Sustainable organic salt-derived porous carbons: Activation/self-activation fabrication, dimensional control and environmental applications

Mingxing Shi Jiahui Liu Wei Jin Zahira Bano Yubo Pan Jianzhe Ma Xu Wu Huijuan Jia Guolin Tong

Citation:  Mingxing Shi, Jiahui Liu, Wei Jin, Zahira Bano, Yubo Pan, Jianzhe Ma, Xu Wu, Huijuan Jia, Guolin Tong. Sustainable organic salt-derived porous carbons: Activation/self-activation fabrication, dimensional control and environmental applications[J]. Chinese Chemical Letters, 2026, 37(9): 112411. doi: 10.1016/j.cclet.2026.112411 shu

Sustainable organic salt-derived porous carbons: Activation/self-activation fabrication, dimensional control and environmental applications

English

  • In the background of accelerated global industrialization and urbanization, environmental pollution has been a huge challenge of growing complexity and severity, posing significant threats to ecological equilibrium and human health [1,2]. Critical issues ranging from water quality deterioration induced by freshwater scarcity to air/soil contamination from diverse pollutant emissions (e.g., pharmaceuticals, heavy metals, nuclides, chloride, CO2 and SO2) and electromagnetic radiation from ubiquitous electronic devices, insistent need for effective mitigation strategies [35]. Such multifaceted environmental pressures inherently necessitate the development of advanced porous materials with tunable properties and broad applicability in the fields of detection, adsorption, catalysis and absorption. Thus, various functional porous materials have been exploited, e.g., Mxene, hydrotalcite, metal-organic frameworks (MOFs), covalent organic frameworks (COFs) and porous carbons (PCs), as the core for treating various environmental issues [68].

    Currently, PCs have emerged as promising candidates for environmental applications due to their low cost, sustainability, tunable physicochemical properties and high structural stability [9,10]. Well-designed PCs deliver unique hierarchical porous structures, improved hydrophilicity, enhanced conductivity and superior mechanical properties [11,12]. According to IUPAC classification, porosity is categorized into micropore (< 2 nm), mesopore (2-50 nm) and macropore (> 50 nm) [13]. Normally, macropores act as electrolyte/gas highways. Mesopores optimize mass transport rate, while micropores are effective active sites [14]. Advanced PC-based materials such as carbon aerogels prove hierarchical porosity integrated with broad pore size distribution that combine high surface accessibility with efficient reactant transport [15]. Novel strategies involving heteroatom doping (e.g., N, S, P, B, Fe, Co) further reinforce the property adjusting electronic/lattice configurations to activate active zones, while self-supporting designs realize rapid recovery of materials [16]. These engineering, particularly hierarchical porous structures, high specific surface area (SBET), large pore volume (Vpore) and splendid stability, pose PCs as core materials [17]. Current applications span sensing, adsorption, capacitive deionization (CDI), peroxymonosulfate (PMS) activation, electro-Fenton (EF) and microwave absorption, where the unique combination of morphology, porosity and stability addresses key challenges in the detection and removal of pollutants [1820].

    Normally, typical manufacturing strategies for PCs include the hydrothermal-activation method, carbonization-activation method, template method and gas exploiting method [21,22]. However, these strategies frequently encounter challenges associated with using toxic solvents (e.g., methanol and DMF), costly raw materials, complex preparation craft and risky HF washing, particularly when employing hazardous chemicals like KOH, H3PO4 and ZnCl2, etc. [23,24]. These strongly corrosive activators, especially high-powered KOH (detailed activation mechanism see Text S1, Eqs. S1-S5 and Fig. S1 in Supporting information), not only raise device corrosion and environmental concerns via corrosive waste generation but also hinder further commercial production. Thus, there is an urgent need to develop an eco-friendly, simple and scalable synthesis strategy.

    Notably, organic salt activation/self-activation is a green and effective strategy to exploit PCs, but suffers from less research [25,26]. Differently, organic salt-derived PCs (OAPCs) can often be fabricated via only one-step pyrolysis and have high carbon yields due to their mild and efficient activation effect. Also, organic salts have copious types (e.g., potassium, sodium and zinc), which can meet the preparation needs of single- or hierarchical-porous OAPCs [27,28]. More importantly, organic salts could realize the precise design of OAPCs in diverse dimensions from 0D to 3D by using the decomposition, catalysis and pore-forming effects of metal ions, anions and organic ligands in their composition during pyrolysis [29,30]. The unique effect makes OAPCs have highly customized features, thus meeting the strictly needs of material morphologies and structures for diverse environment applications.

    Herein, the review overviews sustainable OAPCs, stressing their dual effect as activators/self-activators. Six diverse organic salts are studied for their decomposition pathways and activation mechanisms, governing hierarchical pore formation and heteroatom doping. Also, the mechanism identification between organic salts and OAPCs was disclosed. More importantly, the dimensional control of OAPCs from 0D to 3D is minute discussed, reinforcing ion transport and active site accessibility. Eventually, OAPCs show high potential in adsorption, CDI, PMS activation, EF and microwave absorption, being mainly driven by adjustable morphology, controllable pore structure, enhanced conductivity and optimized hydrophilicity. The corresponding schematic illustration is given in Fig. 1.

    Figure 1

    Figure 1.  Schematic illustration of emerging OAPCs: Activation/self-activation fabrication, dimensional control and environmental applications.

    Organic salts, as both activators and self-activators, abundant and featured by specific chemical structures and unique activation mechanisms [31], favor developing OAPCs with high SBET and large porosity, while also enabling N or S doping [32]. The section systematically discusses the effect of six diverse organic salts in the synthesis of OAPCs. By researching the specific activation mechanisms, we can more deeply understand the roles in building hierarchical porosity and improving surface chemical property, realizing effective construction of high-performance OACPs.

    2.1.1   Potassium citrate (C6H5K3O7)

    C6H5K3O7 is the most widely used organic salt. It can generate OAPCs either via self-activation or by activating other precursors [33]. Normally, C6H5K3O7 can decompose at temperatures below 650 ℃ to form K2CO3 (Eq. 1), which then follows the same activation pathways as K2CO3 (Eqs. S2-S5 in Supporting information)) [34]. Structurally, it features copious -COOH and -OH, favoring the release of active gases like CO2 and H2O during pyrolysis. Besides, -COOH can promote crosslinking reactions, thus inducing more porosity. The combination of high reactivity, inherent structure of the precursor and effective K2CO3 induces C6H5K3O7-based OAPCs delivering excellent SBET and plentiful microporous [35].

    2C6H5K3O7H2O3K2CO3+9C+7H2O

    (1)

    C6H5K3O7-based OAPCs often have a high micropore proportion. However, their carbon skeleton is relatively closed. This can to some extent hinder the target ions or molecules from diffusing into the internal active sites [36]. C6H5K3O7 self-activation-derived OAPCs designed by Tian et al. [37] indicated a superior SBET of 2337.1 m2/g. However, Smicro and Vmicro/Vpore were 2008.6 m2/g and 89.1%, respectively (Figs. 2a and b).

    Figure 2

    Figure 2.  (a) N2 adsorption-desorption curves and (b) pore size distribution of PCPCs-x. Reprinted with permission [37]. Copyright 2017, Elsevier. (c) Schematic illustration of the fabrication process of NSHPC. (d) N2 adsorption-desorption isotherms, (e) SEM and (f) TEM images of NSHPC. Reprinted with permission [41]. Copyright 2021, Elsevier. (g) Specific capacitance of PC-700 and APC-X. Reprinted with permission [42]. Copyright 2021, Elsevier. (h) The fabrication route and (i) SEM images of NOS-AC. Reprinted with permission [46]. Copyright 2024, Elsevier. (j) Diluted CO2 uptake isotherms of PGNC at 25 ℃. Reprinted with permission [47]. Copyright 2021, Elsevier.
    2.1.2   Potassium gluconate (C6H11KO7)

    C6H11KO7 is another novel organic salt for the synthesis of OPACs, but suffers from less research compared with C6H5K3O7 [38]. Activation mechanism studies uncover that it is chemically stable and has analogous thermal decomposition pathways to K2CO3 (Eqs. S2-S5). Specifically, C6H11KO7 first decomposes into K2CO3 (Eq. 2), which then joins in the structural evolution of the carbon skeleton by chemical etching and intercalation effect [39]. Attributed to the synergistic effects of gaseous products and alkaline species during pyrolysis, the multistage activation favors a rapid increase in both SBET and porosity.

    2C6H11KO7K2CO3+11C+11H2O

    (2)

    C6H11KO7 owns copious -CHO and -COOH [41]. Its structural simplicity and high O content render it favorable for constructing O-rich OAPCs with massive micro-mesopores and increased bulk densities [40]. Moreover, their intrinsic 3D interconnected frame minimizes matter diffusion resistance by reducing the tortuosity of transport pathways, increasing the accessibility and interaction between ions/molecules and active sites. Wu et al. [41] adopted C6H11KO7 self-activation and thiourea self-doping craft, acquiring mesopore-dominated N/S co-doped hierarchical porous carbons (HPCs) (NSHPC) with a high SBET of 920.0 m2/g and plentiful mesopores (Figs. 2c-f). By using bacterial celluloses, Feng et al. [42] introduced extra microporosity into C6H11KO7-based OAPCs, gaining a high specific capacitance of 437 F/g at 0.5 A/g (Fig. 2g).

    2.1.3   Potassium acetate (CH3COOK)

    CH3COOK, recognized as a non-corrosive and eco-friendly organic salt, holds industrial potential for the scalable production of OAPCs. While it’s monofunctional -COOH and low carbon content often induces limited SBET and underdeveloped porosity, it proves distinct activation efficacy ascribed to its structural analogy to K2CO3. Reports reveal that CH3COOK decomposition initiates at 500 ℃, forming K2C2O4 intermediate phase, which then undergoes decarbonylation to generate K2CO3 (Eq. 3) [43]. This multistage pyrolysis pathway induces intensive etching of carbon matrices by redox reactions between alkaline species (K2CO3/K2O) and carbon skeletons (Eqs. S2-S5) [44], producing OAPCs with tunable micro-mesopore ratios and enhanced structural stability.

    CH3COOKK2CO3+CO2

    (3)

    CH3COOK-based OAPCs often have rich micropores [45]. Yue et al. [46] designed novel N/O/S co-doping PCs (NOS-AC) using CH3COOK activating spiral algae or bamboo (Fig. 2h). Based on the gas exfoliation effect, NOS-AC delivered superior hierarchical porous structures with a high SBET of 1285.2 m2/g and large Vpore of 0.57 m3/g (Fig. 2i). Also, Hui et al. [47] fabricated an N/O-rich irregular block structural ultramicropore carbon by CH3COOK co-activating urea-d-glucose. When utilized for the capture of CO2, it respectively achieved a high adsorption capacity of 1.38 mmol/g and 0.57 mmol/g at 0.15 and 0.05 bar (0 ℃) (Fig. 2j).

    2.1.4   Other organic potassium salt

    Another potassium salts, e.g., potassium tartrate (C4H4K2O6), potassium alginate (C12H16K2O13) and EDTA-2K (C10H17KN2O8), have manifested nailing efficacy in the synthesis of OAPCs [4850]. Pyrolysis analysis uncovers that most potassium salts undergo a similar activation pathway, which is first conversion into K2CO3, followed by a violent activation reaction (Eqs. S2-S5), thus in turn forming developed pore structures. As a special case, the multi-level porosity of EDTA-2K-derived OAPCs is from the gas etching effect (in-situ released H2O, CO, CO2 and NOx) and group self-intercalation effect (-COOK) [48]. Notably, potassium salts have clear advantages in activation ability and template removal, and their activity is higher than but not limited to sodium, magnesium, calcium, zinc and ammonium-based organic salts.

    2.2.1   Ethylenediaminetetraacetic acid disodium (C10H14N2Na2O8)

    EDTA-2Na, an economical chelating agent, is suited to develop N-rich OAPCs [51]. Research highlights that EDTA-2Na-derived OAPCs are superior candidates due to the unique micro-mesopore structures, N self-doping feature and excellent hydrophilicity [52]. Related to heavy metal salts (e.g., ZnCl2) and rigid templates (e.g., SiO2), it has the unique gas etching effect that can form controllable hierarchical porosity by releasing H2O, CO, CO2 and NOx during pyrolysis [52]. Also, in situ -COONa further betters the activation ability by group self-intercalation effect, inducing improved porosity [53].

    Tan et al. [54] built a series of OAPCs by EDTA-2Na self-activation (Fig. 3a). The optimal PC-750 achieved a high SBET of 976.9 m2/g, large Vmeso/Vpore of 24.2% and 4.86% high N-doping, thus inducing a high desalting capacity of 8.02 mg/g in 25 mg/L NaCl (Figs. 3b and c). By adopting EDTA-2Na activating taraxacum mongolicum, Chen et al. [52] designed biomass-derived OAPCs with legible meso-macropore structures, plentiful active sites and higher N content of 5.99%. When utilized for EF degradation of methylene blue (MB), it realized rapid electrolyte penetration and ion transport rate. Through transition metal-EDTA-2Na one-step complexation and self-template strategy, Song et al. [55] designed one Fe/Mn-NHPC with a high SBET of 939.1 m2/g and impressive Vmeso/Vpore of 68% (Figs. 3d and e).

    Figure 3

    Figure 3.  (a) Schematic of the fabrication process of PC-X and the CDI tests. (b) SEM images of PC-750. (c) N2 adsorption-desorption isotherms of PC-X. Reprinted with permission [54]. Copyright 2019, Elsevier. (d) Schematic of the preparation process and (e) N2 adsorption-desorption isotherms of Fe/Mn–NIHPC. Reprinted with permission [55]. Copyright 2022, Elsevier. (f) Schematic of the fabrication process of 3D framework carbon (3DFC). (g) SEM and (h) TEM images of 3DFAC. (i) Distance dependence of adsorption energy between Na atom and graphene layers. Reprinted with permission [28]. Copyright 2017, Wiley.
    2.2.2   Sodium citrate (C6H5Na3O7)

    C6H5Na3O7 has been used for high-yield synthesis of OAPCs. However, they are mainly adopted for the energy and sensing fields. It features copious -COOH and -OH, favoring the precursor crosslinking and O self-doping. Mass spectrometry coupled with thermogravimetric reveals a dual-stage activation mechanism: (i) Initial decomposition below 650 ℃ to generate Na2CO3 (Eq. 4); (ii) Na2CO3-mediated redox reaction and gas etching effect (Eqs. S6-S9 in Supporting information) [28]. Notably, the released Na vapors, CO2 and CO favor effective pore expansion, promoting the development of regular mesoporous structures with moderate SBET [56].

    C6H5Na3O73Na2CO3+CO2+H2O

    (4)

    C6H5Na3O7-based OAPCs normally exhibit limited Vpore and narrow pore size distribution, which shackles the synergistic effect between tertiary pores. Although adding the pyrolysis temperature can improve the porosity, it may lead to a lower carbon yield [57]. Moreover, due to the nature of sodium, the obtained OAPCs often have lower conductivity than that of potassium salts. Yang et al. [28] fabricated well-designed 3D framework carbons (3DFC) by direct C6H5Na3O7 pyrolysis (Figs. 3f-h). DFT calculations uncovered that its large interlayer spacing and curvature structure accelerated the insertion and extraction of Na+ (Fig. 3i). Thus, 3DFC displayed a high reversible capacity and splendid cycling stability. The diversity in the pore-forming mechanisms between potassium and sodium salts present a promising research area for exploiting OAPCs with wonderful SBET and porosity.

    2.2.3   Sodium lignosulfonate (C20H24Na2O10S2)

    Lignosulfonate (SLS), as a by-product from the sulfite pulping, converting to OAPCs is an alternative potential path [58]. SLS is a promising self-activator for preparing mesoporous-dominated OAPCs due to its natural structure, high carbon content and rich N/O/S elements. However, SLS-based OAPCs often have a low SBET, limited Vmicro and poor graphitization degree [59,60]. This is owing to the inadequate activation and pyrolysis ability of the produced Na2SO4 during pyrolysis [61]. Their low SBET translates to fewer active sites, thus reducing the material capability.

    To address the above obstacles, Shi et al. [62] developed a GO-mediated activation-self-activation craft using K2C2O4-SLS bi-activators (Fig. S2a in Supporting information), designing mesopore-dominated N-doped HPCs (ENHPC) with a high SBET of 1795.5 m2/g, improved Vmicro/Vpore of 23% and enhanced conductivity (Figs. S2b-d in Supporting information). When assembled for Ni(Ⅱ) desalination, ENHPC respectively acquired a high salt removal capacity and rate of 17.86 mg/g and 0.99 mg/g/min in 10 mg/L Ni(Ⅱ). To integrate high yield-high performance, Shi et al. [63] designed SLS-KHCO3-KNO3 systems, yielding defect-rich N/S Co-doped HPCs (NSHPCSKK) (Fig. S2e in Supporting information). Its extensive defect structures were certified by ex-situ Raman (Fig. S2g in Supporting information), with further revelation of N/S co-doping at defect sites by XPS. DFT analysis determined that N/S co-doped defect structures had strong adsorption effects on Na atoms. Therefore, it depicted a rapid average desalting rate of 12.1 mg g−1 min−1.

    2.2.4   Sodium glutamate (C5H8NNaO4)

    Gourmet powder, e.g., C5H8NNaO4, is an easily accessible organic salt rich in N, making it suitable for fabricating N-doped OAPCs [64]. Activation mechanism involves the transformation of C5H8NNaO4 into C5H6NO3-Na through decomposition and gasification. Whereafter, it decomposes to form Na2CO3 at 550-650 ℃, followed by the same activation mechanism as Na2CO3 (Eqs. S6-S9) [65]. C5H8NNaO4-based OAPCs normally have unique hierarchical porous structures that favor rapid ion transfer. Meanwhile, the N self-doped characteristic introduces the extra pseudocapacitance effect, strengthening the specific capacitance.

    By C5H8NNaO4-NaCl co-activation, Qian et al. [66] prepared a series of C5H8NNaO4-derived N-doped HPCs under different pyrolysis temperatures and times. The optimal SMC-800-2 exhibited a large SBET of 1007.62 m2/g, superior Vpore of 0.56 cm3/g and high N doping level (Fig. S2f in Supporting information). Similarly, Sun et al. [67] also manufactured 3D N-doped OAPCs (3D-NPC) by C5H8NNaO4-NaCl co-carbonization (Fig. S2h in Supporting information). Due to high N content of 4.93% and large SBET of 1481.0 m2/g, 3D-NPC with an interconnected hierarchical porous structure displayed an excellent desalting capacity of 19.4 mg/g and superior cycle stability (Fig. S2i in Supporting information).

    Organic zinc salts include zinc gluconate (C12H22O14Zn), zinc acetate (Zn(CH3COO)2), EDTANa2Zn (C10H14N2O8Na2Zn), etc. [68,69]. For C12H22O14Zn, it initiates with carbothermal reduction, yielding ZnCO3 that self-integrates into the carbon matrix (Eq. S10 in Supporting information). As temperature increases, the residual ZnCO3 decomposes to ZnO, which chemically interacts with the carbon (Eq. S11 in Supporting information). When temperatures > 900 ℃, ZnCO3 races reductive reactions with carbon to produce metallic Zn and Zn vapors. These reactions induce intense surface etching, generating micropore-dominated hierarchical porous structures (Eqs. S12 and 13 in Supporting information) [69]. Similarly, Zn(CH3COO)2 thermally decomposes into ZnO and other gases, which synergistically engineer mesopore-rich carbon networks via dual mechanisms: (i) ZnO for pore confinement and (ii) in situ gas etching effect for pore interconnection enhancement.

    EDTANa2Zn delivers distinct activation pathways, primarily through its thermal decomposition under elevated temperatures to produce ZnO and Na2CO3 (Eq. 5) [70]. During pyrolysis, organic components can carbonize to form a carbon matrix, which then engages in carbothermal reduction with ZnO, thus releasing gases and Zn vapors. The gas etching effect can adjust porosity and refine pore size distribution. Moreover, its intrinsic N species can be incorporated into the carbon lattice via in-situ doping, thereby introducing extra active sites and bettering surface hydrophilicity. This favors matter transport and augments material performance.

    C10H14N2O8Na2ZnZnO+Na2CO3+CO2+H2O

    (5)

    Through directly pyrolyzing EDTA-2K at 800 ℃, Shi et al. [48] fabricated an N-doped HPC (NC-800). As expected, it acquired a prominent SBET of 2703.0 m2/g, large Vpore of 1.7 cm3/g and doped carbonyl and nitrogen groups (Figs. 4a and b). When taken for the adsorption of sulfamethoxazole (SMX), it realized an almost 99.5% removal rate. Gao et al. [70] designed rich-defective OAPCs via EDTA-3K-Zn(CH3COO)2 co-activation (Fig. 4c). Herein, EDTA-3K produced micropores, while Zn (CH3COO)2 generated meso-macropores, thus building hierarchical porous structures (Fig. 4e). This scheme accelerates electrolyte penetration and ion diffusion pathways. Moreover, O-containing groups and intrinsic defects in OAPCs promoted charge transfer, expanded the graphite layer spacing and constructed more accessible active sites (Fig. 4d).

    Figure 4

    Figure 4.  (a) SEM images and (b) N2 adsorption-desorption isotherms of NC800. Reprinted with permission [48]. Copyright 2020, Elsevier. (c) Schematic illustration of the preparation process and (e) TEM images of Defect/O modified-C. (d) The interlayer space and intercalated energy of K+ on diverse GO configurations of pure carbon. Reprinted with permission [70]. Copyright 2021, Elsevier. (f) Schematic illustration of the preparation of HPC-700. (g) N2 adsorption-desorption isotherms of AC and HPC-X. (h) Cations’ selective adsorption ability of HPC-700. Reprinted with permission [73]. Copyright 2022, Elsevier. (i) Schematic illustration of the preparation process of MNCs. Reprinted with permission [74]. Copyright 2025, Elsevier.

    Organic magnesium salts are also excellent activators owing to their sustainability and high pore formation ability. Magnesium salts involve magnesium citrate (C12H10Mg3O14), magnesium acetate (Mg(CH3COO)2) and magnesium gluconate (C12H22MgO14) [71,72]. For C12H10Mg3O14, the molten-phase behavior at high temperatures facilitates the graphitic domain delamination and pore structure reconstruction. Meanwhile, in situ formed MgCO3 can be embedded within the carbon framework. Subsequent thermal dissociation of residual MgCO3 yields MgO and CO2, the latter can improve surface porosity by gas etching effect [72]. The coordinated templating-etching strategy produces carbon networks with multiscale porosity spanning micro- and mesopores, exhibiting optimized matter transport kinetics. Similar activation principles govern Mg(CH3COO)2-based OAPCs, where staged decomposition products co-modulate pore structures [71].

    Nie et al. [73] prepared unique HPCs by the C12H10Mg3O14 self-activation strategy (Fig. 4f). Research revealed that HPC-800 exhibited a high SBET of 1636.0 m2/g, prominent Vpore of 2.30 cm3/g, ultrahigh Vmeso/Vpore of 95.5% and plentiful negative surface charges (Fig. 4g). Further CDI tests indicated that it had excellent ion-selective and rapid dynamic rate (Fig. 4h). 3D interconnected hierarchical structures are much more conducive to the diffusion, migration and adsorption of matters. Shi et al. [74] prepared 3D N-doped HPCs via a carbonization-activation method (Fig. 4i). In the carbonization step, the 3D interconnected skeleton was built by C12H22MgO14-NaCl co-pyrolysis, where NaCl and pyrolysis-generated MgO played a crucial role. During the activation step, KHCO3 and urea expanded the micropores and introduced massive N elements. Eventually, C12H10Mg3O14-derived N-doped OAPCs (MNC) delivered a high SBET of 2423.0 cm2/g and large Vpore of 1.24 cm3/g. When taken for CO2 capture, it gained a high adsorption capacity of 4.22 mmol/g at 25 ℃ and 1 bar.

    Organic calcium salts can often pyrolyze and decompose before self-activation, in situ generating CaCO3, and then producing CaO and massive gases, thus gradually converting organic components into OAPCs. For instance, calcium acetate (Ca(CH3COO)2) can pyrolyze and generate CaCO3, which further yields CaO to interact with carbon and produce CO2 to etch the carbon skeleton, thereby forming copious porosity (Eqs. S14 and S15 in Supporting information) [75]. Another typical salt is EDTANa2Ca (C10H12CaN2Na2O8). It can first pyrolyze to form CaO and Na2CO3 as well as CO2 and H2O vapors (Eq. S16 in Supporting information), producing strong internal activation of the carbon skeleton and promoting the pore structure development, thus forming micro-mesopores. According to the dual template effect and gas etching effect, EDTANa2Ca-derived OAPCs often possess hierarchical porous structures and a more reasonable pore size distribution. Moreover, its pyrolysis can also in situ introduce N elements into OAPCs, which can greatly improve their surface wettability and conductivity, thus favoring the migration, diffusion and adsorption of matters and enhancing mass/charge transfer.

    Sheng et al. [76] designed N-doped porous carbon nanosheets (NPC-CaxKy) by the synergy effect of Ca(CH3COO)2-CH3COOK-melamine (Fig. S3a in Supporting information). Due to the in situ generated CaCO3/K2CO3 and the foaming effect of melamine, the optimal NPC-Ca1.5K3 showed clear hierarchical porosity with a high SBET of 2546.6 m2/g, large Vpore of 1.32 cm3/g and 2.47% high N doping (Fig. S3b in Supporting information). By direct pyrolysis of EDTANa2Ca, Hu et al. [77] gained a series of NHPCs. Herein, Na2CO3 templates promoted the production of meso-macropores, thus inducing the formation of well-developed hierarchical porosity. Ultimately, NHPC-850 acquired a high SBET of 2015.0 m2/g and large Vpore of 1.74 cm3/g.

    Zhang et al. [78] constructed biomass-derived OAPCs by Ca3(C6H5O7)2 activating biomass pyrolysis vapors (Figs. S3c and d in Supporting information). The influences of precursor preparation and pyrolysis temperature, and heating rate on the yield of biomass pyrolysis products, composition of light bio-oil and structure of OAPCs were explored. Research indicated that its plentiful O-containing functional groups induced the gas etching effect, which combined with the CaO template effect, realized the micropore generation. The optimal material gained a high SBET of 1703.0 m2/g and splendid Vmeso/Vpore of 24.17%. Thus, it realized a superior H2 adsorption capacity of 170.1 cm3/g (1.53 wt%) at 77 K at 25 ℃.

    Organic ammonium salts are a kind of wonderful activator due to their sustainability and outstanding activation effects. However, there is relatively little research. Ammonium salts mainly include ammonium citrate (C6H5O7(NH4)3), ferric citrate (C6H5FeO7) and ferric ammonium citrate ((NH4)xFey(C6H4O7)z). For C6H5O7(NH4)3, the generated volatile compounds can be embedded into the carbon frame during pyrolysis, and then decompose to produce NH3 and CO2 via the decarboxylation reaction. This behavior constitutes a strong gas etching effect on the precursor, thus forming copious porosity. This improvement induced a decrease in matter diffusion/charge transfer resistance, thereby improving the overall performance and enhancing the dynamic [79].

    Zhu et al. [80] adopted (NH4)xFey(C6H4O7)z as C/Fe sources and GO as structure-directing agents, building a C-G/AFC with interconnected structures (Fig. S3e in Supporting information). Viewing the synergy effect of (NH4)xFey(C6H4O7)z and GO, C-G/AFC achieved a medium SBET of 113.4 m2/g and 1.73% high N doping (Fig. S3f in Supporting information). In another research, Cheng et al. [81] took kiwifruit as precursors and (NH4)xFey(C6H4O7)z as activators, gaining biomass-based OAPCs (Fig. S3g in Supporting information). Here, Fe and NH3 generated form (NH4)xFey(C6H4O7)z improve the graphitization degree of OAPCs and construct porous framework structures, respectively.

    It is vital to reveal the effect of organic ammonium salt on the morphology of OAPCs. Qiang et al. [82] adopted C6H5O7(NH4)3-C6H5K3O7 co-activation craft to fabricate crimped porous carbon nanosheets (Fig. S3h in Supporting information). Compared with the SBET of 1159.2 cm2/g, Vmicro of 0.48 cm3/g and Vmeso/Vpore of 27.3% for single C6H5K3O7 derived OAPCs, its SBET, Vmicro and Vmicro/Vpore were 1668.3 cm2/g, 0.52 cm3/g and 42.2%, respectively. Next, by introducing urea co-pyrolysis, the final HNHPCPUA had up to 3280.2 m2/g for SBET, 2.49 cm3/g for Vpore and 6.4% for N doping (Fig. S3i in Supporting information). These results revealed that both urea and C6H5O7(NH4)3 can tune the pore structure and surface chemistry properties of OAPCs, and C6H5O7(NH4)3 mainly adjusted the pore size.

    High-performance OAPCs should own the following merits, such as high accessible SBET, appropriate pore size distribution, superior conductivity, prominent stability and high carbon yield. The physicochemical properties and pore structure indices of diverse OAPCs were summarized in Fig. 5 and Table S1 (Supporting information). The evaluation indicators involved activation ability, SBET, pore size distribution, activator types, surface charges, graphitization degree and element doping. It can be seen that single organic salt-based OAPCs are hard to integrate the above advantages. Sodium salts often have weak activation ability, thus inducing a medium SBET. Due to the size effect of Na2CO3 and in situ N-doping of sodium salts, its derived OAPCs are mainly mesoporous and own certain N-doping. Zinc salts-derived OAPCs indicated similar structural characteristics and chemical properties to sodium salts. However, because it releases Zn vapor during pyrolysis, its derived OAPCs also have certain micropores. Notably, viewing calcium salts and ammonium salts has extra gas etching effects, SBET of their derived OAPCs can be further improved. Although manesium salts delivered a strong activation ability, its derived OAPCs are also mainly mesoporous. Notably, among the various salts, potassium salts are still optimal and it is vital to identify the other salts that as auxiliary activators, may have a better effect. Future exploration of potassium-based OAPCs involves the following three aspects: (1) Construct bi- or multi-activator systems that utilize the synergistic effects of diverse metal activators to build OAPCs with tertiary pore structures and high yield; (2) Construct foaming agent-assisted activation systems (e.g., urea, melamine and thiourea), fabricate high N/S-doped OAPCs with ultrahigh SBET and microporous ratio; (3) Construct O-rich activation systems, prepare OAPCs with ample surface charges to reinforce their application selectivity.

    Figure 5

    Figure 5.  Physicochemical properties of different sustainable OAPCs.

    Compared with biomass, polymer and template-constructed precursors, the structure of OAPCs is greatly limited by the molecular arrangements and chemical nature of organic salts. So far, massive work has been devoted to optimizing their structure from 0D to 3D, e.g., carefully choosing organic salts, precisely controlling synthesis conditions and innovatively exploiting new fabrication processes [83]. These efforts aim to surmount the limitations of organic salts and develop OAPCs with tailored structures to adapt to diverse environmental applications.

    0D PCs, e.g., carbon nanoparticles, refer to PCs that are confined to the nanoscale in all three dimensions, which mainly exist in the form of spherical, cubic and prismatic [84]. 0D PCs hold several distinctive characteristics. It can serve as both active materials or carriers, achieving high exposure of the accessible active sites of active materials [85]. Due to the regular geometry, small structural size and tunable pore structure, OD PCs also own an excellent SBET and improved hydrophilicity, thereby bettering the interaction between ions/molecules and target OAPCs [86,87]. Further, their high tap density favors high volumetric performance. Their typical synthesis methods include the hydrothermal method, multi-stage pyrolysis method, spray drying method, etc.

    Based on the spray drying and carbonization-activation craft, Liu et al. [58] designed hierarchical porous carbon spheres (HPCS) from SLS (Fig. 6a). Research disclosed that the spray drying played a decisive role in the 0D precursor formation. As expected, HPCS delivered tertiary structures, ultrahigh SBET of 3402 m2/g and superior Vpore of 2.46 cm3/g. When adopted for CH2Cl2 capture, HPCS acquired a high adsorption capacity of 181.0 mg/g (Fig. 6b). Mechanism research revealed that meso-macropores offer rapid transport channels, and micropores provide massive adsorption sites. Pang et al. [88] exploited a two-stage pyrolysis craft, gaining a series of SLS-derived HPCSs with clear tertiary structures (Fig. 6c). Here, the low-temperature carbonization step was mainly used for the finalization of spherical precursors, while the high-temperature pyrolysis was utilized to obtain multi-level porosity. By temperature regulation, HPCS-900 acquired a high SBET of 1939.0 m2/g and large Vpore of 1.42 cm3/g (Fig. 6d).

    Figure 6

    Figure 6.  (a) Schematic illustration of the preparation process of HPCS-X-Y (inset: SEM images). (b) CH2Cl2 adsorption capacity and time of HPCS-X-Y. Reprinted with permission [58]. Copyright 2022, Elsevier. (c) SEM images of HPCS-900. (d) N2 adsorption-desorption isotherms of HPCS-X. Reprinted with permission [88]. Copyright 2018, Elsevier. (e, f) SEM images of HNPCPA. (g) N2 adsorption-desorption isotherms and (h) XPS spectra of diverse OAPCs. Reprinted with permission [89]. Copyright 2023, Elsevier. (i) Scheme of the fabrication process and (j) TEM images of Se-HPCF. Reprinted with permission [95]. Copyright 2020, RSC. (k) SEM images of 1D CFM. Reprinted with permission [96]. Copyright 2022, MDPI.

    Integrating highly developed pore structures in 0D OAPCs is vital to accelerate the matter diffusion and enhance the material ability. Qiang et al. [82] designed C6H5O7(NH4)3-urea-co-assisted C6H5K3O7 crafts to gain high N-doped hierarchical porous carbon nanogranules (HNHPC) (Figs. 6e and f). Viewing the synergistic effect of the self-activation effect (C6H5O7(NH4)3-C6H5K3O7) and foaming effect (urea), it realized an ultrahigh SBET of 3280.2 m2/g, large Vmeso/Vpore of 57.83% and 6.40% high N-doping level (Figs. 6g and h). Research showed that C6H5O7(NH4)3 took a decisive role in the formation of HPCS, while urea played a leading role in regulating the N content and the particle size.

    1D PCs, e.g., carbon nanowires or carbon nanotubes (CNTs), have multiple advantages such as high SBET and controllable pore structure, efficient mass transfer and superior structural stability [8992]. Typically, the unique hollow configuration and superior charge transport properties of CNTs have driven wide research interest [93]. Nonetheless, scaling up CNTs faces huge challenges, e.g., costly precursor expenses and intricate synthesis processes needing precise control [94]. Despite these advantages, the current research indicates that exploited organic salt-derived 1D OAPCs is still very limited. In a case, to seek 1D frameworks to inhibit the inactivation of Se, Chen et al. [95] manufactured a Se-hierarchical porous carbon fiber (Se-HPCF) by electrostatic spinning craft taking SLS as precursors/self-activators (Fig. 6i). As a result, Se-HPCF with 1D hierarchical porous structures and copious accessible SBET effectively alleviated the Se inactivation (Fig. 6j). Based on C6H5K3O7/polyacrylonitrile (PAN), Zhang et al. [96] constructed a 1D nanoscale carbon fiber membrane (CFM) by the same strategy (Fig. 6k). The optimal CFM gained a medium SBET of 347.8 m2/g and copious porosity.

    2D PCs, e.g., carbon nanosheets, often have a thin thickness on the nanometer scale along with a relatively large aspect ratio and highly exposed SBET. The structure confers many advantages, e.g., short matter diffusion channels and abundant interfacial contact area for migration [97,98]. There is a consensus that graphene is a well-known 2D PC, which is the world’s thinnest, strongest and most conductive material [99]. The orthodox preparation methods include the mechanical exfoliation, solution exfoliation and Hummers method [100]. However, these crafts face considerable limitations, e.g., easy stacking, severe oxidation degree and high production cost [101,102]. In this condition, leveraging organic salts for fabricating 2D OAPCs provides a potential proposal. This strategy reduces reliance on costly raw materials, increases structural control precision and streamlines the preparation craft, enhancing the production feasibility for 2D OAPCs.

    Single organic salts can be directly pyrolyzed to obtain 2D OAPCs. By directly pyrolizing C12H22Ca3O14, Zhang et al. [103] prepared a carbon nanosheet with a thickness of 29 nm. SEM and TEM disclosed that the thickness can be controlled within a range of 20-30 nm by varying the pyrolysis temperatures (Figs. S4a-j in Supporting information). XRD and BET showed that the nailing carbon frame was mainly from in situ-generated CaCO3, CaO and CO2. Based on the in situ self-activation and KOH activation, C6H11KO7-based 2D porous carbon nanosheet (2D PCNS) with a superior SBET of 2793.5 m2/g and splendid Vpore of 1.67 cm3/g was fabricated (Fig. S4k in Supporting information) [104]. When utilized for the capture of MB, it acquired a high adsorption capacity of 688.76 mg/g. Besides, Luo et al. [105] prepared a PCN by a rapid EDTA-4Na self-activation strategy (Figs. S4l-n in Supporting information).

    Achieving universal preparation and further pore expansion of 2D OAPCs is crucial. Hou et al. [106] exploited N/O co-doped PCNs (NOPC) based on the g-C3N4-C6H5K3O7 co-activation craft (Fig. S4o in Supporting information). C6H5K3O7 here served as precursors/self-activators, and g-C3N4 was adopted to adjust the morphology, porosity and elemental composition of OAPCs. As a result, the optimal NOPC delivered an ultrahigh SBET of 2557 m2/g, excellent Vpore of 1.6 cm3/g and 3.38% high N content. Wu et al. [29] prepared sodium humate-based PCNS via the urea-C6H5K3O7 co-activation strategy (Fig. S4p in Supporting information). By case comparison, we found that urea and g-C3N4 had the same pore formation effect, which was mainly due to their unique gas exfoliation effect regulating the morphology of OAPCs and accelerating the formation of sheet layers.

    Although 2D PCs possess distinctive advantages, they normally suffer from the drawbacks of easy-to-layer stacking, thus reducing exposed accessible SBET and hindering internal matter migration [107,108]. In contrast, 3D PCs fabricated from low-dimensional subunits preserve the intrinsic merits of individual nanosheets while introducing emergent properties [109]. For instance, such 3D architectures manifest superior structural robustness compared with their 2D counterparts, enabling better tolerance to mechanical stress during usage [110]. Besides, their interconnected porous networks favor directional matter flux and establish seamless conductive/transport pathways [111]. Therefore, engineering 3D OAPCs with hierarchical porosity, improved hydrophilicity and enhanced conductivity is a critical objective.

    Sun et al. [49] exploited 3D interconnected PCs (IPCs) by facile C12H16K2O13 self-activation (Fig. S5a in Supporting information). The optimized IPC-800 showed an SBET of 1145.8 m2/g and Vpore of 0.58 cm3/g (Figs. S5b-d in Supporting information). To further augment the interconnection degree within carbon skeletons, Wang et al. [112] fabricated 3D interconnected NSHPCs using C6H5K3O7 as activators, enzymes as biocatalysts and cottonseed meal as precursors. Herein, cellulase pretreatment greatly reduced the cellulose content in cottonseed meal from 12.5% to 2.2% while establishing porous precursor frameworks. Vitally, the enzymolytic process validly added the O content and promoted the activation efficiency of C6H5K3O7. Thus, the resultant CCM-800-2 showed a high SBET of 1528.0 m2/g, superior disorder degree and 11.3% high O content (Fig. S5e in Supporting information). This unique 3D structure effectively accelerated the ion migration and adsorption, thereby realizing an obvious performance breakthrough.

    Wang et al. [23] developed a novel in-situ template-assisted self-activation strategy to construct a series of X-NSMHPCs (X = A, M, N) from diverse sulfate (Al2(SO4)3/MgSO4/(NH4)2SO4) precipitated kraft lignins (X-KLs, X = Al, Mg, NH4) (Fig. S5f in Supporting information). Related to other X-NSMHPCs, N-NSMHPC presented distinct mesoporous-dominated hierarchical porous structures with high SBET of 622.1 m2/g and copious N/S doping level (Figs. S5g-i in Supporting information). Research depicted that its distinct tertiary pore structure and massive surface-exposed active sites accelerated electrolyte penetration and promoted ion insertion and extraction. Zhu et al. [113] utilized C4H4K2O6 to activate fallen leaves (FL)/chicken feathers (CF)/Enteromorpha prolifera (EP) to gain three diverse 3D OAPCs (Figs. S5j and k in Supporting information). Compared with the low SBET (256.0 m2/g) of C4H4K2O6-derived OAPCs, SBET for FL-PCM, CF-PCM and EP-PCM were 1721.0, 1819.0 and 2151.0 m2/g, respectively.

    In summary, the section systematically classifies OAPCs into 0D, 1D, 2D and 3D, each with distinct structural characteristics and application advantages. 0D OAPCs (e.g., nanospheres and particles) have high SBET and uniform pore distribution, enabling efficient adsorption and rapid charge transfer, which are ideal for ion/molecule capture. 1D OAPCs (e.g., nanowires and tubes) offer unique axial channels, optimizing mass transport and mechanical stability, making them more suitable for electrochemical devices and composite reinforcements. 2D OAPCs (e.g., nanosheets) show ultrathin structures with highly exposed active sites, favoring rapid ion diffusion and catalytic reactions. 3D OAPCs (e.g., foams and networks) integrate interconnected pore systems, combining high SBET with superior structural robustness, excelling in applications requiring multi-scale mass transport, such as adsorption and CDI. This dimensional diversity enables OAPCs to address specific environmental issues by tailoring structure-property relationships for targeted applications.

    OAPCs, ascribed to the high SBET, tunable pore structure, excellent conductivity and superior chemical stability, have been proven wide application foreground in the environmental fields. OAPCs provide innovative solutions to challenges such as water pollution, gas purification and electromagnetic radiation via different mechanisms of adsorption, catalysis and absorption. Their environmental applications are prominently reflected but not limited to the following five domains.

    Adsorption is a phenomenon where gas or liquid molecules are concentrated on the adsorbent surface [114]. Presently, adsorption has been used for the deep treatment and purification of hazardous substances in soil, water and gas. Compared with biodegradation, membrane technology and ozonation with poor longevity, high costs, serious membrane fouling and massive toxic degradation intermediates, adsorption has attracted broad attention owing to its low costs, facile operation, high efficiency and sustainability [115]. Normally, traditional PCs face high costs, process complexity and low carbon yield, whereas OAPCs can avoid the above constraints. The adsorption of pollutants on OAPCs is mainly determined by physical-chemical nature, e.g., SBET, Vpore, pore size distribution and chemical composition. The main adsorption mechanisms involve pore filling, electrostatic interaction, hydrogen bonding, π-π interaction etc. Table S2 (Supporting information) gives the adsorption capacity and adsorption mechanism of typical OAPCs.

    In the solution adsorption aspect, Tan et al. [116] adopted the EDTA-2Na self-activation to build PC-650 and PC-750 (Fig. 7a). Thereinto, PC-750 gained a high SBET of 1354.7 m2/g and large Vmeso/Vpore of 37.5% (Fig. 7b). As expected, PC-750 achieved a high MB adsorption capacity of 1354.7 mg/g, and its adsorption behavior was coincidental to the Langmuir isotherm model and pseudo-second-order kinetic model. By C6H5K3O7-C6H5FeO7 co-activating EP, Qin et al. [117] fabricated a porous carbon/porous biochar (PC/PB). Viewing their synergistic effect, PC/PB showed unique tertiary pore structures with a high SBET of 1415.0 m2/g and large Vpore of 1.08 cm3/g (Fig. 7c). Thus, PC/PB gained a superior adsorption capacity of 844 mg/g for SMX, which is higher than that of reported sorbents (Fig. 7d). Research depicted that the high property mainly relied on pore filling, hydrogen bonding, π-π interaction and electrostatic interaction (Fig. 7e).

    Figure 7

    Figure 7.  (a) Schematic illustration of the preparation process and (b) N2 adsorption-desorption isotherms of PC-650 and PC-750. Reprinted with permission [116]. Copyright 2020, RSC. (c) N2 adsorption-desorption isotherms and (d) comparison of the adsorption ability of SMX with reported sorbents. (e) Adsorption mechanism of SMX on PC/PB. Reprinted with permission [117]. Copyright 2023, Elsevier. (f) Schematic illustration of the preparation craft of CPCs. (g) SEM images of CPC-3. (h) CO2 capture capacity of CPC-3 at 0, 10 and 25 ℃. Reprinted with permission [118]. Copyright 2021, RSC. (i) Schematic illustration of the preparation craft of DT-NPC-xs. (j) N 1s spectra and (k) SEM images of DT-NPC-5. IAST selectivities for (l) SO2/N2 and (m) SO2/CO2 at 25 ℃ and 100 kPa. Reprinted with permission [119]. Copyright 2022, Elsevier.

    In the gas adsorption aspect, Singh et al. [118] developed N/O-doped biocarbons using C6H5K3O7 activating casein (Fig. 7f). The optimal CPC-3 (mcasein: mactivator = 1: 3) showed a rough morphology with an ultrahigh SBET of 2212.0 m2/g and plentiful O/N functional groups (Fig. 7g). Thus, it delivered a high CO2 capture capacity of 25.4 mmol/g (Fig. 7h). By using urea as N sources/foaming agents and C12H22O14Zn as self-activators, Zhu et al. [119] prepared N-doped PCs (DT-NPC) (Figs. 7i and k). Notably, Zn evaporation induced copious micropores, while the gas etching effect helped to build tunable meso-macropores and massive N-doping sites (Fig. 7j). Thus, DT-NPC-3 acquired a high SO2 adsorption capacity of 11.8 mmol/g (25 ℃, 1.0 bar). Besides, the selectivity of SO2/N2 (0.1/0.9) and SO2/CO2 (0.1/0.9) was separately198.7 and 21.5 (Figs. 7l and m).

    CDI is an emerging seawater desalination technique based on electric double-layer capacitors [120]. Related to electrodialysis, reverse osmosis and multi-stage flash, CDI is more competitive to treat low-concentration brine and is energy-saving, no secondary pollution and low cost [121]. In operation, ions in brackish water can be rapidly adsorbed onto electrodes with opposite charges at a low voltage, and they can then be desorbed by the short-circuit [122]. Electrode materials (e.g., PCs and carbon composites) are the CDI core that greatly affect the key indexes of salt adsorption capacity/rate, productivity and cycle stability [120123]. OAPCs are a splendid selection by virtue of their high SBET, adjustable pore structure, high conductivity and prominent stability. Table S3 (Supporting information) gives the CDI desalination capacity of typical OAPCs.

    Shi et al. [35] exploited a double organic salt activation craft that utilized Na2EDTA-C6H5K3O7 to co-activate lotus stems (Fig. S6a in Supporting information). The final 3D N-doped HPC (3DNHPC11) achieved a high SBET of 2256.2 m2/g and large Vmeso/Vpore of 60.0% (Figs. S6b and c in Supporting information). When taken for CDI desalination, it respectively gained a superior desalting capacity/rate of 22.21 mg/g and 5.56 mg g-1 min-1 in 500 mg/L NaCl at 1.2 V. The excellent performance was due to unique hierarchical porous structures and massive accessible active sites promoting electrolyte penetration and ion transport (Fig. S6d in Supporting information).

    To further accelerate the desalting dynamics, Lu et al. [63] designed SLS-KHCO3-KNO3 co-activation systems and prepared defect-rich N/S co-doped HPCs (NSHPC). Its defective structure was certified by Raman, with further revealing N/S co-doping at defect sites by XPS. DFT analysis disclosed that N/S co-doped defects had a strong adsorption effect on Na atoms. Thus, NSHPC showed a faster desalting rate of 12.1 mg g-1 min-1. Qiang et al. [89] used C6H5O7(NH4)3-urea co-assisted C6H5K3O7 activation craft to build nanogranule-like NHPCs with ultrahigh SBET and nailing hydrophilicity (Figs. S6e and f in Supporting information), greatly accelerating the electrolyte penetration, inducing a high salt adsorption capacity and ultrarapid desalting rate (Figs. S6g and h in Supporting information).

    Because of the widespread application of refractory organic compounds in industry and daily life, it is inevitably detected in water and wastewater [124,125]. Thus, numerous strategies have been explored to reduce the adverse consequences caused by organic pollutants. Compared with the orthodox crafts, advanced oxidation processes (AOPs), especially the PMS activation that can achieve the pollutant complete degradation. This is due to their robust oxidation capability and versatile adaptability [126]. The current core of PMS activation is to develop catalysts that can generate highly reactive oxygen species [127]. Various advanced transition metal-based catalysts, e.g., Co3O4, Fe3O4 and FeOOH, have been successively exploited [128]. However, the suboptimal durability and unavoidable metal leaching greatly hindered their application in PMS systems [129]. Notably, OAPCs have obtained more and more attention ascribed to their large SBET, adjustable porous structure and remarkable structural stability.

    By C6H5Na3O7 self-activation, Zhang et al. [96] synthesized a series of 3D PCs (3DPCs) with interconnected carbon skeletons and abundant intrinsic defects (Fig. 8a). The optimal 3DPC-900 obtained a high SBET of 904.9 m2/g and large Vpore of 0.93 mg/cm3, favoring exposing more active sites (Fig. 8b). When taken for the phenol degradation, an ultrapid degradation kinetic constant of 1.45 min-1 was achieved (Fig. 8c). Moreover, 3DPC-900 also presented a superior degradation efficiency for other pollutants, such as bisphenol A (BPA) and SMX.

    Figure 8

    Figure 8.  (a) Scheme of the manufacture process and (b) N2 adsorption-desorption isotherms of 3DPC-X. (c) The change trend of k and the SBET along with the increased carbonization temperature. Reprinted with permission [96]. Copyright 2022, Elsevier. (d) Influence of Zn1Co5/P4C dosage on the degradation efficiency. Reprinted with permission [130]. Copyright 2023, Elsevier. (e) SEM images of MEP-2. (f) The curves of dependence of pyrrolic-N and P-C (%) on the ORR potential and degradation efficiency. Reprinted with permission [135]. Copyright 2023, Elsevier. (g) UV−vis spectra of degradation of MB driven by DLRD-TENG systems. Reprinted with permission [52]. Copyright 2019, Elsevier. (h) Schematic illustration of the formation mechanism for ZGD-x. (i) The influence of indicators on the EF degradation efficiencies for MG and MB. Reprinted with permission [136]. Copyright 2021, Elsevier.

    Transition metal-doped PCs have many oxidation mechanisms and low secondary pollution, favoring further adding degradation efficiency. Lv et al. [130] used Co(CH3COO)2 and Zn(CH3COO)2 as Co-/Zn-containing precursors/activators, and polyester waste as carbon sources, fabricating Co/Zn Co-doped PCs (Zn1Co5/P4C). Characterization results indicated that Zn evaporation favored the formation of PC frameworks, and Co nanoparticles can enhance the graphitization degree and act as extra active sites. Notably, levofloxacin degradation efficiency was as high as 96.60% within 90 min (Fig. 8d). Mechanism analysis revealed that the excellent catalytic efficiency may be because the PC frameworks can effectively support and protect the highly active Co nanoparticles, while the evaporated Zn could increase the SBET.

    EF is an electrochemical AOP technique (EAOPs), having obvious advantages of low cost, high efficiency, high integration and sustainability [131]. EF can in situ produce H2O2 on the cathode by a selective 2e oxygen reduction reaction (ORR), thus yielding OH with highly non-selective oxidation. Thus, the process highly depends on the continuous H2O2 generation, which is primarily determined by the cathode materials [132,133]. Carbon-based materials are prominent cathode catalysts so far that have superior SBET, adjustable pore structure, nailing conductivity and high structural stability [134]. However, the orthodox graphene, carbon aerogel and carbon felt are greatly constrained by the inadequate 2e ORR catalytic activity and selectivity. In constant, OAPCs are suitable catalysts for EF systems.

    Chen et al. [135] prepared N/P co-doped PCs with unique 3D hierarchical porous structures and copious N (2.9%) and P doping (2.9%) (Fig. 8e). Viewing the synergistic effect of NaH2PO2 and EDTA-2K, the generated micro-mesopores from gas templates could well accommodate OH radicals, and the massive pyrrolic-N and P-C active sites enhance 2e ORR selectivity. Therefore, when utilized for the MB degradation, the optimal MEP-2 gained a high degradation efficiency of 98.4%, and for mixed dyes was 97.1% (Fig. 8f). To harvest renewable mechanical energy to achieve deeper degradation, Chen et al. [52] exploited an double layer rotary disc-structured MB triboelectric nanogenerator (DLRD-TENG). When using DLRD-TENG to drive EF systems that used C10H14N2Na2O8 activated taraxacum-derived OAPCs, an ultrahigh degradation efficiency of 96% was achieved (Fig. 8g).

    Further, Tian et al. [136] proposed a template-assisted self-activation craft to fabricate N/O co-doped mesoporous carbons, where C12H22O14Zn served as self-activators and dicyandiamide acted as gas foaming agents/N sources (Fig. 8h). When taking the DLRD-TENG system, it acquired both high degradation efficiencies of 98.2% and 97.3% for malachite green (MG) and MB, respectively. Mechanism research showed that the excellent property was mainly attributed to high Vmeso, broad pore size distribution and the optimal N-O configuration (Fig. 8i).

    With the wide usage of electronic devices, electromagnetic radiation has become a new pollution source. An effective way to solve the threat is microwave absorption. Microwave absorber (MA) can absorb massive electromagnetic waves and then convert them into other forms of energy dissipation. The performance of MA is dependent on its internal components and microstructure [137]. PCs have copious porosity and periodic structures with micro-distributed units, which can realize deep penetration in the microwave absorption process [138]. However, orthodox PCs are apt for oxidation and degradation [139]. As a better selection, the thermal decomposition of organic salts into highly amorphous carbon and the concomitant generation of reducing gases to rebuild the carbon skeleton help to optimize the pore structure and surface chemical property of OAPCs.

    Shen et al. [140] prepared 3D interconnected GO nanocapsules (IGNCs) using C6H5Na3O7 self-activation (Figs. S7a and b in Supporting information). Notably, in situ-generated Na2CO3 can be evenly distributed in the carbon substrate, favoring the porosity formation. Thus, IGNCs gained massive oxygen-containing groups and copious disorder degrees, which not only enhanced the impedance matching characteristics but also enhanced the dipole and favored the amplified polarization loss capacity. As a result, it illustrated an effective absorption bandwidth (EAB) of 4.32 GHz, at a fill concentration of only 5 wt% and a matched thickness of 2.3 mm (Figs. S7c and d in Supporting information).

    Innovatively, by the direct pyrolysis of C6H5K3O7 in sealed tubes with diverse volumes, Hou et al. [141] fabricated a series of rich-defect PCNs (S-PCNs) (Fig. S7e in Supporting information). The optimal S-PCN-3 with clear micro-mesopore structures gained a large SBET of 825.6 m2/g and ultrahigh disorder degree (Figs. S7f-h in Supporting information). Study displayed that the induced defective carbon structures can effectively enhance microwave absorption. Thereby, S-PCN-3 acquired a remarkable electromagnetic wave absorption property, with a reflection loss of up to −58.2 dB and an effective EAB of 3.2 GHz, even at an ultra-low filler content of 5 wt% (Fig. S7i in Supporting information).

    Although there have been widely investigations on developing advanced OAPCs for treating various environmental applications, further research is required to sufficiently understand the drawbacks of OAPCs and how to further effectively reinforce them to maximize the material performance.

    (1) In the future, it is vital to develop magnetic or self-supporting OAPCs to realize their effective performance release and rapid material recovery. For non-electrochemical applications, OAPCs own a strong ability, however, a tedious recovery step is often required, especially for particles with small sizes and low density. This greatly adds to the overall treatment cost. Thus, introducing magnetic particles into OAPCs is necessary, which can not only solve the recycling issues and improve the reusability of OAPCs. To meet all the applications, more advocacy is to construct self-supported OAPCs. This is similar to activated carbon fiber and activated carbon cloth, which contain 100% active material and copious porosity. Currently, constructing carbon aerogel-based or wood-based OAPCs is an important research direction.

    (2) In the future, a deeper understanding of the basic theories of OAPCs is required. In-depth research on the decomposition and activation mechanisms of organic salts, clarifying the reaction processes of diverse organic salts at the atomic and molecular levels, will help to more precisely regulate the synthesis (reasonable hierarchical porous structure, ample ion/molecule accessible surface, copious defect degrees, appropriate heteroatom doping and superior mass/charge transfer efficiency) of OAPCs to meet diverse applications. Advanced in situ characterization techniques, e.g., in-situ SEM, in-situ FTIR and in-situ Raman, can monitor the structural evolution of organic salts during the activation process in real-time, providing direct evidence for optimizing the synthesis process.

    (3) Currently, artificial intelligence has been extensively applied in pharmaceutical research. As one subset, machine learning (ML) enables computer software to predict outcomes without the need for massive programming. A key characteristic of ML lies in its capability to train algorithms for handling complex and large-scale multidimensional datasets. Although existing studies have proved the application of ML in OAPCs for environmental remediation, this field remains in the early development stage. ML-based prediction models hold the potential to greatly reduce research workloads, making it worthwhile to explore the comprehensive application of ML in composite material combination prediction and production condition prediction.

    Overall, this review overviews sustainable OAPCs, stressing their multiple roles as activators and self-activators. Six diverse organic salts are comprehensively analyzed and identified for their unique decomposition pathways and activation mechanisms. Notably, structural control of OAPCs from 0D to 3D is discussed by regulating the precursor chemistry and pyrolysis conditions, optimizing ion transport and surface accessibility. Eventually, the environmental applications of OAPCs are assessed, proving superior application potential in various fields, such as adsorption, CDI, PMS activation, EF and microwave absorption. New manufacturing and recovery craft, advanced characterization methods and ML prediction are vital for the future development. We underline that the collaboration of researchers from diverse fields will further reinforce the scientific understanding of OAPCs and promote practical applications.

    Mingxing Shi: Writing – review & editing, Visualization, Funding acquisition, Conceptualization. Jiahui Liu: Writing – original draft, Visualization, Software. Wei Jin: Writing – review & editing, Funding acquisition. Zahira Bano: Writing – review & editing, Supervision, Software. Yubo Pan: Visualization, Software. Jianzhe Ma: Writing – review & editing. Xu Wu: Writing – review & editing, Software. Huijuan Jia: Supervision, Funding acquisition. Guolin Tong: Supervision, Project administration, Funding acquisition.

    The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

    The authors would like to acknowledge the financial support of the Natural Science Foundation of Jiangsu Province (No. BK20250707), Postgraduate Research & Practice Innovation Program of Jiangsu Province (No. KYCX25_1494), Nanjing Forestry University High-level Talent Scientific Research Start-up Foundation (No. 163105774) and Suzhou Project (No. ZXL2024374).

    Supplementary material associated with this article can be found, in the online version, at doi:10.1016/j.cclet.2026.112411.


    1. [1]

      J.L. Carrillo, A.A. Ezazi, S. Perez-Beltran, et al., Chem 111 (2025) 102486.

    2. [2]

      Y. Pan, R. Che, K. Lu, et al., Chem. Eng. J. 508 (2025) 161229. doi: 10.1016/j.cej.2025.161229

    3. [3]

      D. Jiang, R. Xu, L. Bai, et al., Coord. Chem. Rev. 516 (2024) 215923. doi: 10.1016/j.ccr.2024.215923

    4. [4]

      K. Chen, S.H. Mousavi, R. Singh, et al., Chem. Soc. Rev. 51 (2022) 1139–1166. doi: 10.1039/d1cs00822f

    5. [5]

      L. Men, H. Lin, L. Zhu, et al., ACS Sust. Chem. Eng. 12 (2024) 8780–8791. doi: 10.1021/acssuschemeng.4c01654

    6. [6]

      J. Lu, Z. Xiong, M. Sakil, et al., J. Hazard. Mater. 471 (2024) 134464. doi: 10.1016/j.jhazmat.2024.134464

    7. [7]

      J. Wang, S. Zhuang, Coord. Chem. Rev. 400 (2019) 213046. doi: 10.1016/j.ccr.2019.213046

    8. [8]

      L. Men, S. Feng, J. Zhang, et al., Green Chem. 26 (2024) 1170–1193. doi: 10.1039/d3gc04088g

    9. [9]

      M. Shi, K. Lu, H. Jia, et al., Sci. Total. Environ. 904 (2023) 167339. doi: 10.1016/j.scitotenv.2023.167339

    10. [10]

      V. Pavlenko, S. Żółtowska, A. Haruna, et al., Mat. Sci. Eng. R 149 (2022) 100682. doi: 10.1016/j.mser.2022.100682

    11. [11]

      H. Qiang, M. Shi, Y. Pan, et al., Sep. Purif. Technol. 361 (2025) 131294. doi: 10.1016/j.seppur.2024.131294

    12. [12]

      D. Barker, J. Chen, Z. Wan, et al., Chem. Soc. Rev. 54 (2025) 623–652. doi: 10.1039/D4CS00923A

    13. [13]

      I. Alali, A. Shehu, R. Mokaya, et al., Energy. Environ. Sci. 17 (2024) 5024–5038. doi: 10.1039/d4ee00749b

    14. [14]

      H. Qiang, M. Shi, K. Lu, et al., Desalination 593 (2025) 118246. doi: 10.1016/j.desal.2024.118246

    15. [15]

      Z. Yu, B. Qin, Z.Y. Ma, et al., Adv. Mater. 31 (2019) 1900651. doi: 10.1002/adma.201900651

    16. [16]

      H. Wang, Y. Shao, S. Mei, et al., Chem. Rev. 120 (2020) 9363–9419. doi: 10.1021/acs.chemrev.0c00080

    17. [17]

      R. Ding, Y. Zhou, Y. Zhang, et al., Adv. Funct. Mater. 35 (2025) 2415006. doi: 10.1002/adfm.202415006

    18. [18]

      M. Mudassir, S. Kousar, M. Ehsan, et al., Renew. Sust. Energy Rev. 185 (2023) 113594. doi: 10.1016/j.rser.2023.113594

    19. [19]

      R. Chakraborty, K. Vilya, M. Pradhan, et al., J. Mater. Chem. A 10 (2022) 6965–7005. doi: 10.1039/d1ta10269a

    20. [20]

      L. Men, B. Luo, L. Zhu, et al., Chem. Eng. J. 513 (2025) 163013. doi: 10.1016/j.cej.2025.163013

    21. [21]

      C. Yang, Y. Wang, M. Liang, et al., Appl. Catal. B: Environ. 323 (2023) 122133. doi: 10.1016/j.apcatb.2022.122133

    22. [22]

      B. Xue, C. Liu, X. Wang, et al., Chem. Eng. J. 480 (2024) 147994. doi: 10.1016/j.cej.2023.147994

    23. [23]

      D. Wang, H. Dong, D. Zhang, et al., Int. J. Biol. Macromol. 305 (2025) 141361. doi: 10.1016/j.ijbiomac.2025.141361

    24. [24]

      H. Qiang, M. Shi, F. Wang, et al., Sep. Purif. Technol. 333 (2024) 125915. doi: 10.1016/j.seppur.2023.125915

    25. [25]

      H. Arslanoğlu, J. Hazard. Mater. 374 (2019) 238–247. doi: 10.1016/j.jhazmat.2019.04.042

    26. [26]

      L. Hao, J. Wen, Z. Yun, et al., Carbon 128 (2018) 97–105. doi: 10.1016/j.carbon.2017.11.058

    27. [27]

      P. Li, P. Liu, H. Liu, et al., J. Energy Storage 121 (2025) 116349. doi: 10.1016/j.est.2025.116349

    28. [28]

      B. Yang, J. Chen, S. Lei, et al., Adv. Energy Mater. 8 (2018) 1702409. doi: 10.1002/aenm.201702409

    29. [29]

      X. Wu, J. Liu, Y. Wang, et al., Chem. Eng. J. 512 (2025) 162487. doi: 10.1016/j.cej.2025.162487

    30. [30]

      Y. Yao, Y. Yu, Y. Liu, et al., J. Energy. Storage. 74 (2023) 109261. doi: 10.1016/j.est.2023.109261

    31. [31]

      S. Yu, N. Sun, L. Hu, et al., J. Power Sources 405 (2018) 132–141. doi: 10.1016/j.jpowsour.2018.10.033

    32. [32]

      M. Shi, K. Lu, X. Hong, et al., Chem. Eng. J. 471 (2023) 144465. doi: 10.1016/j.cej.2023.144465

    33. [33]

      L. Hou, W. Yang, B. Jiang, et al., Carbon 183 (2021) 176–186. doi: 10.1016/j.carbon.2021.06.072

    34. [34]

      M. Sevilla, ACS Nano 8 (2014) 5069–5078. doi: 10.1021/nn501124h

    35. [35]

      M. Shi, X. Hong, C. Liu, et al., Chem. Eng. J. 453 (2023) 139764. doi: 10.1016/j.cej.2022.139764

    36. [36]

      Y. Wang, Y. Liu, X. Huang, et al., Chin. Chem. Lett. 35 (2024) 109301. doi: 10.1016/j.cclet.2023.109301

    37. [37]

      S. Tian, J. Dai, Y. Jiang, et al., J. Colloid. Interf. Sci. 505 (2017) 858–869. doi: 10.1016/j.jcis.2017.06.062

    38. [38]

      M. Shi, H. Jia, J. Liu, et al., Coordin. Chem. Rev. 543 (2025) 216949. doi: 10.1016/j.ccr.2025.216949

    39. [39]

      B. Qi, J. Wang, H. Sun, et al., Sep. Purif. Technol. 382 (2025) 136012.

    40. [40]

      X. Shi, C. Zhou, Y. Gao, et al., Carbon Energy 6 (2024) 534. doi: 10.1002/cey2.534

    41. [41]

      X. Wu, B. Ding, C. Zhang, et al., Carbon 153 (2019) 225–233. doi: 10.1016/j.carbon.2019.07.020

    42. [42]

      Y. Feng, G. Li, X. Wu, et al., J. Porous Mater. 30 (2023) 2113–2120. doi: 10.1007/s10934-023-01487-3

    43. [43]

      G. Singh, I. Ismail, C. Bilen, et al., Appl. Energy 255 (2019) 113831. doi: 10.1016/j.apenergy.2019.113831

    44. [44]

      H. Liao, L. Zhong, H. Zeng, et al., Carbon 213 (2023) 118305. doi: 10.1016/j.carbon.2023.118305

    45. [45]

      M. Xia, W. Chen, J. Wu, et al., Fuel 291 (2021) 120185. doi: 10.1016/j.fuel.2021.120185

    46. [46]

      W. Yue, Z. Yu, X. Zhang, et al., J. Anal. Appl. Pyrolysis 178 (2024) 106409. doi: 10.1016/j.jaap.2024.106409

    47. [47]

      W. Hui, F. Mao, W. Xiang, et al., Compos. Commun. 28 (2021) 100961. doi: 10.1016/j.coco.2021.100961

    48. [48]

      Y. Shi, J. Zhu, G. Yuan, et al., Chem. Eng. J. 386 (2020) 124009. doi: 10.1016/j.cej.2019.124009

    49. [49]

      S. Sun, B. Ding, R. Liu, et al., J. Alloys Compd. 803 (2019) 401–406. doi: 10.1016/j.jallcom.2019.06.212

    50. [50]

      T. Lu, J. Bai, M. Demir, Sep. Purif. Technol. 296 (2022) 121368. doi: 10.1016/j.seppur.2022.121368

    51. [51]

      G. Tan, X. Li, D. Xiao, New J. Chem. 44 (2020) 4071–4080. doi: 10.1039/c9nj06154a

    52. [52]

      Y. Chen, Y. Zhu, M. Tian, et al., Nano Energy 59 (2019) 346–353. doi: 10.1016/j.nanoen.2019.02.055

    53. [53]

      M. Taha, S. Anwar, M. Ramadan, et al., Desalination 511 (2021) 115099. doi: 10.1016/j.desal.2021.115099

    54. [54]

      G. Tan, Q. Liu, X. Li, et al., Appl. Surf. Sci. 496 (2019) 143526. doi: 10.1016/j.apsusc.2019.07.268

    55. [55]

      S. Song, Y. Wang, P. Tian, et al., Int. J. Hydrogen. Energy 47 (2022) 24728–24737. doi: 10.1016/j.ijhydene.2022.05.218

    56. [56]

      M. Jafari, G. Botte, ACS Omega 9 (2024) 13134–13147.

    57. [57]

      W. Yang, W. Yang, F. Ding, et al., Carbon 111 (2017) 419–427. doi: 10.1016/j.carbon.2016.10.025

    58. [58]

      J. Liu, X. Mei, F. Peng, et al., Chin. Chem. Lett. 34 (2023) 108187. doi: 10.1016/j.cclet.2023.108187

    59. [59]

      S. Kang, D. Wang, M. Ma, et al., Bioresource. Technol. 442 (2026) 133695. doi: 10.1016/j.biortech.2025.133695

    60. [60]

      R. Sun, Y. Chen, X. Gao, et al., J. Energy. Storage 91 (2024) 112025. doi: 10.1016/j.est.2024.112025

    61. [61]

      S. Liu, S. Wu, H. Cheng, et al., Ind. Crops Prod. 179 (2022) 114657. doi: 10.1016/j.indcrop.2022.114657

    62. [62]

      M. Shi, X. Liu, H. Jia, et al., Sep. Purif. Technol. 330 (2024) 125354. doi: 10.1016/j.seppur.2023.125354

    63. [63]

      K. Lu, H. Jing, H. Jia, et al., J. Colloid. Interf. Sci. 679 (2024) 262–272. doi: 10.56028/aetr.12.1.262.2024

    64. [64]

      J. Zhu, D. Xu, W. Qian, et al., Small 12 (2016) 1935–1944. doi: 10.1002/smll.201600010

    65. [65]

      Z. Wang, C. Liu, O. Jia, et al., Ind. Crop. Prod. 227 (2015) 120808.

    66. [66]

      W. Qian, J. Zhu, Y. Zhang, et al., Small 11 (2015) 4959–4969. doi: 10.1002/smll.201500859

    67. [67]

      N. Sun, X. Zhang, C. Zhao, et al., ChemElectroChem 5 (2018) 3873–3880. doi: 10.1002/celc.201801063

    68. [68]

      G. Duan, L. Zhao, C. Zhang, et al., Diamond. Relat. Mater. 129 (2022) 109339. doi: 10.1016/j.diamond.2022.109339

    69. [69]

      G. Duan, J. Xiao, L. Chen, et al., J. Energy. Storage. 67 (2023) 107559. doi: 10.1016/j.est.2023.107559

    70. [70]

      Y. Gao, S. Zhang, X. Li, et al., Carbon 181 (2021) 323–334. doi: 10.1016/j.carbon.2021.05.039

    71. [71]

      Y. Zhang, G. Ji, C. Li, et al., Chem. Eng. J. 390 (2020) 124398. doi: 10.1016/j.cej.2020.124398

    72. [72]

      L. Wan, P. Song, J. Liu, et al., J. Power. Sources 438 (2019) 227013. doi: 10.1016/j.jpowsour.2019.227013

    73. [73]

      P. Nie, X. Shang, B. Hu, et al., J. Colloid. Interf. Sci. 612 (2022) 277–286. doi: 10.1016/j.jcis.2021.12.156

    74. [74]

      J. Shi, J. Xu, H. Cui, et al., Sep. Purif. Technol. 355 (2025) 129756. doi: 10.1016/j.seppur.2024.129756

    75. [75]

      S. Gu, Y. Wang, D. Zhang, et al., Chemosphere 289 (2022) 133148. doi: 10.1016/j.chemosphere.2021.133148

    76. [76]

      S. Zhe, L. Xiong, W. Hao, et al., J. Energy. Storage 515 (2021) 230629.

    77. [77]

      L. Hu, L. Ma, Q. Zhu, et al., New J. Chem. 22 (2017) 13185–14002.

    78. [78]

      Z. Hui, Z. Yi, L. Qing, et al., Appl. Energy. 306 (2021) 118131.

    79. [79]

      T. Sun, C. Wang, D. Jiao, et al., J. Mater. Sci.: Mater. Electron. 28 (2017) 8993–9002. doi: 10.1007/s10854-017-6630-2

    80. [80]

      J. Zhu, D. Xu, C. Wang, et al., Carbon 115 (2017) 1–10.

    81. [81]

      D. Cheng, M. Tian, B. Wang, et al., J. Colloid. Interf. Sci. 572 (2020) 216–226. doi: 10.15767/feministstudies.46.1.0216

    82. [82]

      H. Qiang, M. Shi, F. Wang, et al., Sep. Purif. Technol. 308 (2023) 122918. doi: 10.1016/j.seppur.2022.122918

    83. [83]

      X. Yu, J. Zhao, R. Lv, et al., J. Mater. Chem. A 36 (2015) 18313–18736.

    84. [84]

      X. Zhao, H. Chen, F. Kong, et al., Chem. Eng. J. 364 (2019) 226–243. doi: 10.1016/j.cej.2019.01.159

    85. [85]

      Z. Chen, C. Feng, W. Li, et al., Chin. J. Catal. 39 (2018) 841–848. doi: 10.1016/S1872-2067(17)62972-3

    86. [86]

      S. Chongdar, R. Chatterjee, S. Reza, et al., Adv. Energy. Mater. 15 (2024) 2403809.

    87. [87]

      R. Ding, F. Zeng, H. Zhao, et al., Compos. Part. B 288 (2024) 111932.

    88. [88]

      J. Pang, W. Zhang, H. Zhang, et al., Carbon 132 (2018) 280–293. doi: 10.1016/j.carbon.2018.02.077

    89. [89]

      H. Zhao, P. Lu, F. Chen, et al., Chin. Chem. Lett. 35 (2024) 108694. doi: 10.1016/j.cclet.2023.108694

    90. [90]

      Y. He, D. Gehrig, F. Zhang, et al., Adv. Funct. Mater. 26 (2016) 8255–8265. doi: 10.1002/adfm.201603693

    91. [91]

      L. Yao, B. Zhan, X. Qi, et al., J. Mater. Sci. Technol. 224 (2024) 56–65. doi: 10.1111/cge.14510

    92. [92]

      Y. Zhao, X. Zuo, Y. Guo, et al., Nano. Micro. Lett. 13 (2021) 144. doi: 10.1007/s40820-021-00667-7

    93. [93]

      W. Zhang, H. Li, D. Feng, et al., Carbon Energy 6 (2024) 461. doi: 10.1002/cey2.461

    94. [94]

      G. Liu, X. Li, M. Liu, et al., SusMat 3 (2023) 834–842. doi: 10.1002/sus2.167

    95. [95]

      X. Chen, L. Xu, L. Zeng, et al., Dalton Trans 41 (2020) 14299–14708.

    96. [96]

      Z. Hang, G. Xiao, C. Shuo, et al., Sep. Purif. Technol. 292 (2022) 121048. doi: 10.1016/j.seppur.2022.121048

    97. [97]

      J. Earnshaw, A. Ashok, K. Leong, et al., Small 21 (2024) 2406174.

    98. [98]

      C. Li, E. Zhou, Z. Yu, et al., Appl. Catal. B: Environ. 269 (2020) 118771. doi: 10.1016/j.apcatb.2020.118771

    99. [99]

      W. Eom, A. Kim, H. Park, et al., Adv. Funct. Mater. 26 (2016) 7605–7613. doi: 10.1002/adfm.201602320

    100. [100]

      C. Zhao, L. Shan, R. Sun, et al., Mater. Today 81 (2024) 104–117. doi: 10.1016/j.mattod.2024.11.002

    101. [101]

      L. Dong, J. Yang, M. Chhowalla, et al., Chem. Soc. Rev. 46 (2017) 7097–7472. doi: 10.1039/C7CS90122D

    102. [102]

      M.J. Yoo, H.B. Park, Carbon 141 (2019) 515–522. doi: 10.1016/j.carbon.2018.10.009

    103. [103]

      Y. Zhang, Z. Wang, D. Li, et al., J. Mater. Chem. A 8 (2020) 22874–22885. doi: 10.1039/d0ta08577d

    104. [104]

      L. Chen, J. Sun, J. Dai, et al., J. Taiwan Inst. Chem. Eng. 95 (2018) 660–668.

    105. [105]

      Q. Luo, Q. Chen, Y. Wang, et al., Chem. Eng. J. 420 (2021) 130483. doi: 10.1016/j.cej.2021.130483

    106. [106]

      L. Hou, W. Yang, Y. Li, et al., Chem. Eng. J. 417 (2021) 129289. doi: 10.1016/j.cej.2021.129289

    107. [107]

      F. Li, J. Jiang, J. Wang, et al., Nano Res 16 (2022) 127–145.

    108. [108]

      B. Xue, J. Xu, Y. Feng, et al., J. Colloid. Interf. Sci. 642 (2023) 736–746. doi: 10.1016/j.jcis.2023.03.200

    109. [109]

      M. Zhang, H. Ling, T. Wang, et al., Nano-Micro Lett. 14 (2022) 157. doi: 10.1007/s40820-022-00900-x

    110. [110]

      Q. Wang, Y. Qu, Y. Yuan, et al., Adv. Mater. 37 (2025) 2418997. doi: 10.1002/adma.202418997

    111. [111]

      Z. Zhao, S. Das, G. Xing, et al., Angew. Chem. Int. Ed. 57 (2018) 11952–11956. doi: 10.1002/anie.201805924

    112. [112]

      T. Wang, L. Peng, B. Deng, et al., Fuel 357 (2024) 129653. doi: 10.1016/j.fuel.2023.129653

    113. [113]

      X. Zhu, Y. Gao, Q. Yue, et al., J. Taiwan Inst. Chem. Eng. 85 (2018) 141–148. doi: 10.1016/j.jtice.2018.01.025

    114. [114]

      H. Jia, H. Xu, M. Shi, et al., J. Colloid. Interf. Sci. 650 (2023) 1152–1163. doi: 10.1016/j.jcis.2023.07.050

    115. [115]

      H. Jia, H. Xu, M. Shi, et al., Sep. Purif. Technol. 325 (2023) 124652. doi: 10.1016/j.seppur.2023.124652

    116. [116]

      G. Tan, X. Li, D. Xiao, et al., New J. Chem. 44 (2020) 4071–4080. doi: 10.1039/c9nj06154a

    117. [117]

      J. Qin, R. Ji, Q. Sun, et al., Bioresour. Technol. 369 (2022) 128361.

    118. [118]

      G. Singh, R. Bahadur, A.M. Ruban, et al., Green Chem. 23 (2021) 5571–5583. doi: 10.1039/d1gc01376a

    119. [119]

      Q. Zhu, F. Li, Y. Zheng, et al., Sep. Purif. Technol. 284 (2022) 120272. doi: 10.1016/j.seppur.2021.120272

    120. [120]

      Q. Ma, Z. Wang, L. Zhang, et al., Sep. Purif. Technol. 353 (2025) 128503. doi: 10.1016/j.seppur.2024.128503

    121. [121]

      B. Xiao, L. Zhang, Q. Ma, et al., Desalination 612 (2025) 118955. doi: 10.1016/j.desal.2025.118955

    122. [122]

      Z. Guo, G. Shen, Z. Wang, et al., Desalination 576 (2024) 117329. doi: 10.1016/j.desal.2024.117329

    123. [123]

      Y. Liu, L. Wang, Q. Ma, et al., Nat. Commun. 15 (2024) 10175. doi: 10.1021/acs.jpcc.4c01409

    124. [124]

      X. Wang, Z. Li, R. Gao, et al., Environ. Sci. Technol. 58 (2024) 17190–17200.

    125. [125]

      Y. Chai, F. Wang, Y. Gao, et al., Environ. Res. 282 (2025) 122099. doi: 10.1016/j.envres.2025.122099

    126. [126]

      B. Hua, L. Zheng, A. Awomuti, et al., Chem. Eng. J. 443 (2022) 136439. doi: 10.1016/j.cej.2022.136439

    127. [127]

      A. Pophali, K. Lee, L. Zhang, et al., Chem. Eng. J. 373 (2019) 365–374. doi: 10.1016/j.cej.2019.05.029

    128. [128]

      Y. Liu, X. Niu, X. Yang, et al., Chem. Eng. J. 489 (2024) 151417. doi: 10.1016/j.cej.2024.151417

    129. [129]

      G. Jin, Y. Ping, C. Yi, et al., Chin. Chem. Lett. 33 (2022) 4792–4797. doi: 10.1016/j.cclet.2022.01.029

    130. [130]

      H. Lv, Y. Huo, M. Cheng, et al., Chemosphere 335 (2023) 139020. doi: 10.1016/j.chemosphere.2023.139020

    131. [131]

      S.O. Ganiyu, M. de Araújo, E. Costa, et al., Appl. Catal. B: Environ. 283 (2020) 119652.

    132. [132]

      S. Zheng, Z. Yuan, D. Dionysiou, et al., Chem. Eng. J. 458 (2023) 141471. doi: 10.1016/j.cej.2023.141471

    133. [133]

      G. Zhu, X. Fan, Y. Yu, et al., Environ. Sci. Technol. 58 (2024) 19093–19570. doi: 10.1021/acs.est.4c07737

    134. [134]

      J. Chen, W. Ren, S. Zhong, et al., Chem. Eng. J. 500 (2024) 157125. doi: 10.1016/j.cej.2024.157125

    135. [135]

      C. Chen, M. Tian, H. Han, et al., Electrochim. Acta 389 (2021) 138732. doi: 10.1016/j.electacta.2021.138732

    136. [136]

      M. Tian, Y. Zhu, Y. Chen, et al., Nano Energy 83 (2021) 105825. doi: 10.1016/j.nanoen.2021.105825

    137. [137]

      Z. Wang, X. Liu, G. Zhang, et al., Ceram. Int. 49 (2023) 35885–35897. doi: 10.1016/j.ceramint.2023.08.269

    138. [138]

      R. Ding, Y.Q. Wang, F. Zeng, et al., Small 19 (2023) 2302132. doi: 10.1002/smll.202302132

    139. [139]

      S. Sharma, S. Parne, S. Panda, et al., Adv. Colloid. Interf. Sci. 327 (2024) 103143. doi: 10.1016/j.cis.2024.103143

    140. [140]

      X. Shen, K. Ran, B. Zheng, et al., Inorg. Chem. Commun. 153 (2023) 110863. doi: 10.1016/j.inoche.2023.110863

    141. [141]

      H. Liqiang, Y. Wang, J. Bo, et al., Carbon 183 (2021) 176–186. doi: 10.1016/j.carbon.2021.06.072

  • Figure 1  Schematic illustration of emerging OAPCs: Activation/self-activation fabrication, dimensional control and environmental applications.

    Figure 2  (a) N2 adsorption-desorption curves and (b) pore size distribution of PCPCs-x. Reprinted with permission [37]. Copyright 2017, Elsevier. (c) Schematic illustration of the fabrication process of NSHPC. (d) N2 adsorption-desorption isotherms, (e) SEM and (f) TEM images of NSHPC. Reprinted with permission [41]. Copyright 2021, Elsevier. (g) Specific capacitance of PC-700 and APC-X. Reprinted with permission [42]. Copyright 2021, Elsevier. (h) The fabrication route and (i) SEM images of NOS-AC. Reprinted with permission [46]. Copyright 2024, Elsevier. (j) Diluted CO2 uptake isotherms of PGNC at 25 ℃. Reprinted with permission [47]. Copyright 2021, Elsevier.

    Figure 3  (a) Schematic of the fabrication process of PC-X and the CDI tests. (b) SEM images of PC-750. (c) N2 adsorption-desorption isotherms of PC-X. Reprinted with permission [54]. Copyright 2019, Elsevier. (d) Schematic of the preparation process and (e) N2 adsorption-desorption isotherms of Fe/Mn–NIHPC. Reprinted with permission [55]. Copyright 2022, Elsevier. (f) Schematic of the fabrication process of 3D framework carbon (3DFC). (g) SEM and (h) TEM images of 3DFAC. (i) Distance dependence of adsorption energy between Na atom and graphene layers. Reprinted with permission [28]. Copyright 2017, Wiley.

    Figure 4  (a) SEM images and (b) N2 adsorption-desorption isotherms of NC800. Reprinted with permission [48]. Copyright 2020, Elsevier. (c) Schematic illustration of the preparation process and (e) TEM images of Defect/O modified-C. (d) The interlayer space and intercalated energy of K+ on diverse GO configurations of pure carbon. Reprinted with permission [70]. Copyright 2021, Elsevier. (f) Schematic illustration of the preparation of HPC-700. (g) N2 adsorption-desorption isotherms of AC and HPC-X. (h) Cations’ selective adsorption ability of HPC-700. Reprinted with permission [73]. Copyright 2022, Elsevier. (i) Schematic illustration of the preparation process of MNCs. Reprinted with permission [74]. Copyright 2025, Elsevier.

    Figure 5  Physicochemical properties of different sustainable OAPCs.

    Figure 6  (a) Schematic illustration of the preparation process of HPCS-X-Y (inset: SEM images). (b) CH2Cl2 adsorption capacity and time of HPCS-X-Y. Reprinted with permission [58]. Copyright 2022, Elsevier. (c) SEM images of HPCS-900. (d) N2 adsorption-desorption isotherms of HPCS-X. Reprinted with permission [88]. Copyright 2018, Elsevier. (e, f) SEM images of HNPCPA. (g) N2 adsorption-desorption isotherms and (h) XPS spectra of diverse OAPCs. Reprinted with permission [89]. Copyright 2023, Elsevier. (i) Scheme of the fabrication process and (j) TEM images of Se-HPCF. Reprinted with permission [95]. Copyright 2020, RSC. (k) SEM images of 1D CFM. Reprinted with permission [96]. Copyright 2022, MDPI.

    Figure 7  (a) Schematic illustration of the preparation process and (b) N2 adsorption-desorption isotherms of PC-650 and PC-750. Reprinted with permission [116]. Copyright 2020, RSC. (c) N2 adsorption-desorption isotherms and (d) comparison of the adsorption ability of SMX with reported sorbents. (e) Adsorption mechanism of SMX on PC/PB. Reprinted with permission [117]. Copyright 2023, Elsevier. (f) Schematic illustration of the preparation craft of CPCs. (g) SEM images of CPC-3. (h) CO2 capture capacity of CPC-3 at 0, 10 and 25 ℃. Reprinted with permission [118]. Copyright 2021, RSC. (i) Schematic illustration of the preparation craft of DT-NPC-xs. (j) N 1s spectra and (k) SEM images of DT-NPC-5. IAST selectivities for (l) SO2/N2 and (m) SO2/CO2 at 25 ℃ and 100 kPa. Reprinted with permission [119]. Copyright 2022, Elsevier.

    Figure 8  (a) Scheme of the manufacture process and (b) N2 adsorption-desorption isotherms of 3DPC-X. (c) The change trend of k and the SBET along with the increased carbonization temperature. Reprinted with permission [96]. Copyright 2022, Elsevier. (d) Influence of Zn1Co5/P4C dosage on the degradation efficiency. Reprinted with permission [130]. Copyright 2023, Elsevier. (e) SEM images of MEP-2. (f) The curves of dependence of pyrrolic-N and P-C (%) on the ORR potential and degradation efficiency. Reprinted with permission [135]. Copyright 2023, Elsevier. (g) UV−vis spectra of degradation of MB driven by DLRD-TENG systems. Reprinted with permission [52]. Copyright 2019, Elsevier. (h) Schematic illustration of the formation mechanism for ZGD-x. (i) The influence of indicators on the EF degradation efficiencies for MG and MB. Reprinted with permission [136]. Copyright 2021, Elsevier.

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  • 发布日期:  2026-09-15
  • 收稿日期:  2025-05-27
  • 接受日期:  2026-01-12
  • 修回日期:  2025-12-09
  • 网络出版日期:  2026-01-14
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