Open Access Article
Ana Paula
Mártire
,
Omar
Azzaroni
,
Waldemar
Marmisolle
* and
Matias
Rafti
*
Instituto de Investigaciones Fisicoquímicas Teóricas y Aplicadas (INIFTA), Departamento de Química, Facultad de Ciencias Exactas, Universidad Nacional de La Plata-CONICET, La Plata B1904DPI, Argentina. E-mail: wmarmi@infita.unlp.edu.ar; mrafti@quimica.unlp.edu.ar
First published on 13th November 2025
Amid the global energy crisis, the search for safe, sustainable, and high-performance energy storage is urgent. Supercapacitors—renowned for their exceptional power density and cycling stability—offer a compelling path forward, especially when engineered with eco-friendly materials and neutral-pH aqueous electrolytes. In this work, we present a simple yet powerful layer-by-layer (LbL) strategy to fabricate supercapacitor electrodes by integrating porous carbon from pyrolyzed ZIF-8 (PCZIF-8) with a polyaniline–polystyrene sulfonate (PANI-PSS) complex. The resulting films were probed via cyclic voltammetry and electrochemical quartz crystal microbalance (eQCM) to unravel their charge-storage dynamics, while galvanostatic cycling tested their long-term resilience. The composite film exhibits specific capacitances of 225 F g−1 in 0.1 M HCl and 160 F g−1 in 0.1 M KCl for 1 A g−1 charge–discharge galvanostatic curves. The specific capacitance increased by more than 1000% when a porous carbon was used instead of a non-porous one. The inclusion of PCZIF-8 delivered a substantial performance leap under mild, environmentally benign conditions—all using low-cost, readily synthesized components. This synergy between conductive polymers and porous carbons from MOFs opens a sustainable and scalable route to next-generation energy storage.
Due to the important sustainability requirement, great efforts are currently being devoted to designing SC with low environmental impact, both regarding synthetic procedures and operating conditions.10 Main challenges for such a goal are the substitution of commonly used hazardous electrolytes and highly corrosive chemicals involved in the synthesis and activation of porous materials.11 A way to tackle the above-discussed issues would be, for example, to obtain porous carbon materials using synthetic procedures that do not require harsh activation, and ideally, integrating them into electrochemical systems that could operate efficiently with aqueous neutral electrolytes.12
Thinking of possible ways to address the above challenges, metal organic frameworks (MOFs) become an interesting option. MOFs are crystalline solids composed of metal ions coordinated with organic linkers into high surface area, non-covalent porous networks that yield porous carbon particles when pyrolyzed under appropriate conditions.9,13–15 MOFs are extensively used in energy-related applications due to their tuneable pore-wall chemistry, high surface areas, and the possibility of controlling particle size and morphology.16 Most common applications use pyrolyzed MOFs for SC assembly due to their dielectric nature; however, the number of conductive MOFs reported is rapidly increasing, thus opening new paths for innovation in this regard.17,18 Pyrolysis conditions and parent MOF chosen are decisive for the resulting material and must be tuned accordingly. For example, relatively low temperatures (up to 600 °C) render incomplete carbonization and partial elimination of common carbon templates added. Although high temperature pyrolysis (up to 1000 °C) favours the appearance of additional porosity due to increased graphitization and elimination of metal atoms present, excessive and fast heating can cause the collapse of the porous network together with loss of heteroatoms from MOF linkers, which in turn reduces nanocarbon conductivity.19–21
One of the most visited MOF subclasses for this and other related applications is the so-called zeolite imidazolate frameworks (ZIFs), built from the combination of N-bidentate imidazole linkers and tetrahedrally coordinated M2+ metal ions (e.g., M = Co, Zn).22 Depending on the actual imidazole ring present, ZIF materials receive a distinctive number added to the acronym for their identification. A particularly popular member is the material composed of 2-methyl-imidazolate linkers, known as ZIF-8, which due to its biocompatibility, relatively high thermal/chemical stability, and both varied and straightforward synthesis with inexpensive chemicals and solvents, has been employed for several different applications ranging from catalysis to separations and optics23–27 Since pioneering reports from almost a decade ago, there have been multiple efforts oriented to establishing protocols for controlled production of micro/mesoporous carbon from ZIF-8 (PCZIF-8) that could be employed in the assembly of electroactive nanoarchitectures.23,28–33
One of the main issues to be addressed in the assembly of PCZIF-8 SC electrodes is ensuring mechanical stability and electrochemical connectivity when processed into films. Conducting polymers (CPs) such as poly(3,4-ethylenedioxythiophene) (PEDOT) or polyaniline (PANI) and their complexes with other polymers like poly(styrenesulfonate) (PSS) offer a compelling solution, as they can provide both adhesion and additional electrochemical activity34–36 The combination can be achieved through several approaches, e.g., by carrying surface chemical polymerization of aniline in the presence of colloidal PCZIF-8 (yielding core@shell nanoarchitectures),37via mixing with (PEDOT:PSS),36,38 or by creating porous carbon covered PANI fibres, which are then deposited on a conductive electrode substrate.39,40 Another reported method incorporates both PANI and ZIF-8 into an aerogel matrix, which is subsequently co-carbonized within the aerogel structure.41
In all the above-discussed approaches, the porous carbon nanomaterial needs to be processed using adequate solvents, deposited, and then dried before the SC can be subjected to electrochemical testing. Our contribution aims to demonstrate a sequential soft assembly of SC components, which can also perform under neutral aqueous electrolyte. For this end, we took advantage of our previous experience with electrode–electrolyte interface engineering via layer-by-layer (LbL) assembly, enabling thus precise control over film architecture by alternately depositing positively and negatively charged species, thereby promoting intimate contact in well-organized hybrid three-dimensional structures.42–45 Aqueous near-neutral conditions employed are appealing to the environmental impact of the approach; however, poses a challenge due to PANI's limited electroactivity.46,47 To overcome this limitation, we included instead (PANI:PSS) complexes obtained through ad-hoc template polymerization, improving stability and procesability.48–50 Following previously explored approaches, we propose the use of ZIF-8 MOF-derived porous carbon using commercial non-porous graphitic carbon as a benchmark.51,52
Films obtained via LbL were investigated by a combination of cyclic voltammetry and galvanostatic charge–discharge experiments. Their electrochemical capacitance and process dynamics were studied using a quartz crystal microbalance (QCM and eQCM). This work shows that the incorporation of porous carbon nanoparticles into (PANI:PSS) composite films increase the EDLC contribution to the electrode's capacitance and significantly improves its electrochemical response. This approach presents a promising pathway to develop high-performance, neutral-electrolyte supercapacitors with improved efficiency and durability.
400 rpm, 10 minutes), washed twice with fresh methanol, and dried overnight at 60 °C.
Next, the sample underwent pyrolysis at 750 C for 4 hours in a nitrogen atmosphere, resulting in a black powder identified as ZIF-8 porous carbon (PCZIF-8). This process is illustrated in Fig. 1A. The N2 adsorption isotherms for both ZIF-8 and PCZIF-8 were measured (Fig. 1B), and BET surface area analysis (Fig. S3) revealed values of 1475 m2 g−1 for fresh ZIF-8 and 875 m2 g−1 for the pyrolyzed material. The adsorption isotherm of the PCZIF-8 also revealed, in addition to the preserved microporosity, a characteristic hysteresis loop indicative of mesoporosity. Although some reduction in surface area is to be expected from pyrolysis, the value obtained is relatively lower compared to other reported protocols. This can be understood considering that, although the selected temperature is high enough to cause graphitization and conversion into amorphous carbon (see Raman spectra below), yet low enough to ensure the preservation of both N and Zn heteroatoms in the PCZIF-8. We have selected this temperature, which represents an optimal balance between the upper and lower pyrolysis limits, in order to preserve the conductivity and microporosity of the material obtained, features that contribute to the enhancement of SC performances.
![]() | ||
| Fig. 1 (A) Scheme of the synthesis of PCZIF-8. (B) N2 adsorption isotherm for ZIF-8 and PCZIF-8. (C) XPS Zn 2p band and (D) N 1s band for PCZIF-8. | ||
To analyse the composition of PCZIF-8, X-ray photoelectron spectroscopy (XPS) was used, focusing on the Zn (Fig. 1C) and N (1D) binding energy regions. Two oxidation states of Zn were identified: Zn2+ at 1046.22 and 1023 eV, and Zn0 at 044.75 and 1021.7 eV. Additionally, pyridinic, pyrrolic, and graphitic nitrogen were detected at 398.3, 399.67, and 400.9 eV, respectively. These results confirm that PCZIF-8 is a porous carbon material with a high surface area including nitrogen and zinc into its porous matrix.
To optimise the conditions for film growth, different assembly conditions were tested. PCZIF-8 was dispersed in water using two concentrations of CTAB: 10 mg ml−1 (C1) and 20 mg ml−1 (C2). The PANI-PSS dispersion was prepared in two forms: acidic (diluted in 0.5 M HCl) and neutral (neutralised with KOH and then diluted in deionized water). These variables were combined to create four different systems, which were tested by growing films on clean glass substrates and measuring absorbance at 750 nm, at which PANI-PSS shows maximum absorption (Fig. 2B). Absorbance increased with each deposition cycle for all four systems. However, the most consistent and regular growth was observed in the system combining neutral PANI-PSS with PCZIF-8 dispersed in C1. This system was selected for further experiments.
The prepared dispersions were analysed using Z-potential measurements (Fig. 2C). The PCZIF-8 dispersions had a Z-potential of +40.2 mV (C1) and, +32.2 mV (C2). In contrast, the neutral PANI-PSS dispersion showed a Z-potential of −21.6 mV and, acidic PANI-PSS -13.8 mV. These opposite surface charges confirm that electrostatic interactions make the LbL assembly feasible. Additionally, the size of the dispersed meso-microporous carbon particles was measured using dynamic light scattering (DLS), revealing a hydrodynamic size of 440 nm in diameter for both CTAB concentrations.
Next, the film produced and each component were studied by Raman spectroscopy (Fig. 2D). For the PCZIF-8 a typical graphitic carbon spectrum was observed: the G band associated with the ordered sp2 structure at 1570 cm−1 and the D band related to the defective structure at 1330 cm−1.55–57 The ratio IG/ID = 0.3 is indicative of a graphitic-type material. In the PANI-PSS sample three characteristic signals were identified: at 810 and 1170 cm−1 the C–H bending in the quinoid and benzenic ring and at 1486 cm−1 the C
N stretching.51 These five signals could also be observed in the assembly spectrum, confirming the presence of PANI-PSS and PCZIF-8 in the composite film.
To further characterise the PCZIF-8 dispersion and the assembly, microscopic images were taken with a scanning electron microscope (SEM). Fig. 2D (left), shows the PCZIF-8 dispersion deposited on a clean Au surface. The PCZIF-8 were identified as monodispersed polyhedrons with an average particle size of 290 ± 30 nm (n = 138). The same particles were observed in clusters in the LbL assembly (Fig. 2D, right) confirming the PCZIF-8 integration in the film.
The electrochemical performance of the 11.5 BL assembly with PCZIF-8 was studied at different scan rates (Fig. 3C and D). The peak current showed a linear dependence on the potential scan rate, indicating a surface-confined electrochemical process with no diffusion constraints (inset Fig. 3C and D).58 For these voltammograms, eqn (1) was applied to calculate the specific voltammetric capacitance:
![]() | (1) |
To evaluate the carbon porosity contribution to the film's capacitance, the PCZIF-8 assembly was compared to another assembly prepared with a commercial graphitic carbon (GC) dispersion. The dry mass growth of both films was monitored via QCM (Fig. 3F) performing the LbL process on top of a gold QCM sensor. The two systems grew linearly; however, the GC assembly reached higher mass deposition than the PCZIF-8 one.
The electrochemical growth of the GC assembly was also followed by cyclic voltammetry. Fig. S5 displays the voltammograms for this film with increasing deposition cycles. The comparison of the voltammograms of 11.5 bilayers for the two systems is presented in Fig. 3G and S6 for 0.1 M HCl and 0.1 M KCl, respectively. The performance observed was notably different; although the PCZIF-8 assembly has less deposited material, it exhibits a much higher voltammetric current response than the GC films.
Integrated charge calculations (Fig. 3H) further highlight these differences: charge increased substantially with bilayer number in PCZIF-8 films but remained nearly constant for GC assemblies.
Specific capacitance values at different scan rates for both 11.5 BL assemblies are summarized in Table S1. These results indicate that the carbon porosity enhances the electrochemical capacity, leading to an efficient performance even in lighter films.
Specific voltammetric capacitance values were also compared across different number of bilayers in Fig. S7. The disparity in electrochemical performance between the two systems becomes more pronounced when comparing specific capacitance, as GC film has a higher mass and a lower current response than the PCZIF-8 one. Furthermore, for PCZIF-8 assembly, a nearly constant specific capacitance values with increasing bilayers are observed. This trend indicates electrochemically interconnected material inclusion.
| CT = Cc + Cd | (2) |
In this equation Cc is the electric double layer capacitance and Cd is the pseudocapacitance.4,61 The capacitance increases with decreasing scan rate; thus, the capacitance attributed to the total surface area can be estimated from eqn (3) by extrapolating to zero scan rate:
![]() | (3) |
In this equation, v is the scan rate, k1 is a constant and CCV,SP is the specific capacitance calculated at each scan rate.
Assuming that Cc is independent of the scan rate, its value can be determined from eqn (4) by extrapolating to the infinite-scan rate limit.
| CCV,SP = Cc + k2v−1/2 | (4) |
In this equation, k2 is another constant. Fig. 4A and B show the plots from eqn (3) and (4), respectively. CCV,SP was analysed for scan rates from 10 to 500 mV s−1.
![]() | ||
Fig. 4 (A) Dependence of the inverse of the specific capacitance with v0.5. (B) Dependence of the specific capacitance with v−0.5. (C) b-Values calculated from the slope of eqn (6). (D) j v−0.5 with v0.5 with their linear regression fitting used to obtain and in 0.1 M HCl. Cyclic voltammograms for 100 mV s−1 with jd and jc contributions for (E) KCl and (F) HCl. (G) Specific capacitance contributions calculated by the Trasatti and Dunn methods in 0.1 M KCl and 0.1 M HCl. | ||
Second, Dunn method was applied, analysing the behaviour of the current density (j) with the scan rate. The dependence of j on v is expressed in eqn (5):
| j = avb | (5) |
In eqn (5), a and b are constants. Two characteristic b values are commonly recognized: b = 0.5 for diffusion-controlled processes and b = 1 for capacitive behaviour. The b value for our assemblies was determined, applying log to eqn (5):
log(j) = log(a) + b log(v) | (6) |
The linear regression fitting for log(j) vs. log(v) is shown in Fig. S8. The b values obtained for our assemblies in KCl and HCl solutions are shown in Fig. 4C. All b values range between 0.78 and 0.97. Although this indicates a combination of contributions to the current density and b is not strictly equal to 1, according to previous reports, the overall behaviour of the composite film can be considered characteristic of a supercapacitor.62,63
Thus, the total current density can be expressed as the sum of two components, as shown in eqn (7):
| jT = jc + jd | (7) |
The total density current (jT) is composed by the diffusion-controlled current density (jd, b = 0.5) and the capacitive current density (jc, b = 1). Based on these b values, eqn (8) is obtained:
![]() | (8) |
Here,
and
are constants. Dividing the equation by v1/2 allows expressing the relationship in linear form, as given in eqn (9).
![]() | (9) |
Fig. 4D and S9 display representative linear regressions obtained from eqn (9) using HCl and KCl as electrolyte. From the
and
values determined along the voltammetric cycle, the diffusion-controlled (jd) and capacitive (jc) current profiles were reconstructed for each voltammogram. Results for 100 mV s−1 in KCl and HCl are shown in Fig. 4E and F, while those for 50 and 200 mV s−1 are shown in Fig. S10. Integration of each curve allowed the calculation of the specific capacitance corresponding to each contribution (Cd and Cc) at different scan rates. Fig. 4G summarizes these results along with those obtained from the Trasatti method.
As shown in Fig. 4G, the component analysis indicates that, regardless of the scan rates or the specific methods used for evaluation, the differences in capacitance between acidic and neutral media are mainly attributed to the Cc component. This contribution is commonly associated with EDL processes and, in this type of system has a great influence from the PANI block, which constitutes a conducting component.64,65 Polyaniline exhibits a more pronounced electrical conductivity under acidic conditions; therefore, it is reasonable that composite materials containing PANI display a stronger EDL contribution to the overall capacitance in acidic media. On the other hand, the components that vary linearly with the square root of the scan rate are typically assigned to diffusive processes.66,67 In the materials developed here, although polyaniline contributes partially to this capacitive behaviour, the main contributors to the linear (capacitive) component are the carbon-based nanomaterials. However, no major differences in this contribution are expected when switching from acidic to neutral media.
As already reported, PANI-PSS has a negative charge excess provided by the polystyrene sulfonate (PSS) polyanion. Negative charge excess was confirmed with the z-potential measured of −21.6 mV. Then, the film is expected to exchange cations as charge carriers with the electrolyte during the redox switching.70–72 To explain the mass exchange Fig. 5B illustrates the oxidation and reduction of the film with PANI-PSS considering the cation exchange. Thus, the oxidation releases cations to the solution driving a mass loss and the reduction captures the cations from the solution leading to a mass gain. These exchanged cations are accompanied by solvent molecules, which also modifies the film hydration during redox switching.
The mass exchange was measured after different numbers of deposition cycles of the assembly procedure. Fig. 5C above and S12 represent the mass change with time during cyclic voltammetry performed at 50 and 200 mV s−1. In Fig. 5C mean mass exchange values are shown as a function of the number of deposition cycles. As expected, as the number of deposition steps increases, more conductive polymer is attached to the film and the electrochemical mass exchange increments. This result reinforces the idea that the added material is electrochemically interconnected and exchanging cations and solvent during redox switching.
![]() | (10) |
This enhancement is primarily attributed to the increase in the surface area provided by the PCZIF-8 inclusion. The carbon porosity significantly improves ion accessibility, facilitating efficient electrolyte penetration and maximizing the contact between the electrolyte and the conductive material. Another key factor in this improvement is the contribution of the electric double-layer formation, which plays a major role in the charge storage and calculated specific capacitance. In summary, the porous interface not only enhances ion transport but also reinforces the double-layer capacitance, making the system highly suitable for energy storage applications.
To place our results in context, Tables 1 and S2 compare the specific capacitance values from this work with those reported for PCZIF-8-based and PANI-based supercapacitors. Although the value obtained here is not the highest in the table, it must be highlighted that the other studies operate in more aggressive electrolytes and extreme pH conditions. Considering the environmental friendliness and neutral electrolytes, the capacitance values achieved here are competitive with those of the other systems. Moreover, in several cases, the current densities applied in previous works are lower than those used in these experiments. For comparison at identical current densities, Table S3 presents the results for electrodes cycled at 1 A g−1. These findings emphasized the efficiency of this composed film, which delivers competitive performance without compromising on sustainability.
| Electrodes using PCZIF-8 | Electrolyte | C CG,SP (F g−1) | Cycling stability (GCD) | Reference |
|---|---|---|---|---|
| 2 layers PCZIF-8-PANI | 1 M H2SO4 – 3 electrodes | 322–1 A g−1 | 100% - 10 000 cycles - 5 mA s−1 |
37 |
| Core–shell PCZIF-8@PANI | 1 M H2SO4 – 2 electrodes | 236–1 A g−1 | 86% - 20 000 cycles - 5 A g−1 |
39 |
| Aerogel with PANI and ZIF-8 is carbonized | 2 M KOH – 3 electrodes | 338–0.5 A g−1 | 91.2% - 5000 cycles - 5 A g−1 | 41 |
| Co3O4 + PCZIF-8 and PANI polymerized outside | 3 M KOH – 3 electrodes | 1407–1 A g−1 | 87.7% - 10 000 cycles - 20 A g−1 |
40 |
| PCZIF-8 in a Ni foam | 2 M KOH – 3 electrodes | 187–0.5 A g−1 | 100% - 10 000 cycles - 5 A g−1 |
73 |
| ZIF-8 + phytic acid is carbonized | 6 M KOH – 3 electrodes | 219.4–1 A g−1 | 100% - 2000 cycles - 5 A g−1 | 74 |
| ChNF@ZIF-8 is carbonized | 6 M KOH – 3 electrodes | 182.5–0.2 A g−1 | 94.8% - 5000 cycles - 1 A g−1 | 75 |
| CNC@ZIF-8 is carbonized | 6 M KOH – 3 electrodes | 172–0.1 A g−1 | 94.5% - 5000 cycles - 0.1 A g−1 | 76 |
| Layer by layer PCZIF-8/PANI:PSS | 0.1 M KCl – 3 electrodes | 160–1 A g−1 | 88% - 2400 cycles - 3 A g−1 - 0.1 M KCl | This work |
| 0.1 M HCl – 3 electrodes | 225–1 A g−1 |
The prepared PANI-PSS/PCZIF-8 assembly exhibits good stability during electrochemical cycling in a neutral electrolyte, which is crucial for its practical application ensuring a long-term performance. Comparing with stability values of other electrodes shown in Table 1, the capacity retention obtained is very promising. Additionally, the ability to operate in a neutral medium is crucial for including it in wearable and portable energy storage devices. Using 0.1 M KCl makes the system more environmentally friendly, as it avoids the use of corrosive or hazardous electrolytes.
Electrochemical analysis revealed that incorporating PCZIF-8—with its high surface area and interconnected pore network—greatly enhanced the specific capacitance of the assemblies in neutral aqueous electrolytes. The abundant porosity facilitates ion transport and maximizes the active surface available for charge storage, while the environmentally benign fabrication route avoids corrosive reagents and extreme pH conditions. These combined advantages demonstrate that the rational use of porous carbons derived from MOFs offers a straightforward, scalable, and sustainable strategy to boost the performance of supercapacitors. Such eco-friendly devices hold strong potential for secure, low-impact energy storage applications, from wearable electronics to portable power systems.
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