Arsha
M S
and
Biju
V
*
Department of Physics, University of Kerala, Kariavattom, Thiruvananthapuram, Kerala Pin – 695 581, India. E-mail: bijunano@gmail.com
First published on 26th February 2024
This study focuses on enhancing the performance of thermally deoxygenated graphite oxide (TDGO) supercapacitor electrodes by incorporating a redox additive viz., 0.03 M K3Fe(CN)6 in 6 M KOH. Characterization of the prepared TDGO was conducted through XRD, Raman, XPS, FESEM and BET surface area analysis, revealing incomplete deoxygenation and the presence of oxygen functional groups. TDGO exhibits a maximum significant surface area of 288.3 m2 g−1 with an average pore diameter of 2.4 nm. The ID/IG ratio of 0.98 suggests the prevalence of structural defects dominating the sp2 graphitic structure. FESEM images reveal exfoliated irregular layers in TDGO. In a three-electrode configuration, the optimized system achieves an areal specific capacitance (Csp) of 817 F cm−2 at 1 A g−1, a 2.5-fold increase compared to 6 M KOH alone. The [Fe(CN)6]3−/[Fe(CN)6]4− redox couple in the electrolyte alters the charge storage mechanism from surface-controlled to diffusion-controlled pseudocapacitance. A symmetric TDGO300 supercapacitor in the KOH/K3Fe(CN)6 redox electrolyte system exhibits a Csp of 414.6 F cm−2, delivering an energy density of 17.4 W h kg−1 at a power density of 235 W kg−1. Notably, the TDGO300 supercapacitor retains 97.4% of its initial capacitance after 2000 continuous charge–discharge cycles. This work establishes a straightforward strategy to significantly improve the capacitive performance of TDGO supercapacitors by leveraging redox additives, showcasing their potential for advanced energy storage applications.
The strategy of employing redox additives to improve the electrochemical performance of rGO has been widely explored.3–5 In most of these studies, composites with rGO were prepared, followed by the optimization of a redox additive electrolyte to enhance the overall performance. Ahmed Galal et al. investigated the impact of a redox electrolyte (0.08 M KI − 1 M NaNO3) on the specific capacitance of SrRuO3−reduced graphene oxide nanocomposites.5 The addition of KI to the NaNO3 solution led to a remarkable 21.6-fold increase in specific capacitance. Adam Moyseowicz et al. demonstrated the superior electrochemical performance of the polypyrrole/reduced graphene oxide (PPy/rGO-HT) composite electrode in an aqueous electrolyte containing hydroquinone redox-active species.3 Sankar et al., conducted a study on the electrochemical performance of hydrothermally reduced graphene oxide (rGO) in a KOH + KI redox additive electrolyte, resulting in superior specific capacitance and energy density.4 The optimized 1 M KOH + 0.05 M KI electrolyte yielded a specific capacitance of 500 F g−1 with an energy density of 44 W h kg−1 at 0.83 A g−1. This stands as the sole study attempting to modify the electrochemical properties of rGO using a redox additive. However, no report has yet appeared in the literature where redox additives were added to electrolytes to boost the energy storage ability of thermally deoxygenated graphene oxide (TDGO) electrodes.
Different reduction techniques have been employed to obtain reduced graphite oxide (rGO) from graphite oxide (GO), including chemical reduction, photo-assisted methods, microwave routes, thermal deoxygenation etc.6 Among the reduction techniques, chemical reduction stands out as the widely used method, primarily due to the quality of the end product. Chemical reduction of GO can be effectively done by using a wide range of reducing agents such as hydrazine,7 alcohol,8 sodium/potassium hydroxide,9 sodium borohydride,10 hydriodic acid,11 acetic acid,12 and iron/aluminum powder.13 However, envisioning the use of chemical reduction at a large-scale poses challenges because the commonly used reductants are unsuitable, given their safety concerns and high cost. For example, the instability and carcinogenic nature of hydrazine, a widely used reductant, and the reactivity and harmful effects of sodium borohydride limit their practicality.14 Moreover, the exfoliation process using organic solvents is often hindered by the difficulty of eliminating the solvent due to their high boiling points.15 In chemical reductions, the reduction level of rGO cannot be easily controlled and the conductivity of rGO is relatively low when compared with graphite or graphene.13 In this context, the direct thermal treatment/deoxygenation of graphite oxide (GO) is a highly desirable approach for synthesizing large scale, porous reduced graphene oxides (rGOs) for energy storage applications. The process relies on the energetic thermal exfoliation of GO's lamellar structure during heating. We prefer to use the term “thermal deoxygenation” rather than the commonly used “thermal reduction”, because the latter requires the use of a reducing agent, a chemical compound that readily donates electrons.16 One significant advantage of thermal deoxygenation is its ability to simultaneously achieve both exfoliation and deoxygenation without introducing impurities from heteroatoms.
The present work reports a simple, straightforward method to enhance the Csp of TDGO supercapacitors. We designed a supercapacitor system with a TDGO electrode and a redox-electrolyte, 6 M KOH + 0.03 M potassium ferricyanide (K3Fe(CN)6), which combines two kinds of charge storage mechanism, viz., surface controlled, and diffusion controlled pseudocapacitance. The [Fe(CN)6]3−/[Fe(CN)6]4− redox couple present in the redox additive electrolyte system entirely alters the charge storage mechanism of the supercapacitor. The charge storage became controlled by diffusion, whereas previously, it was limited to the surface in the 6 M KOH electrolyte. In the redox additive electrolyte, we obtained capacitance values of 817 F cm−2 in the redox-electrolyte and 316 F cm−2 in the 6 M KOH electrolyte. This significant improvement in capacitance is attributed to the additional redox reactions near the electrode interface via the constituent ions of the KOH/K3Fe(CN)6 redox electrolyte.
Fig. 1 XRD patterns of graphite (GR), graphite oxide (GO), and TDGO100, TDGO200, TDGO300 and TDGO400 active materials. |
Fig. 2 shows the Raman spectra of the TDGO samples alongside the spectra of GR and GO. In both the GO and TDGO samples, D and G bands are present as in the case of GR, although with variations in position and intensity. The spectrum of graphite displays a strong band at 1575 cm−1 (G band) and a weak band at 1344 cm−1 (D band), which is typical in polycrystalline samples.23 Additionally, GR exhibits a second harmonic of the D band, the G′ band, around 2700 cm−1. In the Raman spectrum of GO, the D band is at 1355 cm−1, and the G band is at 1594 cm−1, with comparable intensity, resulting in an ID/IG ratio of 0.84. For TDGO samples, the positions of the G and D bands appear at the same positions as in GO with variations in the ID/IG ratio. The ID/IG ratios are 1.03, 0.87, 0.98 and 0.96 for TDGO100, TDGO200, TDGO300, and TDGO400, respectively. The ID/IG ratio is inversely proportional to the in plane crystalline size.21 Notably, in the spectra of TDGO300 and TDGO400, the intensity of the D band is almost equal to that of the G band, indicating a prevalence of structural defects dominating the sp2 graphitic structure. These defects may involve misarranged C atoms or missing atoms.16 In contrast, for TDGO200 the intensity of the G band is higher, suggesting a lower degree of structural distortion.
Fig. 2 Raman spectral analysis of graphite (GR), graphite oxide (GO), and TDGO100, TDGO200, TDGO300 and TDGO400 active materials. |
Additionally, a broad second-order band centred at ∼2930 cm−1 is present in the spectra of the GO and TDGO samples. To assign the spectral features in the second-order region, the spectra were fitted to three Lorentzian peaks (ESI,† Fig. S4). The bands appearing at about 2690, 2930 and 3190 cm−1 were assigned to the 2D, D + D′ (combination band) and 2 D′ (overtone band) band, respectively.24 In addition to these a peak marked as the C peak in TDGO100 corresponds to the C–H stretching mode of aromatic C.25 The 2D and 2D′ bands originate from processes in which momentum conservation is satisfied by two phonons with opposite wave vectors and they do not require defects for activation. In contrast, the D + D′ band is the combination of phonons with different moments and therefore requires defects for its activation.24
To investigate the surface morphology, FESEM images were obtained. The FESEM images of TDGO samples are displayed in Fig. 3(a) to (d). The microstructure changed significantly on thermal deoxygenation. TDGO100 and TDGO200 contain closely stacked layers of rough, wrinkled, and irregular graphene sheets as shown in Fig. 3(a) and (b). While TDGO300 and TDGO400 sheets exhibit exfoliated graphene sheets as depicted in Fig. 3(c) and (d). The separation between layers is evident for TDGO300 and TDGO400, resulting in a large surface area.26
The surface areas of the TDGO samples were analyzed using the Brunauer–Emmett–Teller (BET) method based on nitrogen adsorption–desorption isotherms at 77 K. The results, illustrated in Fig. 4 analysis, revealed a typical type IV isotherm with an H3 hysteresis loop for all samples, indicating mesoporous nature.27 Pore size distribution analysis using the Barrett–Joyner–Halenda (BJH) method further confirmed a mesoporous structure, with average pore diameters of 3.8, 9.8, 2.4, and 10.2 nm for TDGO100, TDGO200, TDGO300, and TDGO400, respectively. At a relative pressure above 0.4, a distinct hysteresis loop suggests capillary condensation in mesopores across all samples.28 The specific surface areas were calculated as 66.1, 120.3, 288.3, and 229.6 m2 g−1 for TDGO100, TDGO200, TDGO300, and TDGO400, respectively. The specific surface area increased with deoxygenation temperature up to 300 °C, with TDGO300 exhibiting the highest value. Beyond 300 °C, an increase in temperature led to a decrease in the surface area, which was attributed to restructuring and significant carbon atom loss. During thermal deoxygenation, carbon atoms in the GO structure with an oxidation state of +1 transform into elemental carbon (oxidation state 0) and carbon dioxide (CO2, with an oxidation state of +4). The elimination of carbon atoms as carbon monoxide (CO) and CO2 results in vacancy defects.16 The redox reactions for these transformations are detailed in the ESI† (see section ‘Redox reactions during thermal deoxygenation and vacancy defects’).
Fig. 4 Nitrogen adsorption desorption isotherms and pore size distributions of (a) TDGO100, (b) TDGO200, (c) TDGO300 and (d) TDGO400 active materials. |
XPS analyses were conducted to quantitatively assess the oxygen functional groups present in each TDGO sample. During the thermal deoxygenation of graphene oxide (GO), the elimination of hydroxyl (O–H) and epoxy (C–O–C) groups, as well as carbonyl (–CO) and carboxylic (–COOH) groups, takes place. Deconvolution of the XPS C1s spectrum of each TDGO sample was performed to provide a detailed analysis of the evolution of these functional groups with temperature, as illustrated in Fig. 5. In GO, hydroxyl and epoxide groups are attached to the basal plane, while carboxyl groups are located on the edges.29 According to a previous report by Gao et al., hydroxyl groups attached to the inner part are less stable and more easily removed compared to those attached at the edges.30 Upon deconvolution, the relative atomic percentage of hydroxyl groups decreases with increased temperature. For TDGO100 and TDGO200, 23.6% and 13.91% of hydroxyl groups are retained, respectively, while in the rest of the samples, these groups are eliminated. In TDGO100, hydroxyl groups within the inner planes are removed, and some still persist in TDGO, as evidenced by the small (001) peak on the lower 2 theta side of XRD (Fig. 1).
Fig. 5 Deconvoluted C 1s XPS narrow scans of (a) TDGO100, (b) TDGO200, (c) TDGO300 and (d) TDGO400 active materials. |
For TDGO300 and TDGO400, the percentage of other functional groups varies, as indicated in Table 1. The only consistent trend among these TDGO samples is the increase in the CC bond with deoxygenation temperature.
Functional groups | TDGO100 | TDGO200 | TDGO 300 | TDGO400 | ||||
---|---|---|---|---|---|---|---|---|
Binding energy (eV) | Relative atomic percentage (%) | Binding energy (eV) | Relative atomic percentage (%) | Binding energy (eV) | Relative atomic percentage (%) | Binding energy (eV) | Relative atomic percentage (%) | |
CC | 284.8 | 14.81 | 284.6 | 44.72 | 284.9 | 57.25 | 284.8 | 64.68 |
C–OH | 285.4 | 23.60 | 285.5 | 13.91 | — | — | — | — |
C–O–C | 285.9 | 18.20 | 286.4 | 11.31 | 286.3 | 21.38 | 286.3 | 11.50 |
CO | 287.4 | 30.51 | 287.4 | 14.60 | 288.4 | 12.41 | 287.4 | 16.46 |
COOH | 289.2 | 12.80 | 289.2 | 15.46 | 291.5 | 8.96 | 289.4 | 7.36 |
Initial electrochemical studies were carried out in a three-electrode system, with platinum (Pt) wire, Ag/AgCl, and 6 M KOH solution as the counter electrode, reference electrode, and electrolyte, respectively. Fig. S5(a) to (d) (ESI†) depict the CV curves recoded by varying the scan rate (ν) from 50 to 100 mV s−1 for TDGO100, TDGO200, TDGO300 and TDGO400, respectively. The response current (i) to an applied scan rate varies depending on whether the charge storage kinetics is diffusion controlled, or surface controlled (capacitive). The general relationship between the peak current (ip) and the scan rate (ν) can be written as follows, as suggested by Dunn's method:31
ip = k1ν + k2ν0.5 | (1) |
For a diffusion-controlled reaction, ip ∝ ν0.5, while ip ∝ ν represents a surface controlled reaction. The anode peak current (ip) values of TDGO100, TDGO200, TDGO300 and TDGO400 active materials fit well to the scan rates ν1.1, ν0.74, ν1.2, and ν0.53, respectively (ESI,† Fig. S6(a) to (d)). This suggests that the charge storage mechanisms in TDGO100 and TDGO300 are predominantly governed by surface-controlled kinetics, while TDGO400 exhibits diffusion controlled charge storage and TDGO200 experiences a combination of both surface-controlled kinetics and diffusion.
The areal specific capacitance (Csp) of these TDGO electrodes was calculated from the GCD curves using the following equation:
(2) |
Fig. S7(a) to (d) (ESI†) show the GCD curves of the TDGO active materials with the current density varying from 0.5 to 1 A g−1. The Csp values of these active materials were 9.4, 51, 316, and 126 F cm−2 for TDGO100, TDGO200, TDGO300 and TDGO400, respectively, at 1 A g−1. Based on the GCD curves, the energy density, E (W h kg−1) and power density, P (W kg−1) were calculated using eqn 3 and 4 given below:
(3) |
(4) |
The energy density values were remarkably low, 0.39, 2.14, 13.27 and 5.29 W h kg−1, respectively, for TDGO100, TDGO200, TDGO300 and TDGO400 with a consistent power density of 275 W kg−1 at 1 A g−1. Considering the notable specific capacitance and energy density of TDGO300, further studies were focused on this active material and the results of GCD measurements are given in Table S2 (ESI†). In order to optimize the redox additive for enhanced performance, we have examined the compatibility of various redox additives such as potassium ferricyanide (K3Fe(CN)6), potassium ferrocyanide (K4Fe(CN)6), and potassium bromide (KBr) with 6 M KOH electrolyte as shown in Fig. S8 (ESI†). Among these, 6 M KOH with 0.03 M K3Fe(CN)6, in conjunction with TDGO300, exhibited the best current response in cyclic voltammetry (CV) studies, as shown in Fig. S8(a) (ESI†). This optimal redox additive combination was selected for further electrochemical characterizations.
Fig. 6a displays the CV curves of TDGO300 electrodes at various scan rates ranging from 50 to 100 mV s−1. The response current increases as the scan rate rises from 50 to 100 mV s−1. At lower scan rates, a thick diffusion layer forms on the electrode surface, impeding the flow of electrolyte towards the electrode resulting in a lower current.32 Conversely, at higher scan rates, the limited time available prevents the formation of a thick diffusion layer and consequently, the electrolyte can readily access the electrode, leading to an increase in the response current.33
Fig. 6b shows the dependence of the anode peak current “ip”on the scan rate “ν”. The best fit of the data to the power law dependence yields ip ∝ ν0.62. The power-law dependence ip ∝ ν0.62 suggests that the charge storage mechanism of TDGO300 in KOH/K3Fe(CN)6 redox additive electrolyte involves the combined contributions from diffusion-controlled and surface-controlled reactions. The index 0.62 (close to 0.5) signifies the predominant contribution of diffusion- over surface-controlled reactions. Fig. 6c further distinguishes the fractions of current contributions by determining the factors k1 and k2 in eqn (1) at a specific potential of 0.45 V (vs. Ag/AgCl). It is noted that the diffusion contribution dominates over the other at all scan rates, and this dominance eventually decreases at high scan rates. The diffusion-controlled capacitance varies from 87.2 to 83.5% as the scan rate increases from 50 to 90 mV s−1. This observation validates the high response current at high scan rates.
The following surface redox reactions can describe the pseudocapacitive contribution of the TDGO300 electrode.2,34
>C–OH ⇌ >CO + H+ + e− | (5) |
–COOH ⇌ –COO + H+ + e− | (6) |
>CO + e− ⇌ >C–O− | (7) |
The above reactions represent the surface redox reactions from the oxygen functional groups in TDGO300, while the contribution of the redox-electrolyte can be described by the following equation:35
[Fe(CN)6]3− + e− ↔ Fe(CN)64− | (8) |
During charging, Fe(CN)63− is reduced to Fe(CN)64− ions at the cathode, similarly during discharging Fe(CN)64− ions get oxidised to Fe(CN)63− ions at the anode side.
Fig. 6d shows the GCD curves with current density ranging from 1 to 5 A g−1. The nonlinear GCD curves confirm the redox contribution from the electrode as well as the electrolyte side during the charge/discharge. The specific capacitance in this system is contributed by both the TDGO300 electrode and KOH/K3 Fe(CN)6 electrolyte together.36 To evaluate the gravimetric capacitance (F g−1), it is essential to know the weight of all K3 Fe(CN)6 ions participating in the charge transfer process. However, not all K3 Fe(CN)6 ions in the electrolyte take part in the charge transfer process. Given this situation, instead of reporting gravimetric capacitance, it is more reliable to express the areal specific capacitance (Csp in F cm−2).35 The reaction described in eqn (8) takes place at the surface of the electrode. Consequently, the redox dependent areal specific capacitance can be determined from the GCD curve using eqn (2) mentioned earlier.
The calculated specific capacitance is 817 F cm−2 at 1 A g−1, and when the current density is increased to 2, 3, 4, and 5 A g−1, the specific capacity is decreased to 732, 680, 601 and 564 F cm−2, respectively. To gain a better understanding of the enhanced electrochemical performance of TDGO300 in a redox additive electrolyte, we compared the performance of the TDGO300 electrode in 6 M KOH alone. In Fig. S5(c) (ESI†), the CV curves in 6 M KOH over a scan rate from 60 to 100 mV s−1 are depicted. The characteristic CV shape is not significantly influenced as the scan rate is increased. The power law dependence of ip ∝ ν1.2 (shown in ESI,† Fig. S6(c)), shows that the charge storage kinetics of the TDGO300 electrode is primarily surface controlled in 6 M KOH. The visible redox peaks in CV and plateau regions in the GCD curves (ESI,† Fig. S7(c)) indicate the surface redox reactions from the oxygen functional groups. The linearity between ip and ν indicates the reversible charge transfer process from the oxygen functional groups. The charging process corresponds to the oxidation of oxygen functional groups, while the discharging process corresponds to their reduction. Meanwhile in the case of KOH/K3 Fe(CN)6 redox electrolyte there is a noticeable shift in the reduction peak towards a lower potential (Fig. 6(a)). This signifies the irreversibility of the redox couple Fe(CN)63−/Fe(CN)64−.35 The specific capacitance (Csp) of TDGO300 was 316 F cm−2 at 1 A g−1 in 6 M KOH electrolyte. The Csp shows an approximately 2.5-fold increase with the addition of 0.03 M K3Fe(CN)6 at 1 A g−1. The electron transfer between the redox species [Fe(CN)6]3− and [Fe(CN)6]4− is responsible for the enhanced charge storage capacity in the KOH/K3Fe(CN)6 redox additive electrolyte. Based on the GCD curves, the energy and power densities were calculated using eqn 3 and 4 and are shown in Table S2 (ESI†).
The energy power densities of TDGO300 with redox additives are significantly higher than those without redox additives (ESI,† Table S3). In the KOH/K3Fe(CN)6 redox additive system, TDGO300 exhibited an energy density of 34.3 W h kg−1 and a power density of 189.2 W kg−1 at a current density of 1 A g−1. In contrast, the energy density of TDGO300 in 6 M KOH alone is much lower at 13.3 W h kg−1, with a power density of 275 W kg−1.
A cycling stability test in KOH/K3Fe(CN)6 redox additive electrolyte was performed to further assess the electrochemical properties of the TDGO300 electrode as depicted in Fig. 7a. Notably, there is a fluctuation in specific capacitance compared to the case of 6 M KOH alone (Fig. 7b). The TDGO300 electrode exhibits capacitance retention of 93% in the presence of redox additive after 2000 charge–discharge cycles, whereas it achieves 98% in the absence of the redox additive. The reason behind the lower specific capacitance retention of TDGO300 in the redox additive system can be explained as follows. Initially, in the redox additive system, the electrolyte consists of only [Fe(CN)6]3− ions. After the initial electrochemical reaction, the [Fe(CN)6]3− ions get reduced to [Fe(CN)6]4− ions. As the reaction proceeds, more redox species get adsorbed on the TDGO300 electrode surface. This results in larger diffusion resistance for other ions in the electrolyte such as K+ and OH−. Consequently, there is a gradual decrease in specific capacitance, observed over 750 continuous charge–discharge cycles (Fig. 7a). As the cycling number increases, the redox couple shuttles between 3− and 4− oxidation states, leading to an eventual increase in capacitance retention. The fluctuation in specific capacitance retention is attributed to the competition between the diffusion effect and redox transition of [Fe(CN)6 ]3−/[Fe(CN)6]4− ions.35 Finally, after 2000 charge–discharge cycles 93% of the initial capacitance is retained.
Fig. 7 The results of cycling stability tests of (a) 6 M KOH + 0.03 M redox additive electrolyte and (b) 6 M KOH alone. |
The electrochemical impedance spectroscopy (EIS) results are presented in Fig. 8. In Fig. 8(a), the EIS of the redox additive system is depicted, while Fig. 8(b) corresponds to 6 M KOH alone. The Nyquist plot can be fitted by a circuit equivalent to that present in the inset of the figure. The charge transfer resistance and reaction kinetics were analysed using EIS, consisting of a semicircle and a straight line region. The interfacial charge transfer resistance (Rct) was calculated from the span of the semicircle along the real axis of the spectrum from the high to low frequency region. The equivalent series resistance (Rs) is obtained from the intersecting point of the spectrum with the real axis in the high frequency limit. Here, Rs represents the sum of ionic resistance of the electrolyte, the intrinsic resistance of the electrode material and the contact resistance at the electrode electrolyte interface.37 The figure indicates that the redox additive system has a smaller Rct (1.26 × 102 Ω) and Rs (1.39 Ω) compared to others (Rct = 3.24 × 102 Ω, Rs = 2.21 Ω). The transition from the semicircle to a slopped tail in the low frequency region can be described by the Warburg element (W), which is a result of the frequency dependence of ion diffusion/transport in the electrolyte to the electrode surface. The higher W element (1.59 × 10−2) of the redox additive system compared to other (1.86 × 10−3) signifies dominant diffusion-controlled charge storage kinetics of TDGO300 in the redox system. This also suggests that redox additives can facilitate faster ion diffusion/transport to the electrode surface.
Fig. 8 EIS measurements in the frequency range of 0.1 to 105 Hz with the equivalent circuit for the TDGO300 electrode in (a) 6 M KOH + 0.03 M K3Fe(CN)6 redox additive system, and (b) 6 M KOH. |
In addition to the three electrode cell characterization, we conducted symmetric two electrode measurements using a Swagelok cell assembly with KOH/K3Fe(CN)6 redox additive electrolyte. Electrochemical performance was assessed through CV, GCD, EIS and cycle stability studies. The electrodes were tested in the same voltage window, viz. 0.55 V. The CV curves, recorded at different scan rates ranging from 50 to 100 mV s−1 (Fig. 9(a)), exhibit quasi-rectangular shapes. Notably, this quasi-rectangular CV profile persists even at a high scan rate of 100 mV s−1, with a b value of 0.61 confirming the predominant contribution of diffusion-controlled charge storage kinetics as shown in Fig. 9(b). This observation was further verified by the cyclic voltammetry data, showing that the surface capacitive contribution varies from 60.7% to 52.2% as the scan rate increases from 50 to 100 mV s−1 shown in Fig. 9(c).
The GCD curves, recorded at various current densities from 1 to 4 A g−1 (Fig. 9(c)), demonstrate a nonlinear response, confirming the prevalence of surface redox capacitive behaviour. However, it is worth noting that the GCD profile does not exhibit any plateau region compared to three-electrode measurements. The difference in the shape of the GCD curves between three-electrode and two-electrode characterizations could be attributed to several factors. One potential reason is that the three-electrode characterization method is more sensitive to the impedance of the redox electrolyte and the contact resistance between the electrode and redox electrolyte. Additionally, redox transitions are more pronounced in the three-electrode configuration, resulting in plateau regions in the GCD curves. In contrast, the two-electrode method is less sensitive to these factors, hence yielding a different shape for the GCD curves as shown in Fig. 9(c). The specific capacitance values were calculated from the GCD curves using the equation:
(9) |
The specific capacitance values were obtained as 414.6, 331.4, 254.4, 168.2 F cm−2, respectively, at 1, 2, 3, and 4 A g−1. The symmetric system delivers an energy density of 17.4 W h kg−1 at a power density of 235 W kg−1 (ESI,† Table S4).
Fig. 10(a) depicts the EIS spectrum together with the equivalent circuit. The faradaic charge transfer resistance Rct is 23.67 Ω, which is responsible for the electron transfer kinetics of redox reactions at the electrode–electrolyte interface. The combined effect of ionic resistance of the electrolyte and interfacial system resistance results in a series resistance of Rs = 2.55 Ω. In addition to this, the EIS plot exhibits a Warburg impedance W of 4.90 × 10−2, appearing as a 45° inclined line. The cycling stability of the supercapacitor was examined at a current density of 5 A g−1 for up to 5000 charge–discharge cycles as shown in Fig. 10(b). The TDGO300 supercapacitor retained 96.8% of its initial capacitance in the redox additive electrolyte.
Fig. 10 (a) EIS spectra of TDGO300 in a redox additive electrolyte with equivalent circuit and (b) result of the cycling stability test for up to 5000 charge–discharge cycles. |
The specific capacitance, energy density, and power density values obtained for the TDGO300 supercapacitor in the redox additive electrolyte are comparable with the values reported for other carbon materials, including activated carbon, carbon nanotubes, and reduced graphene oxide. Table 2 compares the electrochemical performance of carbon materials with KOH electrolyte with that of the present study. Additionally, reports of composites of rGO with redox-mediated KOH electrolyte are also included. We have also compared the results of the present study with some advanced electrode materials such as perovskites, bimetallic carbide, metal oxides, and transition metal oxides in KOH electrolyte.38–42 It can be noted that the results of the present study are commendable.
Electrode material | Redox additive electrolyte | Specific capacitance, Csp (F g−1), current density (A g−1) | Energy density, E (W h kg−1) | Power density, P (W kg−1) | Ref. | |
---|---|---|---|---|---|---|
Co–Al layered double hydroxide | KOH + K4Fe(CN)6 | 317 F g−1 at 2 A g−1 | — | — | 43 | |
KOH + K3Fe(CN)6 | 712 F g−1 at 2 A g−1 | |||||
Manganese dioxide, MnO2 | KOH + p-phenylenediamine | 325.24 F g−1 at 1 A g−1 | 10.12 | — | 44 | |
Activated carbon | KOH + p-phenylenediamine | 605.22 F g−1 at 1 A g−1 | 19.86 | 16.99 k | 45 | |
Single walled carbon nanotube, SWCNT | KOH + p-phenylenediamine | 162.66 F g−1 at 1 A g−1 | 4.23 | — | 46 | |
MWCNTs | KOH + m-phenylenediamine | 78 F g−1 at 0.5 A g−1 | 9.99 | 5.78 k | 47 | |
SrRuO3 | Hydroquinone + (H3PO4) | 62.4 F g−1 | 5 | |||
Hydroquinone + (NaNO3) | 101 F g−1 | |||||
Polypyrrole/reduced graphene oxide | 1 M H2SO4 + 0.2 M hydroquinone (HQ) | 60 F g−1 | 6.5 | 80 | 3 | |
Reduced graphene oxide | 1 M KOH + 0.05 M KI | 500 F g−1 at 0.83 A g−1 | 44 | — | 4 | |
N,P-doped carbon microsphere/reduced graphene oxide nanocomposites | H2SO4 + KI | 654 F g−1 at 2 A g−1 | 14.53 | 40.2 | 48 | |
Activated carbon (3E) | 1 M H2SO4 + 0.08 KI | 912 F g−1 at 2 mA cm−2 | 19.04 | 224.43 | 44 | |
Polypyrrole-modified SrFeO3−δ perovskite | PVA-KOH | 421 F g−1 at 1 A g−1 | 24.5 | 909 | 42 | |
SrCo0.9Fe0.1O3-δ@CC | — | 91.8 F g−1 at 1 A g−1 | 7.6 | 800 | 41 | |
Fe3Mo3C/Mo2C@CNTs | 1 M KOH | 202.3 F g−1 at 1 A g−1 | 39.9 | 18000 | 40 | |
CoO@Co2V2O7 | — | 7.58 F cm−2 | 0.45 mWh cm−2 | 1.60 mW cm−2 | 39 | |
2 mA cm−2 | ||||||
Copper molybdenum sulfide Cu2MoS4 | 1 M KOH | 33.9 mA h g−1 at 1 A g−1 | 16.8 | 800 | 38 | |
Thermally deoxygenated graphite oxide (TDGO) | 3 E | 6 M KOH | 817 F cm−2 at 1 A g−1 | 34.3 W h kg−1 | 189.2 W kg−1 | Present Work |
6 M KOH + 0.03 M K3Fe(CN)6 | 316 F cm−2 at 1 A g−1 | 13.3 W h kg−1 | 275 W kg−1 | |||
2 E | 6 M KOH + 0.03 M K3Fe(CN)6 | 414.6 F cm−2 | 17.4 W h kg−1 | 235 W kg−1 |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3ma01188g |
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