Open Access Article
J. John Benittoa,
J. Judith Vijaya
*a,
B. Saravanakumar
b,
Hamad Al-Lohedanc and
Stefano Belluccid
aCatalysis and Nanomaterials Research Laboratory, Department of Chemistry, Loyola College, Chennai-600034, Tamil Nadu, India
bDepartment of Physics, Dr. Mahalingam College of Engineering and Technology, Pollachi, Tamil Nadu-642 003, India
cDepartment of Chemistry, College of Science, King Saud University, P. O. Box 2455, Riyadh, 11451, Saudi Arabia
dINFN-Laboratori Nazionali di Frascati, Frascati, Italy
First published on 11th March 2024
Supercapacitors (SCs) have emerged as attractive energy storage devices due to their rapid charge/discharge rates, long cycle life, and high-power density. However, the development of innovative electrode materials to achieve high-performance remains crucial to meet future requirements in supercapacitor technology. In this work, we have explored the potential of a microwave-engineered NiZrO3@GNP composite as a promising electrode material for SCs. A microwave assisted hydrothermal approach was adopted for the fabrication of the NiZrO3@GNP nanocomposite. Structural and morphological investigations showed its structural richness and its chemical compositions. When applied as a SC electrode, this innovative combination exhibits battery-like behaviour with higher specific capacity (577.63 C g−1) with good cyclic stability, and good performance. We have assembled an asymmetric-type two-electrode SC device and analysed its electrochemical features. This NiZrO3@GNP device exhibits the specific capacity of 47 C g−1 with capacitance retention of 70% after 2000 charge–discharge cycles. Further research on optimizing the synthesis process and exploring different device configurations could pave the way for even higher-performance supercapacitors in the future.
Presently, with researchers focusing on the utilization of renewable energy sources and energy conservation for a sustainable and eco-conscious environment, SCs are garnering significant attention owing to their substantial advantages. A huge range of energy storage devices have been developed, from batteries to multi-modal energy storage systems (Pumped Hydro Storage, Compressed Air Energy Storage, Thermal Energy Storage, Hydrogen Storage, Supercritical CO2 Energy Storage, Molten Salt Energy Storage, Hydraulic Accumulators, and Capacitive Deionization). However, these come with several drawbacks like cost ineffectiveness, low energy density, reduced power density, less efficiency, poor shelf life, etc. SCs are energy storage devices that store energy as charges.4 They are more advantageous due to high power and energy density, longevity with respect to shelf life, and cyclic stability. SCs are being used in various industrial equipment, electronic gadgets, electric vehicles and several other major applications. Since the proposal of the Helmholtz concept of capacitive performance of the electrical double layer formed at the electrode–electrolyte interface, followed by Becker's first application of it to electrolytic capacitors, supercapacitors, also called electrical double layer capacitors or ultracapacitors, have undergone various advances to increase the efficiency by increasing their energy storage capacity.5
Supercapacitors are of different types: electrochemical double-layer capacitor (EDLC), pseudocapacitor, and hybrid capacitor. Electrochemical double-layer capacitors involve the accumulation of charges at the electrode surface.6 They exhibit rapid charge–discharge cycles along with high power density but suffer from aging, especially when subjected to high voltage and temperatures over a period of time.7,8 Hybrid capacitors combine the characteristics of SCs and batteries with one electrode being a faradaic electrode and the other a capacitive electrode.9 However, the high energy and power performances are decoupled and do not compete with the conventional lithium-ion batteries.10
SCs store energy by faradaic electron transfer of metal ions and EDLC capacitance through surface reactions at the electrode.11 SCs have exceptional power density and cycle stability and are anticipated to a good competitors against batteries. However, lesser energy density and capacity fading hamper its commercial application.12 The effectiveness of SCs relies on the innovative features of the electrode and electrolyte materials, as well as the mechanism for storing electric charge.4 A 2 M KOH solution served as the electrolyte, where the highly mobile OH− ions facilitated efficient charge transport within the supercapacitor, enhancing its power density.13 The superior ionic conductivity of 2 M KOH, coupled with the exceptional charge storage and robust composite structure of NiZrO3/NiZrO3@GNP electrodes, paves the way for efficient energy storage and rapid delivery. This synergy is further bolstered by NiZrO3's inherent stability, ensuring long-lasting performance.
Recent research has focused on the use of carbon materials,14 molecular organic frameworks,15 different structured metal oxides (spinel, perovskite, corundum, ilmenite, wurtzite, rutile, etc.),16 chalcogenides,17 conducting polymers18 and different kinds of composites. Considering all the above concerns, we have prepared an attractive electrode combination of NiZrO3 on GNP using a fast and cost-effective microwave approach. Microwave (MW) heating presents a compelling alternative to traditional thermal heating methodologies, offering distinct advantages such as rapid and uniform heating, cost-effectiveness, and reduced energy consumption. Unlike conventional methods that rely on conductive heat transfer from the exterior, MW heating leverages its volumetric nature to achieve uniform heating throughout the material's volume. This is accomplished through direct radiation that penetrates the material's molecules, ensuring consistent thermal distribution.19 Also the MW method facilitates fast synthesis of samples. This unique heating mechanism presents a promising avenue for potentially enhancing the mechanical strength and morphology of materials compared to conventional techniques. The structural and morphological properties of the samples were analysed using different analytical tools. Further, the synthesized samples were explored towards supercapacitor electrode applications. As an SC electrode, this new combination exhibits higher capacitance, better rate performance, and good cyclic stability.
:
1. The pH was maintained at 10 by the addition of NaOH. In the temperature range of 60–70 °C, the reaction mixture was heated under constant stirring to obtain a gel. The gel was kept under microwave irradiation (800 W) for 15 minutes for a combustion reaction. The obtained powder was calcinated at 600 °C for about 2 h to get NiZrO3 powder. Fig. 1 depicts schematic illustration of synthesis of NiZrO3 (NZ).
:
1 ratio and dissolved in a beaker using dimethylsulfoxide (DMSO) as solvent. The mixture was sonicated for 30 minutes at room temperature. Then the mixture was heated at 70 °C then it undergoes auto combustion. Then dried powder was obtained as NiZrO3@GNP (NG) composite.
| C = (∫Idv)/2mv (C g−1) | (1) |
From GCD evaluations, the capacitance values were calculated using the following equation given below:
| C = (2I∫vdt)/(m × v) | (2) |
:
5
:
15 was prepared and coated on the electrode which is used as anode. Activated carbon and PVDF were mixed in the ratio of 95
:
5 which is used as cathode.
D = 0.9λ/(β cos θ)
| (3) |
SEM analysis was employed to conduct morphological observations, including the examination of shape, size, and agglomeration, for the prepared nanomaterial powders. The obtained results are presented in Fig. 3(a) and (b). The SEM image of NZ display nanoparticles are well dispersed, spherically shaped particles with an average size of 45 nm and a reasonably narrow size distribution in the range of 40 to 69 nm, SEM images of NG nanocomposite reveal that spherical shaped NZ material dispersed onto GNP surface.24,25 GNPs exhibited crumpled and wrinkled morphology.26 Additionally, the particles appear to be well-dispersed, as evident from their distribution and absence of significant agglomeration. The improved dispersion of NZ on NG nanocomposite is particularly noteworthy. The rougher surface texture and potential graphene presence in the NG image suggest a higher effective surface area compared to pure NZ. This increased surface area can provide more active sites for electrolyte interaction, potentially leading to higher capacitance in a supercapacitor.
The chemical composition of NZ and NG nano composite has been determined by EDX analysis which is displayed in Fig. 4(a) and (b). From the results of NZ material, the spectrum distinctly reveals prominent peaks corresponding to three elements: nickel (Ni), zirconium (Zr), and oxygen (O). This alignment is consistent with the anticipated composition of NiZrO3. Notably, there are no discernible peaks for any other elements, suggesting a lack of significant impurities or contamination in the sample. This attests to the purity and reliability of the analysed material, bolstering confidence in its compositional integrity. NG spectrum additionally shows a clear peak for carbon (C), indicating the presence of the successful incorporation of graphene.
Optical properties of the NZ and NG nanocomposites were studied through UV-DRS analysis which is shown in Fig. 5(a) and (b) respectively. The optical band gap energy value has been determined by means of the Kubelka–Munk function (Tauc plot).27 The graph represents [F(R)hν]2 vs. hν plots, where F(R) is denoted as Kubelka function F(R) = (1 − R)2/2R and R is denoted as reflectance in UV-visible spectra. From the Tauc plot, the estimated band gap values are 1.48 and 1.70 eV for NZ and NG respectively. The bandgap of NG (1.70 eV) is slightly higher than that of pure NZ (1.48 eV), suggesting a modification in the electronic structure due to GNP incorporation.
The management of charges between the electrodes is greatly influenced by 2 M KOH solution and a combination of its low viscosity and elevated conductivity in KOH, results in a more pronounced current response from the electrode. The area under the CV was used to evaluate the specific capacity of the active material NZ and NG. Those capacitance values are 1254, 830, 625, and 466 C g−1 for NZ and 1921.60, 1310.66, 907.49, and 636.59 C g−1 for NG which were recorded at the scan rate of 2, 5, 10, 20 mV s−1. According to the aforementioned findings, following a scan rate of 20 mV s−1, NZ and NG, respectively, preserved 37.21% and 33.13% capacitance. This could be due to the limited interaction of the electrolyte solution with the surface of the active material. Also, it is valid to indicate the presence of GNP in NZ nanocomposite effectively enhances conductivity leading the higher capacitance.
Then Dunn's method was used to evaluate the electrochemical kinetics of NZ and NG.30 Understanding the charge storage mechanisms of SCs is aided by the distinction made by Dunn's method between surface-controlled (capacitive) and diffusion-controlled processes.31 Hence total charge quantity (QT) stored in an electrode during electrochemical performance is the sum of surface capacitive charges (QS) and diffusion-controlled charges (QD).
| QT = QS + QD32 | (4) |
While diffusion-controlled charges (QD) were slowly stored using a semi-indefinite diffusion controlled redox process which is influenced by the reciprocal of the square root of the scan rate (ν−1/2) whereas surface capacitive charges (QS) accumulated rapidly through an electric double layer process which is independent of scan rate (ν).33,34 This can be depicted as follows
| QT = QS + constant 1/(√ν) | (5) |
Diffusion-controlled charges (QD) are determined by subtracting surface-controlled charges (QS) which is the intercept value obtained from an extrapolated line from a linear plot of QT versus the inverse square root of scan rates which is shown in Fig. 6(b) (plot of square root of scan rate vs. total charge (QT)).
The obtained QS values for are 70.88 C g−1 and 104.82 C g−1 for the NG and NZ respectively. Therefore, the diffusion-controlled charge contribution is calculated by deducting the surface contribution from the total charges (QT). Fig. 6(c) and (d) depicts the percentage of surface and diffusion charges that to the overall charge (QT) in the electrode materials NZ and NG respectively. From this analysis, it is apparent that the diffusion-controlled process contributes more in lower scan rates and surface contributes less so it may undergo intercalative process during charge storage mechanism. Fig. 6(e) depicts the energy storage device for characterization by determining the slope value using linear fit. As the slope values lies on 0.5466 and 0.4776 for NZ and NG respectively, which indicates that NZ behave like supercapacitor and NG behave like capacitor type.35 This may be due to the agglomeration found in SEM images that may clogged the pores in the NZ pores.
The sample was analysed with GCD to evaluate capacitive behaviour and real time application of the sample after the CV. Fig. 7 depicts the performance of GCD with varying current densities ranging from 2 to 20 A g−1 with the operating potential window of −0.15 to 0.5 mV. This study was evaluated by the discharge time of the electrode material and from this study, longer discharge time will contribute to the greater specific capacity of the material which proves that energy storage will directly be influenced by the electrochemical redox process. The specific capacity was calculated using the eqn (6). The evaluated specific capacity was 577, 355, 274, and 136 C g−1 at a specific current of 2, 5, 10, and 20 A g−1 respectively for NZ. The specific capacity of NG was calculated by the same above-mentioned method and evaluated specific capacitance (coulombic efficiency) were 1996, 1777, 796, and 398 C g−1 which were recorded at the specific current of 2, 5, 10, and 20 A g−1 respectively. Due to the synergistic effect of the GNP, obtained better results for NG when compared to NZ. At higher specific current, ions present in the electrolyte solution have reduced time to diffuse into ions in the electrode material. So less pushing of charges results in decreased specific capacity at the higher specific current.36,37
![]() | (6) |
An AC impedance analysis was utilized to elucidate the reaction kinetics and impedance in our electrochemical system of NZ of NG which is associated with the diffusion of ions at the boundary between electrode and electrolyte interface. The analysis was conducted employing an AC signal with an amplitude of 5 mV across the frequency range of 10 mHz to 100 kHz. Nyquist plot depicted in Fig. 8(a) shows the impedance which is fitted on the modified Randle's circuit. Randle's circuit encompassing solution resistance (RS), charge transfer resistance (RCT), double layer capacitance (Cdl), and Warburg impedance (ZW).38,39
![]() | ||
Fig. 8 (a) Nyquist plot. (b) Plot of log(1/ω) vs. log|Z′′|. (c) Plot of ω−1/2 (rad s−1)−1/2 vs. Z′. (d) Plot of log f vs. −phase angle (°). | ||
The high-frequency region of the plot displays a semicircular shape, implying that the rate of charge transfer is the dominant factor governing the electrochemical process. At lower frequencies, the plot transitions to an inclined line, suggesting that the diffusion of electrolyte ions becomes the primary factor influencing the storage of electrical energy. The slight leftward shift of the semicircle's center suggests that the electrode resistance plays a more significant role compared to the electrolyte resistance.40 This could be due to factors like the contact resistance between the electrode material and the nickel foam current collector, or possibly due to the intrinsic resistance of NZ itself.
The electrolyte solution resistance yielded from the interception of X in the semicircle is 1.44 Ω which is obtained from high frequency region, while its diameter indicates charge transfer resistance of 44.62 Ω and 59.18 Ω for NZ and NG respectively. In a similar vein, the inclined linear portion of the low-frequency region indicates that the electrochemical process is primarily driven by the diffusion of electrolyte ions. The electrochemical kinetics of the NZ electrode in KOH electrolyte can be further investigated under ac perturbation and the system behaves as follows: the CV analysis and GCD profiles exposed faradaic reaction of the NZ electrode, OH− ions transported through diffusion process onto the surface of the electrode is dominant. Faradaic impedance can be attributed mathematically by the sum of charge transfer resistance and diffusion controlled process (ZF(ω) = RCT + ZW(ω)). In the limit of ω → 0, the electrochemical behavior transitions to diffusion-controlled, characterized by a linear response with a slope of 45° in the low-frequency region of the impedance spectrum.
Mathematically, the impedance (ZW) at an angular frequency (ω) can be expressed using the Warburg coefficient (σ), the imaginary unit (j), and the transfer coefficient (α) and which can be written as
.41 This equation can also be written in logarithmic form. A value of 0.5 for a signifies diffusion-controlled behavior. This relationship can be expressed in both complex and logarithmic forms. Fig. 8(b) depicts log(1/ω) vs. log|Z′′|. The slope of a logarithmic plot of absolute impedance versus inverse frequency provides the transfer coefficient, with a value of 0.5248 for NG and 0.6374 for NGZ indicating diffusion-dominant behavior enhanced by the addition of GNP. The hydroxyl ion diffusion (σ) coefficient is estimated using the following equation,42
![]() | (7) |
485 C mol−1), the molar concentration of OH− ions (2 × 10−3 mol cm−3 for three electrode setup) and σW, Warburg coefficient (∼22.65 for NZ and ∼30.39 for NG) respectively and these values are obtained from the slope of
plot as shown in Fig. 8(c).43 Based on the above equation, the calculated diffusion coefficient is 2.45 × 10−13 s−1 for NZ and 9.39 × 10−12 s−1 for NG material. These results indicate that NG material exhibits a significantly higher diffusion coefficient than NZ, so the addition of GNP enhances NG allows OH− ions for faster diffusion. The Bode phase angle plot of NZ and NG are depicted in Fig. 8(d). Purely capacitive systems usually have a low-frequency phase angle in a Bode diagram that approaches −90°.44 On the other hand, the Bode phase angle plots of NZ and NG show outstanding redox performance, with the latter showing an intercept at low frequency around a phase angle of −40 and −45° respectively. Better charge storage efficiency and faster ion diffusion are associated with smaller phase angles.45 The centre frequency region of the Bode phase angle plot shows a single time constant, indicating the double layer capacitance mechanism.44
As demonstrated in Fig. 9(b), the device's estimated specific capacity based on the GCD profiles is found to start decreasing with an increase in current density, i.e., 47.10, 36.6, 25.44, and 19.2 C g−1 at 2, 4, 6, and 8 A g−1, respectively. At higher currents, the electrolyte ions struggle to reach deeper pores or active regions, resulting in incomplete utilization of the electrode's full capacity. This translates to a lower apparent specific capacity. We estimate the specific energy and power of the system using eqn (8) and (9) (ref. 37) and display the results in a Ragone plot as depicted in Fig. 9(c).
![]() | (8) |
![]() | (9) |
The coulombic efficiency (η%) is evaluated from η = Td/Tc × 100 (Td and Tc represent the discharging and charging time respectively) from the GCD curves.49 The calculated coulombic efficiency (%) is 66.12, 92.06, 95.08 and 97.42 respectively for 2, 4, 6 and 8 A g−1 as plotted in Fig. 9(f). The low coulombic efficiency at low current density is due to the morphology of the electrode material and the shorter charging/discharging times and lower charge loss at high current densities. The spherical-shaped surface is evenly dispersed with metal oxide on the graphene nanoplatelets that facilitate the electron/ions intercalation at high current densities. They provide adequate opportunities for OH− ions to make contact with electrode active sites, thus enabling the transfer of electrons and ions at higher current densities.
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