Cobalt Phthalocyanine-Doped Polymer-Based Electrocatalyst for Rechargeable Zinc-Air Batteries

Rechargeable zinc-air batteries (RZAB) have gained significant attention as potential energy storage devices due to their high energy density, cost-effectiveness, and to the fact that they are environmentally safe. However, the practical implementation of RZABs has been impeded by challenges such as sluggish oxygen reduction reaction (ORR) and oxygen evolution reaction (OER), including poor cyclability. Herein, we report the preparation of cobalt- and nitrogen-doped porous carbon derived from phloroglucinol-formaldehyde polymer networks with 2-methyl imidazole and cobalt phthalocyanine as precursors for nitrogen and cobalt. The CoN-PC-2 catalyst prepared in this study exhibits commendable electrocatalytic activity for both ORR and OER, evidenced by a half-wave potential of 0.81 V and Ej=10 of 1.70 V. Moreover, the catalyst demonstrates outstanding performance in zinc-air batteries, achieving a peak power density of 158 mW cm−2 and displaying excellent stability during charge-discharge cycles. The findings from this study aim to provide valuable insights and guidelines for further research and the development of hierarchical micro-mesoporous carbon materials from polymer networks, facilitating their potential commercialisation and widespread deployment in energy storage applications.


Introduction
Rechargeable zinc-air batteries (RZABs) have emerged as a promising technology for high-energy density-based energy storage systems. However, their practical implementation has been hindered by challenges such as sluggish oxygen reduction and evolution reactions, as well as limited cyclability [1,2]. To overcome these limitations, extensive research efforts have been focused on developing efficient catalysts to enhance the electrochemical performance of the RZABs [3][4][5][6]. Presently, precious metal-based materials (such as Pt, Pd, Ru, and Ir) are used as electrocatalysts, which has hindered their use in practical applications due to their high price, limited resources, and limited stability [7][8][9]. Transition metal-derived catalysts have gained significant attention due to their unique properties, including their abundance, high electrocatalytic activity, tuneable composition, and excellent stability compared to noble metal-based catalysts [10][11][12][13].
Carbon support also plays a vital role in enhancing catalysts' overall electrocatalytic performance by integrating the active centres' distribution and promoting the efficient mass transport of reactant species. There are several methods for preparing porous carbon supports, including pyrolysis of metal-organic frameworks (MOFs), covalent organic frameworks (COFs), polymers, bio-mass, and so on [6,[14][15][16][17]. However, porous carbon materials synthesised using these methods suffer severe degradation at high voltage conditions in

Synthesis of Phloroglucinol-Formaldehyde-Methylimidazole (PFM) Framework
For a standard synthesis procedure, 2.2 g of phloroglucinol was dissolved in 20 mL of Milli-Q water in a beaker at a temperature of 45 • C. Then, 10 g of formaldehyde solution was mixed in phloroglucinol solution under continuous stirring for 30 min. The reaction between phloroglucinol and formaldehyde took place, forming a yellowish-orange precipitate. Next, 4.4 g of 2-methylimidazole was dissolved in another beaker containing 40 mL water at 45 • C. Then, both solutions were mixed and stirred for 12 h at 60 • C. Subsequently, the product underwent filtration, followed by multiple water rinses and drying at a temperature of 60 • C, resulting in the production of the PFM framework.

Synthesis of CoN-PC
For the synthesis of CoN-PC-1, 100 mg of PFM powder and 5 mg of CoPc were suspended in 25 mL of ethanol by sonication for 1 h. Then, the mixture was dried out at 60 • C followed by pyrolysis at 800 • C under an inert atmosphere to get the CoN-PC-1. The CoN-PC-2 was also prepared via a similar route by changing the amount of CoPc to 10 mg and PC-800 was prepared by pyrolysing the PFM polymer at 800 • C without adding CoPc.

Physical Characterisation
The surface morphology of the prepared catalysts was assessed using a Helios Nanolab 600, FEI (Hillsboro, OR, USA) scanning electron microscope (SEM). The elemental mapping of the prepared catalysts and the determination of bulk elemental composition were performed by the energy dispersive X-ray spectrometer (EDX) from Oxford Instruments (Abingdon, UK), coupled to the scanning electron microscope. Catalyst suspension was drop-casted onto a polished glassy carbon (GC) disk to prepare SEM samples. The catalysts' crystallinity was determined through X-ray diffraction (XRD) analysis. The XRD measurements were conducted on a Bruker D8 Advance diffractometer (Billerica, MA, USA) with Ni-filtered Cu Kα (λ = 1.54184 Å) radiation. Scanning steps of 0.0126 • were used to obtain the diffraction patterns over a 2θ range of 5-90 • .
For N 2 physisorption experiments, the catalyst materials were dried in vacuum overnight at 300 • C prior to analysis. The NovaTouch LX2 instrument (Quantachrome) was used for the analysis, and TouchWin 1.11 software was used for all calculations. The specific surface area (S BET ) was calculated utilising the Brunauer-Emmett-Teller method in the P/P 0 range of 0.02-0.2. The quenched solid density functional theory (QSDFT) equilibria model for slit-type pores was utilised for the calculation of the volume of micropores (V µ ), and total pore volume (V tot ) was evaluated at the N 2 saturation pressure (P/P 0 = 0.97).
X-ray photoelectron spectroscopy (XPS) was used to determine the surface elemental composition using the electron energy analyser SCIENTA SES 100 and Mg Kα X-rays (1.2536 keV) from Thermo XR3E2, a twin-anode X-ray tube. The survey scan was measured in the range of 1000 to 0 eV with a 0.5 eV step size, 0.2 s step duration, and an average of five scans. The core-level spectra were averaged with a 0.2 eV step size and 0.2 s step duration over the course of thirty scans. The Gauss-Lorentz hybrid function (GL 70, Gauss 30%, Lorentz 70%) was utilised for the data analysis on CasaXPS software (version 2.3.17).

Electrochemical Characterisation
The electrochemical ORR and OER measurements were performed at room temperature with a potentiostat/galvanostat PGSTAT30 (Metrohm-Autolab, Utrecht, The Netherlands) in a conventional three-electrode system using a platinum wire, saturated calomel electrode (SCE), and catalyst-coated GC rotating disk electrode (geometric area = 0.196 cm 2 ) as a counter electrode, reference electrode, and the working electrode, respectively. A polished GC disk was drop-cast with 10 µL of a homogeneous suspension of 4 mg of prepared catalyst in 1000 µL of 2-propanol: water: Nafion (1: 1: 0.03) and dried at 60 • C to achieve the 0.2 mg cm −2 catalyst loading.
All potentials were converted against the reversible hydrogen electrode (RHE) using the equation E RHE = E SCE + 0.242 + 0.059 × pH, and the electrochemical data given in this work were iR-corrected using the positive feedback method. To measure the background current, cyclic voltammograms (CV) were recorded in an Ar-saturated 0.1 M KOH solution at a potential scan rate (v) of 10 mV s −1 . Furthermore, the rotating disk electrode (RDE) technique was used to investigate the ORR and OER activity of the catalysts. To change the electrode rotation rate (between 360 and 3100 rpm), a speed control unit (CTV101) was attached to a rotator (EDI101, Radiometer). Measurements of the OER polarisation curves were carried out in an Ar-saturated 0.1 M KOH at a 1900 rpm rotation rate and a scan rate of 10 mV s −1 . E j=10 is denoted as the potential at which the OER current density reaches 10 mA cm −2 . For ORR stability, the working electrode was cycled 10,000 times between 1.0 and 0.6 V vs. RHE at 100 mV s −1 in O 2 -saturated 0.1 M KOH solution. Before and during the stability test, the RDE polarisation curves were measured at 1900 rpm at 10 mV s −1 . For the OER stability test, the working electrode was held at 1.7 V at 1900 rpm for 3 h.

RZAB Test
The RZAB performance and stability evaluations of the electrocatalysts were assessed using a homemade battery device. A 6 M KOH solution containing 0.2 M Zn(CH 3 COO) 2 was used as the electrolyte for the RZABs. Seven mg of catalyst was dispersed by sonicating in 800 µL water-ethanol (1:3) solution along with 20 µL Nafion solution as a binder to produce a homogenous catalyst ink. The catalyst ink was drop-casted onto the 3.5 cm 2 carbon paper (Sigracet 39 BB) to obtain the catalyst loading of 2 mg cm −2 . The anode was made of a polished zinc sheet with a 0.2 mm thickness. The exposed surface area to the electrolyte solution for both the electrodes-Zn sheet and the catalyst-coated carbon paper was 0.79 cm 2 . The assembled RZABs' stability was assessed using a 10 min galvanostatic discharge-charge cycle at 5 mA cm −2 .

Physico-Chemical Characterization
XRD analysis was used to investigate the catalyst materials' crystalline structure ( Figure 1a). All XRD patterns depicted two broad peaks around 26 • and 43.5 • , corresponding to the (002) and (100) graphitic planes, respectively. No diffraction peaks were detected corresponding to metals, indicating the absence of large Co nanoparticles in the prepared catalysts. PC-800 showed slightly higher intensity peaks than the Co-doped materials, pointing out that the introduction of transition metal tends to modify the graphitic structure [37]. Further, the N 2 physisorption analysis was carried out to study the textural properties of the materials ( Figure 1b and Table 1). Typical type-II adsorption-desorption isotherms with H3 hysteresis showed the presence of micropores and mesopores in all prepared catalysts. The specific surface area (S BET ) of PC-800, CoN-PC-1, and CoN-PC-2 was 449, 464, and 325 m 2 g −1 . PC-800 displayed the highest total porosity and microporosity, and both tend to decrease with the addition of CoPc. The balance between micro-and mesopores is critical for carbon-based catalyst materials to facilitate the diffusion of reactant species during the ORR/OER processes [38]. Mesopores are considered to be favourable for electrocatalysis, but increasing mesopores tends to decrease the surface area of the catalyst materials, which leads to depletion in active sites. Hence, as-prepared materials are suitable for ORR/OER due to the balanced micro/mesopore structure [39].
PC   Next, these materials were analysed by SEM to study the surface morphology; th obtained images are shown in Figure 2. All materials possess relatively homogenous mor phology with interconnected porous carbon structures. Doping with CoPc leads to mild changes in the morphology. The surface structure of the materials appears to be mor compact with the increased amount of CoPc (see Figure 2 inset). SEM-EDX-assisted ele mental mapping was performed to see the distribution of dopants in the catalysts and detect any potential agglomeration of Co (shown in Figure S1). As expected, no agglom eration of elements was detected in the element mapping, which corroborates the XRD results. The bulk concentration of elements was determined by SEM-EDX (Table 2). Th analyses show the high nitrogen and cobalt concentration, which indicates that doping with CoPc was successful. Additionally, oxygen functionalities are from carbon-oxygen species and metal oxides, which are believed to be suitable for OER [40,41].  The XPS measurements were conducted to identify the surface elemental composi tion and different states of dopants that existed in the prepared catalysts ( Figure 3). Th surface of the catalysts exhibited the presence of C, N, O, and Co, as indicated by the XP Next, these materials were analysed by SEM to study the surface morphology; the obtained images are shown in Figure 2. All materials possess relatively homogenous morphology with interconnected porous carbon structures. Doping with CoPc leads to mild changes in the morphology. The surface structure of the materials appears to be more compact with the increased amount of CoPc (see Figure 2 inset). SEM-EDX-assisted elemental mapping was performed to see the distribution of dopants in the catalysts and detect any potential agglomeration of Co (shown in Figure S1). As expected, no agglomeration of elements was detected in the element mapping, which corroborates the XRD results. The bulk concentration of elements was determined by SEM-EDX ( Table 2). The analyses show the high nitrogen and cobalt concentration, which indicates that doping with CoPc was successful. Additionally, oxygen functionalities are from carbon-oxygen species and metal oxides, which are believed to be suitable for OER [40,41].  Next, these materials were analysed by SEM to study the surface morphology; the obtained images are shown in Figure 2. All materials possess relatively homogenous morphology with interconnected porous carbon structures. Doping with CoPc leads to mild changes in the morphology. The surface structure of the materials appears to be more compact with the increased amount of CoPc (see Figure 2 inset). SEM-EDX-assisted elemental mapping was performed to see the distribution of dopants in the catalysts and detect any potential agglomeration of Co (shown in Figure S1). As expected, no agglomeration of elements was detected in the element mapping, which corroborates the XRD results. The bulk concentration of elements was determined by SEM-EDX ( Table 2). The analyses show the high nitrogen and cobalt concentration, which indicates that doping with CoPc was successful. Additionally, oxygen functionalities are from carbon-oxygen species and metal oxides, which are believed to be suitable for OER [40,41].  The XPS measurements were conducted to identify the surface elemental composition and different states of dopants that existed in the prepared catalysts ( Figure 3). The surface of the catalysts exhibited the presence of C, N, O, and Co, as indicated by the XPS  The XPS measurements were conducted to identify the surface elemental composition and different states of dopants that existed in the prepared catalysts ( Figure 3). The surface of the catalysts exhibited the presence of C, N, O, and Co, as indicated by the XPS survey spectrum ( Table 3). The nitrogen and oxygen contents were similar in all prepared catalysts, with the only variation found in the Co content, which was expected due to the different CoPc amounts used in the catalyst preparation. Different nitrogen species, including pyridinic-N, pyrrolic-N, graphitic-N, and metal-coordinated N (M-Nx), were detected on the catalyst's surface, as revealed by the deconvoluted high-resolution N 1s XPS peak (Figure 3a,c inset). Among all three materials, pyridinic-N and pyrrolic-N exhibited the highest prominence, followed by graphitic-N and M-Nx. (Figure 3d). These results indicate that the doping with 2-methylimidazole and CoPc increased the concentration of different N-species to promote the ORR kinetics. Transition metal-N x centres are also considered to be accountable for high ORR activity via 4e − or 2 × 2e − pathways [42]. It is noteworthy that the Co-N-PC-2 catalyst consisted of relatively higher percentages of pyridinic-N and M-Nx compared to Co-N-PC-1 (Figure 3d), which could be beneficial for the higher electrocatalytic activity. The deconvolution of the O 1s peak from the XPS spectra reveals the presence of cobalt oxide, carboxyl, hydroxyl groups, and chemisorbed water ( Figure S2). These oxygen species were reported to enhance the electrocatalytic activity of the material [43,44]. The increase in cobalt content leads to a higher amount of oxygen species, including metal oxide, carboxyl, hydroxyl groups, and chemisorbed water. Metal oxides can form during the pyrolysis of MN 4 macrocycles ( Figure S2), and their presence has been shown to enhance the ORR/OER activity in alkaline media [41,[45][46][47]. Further, the individual components of the Co2p XPS spectra were resolved to quantify the oxidation state of Co and determine the composition of each Co species. Figure S3 shows two prominent peaks at 780.4 and 796 eV, ascribed for Co2p 3/2 and Co2p 1/2 , respectively. The deconvoluted peaks observed at 778 and 780.4 eV can be attributed to metallic Co and Co-N in the Co2p 3/2 spectrum, respectively. This further assures the presence of Co-Nx centres. For CoN-PC-1, the concentration of Co-N (0.11 at%) is lower than CoN-PC-2 (0.23 at%).

Electrochemical Properties of the Catalysts
Firstly, the ORR results of CoN-PC-2 catalysts prepared at different pyrolysis temperatures (700, 800, and 900 °C) are presented in Figure S4 and Table S1. The observed outcomes suggest that pyrolysis temperatures have an impact on the ORR activity. The catalyst synthesised at 800 °C demonstrated superior ORR activity, exhibiting a half-wave potential (E1/2) of 0.81 V vs. RHE. As a result, 800 °C was selected as the pyrolysis temper-

Electrochemical Properties of the Catalysts
Firstly, the ORR results of CoN-PC-2 catalysts prepared at different pyrolysis temperatures (700, 800, and 900 • C) are presented in Figure S4 and Table S1. The observed outcomes suggest that pyrolysis temperatures have an impact on the ORR activity. The catalyst synthesised at 800 • C demonstrated superior ORR activity, exhibiting a half-wave potential (E 1/2 ) of 0.81 V vs. RHE. As a result, 800 • C was selected as the pyrolysis temperature for the preparation of other catalysts.
Further, the effect of CoPc was studied on the ORR and OER activity using the RDE method. As expected, PC-800 exhibited the least electrocatalytic activity for the ORR, as evidenced by an onset potential for oxygen reduction (E onset ) of 0.79 V, where the ORR current density reaches −0.1 mA cm −2 . Moreover, PC-800 follows two reduction pathways during the ORR process. A substantial improvement in the electrocatalytic activity was noticed with the addition of CoPc. The overall ORR electrocatalytic activity of CoN-PC-1 and CoN-PC-2 was almost the same in the RDE experiment, as both had E onset and E 1/2 values of 0.88 V and 0.81 V, respectively. Commercial Pt/C (E 1/2 = 0.85 V) was also compared using the RDE method, and the results are shown in Figure 4a and Table 4. The OER was evaluated in terms of E j=10 . CoN-PC-2, with an E j=10 value of 1.70 V, exhibited the best OER activity among the as-prepared catalysts (Figure 4b). A slightly higher E j=10 value was observed for CoN-PC-1 (1.73 V), and PC-800 could not attain comparable activity. This trend is expected in these catalysts, as PC-800 does not have any metal-containing active sites for OER and an increased OER activity was observed for catalysts with higher metal contents, which can provide more active sites for OER.  To investigate the ORR pathways, linear sweep voltammograms (LSV) were measured at different rotation rates (360-3100 rpm) using RDE in O2-saturated 0.1 M KOH electrolytes ( Figure S5a-c). Figure S5d-f display the Koutecky-Levich (K-L) plots at different potentials for O2 reduction, while the K-L equation is employed to determine the electron transfer number (n) during the ORR process [48]: In the given equations, j, jk, and jd represent the experimentally measured, kinetic, and diffusion-limited current densities, respectively. F corresponds to the Faraday constant (96,485 C mol −1 ), C0 denotes the bulk concentration of O2 in a 0.1 M KOH solution (1.2 × 10 −6 mol cm −3 ), v represents the kinematic viscosity of the electrolyte solution (0.01 cm 2 s −1 ), D0 is the diffusion coefficient of O2 in a 0.1 M KOH solution (1.9 × 10 −6 cm 2 s −1 ), and ω stands for the electrode rotation rate (rad s −1 ). The linearity of K-L plots suggests To investigate the ORR pathways, linear sweep voltammograms (LSV) were measured at different rotation rates (360-3100 rpm) using RDE in O 2 -saturated 0.1 M KOH electrolytes ( Figure S5a-c). Figure S5d-f display the Koutecky-Levich (K-L) plots at different potentials for O 2 reduction, while the K-L equation is employed to determine the electron transfer number (n) during the ORR process [48]: In the given equations, j, j k , and j d represent the experimentally measured, kinetic, and diffusion-limited current densities, respectively. F corresponds to the Faraday constant (96,485 C mol −1 ), C 0 denotes the bulk concentration of O 2 in a 0.1 M KOH solution (1.2 × 10 −6 mol cm −3 ), v represents the kinematic viscosity of the electrolyte solution (0.01 cm 2 s −1 ), D 0 is the diffusion coefficient of O 2 in a 0.1 M KOH solution (1.9 × 10 −6 cm 2 s −1 ), and ω stands for the electrode rotation rate (rad s −1 ). The linearity of K-L plots suggests the first-order kinetics for ORR ( Figure S5), and the n value was determined to be close to four (~3.5) for CoN-PC ( Figure S6). Table 4 provides a comparison with previously published ORR/OER electrocatalysts, and the comparison clearly demonstrates the efficiency of the catalysts employed in this study in terms of E 1/2 and E j=10 values. The cyanide poisoning test was also carried out to evidence the presence of the M-Nx active sites in the catalyst materials. In principle, cyanide ions strongly bind to the M-Nx sites, impairing the catalysts' ORR activity [57]. The LSV curves were obtained in 0.1 M KOH solution containing 10 mM NaCN. It is clear from Figure 5 that the catalysts' ORR activity significantly dropped with the addition of cyanide ions. These test findings also confirm the catalysts' M-Nx centres, which were identified in the XPS analysis.  Despite the high electrocatalytic activity, good stability is important for electrocatalysts in metal-air batteries due to the high operational voltage. To evaluate the electrochemical stability of the synthesised catalysts, 10,000 repeated potential cycles in an O2saturated 0.1 M KOH solution were performed ( Figure 6). CoN-PC-1 revealed good stability with only 14 mV shift in E1/2, while no difference in E1/2 was observed for CoN-PC-2. This is attributed to the hierarchical porous structures in the CoN-PC catalysts, which mitigate the metal dissolution and aggregation during the vigorous electrocatalytic pro- Despite the high electrocatalytic activity, good stability is important for electrocatalysts in metal-air batteries due to the high operational voltage. To evaluate the electrochemical stability of the synthesised catalysts, 10,000 repeated potential cycles in an O 2 -saturated 0.1 M KOH solution were performed ( Figure 6). CoN-PC-1 revealed good stability with only 14 mV shift in E 1/2 , while no difference in E 1/2 was observed for CoN-PC-2. This is attributed to the hierarchical porous structures in the CoN-PC catalysts, which mitigate the metal dissolution and aggregation during the vigorous electrocatalytic process by stabilising metal-Nx active sites and accelerating the electron transfer process [58]. Therefore, the hierarchical porous structure and optimised metal concentration collectively promoted excellent electrochemical stability. For the purpose of evaluating the stability of the OER, chronoamperometric measurements were conducted at a potential of 1.7 V in an Ar-saturated 0.1 M KOH solution ( Figure S7). After 3 h, CoN-PC-2 and CoN-PC-1 maintained 79% and 51% of the initial OER activity, respectively. Higher stability of CoN-PC-2 was ascribed to the higher content of Co, which can help to stabilise the carbon matrix and mitigate the loss of active sites. Despite the high electrocatalytic activity, good stability is important for electrocatalysts in metal-air batteries due to the high operational voltage. To evaluate the electrochemical stability of the synthesised catalysts, 10,000 repeated potential cycles in an O2saturated 0.1 M KOH solution were performed ( Figure 6). CoN-PC-1 revealed good stability with only 14 mV shift in E1/2, while no difference in E1/2 was observed for CoN-PC-2. This is attributed to the hierarchical porous structures in the CoN-PC catalysts, which mitigate the metal dissolution and aggregation during the vigorous electrocatalytic process by stabilising metal-Nx active sites and accelerating the electron transfer process [58]. Therefore, the hierarchical porous structure and optimised metal concentration collectively promoted excellent electrochemical stability. For the purpose of evaluating the stability of the OER, chronoamperometric measurements were conducted at a potential of 1.7 V in an Ar-saturated 0.1 M KOH solution ( Figure S7). After 3 h, CoN-PC-2 and CoN-PC-1 maintained 79% and 51% of the initial OER activity, respectively. Higher stability of CoN-PC-2 was ascribed to the higher content of Co, which can help to stabilise the carbon matrix and mitigate the loss of active sites.

RZAB Test Results
The performance of the developed CoN-PC-1 and CoN-PC-2 catalyst materials in terms of oxygen bifunctional electrocatalysis at the cathode was evaluated by assembling

RZAB Test Results
The performance of the developed CoN-PC-1 and CoN-PC-2 catalyst materials in terms of oxygen bifunctional electrocatalysis at the cathode was evaluated by assembling and assessing rechargeable zinc-air batteries. The discharge polarisation curves and power density curves for catalysts are shown in Figure 6a. Remarkably, CoN-PC-1 and CoN-PC-2 catalysts showed open circuit voltage (OCV) values as high as 1.45 and 1.47 V, respectively. As shown in Figure 7a, CoN-PC-2 had a greater maximum power density of 158 mW cm −2 , slightly higher than that of CoN-PC-1 (155 mW cm −2 ). Furthermore, a galvanostatic chargedischarge cycling test (10 min/cycle) carried out at a current density of 5 mA cm −2 was used to assess the durability of both catalysts (Figure 7b). Under the same circumstances, the CoN-PC-2 catalyst exhibited an excellent cycling performance in comparison with CoN-PC-1. Interestingly, both CoN-PC-1 and CoN-PC-2 catalysts had an initial voltage gap of around 0.9 V between their charge and discharge potentials. However, after 45 h of cycling, the voltage gap of CoN-PC-2 increased to 1.08 V, while CoN-PC-1-based RZAB failed two times within 30 h. The high stability of CoN-PC-2 is attributed to a higher concentration of metal, which can provide sustainable active sites for ORR/OER and lower carbon decomposition in highly alkaline media. CoN-PC-2 exhibits comparable RZAB performance to the reported RZABs (Table 5). Nonetheless, comparing different RZABs is not always straightforward due to many factors, including electrode distance, air flow, Zn anode, the volume of the electrolyte, etc. [11].

Conclusions
In summary, cobalt-and nitrogen-doped porous carbon was prepared using phloroglucinol-formaldehyde networks and 2-methylimidazole and cobalt phthalocyanine as precursors. The prepared catalyst CoN-PC-2 demonstrated good bifunctional electrocatalytic activity towards the ORR and OER in alkaline media with E1/2 = 0.81 V and Ej=10 = 1.70 V. The controlled synthesis of phloroglucinol-formaldehyde networks resulted in the mixture of micro-and mesoporous carbon structures, which are considered to play

Conclusions
In summary, cobalt-and nitrogen-doped porous carbon was prepared using phloroglucinolformaldehyde networks and 2-methylimidazole and cobalt phthalocyanine as precursors. The prepared catalyst CoN-PC-2 demonstrated good bifunctional electrocatalytic activity towards the ORR and OER in alkaline media with E 1/2 = 0.81 V and E j=10 = 1.70 V. The controlled synthesis of phloroglucinol-formaldehyde networks resulted in the mixture of micro-and mesoporous carbon structures, which are considered to play a vital role in enhancing the overall electrocatalytic activity. Furthermore, the higher cobalt content and hierarchical porous structure of CoN-PC-2 contribute towards the excellent RZAB performance in terms of OCV (1.47 V), P max (158 mW cm −2 ), and the excellent stability of 45 h. Overall, the present work provides new insights for the preparation of active electrocatalysts for rechargeable zinc-air batteries through a facile and simple synthesis route.