrene to styrene oxide in presence of tert-butyl hydroperoxide (TBHP). Reduction of 4-NP to 4-AP has been chosen as one of the catalysis reactions because this reaction has been used as a model reaction to study the catalytic property of varieties of nanostructured catalysts by several researchers.9–11 It has been well proven that this reaction is not only simple to perform but also convincing and trustworthy for this purpose. Moreover, 4-NP and its derivatives are the byproducts produced during the manufacture of many synthetic dyes, pesticides, and herbicides.10,12 The industrial effluents containing 4-NP cause severe water pollution because it is harmful to the liver, kidney, central nervous system, etc.10 Therefore, removal or destruction of 4-NP from the polluted aquatic system is an important task. On the other hand, 4-AP, which is produced due to the reduction of 4-NP, is an essential chemical in many pharmaceutical industries for the production of various antipyretic and analgesic drugs. 4-AP is also used in anti-corrosion lubricant, photographic developer, etc.10 The other catalysis reaction we have investigated here is the epoxidation of styrene to styrene oxide because styrene oxide is used in varieties of applications, such as synthesis of fine chemicals, medicines, many commodities, commercial resin, etc.13,14 However, selective epoxidation of styrene is a challenging issue. The conventional processes for styrene oxide production (e.g. non-catalytic process using chlorine, peracids based catalytic process, etc.) suffer from several limitations, including the production of large amount of waste products, chlorine-laden sewage, difficulty in handling corrosive peracids, difficulty in separation of homogeneous catalysts at the end of the reactions, etc.13,15 Hence, there is a need to develop an efficient catalyst which not only will show high selectivity towards styrene oxide formation but also will not produce any pollutant as a waste product, and will be easily separable from the reaction mixture.
We have also explored the possibility to develop supercapacitor using CuFe2O4–RGO nanocomposites because in recent years the development of electrochemical systems for energy storage and energy conversion has intensified many folds to address the issues related to the increasing cost of energy, exhaustion of fossil fuel reserves, and environmental pollution.16,17 Hence, supercapacitors, which are intermediate systems between the battery and a conventional capacitor, are appearing as an attractive alternative due to their excellent property to deliver high power density along with long life cycle.18–21 Generally, charging and discharging times of supercapacitor is in seconds. Though their energy density (∼5 W h kg−1) is lower than the conventional batteries, they generally deliver higher power density (∼10 kW kg−1) for a shorter time.16,20,22,23 Therefore, supercapacitors can find applications in advanced energy storage systems (e.g., uninterrupted power supplies, load leveling, etc.) as either replacement or complement to the batteries.16,24 Electrochemical double layer electrodes (EDL) and pseudocapacitor electrodes are two prominent class of supercapacitor.25–27 Use of EDL electrode in the AIRBUS A380 is one of the examples of the commercial applications of the supercapacitor.28 However, most of the EDL electrodes suffer from lower energy density than batteries, which often limits their wide application.16 Till date several metal oxides (e.g., RuO2, MnO2, Fe3O4), conducting polymers, and their composites are used to construct pseudocapacitive electrodes.16,29–32 Amongst the transition metal oxide, RuO2 and MnO2 have been extensively investigated.30–32 Though RuO2 exhibits high specific capacitance (>600 F g−1) in aqueous medium but RuO2 based electrodes are very expensive for the large-scale common application.16 The usages of MnO2 is limited because it does not possess any oxidation state below 0 V.16 Recently spinel ferrites (MFe2O4 where M = Mn, Co, Ni, Cu, Zn) are utilized as active material for pseudocapacitive electrode, because of the synergistic effect of Fe and M ions results in richer redox reactions to achieve higher specific capacitance.18,25,33,34 Though ferrites have been regarded as promising active materials to construct supercapacitors, their inherent poor electrical conductivity detrimentally affects their supercapacitance performance.25
In this study, we have designed the nanocomposites consist of CuFe2O4 and RGO. In these nanocomposites, CuFe2O4 has been chosen as one of the components due to its magnetic nature, ability to act as a catalyst for various reactions,35–39 and high theoretical capacity (895 mA h g−1).18 To overcome the limitation associated with its low electrical conductivity, CuFe2O4 nanoparticles have been immobilized on the surface of highly conducting RGO sheets. To understand the influence of RGO on the electronic structure of CuFe2O4, first principles quantum mechanical calculations based on Density Functional Theory (DFT) has been performed.
Though CuFe2O4–RGO nanocomposite is a very promising material till date, it has not yet been well explored. Only limited number of publications are available in the literature, where the synthesis of CuFe2O4–RGO by hydrothermal/solvothermal, and one pot co-precipitation method has been reported.5,18,40–44 Researchers have investigated the application of this nanocomposite in the fields of catalysis reactions (e.g. phenol hydroxylation, photocatalysis degradation of methylene blue, oxidative coupling of amine, and chemoselective reduction of nitroarenes), glucose sensing, and energy storage (supercapacitor, anode material for lithium-ion batteries).5,18,40–44
To the best of our knowledge, this is the first time first-principle calculations based on DFT theory has been reported for CuFe2O4–graphene composite to obtain its electronic structure, which helps us to understand how the presence of RGO influences the electronic property of CuFe2O4 in the nanocomposite, and to interpret the enhanced catalytic property as well as supercapacitor property of CuFe2O4–RGO nanocomposites. Here, we firstly reported the synthesis of CuFe2O4–RGO nanocomposites by an ‘in situ’ co-precipitation reduction technique and their structural characterization by several techniques. The electronic structure of the nanocomposite was determined by performing first principle calculations based on DFT. Quantum ESPRESSO package45 was used for DFT calculations because this package was used by several researchers to calculate a variety of semiconductors, ferrites, graphene, and graphene-based composites.46–52 The catalytic performance of the as-synthesized nanocomposites was tested for (i) reduction of 4-NP in presence of NaBH4, and (ii) epoxidation of styrene. Finally, the supercapacitance performance of CuFe2O4–RGO as electrode material was tested first by constructing a three electrode system, and then a two-electrode system.
dCt/dt = −kapp Ct | (1) |
ln(Ct/C0) = ln(At/A0) = −kappt | (2) |
The value of kapp was calculated from the slope of the ln(At/A0) vs. time plot.
After each reaction cycle, the catalyst was separated from the reaction mixture by applying an external magnet (N35 grade NdFeB magnet having energy product BHmax = 33–36 MGO) and then washed with distilled water and ethanol. It was observed that no unreacted 4-NP molecule was remained adsorbed in the catalyst. After washing, the catalyst was dried for the next reaction cycle.
(3) |
(4) |
The cyclic voltammetry (CV) and galvanostatic charge–discharge (GCD) measurements were performed using a galvanostat–potentiostat. All the CV measurements were conducted in the working potential window between 0 to 0.6 V, and using various scan rates between 10 to 100 mV s−1. GCD measurements were carried out at different current densities ranging from 2 to 10 A g−1.
GCD measurements were employed to determine the specific capacitance (Cs) of pure CuFe2O4 and 96CuFe2O4–4RGO nanocomposite and the following equation was used:18,24
(5) |
The energy density (E), and power density (P) of the electrodes were calculated from the GCD by using the following equations:18,24
(6) |
(7) |
Electrochemical Impedance Spectroscopy (EIS) measurements were conducted in the frequency range of 0.01–10000 Hz at open circuit potential with an alternating current amplitude of 0.01 V.
Here three systems were calculated: (i) superlattice of CuFe2O4 with face-centered cubic structure (space group Fdm),61,62 (ii) graphene, and (iii) CuFe2O4–graphene composite. Ultrasoft pseudopotential for these systems were constructed by using 17, 14, 6, and 4 electrons for Cu (3p63d104s1), Fe (3p63d64s2), O (2s22p4), and C (2s22p2), respectively. The pseudopotentials for Cu, Fe, O, and C were chosen from the Quantum ESPRESSO website.63 The Monkhorst–Pack approach64,65 was used to select the k-point mesh (the details of k points for each system are provided as computational details in ESI†). The Brillouin zone integration was carried out with Methfessel–Paxton smearing technique66 for CuFe2O4 unit cell and Marzari–Vanderbilt smearing technique67 for CuFe2O4 (111) slab, graphene, and CuFe2O4 (111)-graphene superlattice and the smearing parameter was 0.005 Ry. The binding energy was calculated from the difference between the total energy of the CuFe2O4–graphene and the sum of each system (i.e. CuFe2O4 and graphene) alone. The sizes of the unit cells of the simulated systems are listed in Table S1 (ESI†) Details of the sample input files for geometric optimization of CuFe2O4, graphene, and CuFe2O4–graphene superlattice are provided in the ESI.†
Fig. 1 Room temperature wide angle powder XRD pattern of (a) GO, (b) pure CuFe2O4, (c) 98CuFe2O4–2RGO, (d) 96CuFe2O4–4RGO, (e) 94CuFe2O4–6RGO, and (f) 92CuFe2O4–8RGO. |
Fig. 2 displays the TEM micrographs of pure CuFe2O4 nanoparticles, and CuFe2O4–RGO nanocomposite. These micrographs revealed that the average particle size of the CuFe2O4 nanoparticles are 15–20 nm and these CuFe2O4 nanoparticles are immobilized on the surface of (the nanometer thin) RGO sheets. SAED patterns (Fig. 2b) show the Debye–Scherrer diffraction rings for pure CuFe2O4. In HRTEM micrographs (Fig. 2c) well-resolved lattice fringes corresponding to (311) plane of CuFe2O4 were observed. EDS analysis of these nanocomposites also confirmed their compositions. As a representative EDS of 96CuFe2O4–4RGO is shown in Fig. S1 (ESI†).
Fig. 2 TEM micrographs of (a) pure CuFe2O4, (b) SAED pattern of CuFe2O4, (c) HRTEM micrograph of a typical portion of a corresponding CuFe2O4 and (d) CuFe2O4–RGO. |
The FT-IR spectra of GO (Fig. S2, ESI†) showed the presence of peaks at (i) 1232 cm−1 corresponding to the C–O stretching vibration of epoxy groups, (ii) 1728 cm−1 for the carbonyl groups, (iii) 1382 cm−1 corresponding to the –C–O stretching vibration of carboxylic groups, and (iv) 1056 cm−1 for the C–O stretching vibration. Therefore, the FT-IR spectra clearly indicated the presence of carbonyl group, carboxylic group, and epoxy groups on the surface of GO. Moreover, the characteristic peak of the skeletal vibration of the graphitic domains at 1621 cm−1 was also observed.68,69 For CuFe2O4–RGO samples, the disappearance of the peaks at 1728 cm−1, 1231 cm−1 and the decrease of the intensity of the peak at 1382 cm−1 indicated that during formation of CuFe2O4–RGO nanocomposites the oxygen-containing groups (e.g. epoxy, carbonyl, carboxyl) of GO have been reduced significantly and GO has converted to RGO. In the spectra of CuFe2O4–RGO, the presence of a band at 594 cm−1 was also observed, which can be attributed to the lattice absorption of M − O (M = Fe3+, Cu2+), indicating the formation of CuFe2O4.
Raman spectra of GO, RGO, and 96CuFe2O4–4RGO composite are shown in Fig. S3 (ESI†). In Raman spectra of pure GO, the peaks were observed at 1345 and 1587 cm−1, which are the characteristic peaks of D and G band, respectively. In case of 96CuFe2O4–4RGO these peaks appeared at 1332 and 1572 cm−1 whereas, for RGO, characteristic peaks for D and G band were found at 1328 and 1580 cm−1, respectively. It has been reported that when GO is reduced to RGO, the values which correspond to the D and G bands of GO move to the lower values.40,69 For GO sample, the value of ID/IG was ∼0.9 whereas for RGO and 96CuFe2O4–4RGO this ratio was ∼1.04 and ∼1.02, respectively. This increase of ID/IG value for RGO and 96CuFe2O4–4RGO can be attributed to the decrease in the average size of sp2 domains upon reduction of GO during formation of 96CuFe2O4–4RGO composite.5,44
TGA thermograms of pure CuFe2O4, 96CuFe2O4–4RGO, 92CuFe2O4–8RGO and GO are shown in Fig. S4 (ESI†). TGA thermogram of GO showed that (i) ∼16% weight loss in the temperature range of 30–100 °C, which might be due to the loss of surface adsorbed water molecules, and (ii) ∼5% weight loss in 100–200 °C range, and ∼26 wt% loss in 200–275 °C range, which were due to the loss of oxygen-containing groups (e.g. carbonyl, carboxyl, epoxy groups, etc.) from the surface of GO sheets,3,69 (iii) in the temperature range of ∼300 to 600 °C, the oxidative decomposition of C atoms of GO occurred. In case of CuFe2O4–RGO nanocomposites, no weight loss in the temperature range of 200–275 °C was observed, which indicated the conversion of GO to RGO during the synthesis of nanocomposites and the functional groups of GO have been reduced in this process to a great extent.3,69 The thermograms of 96CuFe2O4–4RGO, and 92CuFe2O4–8RGO showed 4% and 8% weight loss in the temperature range of 275–500 °C. This weight loss was due to the decomposition of the carbon content of RGO in the composites. Pure CuFe2O4 was found to be quite stable in the temperature range of 30 to 800 °C.
The surface area of the synthesized pure CuFe2O4 and 96CuFe2O4–4RGO were obtained by conducting multipoint BET surface area analysis (Fig. S5, ESI†). The specific surface area of the pure CuFe2O4 and 96CuFe2O4–4RGO was 133 and 141 m2 g−1, respectively. The total pore volume calculated for pure CuFe2O4 and 96CuFe2O4–4RGO were ∼0.02 cm3 g−1 and 0.04 cm3 g−1, respectively.
The magnetic property of the synthesized materials was measured by VSM. As representative, the M–H hysteresis loops of CuFe2O4 and 96CuFe2O4–4RGO are presented in Fig. S6, ESI† and saturation magnetization values were 13, and 12 emu g−1, respectively.
The reduction of 4-nitrophenol to 4-aminophenol with NaBH4 is a six electron transfer reduction reaction. In the aqueous medium BH4− ions were first adsorbed on the surface of the catalyst. Then the H-atom, which was generated from BH4−, after electron transfer to the catalytically active site (CuFe2O4), attacked 4-NP molecule to reduce it to 4-AP. This electron transfer induced hydrogenation occurred spontaneously.10 As the transfer of electron plays a critical role in this reduction reaction, the presence of RGO in the catalyst became beneficial for the enhancement of its catalytic performance. CuFe2O4–RGO exhibited superior catalytic activity over pure CuFe2O4 because of the following reasons (i) according to Rout et al. RGO possesses high adsorption capacity of 4-NP due to π–π stacking interactions.11 Due to the electron withdrawing nature of –NO2 group, 4-NP molecules are adsorbed efficiently on the electron-rich sites of heterogeneous catalysts (e.g. metal nanoparticles, ferrites, etc) as well as on RGO, where its surface functional group act as strong Lewis acids. Using DFT study Rout et al. have shown that, due to this strong adsorption of 4-NP on RGO, the NO bond of –NO2 group becomes elongated (from 1.23 Å to 1.28 Å), which helps to activate the –NO2 group of 4-NP.4,11 This activation facilitates the reduction reaction of 4-NP. (ii) In this present study, DFT calculation showed the existence of a strong interaction in the electron density level in the interface between CuFe2O4 and graphene in the CuFe2O4–graphene composite. Due to this electronic interaction, CuFe2O4–RGO showed superior electrical conductivity over pure CuFe2O4 (EIS measurement results also support this and has been discussed in Section 3.4). This enhancement of conductivity in CuFe2O4–RGO catalyst accelerates the electron transfer process during the reduction of 4-NP to 4-AP. Therefore, 96CuFe2O4–4RGO exhibited significantly higher catalytic performance than that of pure CuFe2O4. The catalytic activity of 96CuFe2O4–4RGO towards the reduction of 4-NP was found to be comparable and in some cases superior to several reported catalysts. (Table S6, ESI†).
Fig. 5 Gas chromatogram analysis of styrene epoxidation reaction with (a) pure CuFe2O4 (b) 96CuFe2O4–4RGO nanocomposite. |
The reaction mechanism for epoxidation of styrene to styrene oxide in presence of TBHP and catalyst has been reported by many researchers.6,14,15 The reaction proceeds via formation of a metal–alkylperoxy species when TBHP interacts with the active site of the catalyst. This metal–alkylperoxy species undergoes one electron transfer reduction. Addition of oxygen to the terminal double bond of styrene leads to the formation of two types of intermediates which are the isomers of oxametallacyclic species.15 Quiller et al. reported that DFT study indicated both isomers (branched and linear) are relatively stable.71 Conversion of products from this intermediate is the rate-determining step. From the oxametallacyclic intermediate epoxide forms via sharpless mechanism, where the transfer of oxygen occurs to the olefinic bond.69 On the other hand, the breakage of the C–C bond of the intermediate leads to the formation of benzaldehyde.15 In the present study, it has been observed that the presence of RGO in the catalyst (96CuFe2O4–4RGO) resulted in better styrene conversion with higher styrene oxide formation selectivity compared to pure CuFe2O4. This can be explained by the presence of RGO in the catalyst helps to adsorb styrene better on the surface of the catalyst than the catalyst without RGO (i.e. pure CuFe2O4). This might be due to the π–π interaction between the π system of RGO and π system of styrene.6,69 This interaction accelerates the electron transfer process between sp2 hybridized C-atoms of RGO and benzene ring of styrene and facilitates the combination of O– atom of TBHP and C– atoms of vinyl group of styrene.69,72 As a result, the conversion of styrene and selectivity of styrene oxide formation were improved when 96CuFe2O4–4RGO was present as a catalyst. The catalytic activity of 96CuFe2O4–4RGO towards epoxidation of styrene was found to be comparable and in some cases superior to many reported catalysts (Table S7, ESI†).
As CuFe2O4–RGO nanocomposites are magnetic in nature, we have explored the feasibility of the separation of the catalyst from the reaction mixture by the magnetic separation process. After completion of the reactions, the catalysts were removed from the reaction mixture by applying a permanent magnet externally. The magnetic separation of the catalysts is shown in Fig. S13a and S14a (ESI†). After separation, the catalyst was thoroughly washed and dried. The recovered catalyst was then used for the next cycle of the reaction. The efficiency of the catalyst was almost remained the same up to 5th cycle (Fig. S13b and S14b, ESI†). From XRD and TEM analysis of the recovered catalysts showed no significant changes in their crystal structures and morphology (Fig. S15, ESI†) and indicated the robustness of the structure of the catalyst.
As in these catalysis reactions we have observed that presence of 4 wt% RGO in the nanocomposite (96CuFe2O4–4RGO) significantly enhanced the catalytic activity compared to pure CuFe2O4, we have then investigated the electrochemical properties of pure CuFe2O4, and 96CuFe2O4–4RGO to construct high performing supercapacitor.
(8) |
In the CV curve of 96CuFe2O4–4RGO electrode a pair of redox peak was also observed at 0.29 V and 0.43 V (Fig. 6), which indicated the fast redox reaction of CuFe2O4 in the composite. Hence, we have considered that the capacitance of CuFe2O4 and 96CuFe2O4–4RGO were mainly originated from the pseudocapacitance. The excellent conductivity of RGO might cause the negative shifting of redox peaks of 96CuFe2O4–4RGO electrode. Moreover, compared to pure CuFe2O4, the higher response of the peak current, and larger area under the CV curve of 96CuFe2O4–4RGO indicated the higher specific capacitance of 96CuFe2O4–4RGO (Fig. 6). This might be due to the synergistic effect of CuFe2O4 and RGO in the 96CuFe2O4–4RGO nanocomposites arising from the high redox activity of CuFe2O4 nanoparticles, combined with the highly conductive backbone provided by RGO, which not only facilitates the faster electron transport but also offers mechanical support that maintains the integrity of the electrode during the electrochemical process.18,73–75
To evaluate the supercapacitance performance at various scan rate, CV measurements were also conducted with different scan rate (10–100 mV s−1) in 3 M KOH for both CuFe2O4 and 96CuFe2O4–4RGO electrodes, Fig. S16a and b (ESI†). It was observed that the change in scan rate affected both the peak potential and peak current response. The increase of the peak current with increasing scan rate for both CuFe2O4 and 96CuFe2O4–4RGO electrodes indicated their excellent rate capability. With the progressive increase of scan rate, a well linear increase of peak current was observed for both the electrodes in their Randles–Sevcik plot (Fig. S16c, ESI†). This suggested that the electrochemical reaction, which is occurring on the electrode surfaces (pure CuFe2O4, and 96CuFe2O4–4RGO), is a diffusion-controlled redox process. Moreover, it was also observed that the current response was increased with increasing scan rate. This is due to the fact that, the scan rate affects the migration of electrolytic ions, and their diffusion into the electrode. When the scan rate is relatively low, the growth of a thick diffusion layer on the surface of the electrode limits the flux of electrolytic ions towards the electrode and results in the lower current. But at a higher scan rate, this diffusion layer cannot grow on the electrode surface. Hence, in this condition, the electrolyte flux towards the electrode enhances, which leads to the increase of current at the higher scan rate.76 In the CV curves (Fig. S16, ESI†), with increasing scan rate the shifting of both the upper and lower peaks towards positive and negative direction respectively, was also observed. This can be due to the development of overpotential which limits the faradic reaction.76
GCD behavior of the pure CuFe2O4 with varying current densities from 2 to 10 A g−1 in 3 M KOH shown in Fig. S17a (ESI†). The GCD curves suggest that pure CuFe2O4 electrode possess good pseudo-electrochemical character and typical battery like behavior. It was noted that the largest capacitance value for pure CuFe2O4 could be reached up to 83 F g−1 when the current density is 2 A g−1. The value of specific capacitance reported here is higher than that of some of the reported CuFe2O4 electrodes. For example, CuFe2O4 hollow fibres, which were prepared by electrospinning and direct annealing by Zhao et al. exhibited a specific capacitance of 28 F g−1 at 0.5 A g−1.77 Spray pyrolyzed thin films of CuFe2O4 showed specific capacitance of 5.7 F g−1 at 0.3 μA cm−2.78 Hydrothermally synthesized CuFe2O4 nanosphere showed capacitance of ∼81.5 F g−1 at 1 A g−1.18 In the present case the CuFe2O4 nanoparticles, which were synthesized by co-precipitation method showed that with increasing current density (2–10 A g−1) its capacitance was decreased from 83–9 F g−1. This can be explained by the decrease of the diffusion rate of electrolyte anions (OH−) into the electrode with the increase of current density.34
The change in specific capacitance with increasing current density (ranging from 2–10 A g−1) of the 96CuFe2O4–4RGO electrode (which contains 4 wt% RGO) is shown in Fig. S17b.† The discharge time of 96CuFe2O4–4RGO was found to be higher than that of pure CuFe2O4, which is a suggestive of the higher charge capacity of 96CuFe2O4–4RGO than that of CuFe2O4, which was consistent with the CV results. The largest specific capacitance of 96CuFe2O4–4RGO could be reached up to 313 F g−1 when current density was 2 A g−1. For 96CuFe2O4–4RGO electrode also the specific capacitance was decreased from 313 to 174 F g−1 with increasing charge density from 2 to 10 A g−1 like CuFe2O4 electrode. The retention of the initial capacitance was increased from 10% (for pure CuFe2O4) to 56% (96CuFe2O4–4RGO) when CuFe2O4 nanoparticles were immobilized on RGO sheets.
As it was observed that the presence of 4 wt% RGO in CuFe2O4–RGO nanocomposite significantly enhanced the supercapacitance of CuFe2O4, the GCD behavior of pure RGO electrode was also studied. The highest specific capacitance of RGO was 152 F g−1 at the charge density of 2 A g−1, and it was decreased from 152 to 72 F g−1 when current density was increased from 2–10 A g−1 (Fig. S18, ESI†). Though this specific capacitance value was lower than that of the theoretical value of a single layer RGO (550 F g−1), this present value is comparable with the values reported by others.18 The agglomeration of RGO sheets due to their π–π interaction might be the main cause of the lower specific capacitance of synthesized RGO. FESEM micrograph of synthesized RGO reveals the agglomeration of RGO sheets (Fig. S19, ESI†). However, when CuFe2O4–RGO nanocomposites were synthesized by immobilizing CuFe2O4 nanoparticles on the surface of RGO sheets these nanoparticles acted as a spacer between the sheets and prevented the agglomeration of RGO sheets to a great extent (Fig. 2d). Therefore, 96CuFe2O4–4RGO nanocomposite exhibited much higher supercapacitance than that of pure RGO.
EIS is an important tool to investigate the fundamental behavior of electrode materials for supercapacitors. The Nyquist plot is generally generated from the data obtained from EIS measurements. In this plot, the presence of a semicircle in the high-frequency region indicates the charge transfer resistance at the electrode–electrolyte interface. In the high-frequency region, the intercept of the semicircle on the X-axis (Z′) indicates the internal resistance (Rs) of the cell. The ionic resistance of the electrolyte, the intrinsic resistance of the electrode materials, and the contact resistance between the electrode and the current collector are the three major factors, which influence Rs. From the diameter of the semicircle, the charge transfer resistance (Rct) of the electrode–electrolyte interface can be estimated. The straight line at the low-frequency region signifies a diffusion process, which is known as Warburg diffusion. Fig. 7 shows the Nyquist plots of CuFe2O4, RGO, and 96CuFe2O4–4RGO electrodes. The smaller radius of the semicircle of 96CuFe2O4–4RGO than that of pure CuFe2O4 indicated the Rct of 96CuFe2O4–4RGO is lower than that of pure CuFe2O4. The estimated Rct values of pure CuFe2O4 and 96CuFe2O4–4RGO were ∼26 and ∼5 Ω respectively. This relatively lower value of Rct of 96CuFe2O4–4RGO indicated its better charge transferability than pure CuFe2O4. The origin of the smaller value of Rct of 96CuFe2O4–4RGO might be due to the well dispersion of CuFe2O4 nanoparticles which are in intimate contact with the highly conductive RGO. This causes strong interfacial interaction between CuFe2O4 and RGO in 96CuFe2O4–4RGO nanocomposite. The orbital level interaction between RGO and CuFe2O4 as observed from DFT calculation in their interface causes to enhance the electrical conductivity of CuFe2O4–RGO nanocomposite.
To evaluate the effect of electrolyte on the supercapacitance performance of the 96CuFe2O4–4RGO electrode, its electrochemical measurements were performed using a mixture of 3 M KOH and 0.1 M K4[Fe(CN)6] as the electrolyte. The CV curves of 96CuFe2O4–4RGO electrodes in 3 M KOH and 3 M KOH + 0.1 M K4[Fe(CN)6] are shown in Fig. 6. In the CV curve of 96CuFe2O4–4RGO electrode, the presence of a distinct pair of redox peaks at 0.32/0.40 V was observed, which also indicated the fast faradic redox reaction. It was noted that due to the addition of 0.1 M K4[Fe(CN)6] in 3 M KOH electrolyte system the peak area under the CV curve and peak current were increased significantly. During CV measurements of 96CuFe2O4–4RGO electrode at different scan rate (10–100 mV s−1), the increasing trend of peak current with increasing scan rate was observed which is shown in Fig. S20 (ESI†). This indicates the good rate capability of the 96CuFe2O4–4RGO electrode in this modified electrolyte system.
From GCD analysis, the specific capacitance of 96CuFe2O4–4RGO electrode was also measured in 3 M KOH + 0.1 M K4[Fe(CN)6] electrolyte and shown in Fig. S21 (ESI†). In this electrolyte system, the specific capacitance value was significantly increased (up to 797 F g−1 at 2 A g−1) compared to 3 M KOH electrolyte (313 F g−1 at 2 A g−1). The presence of 0.1 M K4[Fe(CN)6] in this electrolyte system was found to be beneficial because it provides an additional complementary redox couple, [Fe(CN)6]4−/[Fe(CN)6]3− with matching potential (0.20/0.37 V) to the electrolyte system, which can act as an electron buffer source in the electrochemical reaction at 96CuFe2O4–4RGO electrode/electrolyte interface.24,79,80 Moreover, as the Born radius of [Fe(CN)6]4−/[Fe(CN)6]3− is ∼0.4 nm (ref. 24) and the total pore volume of 96CuFe2O4–4RGO was ∼0.04 cm3 g−1 (obtained from N2 adsorption–desorption analysis Fig. S5 ESI†), a large number of redox additive anions can be accommodated within the pore of the 96CuFe2O4–4RGO electrode. The decrease of ionic diffusion resistance of the electrolytic ions due to the addition of K4[Fe(CN)6] is one of the major factors which enhances the redox kinetics and hence the supercapacitance of the electrodes. The positive influence of K4[Fe(CN)6] redox additive on the supercapacitance of the electrode is shown in Fig. 8a. However, the value of specific capacitance in this modified electrolyte system was decreased from 797 to 266 F g−1 when current density increase from 2 to 10 A g−1. In this system 96CuFe2O4–4RGO electrode retained ∼33% of its initial capacitance. This significant decrease of supercapacitance value with increasing current density (particularly at comparatively higher current density) was observed which may be due to the sluggish redox reaction kinetics, and low penetration of electrolyte ions in and out of the electrode at higher current density.
Fig. 8 (a) Change of specific capacitance of pure CuFe2O4 and 96CuFe2O4–4RGO electrodes with changing current density from 2 to 10 A g−1, (b) Ragone plots of CuFe2O4 and 96CuFe2O4–4RGO electrodes. |
As a reasonable energy density with high power density required for a high performing supercapacitor, we have calculated the energy density of CuFe2O4 and 96CuFe2O4–4RGO electrodes at different power densities. Fig. 8b shows the Ragone plots of these electrodes when 3 M KOH and 3 M KOH + 0.1 M K4[Fe(CN)6] were used as the electrolyte. In 3 M KOH electrolyte 96CuFe2O4–4RGO delivered an energy density of 11 W h kg−1 at a power density of 543 W kg−1, which was significantly higher than that of CuFe2O4 (energy density 2.4 W h kg−1 at a power density of 460 W kg−1). When 3 M KOH + 0.1 M K4[Fe(CN)6] was used as the electrolyte, 96CuFe2O4–4RGO exhibited larger values of the energy density of 16 W h kg−1 at a power density of 380 W kg−1. The energy density was decreased from 16 to 5 W h kg−1 with increasing power density from 380 to 1900 W kg−1. These values are comparable with commercial supercapacitor (3–9 W h kg−1 at 3000 to 10000 W kg−1).24,74 The supercapacitor performance of 96CuFe2O4–4RGO electrode was found to be comparable and in some cases better than the previously reported ferrite and ferrite-RGO based electrodes (Table S8, ESI†).
Sustainability of high electro-capacitance value at high current density is an important factor to determine the performance of the electrode. The high specific capacitance value at high current density demonstrates the better performance of 96CuFe2O4–4RGO electrode than the work reported by others. Moreover, the symmetric nature of GCD profile even at high current density also indicated high rate performance of the 96CuFe2O4–4RGO electrode.
As 96CuFe2O4–4RGO electrode exhibited better supercapacitance behavior than pure CuFe2O4, we have investigated its cycling behavior to understand its stability. Cycling behavior of 96CuFe2O4–4RGO electrode has been investigated at a constant current density of 6 A g−1 for more than 2000 cycles using both the electrolytes (3 M KOH, and 3 M KOH + 0.1 M K4[Fe(CN)6]), and shown in Fig. 9. The equilibrium was reached after the first few cycles and then the steady capacitance was reached for the subsequent cycles. The 96CuFe2O4–4RGO electrode exhibited a higher specific capacitance (343 F g−1 at 6 A g−1) when the mixture of 3 M KOH and 0.1 M K4[Fe(CN)6] was used as electrolyte than when 3 M KOH was the electrolyte (specific capacitance = 172 F g−1). After 2000 cycle 96CuFe2O4–4RGO electrode exhibited ∼85% retention of its specific capacitance when KOH was used as the electrolyte. However, this retention value was increased up to ∼92% in 3 M KOH + 0.1 M K4[Fe(CN)6] electrolyte, which demonstrated its high cycling stability.
The electrochemical property measurements of the electrode by using a three-electrode system generally provide the insight of the materials electrochemical behavior for its application as a supercapacitor. But as the two electrode test cell measurement system mimics the configuration of the commercial supercapacitor, the results it provides are more significant for the practical purposes.18,81 Hence, we have constructed a two electrode test cell using 96CuFe2O4–4RGO nanocomposite and measured its specific capacitance with 3 M KOH + 0.1 M K4[Fe(CN)6] electrolyte. Fig. S22 (ESI†) shows the CV curves of 96CuFe2O4–4RGO electrode at different scan rates and GCD curves with varying current densities which were measured in two electrode system. The value of specific capacitance in this condition obtained was 160 F g−1 at a current density of 2 A g−1. Though this value is lower than the specific capacitance value, which was obtained from three-electrode measurement system (797 F g−1 at 2 A g−1), this trend is quite normal and consistent with the observations reported by different researchers for various systems.18,74,81
As a demonstration for the real application of the 96CuFe2O4–4RGO electrode as a supercapacitor device, two symmetric cells were fabricated using 96CuFe2O4–4RGO as an active electrode material and they were connected in series and charged for 10 min using a 9 V battery. After charging the cell, a yellow light-emitting diode (LED) (1.8 V) was connected with it. The connected LED was light-up for 6 min. The light-up of LED after connecting with 96CuFe2O4–4RGO electrode is shown in Fig. 10.
Fig. 10 A yellow light-emitting diode (LED) (1.8 V) powered by two 96CuFe2O4–4RGO capacitors connected in series. Glowing LED at a different time interval. |
Here, it has been demonstrated that the presence of RGO caused significant enhancement of the catalytic activities of the CuFe2O4–RGO nanocomposite compared to pure CuFe2O4 for two reactions (i) reduction of 4-nitrophenol, and (ii) epoxidation of styrene. The nanocomposite, which was composed of 96 wt% of CuFe2O4 and 4 wt% RGO (96CuFe2O4–4RGO), exhibited a high catalytic activity towards the reduction of 4-nitrophenol to 4-aminophenol with kapp = 17.2 × 10−3 s−1, and the epoxidation of styrene with ∼90% styrene conversion and ∼65% selectivity of styrene oxide formation. Whereas pure CuFe2O4 showed kapp of 5.7 × 10−3 s−1 for reduction of 4-nitrophenol, and ∼85% styrene conversion with ∼37% selectivity of styrene oxide formation in epoxidation reaction. The magnetic nature of the nanocomposite was exploited for its easy magnetic separation from the reaction mixtures after the completion of the reactions. The recovered catalyst exhibited a very good reusability.
Due to the presence of RGO, 96CuFe2O4–4RGO also exhibited higher supercapacitance performance and cyclic performance compare to pure CuFe2O4. When 3 M KOH was used as the electrolyte, the 96CuFe2O4–4RGO electrode showed a specific capacitance of 313 F g−1, whereas pure CuFe2O4 electrode showed 83 F g−1 at 2 A g−1 current density. Addition of 0.1 M K4[Fe(CN)6] in 3 M KOH solution was found to be beneficial as the electrolyte. In this electrolyte at 2 A g−1 current density 96CuFe2O4–4RGO showed a maximum specific capacitance of 797 F g−1 and retention of ∼92% specific capacitance up to 2000 cycle. It also showed a high energy density of 16 W h kg−1 at a power density of 380 W kg−1.
To the best our knowledge, this is the first time the ability of CuFe2O4–RGO nanocomposite as a magnetically separable catalyst for the reduction reaction of 4-nitrophenol, and epoxidation reaction of styrene, and the investigations on its electronic structures by DFT calculations have been reported. The easy synthetic methodology, high catalytic activity with very good reusability, and excellent supercapacitance performance make 96CuFe2O4–4RGO nanocomposites as an attractive multifunctional material.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c8ra05393f |
This journal is © The Royal Society of Chemistry 2018 |