Open Access Article
Suneel Kumar Srivastava
Department of Chemistry, Indian Institute of Technology, Kharagpur-721302, India. E-mail: suneel@chem.iitkgp.ac.in; suneelchemkgp@gmail.com
First published on 4th November 2025
In recent years, considerable attention has been paid to hollow micro–nano-structured intrinsically conducting polymers (ICPs), like polyaniline, polypyrrole, polythiophene and poly(3,4-ethylenedioxythiophene). The availability of the shells and inner voids in the hollow ICP accounts for their tunable physical/chemical properties, offers low density, a high surface area, reduced length for both mass and charge transport, and offers promising applications in environmental remediation and energy. In view of this, the present review article is focused on the synthesis methods used in the fabrication of hollow intrinsically conducting polymers by means of hard and soft template approaches including template-free methods, synthesis of double-shelled hollow spheres of ICP, hollow ICP nanocomposites and core–shell structural materials of ICP. Subsequently, the review highlights the application of the hollow intrinsically conducting polymers, their nanocomposites and core–shell structured materials for applications in electromagnetic interference shielding/microwave absorption, removal of heavy metal ions and different dyes from wastewater, and as efficient electrode materials in supercapacitors. Finally, the review ends with a summary and future perspective on hollow-structured and core–shell conducting polymers and their applications in the above fields of application.
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| Fig. 1 Hollow and core–shell intrinsically conducting polymers (ICPs) and their applications (Inset: structures of common ICPs.2 Reproduced with permission from Elsevier). | ||
The physical properties of PANI, PPy, PTH and PEDOT are influenced by their morphology.16 In this regard, PANI, compared with other ICPs, has been studied extensively for various reasons to date considering different morphologies, such as granular structure,17 nanoparticles,17 spongy,18 dendrite,19 nano-neddles,20 nanocables,21 nanotubes,21,22 nanofiber,23 nanowire,24 nanobelts,25 nanorods,26 nanostick,27 nanoflakes,28 microspheres,29 nanocapsules,30 flower-like nanosheet clusters,31 coral-like,32 honeycomb,33 worm-like interlinked structures,34 tetragonal star like,35 nanospheres36 etc. Polypyrrole, polythiophene and PEDOT also exist in many of these morphologies. It is well established that manipulation of the morphology can lead to enhancement of the physicochemical properties and the performance of conducting polymers.37,38 In this regard, ‘hollow structure’ ICPs with void space inside a distinct shell and dimensions in the micrometer-/nanometer range have been receiving a considerable amount of attention in recent years.39–50 The synthesis of such hollow materials with a single or double shells of various compositions and morphologies has been reported following hard-templating, soft-templating and template-free methods.49
Hollow structures can be of different shapes, as schematically illustrated in Fig. 2.41 From this perspective, hollow spheres are considered to be more advantageous than their corresponding solid counterparts due to the presence of a large fraction of empty space inside and intact shell(s).50 The interior geometry, surface functionality, high specific surface area, and high conductivity, as well as the controllable chemical and physical properties of the hollow ICP nanostructures make them the most promising candidates in several of the applications stated earlier.6,51 In addition, much attention has also been paid to nanotubes, characterized by their unique hollow tubular structure.52 Furthermore, the introduction of nanomaterial(s) into these conducting polymers can introduce unique properties such as high surface area, high electrical conductivity and other features that could enhance their performance in multifaceted applications.49–53
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| Fig. 2 Schematic illustration showing various hollow structures: (left) hollow spheres/boxes/tubes; (middle) multi-shelled hollow spheres/boxes/tubes; (right) yolk–shell, cube-in-box, and wire-in-tube structures.41 Reproduced with permission from ACS. | ||
The microwave (MW) radiation emitted from various electrical and electronic devices adversely degrades their performance9,54 and is very harmful to human health.55 Therefore, electromagnetic interference (EMI) shielding and microwave absorption materials are essentially needed for mitigating such electromagnetic pollution.56–59 In this context, hollow conducting polymers combined with fillers (such as magnetic nanoparticles) can also facilitate enhanced EMI shielding and microwave absorption due to the dielectric loss owing to the intrinsic conductivity from the polymer and magnetic loss arising from the magnetic filler, respectively. The unique hollow morphology of conducting polymers with increased surface area prevents secondary electromagnetic pollution due to reflection. Furthermore, the presence of multiple internal reflections and the trapping of EM waves contribute to their excellent performance in EMI shielding and microwave absorption. It may be noted that hollow ICPs can interact with EM waves and convert the energy of the microwaves into heat and dissipate it.9 In addition, hollow PANI and PPy have been extensively studied as adsorbents in the removal of heavy metals and dyes in water.60–64 The excellent adsorption performance of hollow conducting polymers in the removal of metals and dyes is ascribed to their large specific surface area and its tunable surface properties. The available functional binding sites in the conducting polymers readily interact with pollutants through various mechanisms, accounting for their effectiveness as adsorbents. Recently, hollow ICPs have also been used in supercapacitor applications due to their low cost and properties.7 It may be noted that the unique hollow spherical morphology of ICPs accounts for their larger surface area, significantly lower density, and high loading capacity, and shorter ion diffusion paths facilitate achieving high-power density, fast charge and discharge rates, and long cycle life.65 In addition, hollow conducting polymers also improve cycling stability by allowing for controlled volume changes during redox reactions.53
In recent years, core–shell-structured materials formed by the judicious tuning of the core as well as the shell(s) have received considerable attention due to their applications in a variety of fields.66–68 In this regard, core–shell materials exhibiting enhanced magnetic and dielectric loss have the ability to perform well in electromagnetic interference shielding and microwave absorption.67,69 In addition, impedance matching in the core–shell materials creates numerous interfaces for multiple reflections and facilitates attenuation of microwaves due to multiple reflections.9 Core–shell materials formed by combining a functional conducting polymer shell with a stable core are also receiving more attention as adsorbents for the removal of pollutants in water.68 The choice is mainly guided by the unique properties of both the core and the shell in achieving high adsorption capacity, separation efficiency, and reusability compared with conductive polymers exhibiting low solubility, limited active sites, poor mechanical strength, and separation difficulties. Most importantly, a magnetic core can facilitate the complete separation of the core–shell adsorbents from water by applying an additional magnetic field.70,71 The core–shell approach has also been used in fabricating ICP-based electrode materials with excellent electrochemical performance in supercapacitor applications.7 This attractive choice is motivated by the synergistic combination of the core and shell materials leading to a high specific surface area for abundant reaction sites, mechanical stability, good electrical conductivity for fast charge transfer, faster diffusion kinetics, high specific capacitance, and longer cyclability.72,73
In view of this, several review articles have appeared in recent years on intrinsically conducting polymers focused on the electromagnetic interference shielding and microwave absorption,2,9,54,74–80 removal of heavy metal ions60–64,81–85 and organic dyes60–64,86–91 in wastewater, and supercapacitors,7,65,72,73,92–98 and several others are also referred to in subsequent sections. However, considering the rapid developments, there exists a lack of a comprehensive review highlighting the novel contribution of hollow and core–shell intrinsically conducting polymers with their applications in mitigating electronic/environmental pollution and their applications in energy storage.
Motivated by this, the present review aims to highlight the novel contribution made by intrinsically conducting polymers in this regard by focusing exclusively on hollow and core–shell morphologies across three distinct application fields (EMI shielding, adsorption, supercapacitors). Accordingly, the present article is focused on the preparation of hollow intrinsically conducting polymers (PANI, PPy, PTP, PEDOT) and core–shell materials comprising ICP through different approaches. This is followed by their applications in electromagnetic interference shielding/microwave absorption, removal of heavy metal ions/dyes in water, and supercapacitors (Fig. 1). Finally, the review article ends with a future perspective and summary. Overall, the fabrication of the unique hollow and core–shell morphology of important intrinsically conducting polymers and the role they play in the multifaceted applications reviewed in this article clearly complements the existing literature.
The electrical properties of conducting polymers are modified by p- and n-type doping.105 The delocalization of the charge carriers over the polymer chain accounts for their electronic conductivity.102 Generally, the negatively charged carriers in n-doping are not as stable as positively charged ones. This makes p-type doping more attractive in academic research as well as for all practical application purposes.102,108,109 Fig. 3(a) describes the electronic and chemical structures of polythiophene as a representative conducting polymer subjected to p-type doping and n-type doping.102 The electronic bands and chemical structures illustrating undoped, polaron, bipolaron and fully doped states of polypyrrole are also described in Fig. 3(b).102
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| Fig. 3 (A) The electronic band and chemical structures of polythiophene (PTh) with (a) p-type doping and (b) n-type doping, and (B) electronic bands and chemical structures illustrating (a) undoped; (b) polaron; (c) bipolaron; and (d) fully doped states of polypyrrole.102 Reproduced with permission from MDPI. | ||
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| Fig. 4 Chemical polymerization mechanisms of polyaniline. Chemical polymerization of polyaniline is carried out in acidic medium by using a common initiator such as ammonium persulfate and potassium persulfate.99 Reproduced with permission from ACS. | ||
The mechanism of pyrrole monomer polymerization has also received a considerable amount of attention.127–131 The most widely accepted polymerization mechanism of PPy is displayed in Fig. 5.127,128 The oxidation of a pyrrole monomer yields a radical cation of the monomer in the initiation step (Fig. 5A). Coupling of the two generated radical cations then deprotonation produces a bipyrrole.130 This bipyrrole in the propagation step is oxidized again and couples with another oxidized segment in the propagation step Fig. 5(B). Further continuation of the re-oxidation, coupling, and deprotonation ultimately leads to the formation of polypyrrole.
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| Fig. 5 The oxidation of a pyrrole monomer (A) and formation of dimer and trimer of pyrrole (B).128 Reproduced with permission from Elsevier. | ||
Another chemical oxidative polymerization mechanism has also been proposed. According to this, the radical cation in the propagation step of this mechanism reacts with a neutral monomer.131 The dimer formed in this manner is oxidized to a dimeric radical cation that subsequently attacks another neutral monomer to form a trimer (Fig. 6(A)),128 and polymer chains grow by the repeated process to ultimately form polypyrrole. Recently, Tan and Ghandi127 observed that a commonly used mechanism (Fig. 5B) for the polymerization of pyrrole is not well suited for the formation of PPy in aqueous medium. Instead, the polymerization mechanism of polypyrrole follows a different mechanism, as schematically shown in Fig. 6.128
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| Fig. 6 The formation of dimer and trimer of pyrrole (A) and further formation of the PPy (B).128 Reproduced with permission from Elsevier. | ||
Fig. 7 describes the electrochemical polymerization mechanisms of polyaniline carried out in the electrolyte solution of aniline and acid through application of a potential difference between the working and counter electrodes.99
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| Fig. 7 Electrochemical polarization mechanism of polyaniline (electro-polymerization is carried out in the electrolyte solution of aniline and acid through applying a potential difference between the working and counter electrode).99 Reproduced with permission from ACS. | ||
The properties of the conducting polymers are influenced by oxidant, monomer molar ratio, type of oxidizing agent, pH, polymerization temperature, time, concentration, electrolyte concentration, and degree of doping.162–165 The electrical conductivity of most conducting polymers increases with dopant concentration and becomes saturated at a high doping level.104 Temperature is another parameter playing a significant role in the synthesis of ICPs. The selection of solvent is also an important factor. Generally, the polymerization of PANI and PPy is reported using solvents like water, MeOH, THF, DMF, DMSO acetonitrile, propylene carbonate and sea water.41,166–168 However, aqueous medium as a solvent is most desirable due to its relatively low cost, ease of handling and nontoxicity.
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| Fig. 8 (a) Representative materials that can be used as templates.173 Reproduced with permission from Elsevier, and (b) schematic representation of the synthesis of materials using different types of templates.175 Reproduced with permission from RSC. | ||
However, the main challenge in the preparation of hollow morphology, such as spheres, using template methods lies in the availability of suitable templates of definite size/shape, surface property, and production availability, and their subsequent removal through chemical or thermal means as an additional step to produce a void space.176 In this regard, the hard template has great advantages, such as adjustable pore structure and morphology; nevertheless, the hard template method also has disadvantages.171 It usually requires a core surface modification to ensure successful coating of shell substances.173 Hollow structures can also be prepared by a soft template method as a viable option.175,176 Although the hard template has high reproducibility and stability, its separation may be troublesome and may damage the structure of the desired materials with hollow morphology.171 On the other hand, with the soft template it is easier to prepare nanomaterials of various sizes and shape due to the simplicity of the process involved, and its easy removal than the hard template.171 In addition, soft templates are sensitive to solution environments (pH, solvents, ionic strength etc.), thereby limiting the application of the soft-core template processes.177 The hollow morphology achieved by the hard template procedure is guided by its adjustable pore structure and morphology. As a result, several hollow nanostructures can be fabricated considering the availability of the wide range of such hard templates.178
Cheng et al.184 prepared highly uniform and ordered polypyrrole nanotube arrays with the help of porous anodic aluminium oxide following chemical oxidation polymerization for 2 hours. Functional polypyrrole nanotubes have been fabricated using the anodized aluminium oxide membrane as template in liquid phase polymerization conditions.185 In another method, Jang et al.186 adopted one-step vapour deposition polymerization to synthesize a highly uniform surface and tuneable wall thickness in polypyrrole nanotubes using anodic aluminium oxide template membranes soaked in ferric chloride aqueous solution.
Quasi-polyaniline hollow nanotubes (outer dia: 230 nm) were prepared by a dipping method based on the highly ordered porous anodic alumina membrane.187 Poly(3, 4-ethylenedioxythiophene) tosylate film was grown in confined anodized aluminium oxide (nanopores) transferred onto cleaned ITO glass substrates following the chemical polymerization of the mixture comprising the solution of EDOT, iron(III)-tosylate in butanol and pyridine.188 Liu et al.189 electrochemically synthesized PEDOT nanotube arrays in the cylindrical pores of an alumina template membrane using acetonitrile solution of 20 mM EDOT.
Fu et al.191 initially prepared silica nanoparticles with surface-grafted polymer of 4-vinylaniline (SiO2-g-PVAn) according to the scheme displayed in Fig. 9(a). Subsequent surface oxidative graft copolymerization of aniline using the aniline moieties of PVAn and deprotonation followed by exposure to HF produced hollow nanospheres of P(VAn-graft-PANI) (thickness of shell: ∼15–40 nm, core void dia: ∼25 nm). A mesoporous polyaniline hollow nanosphere with average diameter and thickness of 330 nm shell 78 nm, respectively, has been prepared using SiO2@resorcinol-formaldehyde/SiO2 as substrate followed by in situ polymerization of aniline on its surface and subsequent expulsion of the silica shell by dispersing it in HF at room temperature.192 Li et al.193 prepared Pt/PPy hollow hybrid microspheres by using NH2-functionized SiO2 as template decorated with H2PtCl6, Fig. 9(b). In another study, SiO2/polymethacrylic acid (PMAA) microspheres were used as templates to synthesize hollow polypyrrole microspheres (Fig. 9(c)).194
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| Fig. 9 (a) Preparation of conductive poly(4-vinylaniline-graft-polyaniline), or P(VAn-g-PANI), hollow nanospheres via surface-initiated atom transfer radical polymerization (ATRP) and oxidative graft copolymerization.191 Reproduced with permission from ACS. (b) The illustration of the formation of Pt/PPy hollow spheres.193 Reproduced with permission from Wiley. (c) Formation of SiO2/PMAA/PPy nanocomposite and PPy hollow spheres.194 Reproduced with permission from Wiley. (d) Schematic representation of the assembly of negatively charged gold nanoparticles on the surface of positively charged core–shell polypyrrole–polystyrene latex particles bearing surface-protonated N-propylamino groups.206 Reproduced with permission from ACS. | ||
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monomer
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oxidant ratio as 1
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1
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1.Mangeney et al.206 used polystyrene latex particles (dia: 1.33 μm) to prepare PPy-coated PS latex polystyrene bearing surface-protonated N-propyl amino functional groups in aqueous solution by copolymerization of pyrrole and N-aminated pyrrole (pyrrole-NH2) using FeCl3. Furthermore, the fabricated (PS-PPyNH2) particles were subsequently decorated with citrate-stabilized gold nanoparticles, as shown in Fig. 9(d). Uniform polyaniline thin shells and hollow capsules were fabricated using polyelectrolyte-coated microspheres as templates.207 Monodisperse hollow polyaniline nanospheres with controlled surface smoothness were synthesized by in situ polymerization of aniline monomers adsorbed on a carboxyl-functionalized polystyrene surface.208 In another study, Sung et al.209 synthesized submicron-size hollow PANI dicarboxylate salt to study the influences of alkyl chain length, functional group and stable dispersion on its electrorheological performance.
Polyaniline/Au composite hollow spheres were successfully synthesized using polystyrene/sulfonated polystyrene as the templates.210 The thickness of the PANI shell can be well controlled by adjusting the amount of aniline monomer. Fig. 10(a–d) shows the morphology of PANI (A: SEM; C: TEM) and PANI/Au (B: SEM; D: TEM) composite hollow spheres under specified preparative conditions. The possible formation of hollow PANI spheres and its Au composites are presented in Fig. 11. Gao et al.211 fabricated hollow polyaniline microspheres in the presence of Cu rings as template using H4SiW12O40 and ammonium persulfate as dopant and oxidant, respectively. Zhang and Liu212 synthesized hollow polyaniline nanoparticles via the chemical oxidative polymerization of aniline using γ-Fe2O3 nanoparticles as the reactive templates in the presence of hydrochloric acid. Their studies have shown that reacting temperature played a vital role in the formation of the hollow nanoparticles. Halloysite was used as a hard template to prepare polyaniline–polypyrrole binary composite nanotubes.213 Gao and coworkers214 demonstrated the fabrication of polyaniline nanotubes using the inner eggshell membrane as a template. Their investigations revealed the key role played by the pore size of the template in the formation of polyaniline nanotubes.
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| Fig. 10 SEM and TEM images of PANI (A: SEM; C: TEM) and PANI/Au (B: SEM; D: TEM) composite hollow spheres (Synthetic conditions: aniline, 1 mmol, APS, 1 mmol, concentration of PANI in the Au colloid, 1.0 mg mL−1).210 Reproduced with permission from ACS. | ||
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| Fig. 11 Scheme of the preparation of PANI and PANI/Au hollow spheres.210 Reproduced with permission from ACS. | ||
Zhu et al.215 reported the double surfactant-layer of polyvinylpyrroldine (PVP) and sodium dodecyl sulfate (SDS)-assisted oxidative polymerization using monodisperse metal oxides (CuO, Fe2O3, In2O3) as templates (Fig. 12(a)). Following this, hollow PANI nanocapsules were prepared by dissolving metal oxides in acid solution. The method has also been used to prepare nanocomposites of CuO/PANI, Fe2O3/PANI, In2O3/PANI and Fe2O3/Si O2/PANI. Further investigations revealed the formation of well-controlled core/shell metal oxides/PANI nanocomposites and PANI capsules. Hollow octahedral PANI nanocapsules have been fabricated using Cu2O (octahedral) as template in the presence of H3PO4.216,217 It may be noted that the removal of the Cu2O template is not required, compared with other conventional methods, due to its reaction with ammonium persulfate (oxidant) to form a soluble Cu2+ salt during the process of the polymerization. The synthesis of nanorings and flat hollow capsules of polyaniline was also reported via the chemical oxidative polymerization of aniline using VOPO4 2H2O nanoplates acting as oxidant and sacrificial template.218
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| Fig. 12 (a) Schematic illustration for the formation of well-controlled core/shell metal oxides/PANi nanocomposites and PANi capsules.215 Reproduced with permission from IOP. (b) The fabrication process of PPy-PS hybrid hollow spheres.225 Reproduced with permission from Elsevier. | ||
According to Qu and Shi,231 the direct electrochemical oxidation of pyrrole in an aqueous solution of poly(styrene sulfonic acid) resulted in microstructures with hollow interiors comprising microspheres, microcrocks, microbowls, and micropumpkins. A stepwise electropolymerization process has been adopted in producing the nanostructured arrays of hollow polypyrrole with a conical shape.232 The pores of nanoporous polycarbonate membrane were used as templates to chemically synthesize polypyrrole nanotubules.233 Kros et al.234 carried out the polymerization of monomers (e.g., pyrrole, thiophenes) inside the pores of track-etched polymeric membranes. The hollow tubules formed in this manner exhibited relatively enhanced electrical properties compared with their respective bulk analogues. In another work, a ZSM-5 molecular sieve was used as a template to synthesize hollow pyrrole–platinum complex spheres following the chemical polymerization of pyrrole with potassium hexachloroplatinate(IV) as oxidant.235 Dubal et al.236 synthesized polypyrrole nanotubes using MnO2 as a sacrificial template in the presence of pyrrole 1 M HCl and K2Cr2O7. Hollow nanotubes of polypyrrole have been prepared rapidly by chemical oxidative polymerization of pyrrole in the presence of V2O5 nanofibers (sacrificial template) and FeCl3 as oxidant. This was followed by the removal of the template by dissolving it in aq. 1.0 M HCl.237 In another study, MnO2 powder was selected for a simultaneous dual role as oxidizing agent and sacrificial template in the chemical synthesis of hollow sea urchin-shaped polypyrrole.238 In another study, polystyrene beads were used as the sacrifice template to prepare hollow polypyrrole nanoparticles.239 Capsular PPy hollow nanofibers were fabricated by polymerizing pyrrole monomer on hollow V2O5 fibers (template) and subjected to acid etching to remove the V2O5 template.240 In addition, Fe3O4@polypyrrole hollow capsules241 and Fe3O4@PPy yolk/shell composites242 were also prepared by a hard-template method.
Han et al.256 synthesized polyaniline nanotubes by the oxidative polymerization of aniline in dilute solution in the presence of cetyltrimethylammonium bromide. Self-assembled PANI nanotubes with a rectangular cross-sectional shape have been synthesized by in situ chemical oxidation polymerization in the presence of citric acid as the dopant.257 In another study, Zhang et al.258 prepared polyaniline nanotubes by a self-assembly process using carboxylic acids (propionic acid, lactic acid, succinic acid, malonic acid, tartaric acid, and citric acid) as dopants. They also investigated the effect of hydrogen bonding on the formation of nanotubes and aggregated dendrites of polyaniline. Highly crystalline polyaniline nanotubes and nanofibers have been synthesized in the presence of dicarboxylic acids (oxalic acid, malonic acid, succinic acid, glutaric acid, and adipic acid) (acting as dopants).259 Zhang et al.260 fabricated nanotubular polyaniline (self-assembled) following the chemically synthesized by ammonium persulfate oxidation of aniline in the presence of amino acid. The role played by the amino acids in this study is guided by their effect on the initial soft template for the growth of nanotubes based on the formation of micelles or oligomeric species during the initial stage of aniline oxidation. Rana et al.261 used a soft template method to prepare PANI nanotubes of almost uniform diameter by selecting benzene 1,2,4,5-tetracarboxylic acid, acting simultaneously as dopant acid as well as structure-directing agent. Huang and Wan262 investigated the influence of the molecular structure of sulfonic acids on the tubular morphology of the doped PANI. According to this, β-NSA-doped PANI exhibited tubular morphology by preparing it using an in situ doping polymerization method. Hollow PEDOT spheres (dia: 1.7–4.6 μm) were synthesized by aqueous chemical polymerization using self-assembled membrane of poly(3,4-ethylenedioxythiophene) doped with acetic acid at room temperature and ammonium persulfate as oxidant.263
Alternatively, synthesis of self-assembled polyaniline nanotubes has also been reported using itaconic acid,264 camphor sulfonic acid,265 polymeric acids: poly(4-styrenesulfonic acid), poly(acrylic acid), poly(methyl vinyl ether-alt-maleic acid),266 malic acid, succinic acid, citric acid, and tartaric acid267 as dopants. Mu et al.268 reported the fabrication of self-assembled polyaniline nanotubes doped with D-tartaric acid for high-performance supercapacitor applications. Zhang and Wan269 synthesized chiral polyaniline nanotubes following the self-assembly process using (1R)-(−)-10-camphorsulfonic acid (L-CSA) and (1S)-(+)-10-camphorsulfonic acid (D-CSA). It was noted that the formation yields and the size of the doped polyaniline nanotubes were guided by the molar ratio of CSA to aniline. Panigrahi and Srivastava270 reported the synthesis of polyaniline hollow microspheres by the ultrasound-assisted emulsion polymerization technique using polystyrene microspheres as a template.
Zhang et al.271 reported a self-assembly process for the syntheses of polyaniline nanotubes (dia:130–250 nm) doped with α-naphthalene sulfonic acid, β-naphthalene sulfonic acid, and 1,5-naphthalene disulfonic acid. According to Sun and Deng,272 DL-tartaric acid played an important role as a dopant in determining the morphology of polyaniline prepared by interfacial oxidation polymerization of aniline using APS as the initiator. These findings led to the formation of spherical mushroom-like morphology and nanotubes of polyaniline corresponding to the DL-tartaric acid concentration of ∼0.02 M and ∼0.04 M, respectively.
Qiu et al.273 synthesized polyaniline nanotubes (dia:100–300 nm, length: up to 2 µm) through a template-free polymerization using (NH4)2S2O8 as an oxidant and a protonic acid dopant (C60-(OSO3H)6 or PAMAM4.0 [naphthyl (SO3H)2]24). The formation of oriented arrays of polyaniline nanotubes (60 to 150 nm in diameter) were also reported by hydrogen-bonding directionality in the presence of a crown ether derivative and ammonium persulfate in HCl solution.274 Poly(2-acrylamido -2-methylpropane sulfonic acid) has been used as a dopant as well as soft template for the synthesis of uniform hollow microspheres of PANI (dia: 410 nm, shell thickness: 72 nm) in aqueous solution following in situ polymerization of aniline in the presence of ammonium persulfate.275 Huang et al.276 reported a template-free method following inversed microemulsion polymerization in fabricating polyaniline hollow microspheres (outer dia: 4–6 mm, shell thickness: 150–250 nm) using β-naphthlene sulfoinic acid as dopant. Zhu et al.277 prepared superhydrophobic rambutan-like hollow spheres of polyaniline by a self-assembly method in the presence of perfluorooctane sulfonic acid (dopant and soft template).
Zhang and Wan278 reported transformation of self-assembled polyaniline from 1 D nanotubes (dia: ∼109–150 nm) to hollow microspheres by changing the molar ratio of the dopant (salicylic acid) to monomer (aniline). The freeze-fracture electron microscopy studies revealed the role played by hollow spherical micelles comprising salicylic acid/aniline as templates in the formation of nanotubes/hollow spheres. The driving force in the self-assembly of hollow microspheres might be due to be the hydrogen bonding of the –OH group (salicylic acid) and amine group (polyaniline). Liang et al.279 synthesized polypyrrole nanotube aerogels by using the weakly interconnected network of self-assembled nanotubes of lithocholic acid as a soft template.
Hollow nanospheres of methyl-substituted polyaniline280 and poly(m-methylaniline)281 microspheres were prepared through the self-assembly processes in the presence of ammonium persulfate. Tavandashti et al.282 studied the transition of polyaniline from nanotubes to nanospheres following a soft template route, as schematically displayed in Fig. 13(a and b). According to this, the fabrication of polyaniline nanospheres was carried out via the oxidative polymerization of aniline in the presence of β-naphthalenesulfonic acid (β-NSA) as both surfactant and dopant, and ammonium persulfate as oxidant at 2–5 °C. Furthermore, control of the morphology of polyaniline was achieved by changing the reaction conditions. Ding et al.283 prepared PANI nanotubes with diameters of 100–150 nm of single nanotubes by carrying out direct oxidation with APS in the absence of hard templates and acidic dopants. During this, the formation of the hollow spheres at the initial stage was accompanied by the micelles (soft template) formed by the aniline monomer in aqueous solution. Furthermore, investigations revealed a decrease in pH with increasing polymerization time resulted in a change in the morphology from hollow spheres to short and long tubes. Triton X-100 has been selected as a soft template to fabricate poly(aniline-copyrrole) hollow nanospheres via oxidative polymerization of aniline.284 In a micelle-mediated phase transfer method, perfluorooctanoic acid/aniline acted as soft templates to form hollow nano/microspheres of polyaniline with mesoporous brain-like convex-fold shell structures.285
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| Fig. 13 The schematics of the formation mechanisms of (a) PANI nanotubes/nanofibres and hollow microspheres and (b) PANI nanospheres.282 Reproduced with permission from Wiley. | ||
Vitamin C upon the addition of aniline monomer ([Vitamin C]/[Aniline] = 0.25) produced polyaniline nanotubes (dia.: 80–120 nm, length extending to several micrometers) via the oxidative polymerization method.22 Ren and others286 adopted a soft template method in the fabrication of a polyaniline microtube acidic solution using methyl orange as dopant in the presence of aniline monomer and ammonium peroxydisulfate. According to this, methyl orange is self-assembled into supramolecular aggregates and acts as templates in the formation of PANI microtubes. Urea has also been used as a soft template in the synthesis of polyaniline nanotubes by in situ chemical oxidative polymerization of aniline monomer.287 Orellana and Roberts288 used a simple approach for preparing polypyrrole microtubes without the need for a solution or substrate-based template. Wang et al.289 synthesized polypyrrole nanotubes of ∼50 nm diameter and a length extending to several micrometers using pyrrole, FeCl3·6H2O, and methyl orange as monomer, initiator, and soft template, respectively.
A self-assembly method has been used to synthesize polyaniline nanotubes in the excess of (NH4)2S2O8 oxidant.290 This could be ascribed to the formation of aniline dimer cation-radicals acting as effective surfactants. Zhang et al.291 fabricated polyaniline hollow spheres with controllable size and shell thickness through the oxidation–reduction reaction-driven approach under hydrothermal conditions in the absence of any sacrificial templates and organic surfactants and using H2O2 and Fe3+ as oxidant and catalyst, respectively. Hollow polyaniline microsphere were also prepared by polymerization of aniline in aqueous medium using K3[Fe(CN)6] as oxidant.292 Wei and Wan293 synthesized hollow microspheres of PANI (dia: 450–1370 nm) using aniline emulsion template doped with β-naphthalene sulfonic acid at −10 °C in the presence of ammonium persulfate acting as the oxidant. Investigations are also reported on the synthesis of PANI nanotubes, nanotubes with rectangular and circular cross-section hollow microspheres294 and 3D hollow microspheres assembled from 1D PANI nanowires.295
Liu et al.296 reported a template-free method to synthesize polyaniline film (thickness: 100 nm) embedded with PANI nanotubes without any surfactant or organic acid. Their studies revealed that oligomers with certain structures are responsible for the growth of the nanotubes. A micelle soft-template method was used in fabricating PANI nanotubes (external dia: 110 internal dia:, 10 nm, length: several μm) in the presence of oxalic acid as a dopant.297 Tajima et al.298 used nanobubble soft templates formed by ultrasonic irradiation in the synthesis of hollow polypyrrole spheres.
Xia et al.302 used poly(vinylpyrr1olidone) (PVP) as a soft template in order to fabricate PEDOT exhibiting hollow spheres (size: 130–820 nm) via a self-assembly method. Bian et al.303 used star-like unimolecular micelles as templates for the controlled syntheses of hollow nanostructures of polythiophene nanoparticles. A reverse emulsion polymerization was described using sodium bis(2-ethylhexyl) sulfosuccinate cylindrical micelles as the template at room temperature for the synthesis of PEDOT nanotubes (dia: 50–100 nm, length: 10–20 mm).304 The synthesis of self-assembled 3D hierarchical PEDOT micro/nanostructures including hollow spheres and double-layer bowls was carried by a template-free method in the presence of perfluorosebacic acid as the dopant and FeCl3 6H2O as the oxidant.305 Ali et al.306 synthesized PEDOT/Au hollow nanospheres by an in situ polymerization method comprising the ratio of EDOT and HAuCl4 from 2
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1 to 1
:
2. In another study, a surfactant-free Ouzo emulsion method was used to synthesize hollow or partially collapsed bowls of PEDOT using FeCl3·6H2O, acetone, and toluene as oxidant, solvent, and anti-solvent, respectively (Fig. 14(a)).307 This method has also been extended in successfully synthesizing PANI, PPy and PTh. Fig. 14(b–d) show the SEM images of PEDOT under different experimental conditions. Ni et al.308 used the chemical polymerization of EDOT to synthesize hollow PEDOT microsphere in the presence of ammonium persulfate (oxidant) and PVP (micelles). Sui et al.309 synthesized hollow microspheres of PEDOT (size: 0.5 to 10 μm) by the chemical oxidative polymerization of EDOT using ammonium persulfate in a catanionic surfactant solution comprising a mixture of cetyltrimethylammonium bromide and sodium dodecylbenzenesulfonate. Recently, Ge et al.195 prepared honeycomb-shaped photothermal polypyrrole by electropolymerization.
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| Fig. 14 (a) Schematic illustration for the oxidative chemical polymerization of PEDOT hollow spheres/bowls. (b–d) SEM images of the synthesized PEDOT nanostructures, (b) PEDOT nanoparticles before wash-removal of oxidant, (c) after the removal of oxidant by ethanol washing, and (d) collapsed hollow bowls after the washing and drying.307 Reproduced with permission from Elsevier. | ||
Recently, electrodeposition has become a promising method for fabricating ICP-based core–shell materials as superior electrodes in supercapacitors, though its potential is yet to be harnessed.145,318 This is ascribed to the superior control over morphology, enhanced performance through binder-free synthesis, and improved interface between the polymer and substrate. Chen et al.319 synthesized polypyrrole (binder free film) on carbon cloth by the electrodeposition method. Core–shell nanorod arrays with polyaniline were successfully electrodeposited into a mesoporous NiCo2O4 support.320 Wu et al. reported321 polypyrrole-coated low-crystallinity Fe2O3 supported on carbon cloth by a combination of chemical reduction and electrodeposition methods. The preparation of a free-standing graphene/polyaniline/MnO2 ternary composite by sequential electrodeposition on carbon cloth as working electrodes was reported.322 In another study, electrodeposition of PANI on the surface of GO/α-MnO2 was used to prepare hierarchical GO/α-MnO2/PANI composites.323 This electrodeposition technique has also been used in fabricating (CoCrFeMnNi)3O4@CC-PPy,324 LaMnO3@CC-PPy,325 and porous PPy/black phosphorus oxide composites electrodeposited on CNT.326 In another approach, Fauzi et al.327 used oxidative chemical vapor deposition to deposit a submicrometer-thick layer of PPy on the carbon fabric.
![]() | (1) |
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| Fig. 15 Electromagnetic radiation hazards and application of EWAMs around daily life.328 Reproduced with permission from Elsevier. | ||
Furthermore, SET is the sum of shielding efficiency originating from absorption (SEA), reflection (SER) and multiple reflections (SEM),9 i.e.,
| SET = SER + SEA + SEM | (2) |
The factors affecting the shielding effectiveness include permeability, permittivity, skin depth and thickness, external physical properties, eddy current loss, magnetic loss, dielectric loss, size and morphology etc.54 The impedance matching ratio, |ZMZ0| (Zin: input impedance, Z0; free space impedance) is also another important factor that provides information about EM waves entering the shield. It may be noted that the reflection loss (RL) of a shielding material is closely related to the input impedance (Zin) and free space impedance (Z0). According to the transmission line theory, both Zin and RL are expressed as shown below.9
![]() | (3) |
![]() | (4) |
The methods commonly used to measure the electromagnetic shielding efficiency (also referred to as effectiveness) of a material can be based on the space transmission, shield box, shield room and coaxial transmission line approaches.75
In this regard, much interest has been focused recently on developing electromagnetic wave (EMW) shielding materials undergoing absorbing mechanisms.9 This is because EMWs, following the reflection mechanism, produce secondary pollution due to their reflection to the environment. Accordingly, conductive polymers have been receiving considerable attention guided by their conductivity, light weight, corrosion resistance and processibility.9 In this regard, the morphology of the intrinsically conducting polymer materials is considered a vital parameter in their functioning as EMW absorbers. This is ascribed to successive internal reflection (multiple internal reflections of incident EM waves).204,329–333 Hollow microhemispheres like polypyrrole and carbon dielectric materials could act as promising high-performance microwave absorbers with strong reflection loss and wide absorption frequency bandwidth.332
According to the available literature, electromagnetic wave absorption materials have proved to be very effective at mitigating electromagnetic pollution and interference.9 The choice of an ideal microwave absorber material is guided by light weight, good thermal stability, antioxidation capability, multi-interfaces, impedance matching, synergistic effects, strong absorption properties and wide bandwidth simultaneously.54,333–335 In addition, other important features that affect the absorption of microwaves include complex permittivity/permeability, impudence matching and morphology of these materials.9 In such studies, the choice of ICPs is guided by the low cost of synthesis and great environmental stability of hollow morphology, to account for the improved microwave absorbing properties. In addition, hollow ICP composites and ICP based core–shell materials have also been fabricated, integrating magnetic and dielectric losses to facilitate the absorption of EM waves.334
Among these, Fe3O4 has drawn a great deal of attention because of its low cost, easy synthesis, saturation magnetization value and high Curie temperature.9 However, several drawbacks of Fe3O4, such as ease of oxidation, high density, dramatic decrease of permeability in the high-frequency range due to the Snoek's limit, weak interfacial compatibility and substrate dispersion difficulty need to be addressed.9,334,335 In view of this, combining ICPs with magnetic materials could be more effective at enhancing the electromagnetic wave attenuation synergistically.329 Furthermore, outstanding performance can also be achieved by combining dielectric and magnetic components together.336 Accordingly, most studies are focused on Fe3O4 in the form of binary composites with ICP or its ternary nanocomposites involving ICPs and carbonaceous materials. It may be noted that the hollow structures of Fe3O4 nanospheres and PANI reduce the weight of the composites. In addition, they also extend the transmission path of microwaves as result of multiple reflection and scattering loss.
Guo et al.339 studied electromagnetic wave absorption of the hollow polypyrrole nanorods fabricated by using the self-assembly template that can be easily removed. These findings have shown that tuning the wall thickness facilitates control of the dielectric constant of HPPy. The variation of reflection loss with frequency in the range of 2–18 GHz with filler loading of 10 wt% indicated the minimum reflection of –54.94 dB with the largest effective absorption bandwidth of 7.36 GHz (thickness: 3.4 mm). The possible EMA mechanism of HPPy nanorods could be ascribed to impedance matching, multiple reflection, a good conductive network and enhancement of polarization loss. In another method, hollow or partially collapsed bowls of polyaniline, polypyrrole, polythiophene and poly(3,4-ethylenedioxythiophene) have successfully been synthesized by surfactant-free Ouzo emulsion.307 Subsequently, the EMI shielding performance of the three samples PEDOT sphere/bowl film (thickness: 6.5 μm), composite film of PEDOT hollow spheres/bowls film (thickness: 6.3 μm) with infiltrated PH1000 and pure PH1000 film (thickness: 6.2 μm) has been investigated in X-band (8–12 GHz). It was noted that EMI SE of the corresponding samples over the X-band follow the order: PEDOT hollow spheres/bowls film with infiltrated PH1000 (∼75 dB) > PEDOT:PSS with infiltrated PH1000 film (∼70 dB) > PEDOT hollow spheres/bowls film (very low). The low electrical conductivity of pure PEDOT hollow spheres/bowls film accounts for their inferior EMI performance. In contrast, the composite comprising the PEDOT hollow spheres/bowls film with infiltrated PH1000 exhibited enhanced EM absorption, as evident from the total EMI SE (SET), due to the larger contribution from the absorption compared with the reflection. Ni et al.308 observed a maximum RL of −24 dB at 15.9 GHz for a sample (thickness: 2 mm) of PEDOT hollow microspheres.
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| Fig. 16 (a) SEM image and (b) TEM image of HPPy/Ag-10.204 Reproduced with permission from Nature Publication. | ||
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| Fig. 17 (a) Variation of EMI shielding of PPy, HPPy, HPPy/Ag-2, HPPy/Ag-5, HPPy/Ag-10 with varying frequency at 0.5–8 GHz, and (b) trapping mechanism of EM wave through enhanced internal reflection in HPPy/Ag: An anticipated scheme.204 Reproduced with permission from Nature Publication. | ||
Microwave absorption of milled carbon fiber (4 wt%) and hollow polyaniline spheres (1 wt%) impregnated in the epoxy matrix (thickness: 1.8 mm) exhibited maximum absorption (−49.3 dB) and the effective bandwidth of 1.7 GHz–10 dB in the X band region.344 The observed reflection loss of EM waves in the given frequency range was attributed to the improvement in impedance matching, multiple reflections and scattering of EM waves. According to Wang et al.,345 hollow polyaniline-derived N/S co-doped carbon nanoflakes possessed RminL of −53.5 dB (10.2 GHz) and a corresponding effective absorption band of 4.5 GHz at 2.9 mm. This could be explained on the basis of conductivity loss, interfacial polarization relaxation and the impedance matching from the hollow structure synergistically, resulting in excellent microwave absorption performance.
Chu et al.346 fabricated a well-designed structure of sandwich-like composite films based on hollow polyaniline and cellulose nanofiber (CNF) in the surface layers and MXene/CNF in the intermediate layer. This displayed an EMI SE of 35.3 dB for a proportion of MXene and PANI achieved at a lower filler loading compared with many others. It was suggested that the formation of such sandwich structure effectively reduced the reflection of the EM wave and made the absorption more dominant. Hollow polyaniline/Fe3O4 microsphere (7.33 wt%) composites showed the maximum reflection loss of −15.6 dB and maximum bandwidth of 8.0 GHz over −10 dB in the frequency range of 2–18 GHz.347 Double-shelled hollow polypyrrole nanotubes were synthesized by using the reactive MnO2 template.317 They exhibited the optimal reflection loss of −50.4 dB and a wide EAB of 7.7 GHz in the presence of 5 wt% in a paraffin wax matrix. Such performance was ascribed to the synergistic effects of interfacial polarization and conduction loss.
Promlok et al.351 reported the formation of the hollow magnetic polyaniline by in situ polymerization in one pot for EMI applications. In another study, Fe3O4–polyelectrolyte modified polyaniline (Fe3O4–PE@PANI) was prepared by the self-assembly approach.352 TEM imaging of the product clearly established the formation of hollow Fe3O4-Polyelectrolyte (PE)@PANI nanocomposites (average size ∼500 nm), with Fe3O4 nanoparticles tightly and completely attached to the PANI hollow sphere surfaces. The 50 wt% of Fe3O4−PE@PANI loaded in paraffin exhibited a minimum reflection loss of −6.5 dB (14.3 GHz) and the frequency bandwidth (<–5 dB) from 12.5 to 15 GHz, and ascribed it to the impedance matching and dielectric/magnetic loss abilities. Hou et al.353 prepared hollow-structure Fe3O4/PANI microspheres based on three steps, namely the preparation of Fe3O4 nanoparticles, hollow PANI microspheres and Fe3O4/PANI microspheres. Subsequently, they investigated the effects of the mass ratio of aniline/PS (template) on their EMW absorption properties. Fe3O4/PANI microspheres corresponding to the mass ratio of aniline/PS of 1
:
6 and thickness of 1.5 mm attained RminL of −24.3 dB, and the bandwidths below −10 dB corresponded to 4.64 GHz (11.04–15.68 GHz) for 2 mm thickness of the sample. It was suggested that dielectric loss, magnetic loss (2–7 GHz) and eddy current loss (7–18 Ghz) played important roles. In addition, hollow Fe3O4/PANI microspheres acted as a potential absorber in the absorption of microwaves due to strong destructive interference and eddy current loss. Hollow poly(aniline-co-pyrrole)–Fe3O4 (0.06 g) composite nanospheres were prepared via the oxidative polymerization of a mixture of aniline and pyrrole in the presence of a magnetic fluid.354 The reflection loss calculations showed the best microwave-absorbing property between 0.5–10 GHz for the hollow poly(aniline-co-pyrrole) filled with 0.06 g of Fe3O4. These studies also revealed that both dielectric and magnetic loss significantly affect the efficiency of microwave absorption.
In another study, a Fe3O4/PANI355 composite was fabricated with hollow Fe3O4 nanospheres and polyaniline nanotubes by the hydrothermal treatment and chemical oxidative polymerization, and its micro absorption properties were studied by varying the ratio of PANI and the loading amount of the composites in paraffin. These findings have shown remarkable performances (RminL: −55.03 dB, EAB: 4.88 GHz) for its thickness of 1.84 mm in the frequency range of 2–18 GHz. This excellent performance was attributed to the interfacial polarization loss, multiple reflection scattering loss and the synergistic effect of hollow Fe3O4 (magnetic) and 1D PANI (dielectric) material. Fe3O4 microsphere core (size: 300 nm)/PANI shell (thickness: 100 nm) synthesized by in situ polymerization reached RmaxL of −37.4 dB at 15.4 GHz.356 Such enhanced microwave absorption properties arise due to the improved impedance, dielectric loss, interfacial loss and synergistic effect. Core–shell Fe3O4−PEDOT microspheres (EDOT)/(Fe3O4 molar ratio = 20) were also prepared by a two-step method in the presence of polyvinyl alcohol (stabilizer) and p-toluenesulfonic acid (dopant) (Fig. 18(a)).357 TEM studies, displayed in Fig. 18(b) established Fe3O4 microspheres coated by PEDOT, and the thickness of the shell corresponded to 90 nm. The variation of reflection losses of Fe3O4/PEDOT with frequency in Fig. 18(c) showed excellent microwave absorbing property (RminL: –30 dB at 9.5 GHz, thickness: 4 mm) due to the impact of layer thickness, volume fraction and conductivity.
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| Fig. 18 (a) Formation mechanism of Fe3O4@PEDOT core–shell microspheres, (b) TEM images of Fe3O4@PEDOT core–shell microspheres prepared with (EDOT)/(Fe3O4) ratios: 20, and (c) reflection losses in different thickness of Fe3O4@PEDOT composites with (EDOT)/(Fe3O4) = 20.357 Reproduced with permission from ACS. | ||
Fe3O4-polyaniline,358 Fe3O4@Polypyrrole,359,360 and BaFe12O19@PANIn361 core–shell structured materials have also been studied for their electromagnetic wave absorption. Hosseini et al.362 used a core–shell approach for fabricating polythiophene nanofiber coated on MnFe2O4/Fe3O4 through the combined co-precipitation and in situ polymerization methods. The micro absorption properties of the 1.5 mm nanocomposite showed minimum RL of −21 dB (12 GHz) in the frequency range 8.0–12.0 GHz. CoSe2@polythiophene363 and rGO/Ni0.5Co0.5Fe2O4@PEDOT364 core–shell composites were also synthesized and studied for their electromagnetic, microwave absorbing properties. Fe3O4 microspheres @PPy anchored on 3D graphene aerogel (GO to Fe3O4@Ppy wt ratio: 1
:
3) of 2.5 mm thickness reached a minimum reflection loss of −40.53 dB at 6.32 GHz and the effective bandwidth of 5.12 GHz (11.12–16.24 GHz).365 Such enhanced microwave absorption properties of the ternary composite could be explained on the basis of abundant interfaces, enlarged dielectric properties, enhanced conductivity and synergistic effect.
Excellent microwave absorption performance has been shown by PANI decorated on prism-shaped hollow carbon (thickness: 2.5 mm) synthesized by in situ polymerization.366 It showed the minimum reflection loss of −64.0 dB (11.1 GHz) and EAB corresponding to 5.0 GHz (9.5–14.5 GHz) attributed to high impedance matching, dielectric loss and geometric effect. Gai et al.367 constructed PPy nanotubes@MoS2 core–shell and observed the optimal RL of −49.1 dB at 6.1 GHz and the widest bandwidth up to 6.4 GHz from 11.5 to 17.5 GHz (RL < −10 dB) corresponding to its thickness of 2.5 mm. Such enhanced microwave absorption properties of PPy@MoS2 composite were ascribed to the morphology, attenuation capacity and the impedance matching.
Tian et al.368 fabricated PPy@PANI of tunable shell thickness (30–120 nm) by direct polymerization of aniline on the surface of PPy microspheres. The fabricated PPy@PANI composite showed a maximum reflection loss of −34.8 dB at 13.9 GHz and bandwidths exceeding −10 dB corresponding to 11.9–16.6 GHz (4.7 GHz). In another study, hollow ZnxFe3−xO4@Polyaniline369 core–shell composites acted as high-performance microwave absorbers with high reflection loss, respectively. In situ polymerized-grown polyaniline nanorod arrays on the surface of carbon (C@PANI) microspheres exhibited a waxberry-like shape.370 Subsequently, their microwave absorption performance was evaluated and displayed considerable reflection loss (samples thickness: 2.2 mm), impedance matching ratio of samples and 3 D reflection loss with different thickness, as shown in Fig. 19(a, b and c), respectively. It was noted that C@PANI exhibited superior microwave absorption performance (sample thickness: 2.2 mm), RminL: −59.6 dB at 15.5 GHz, effective bandwidth for RL < −10 dB: 5.4 GHz (12.6 to 18 GHz) compared with pure PANI and carbon microspheres. It was suggested that dielectric loss ability, synergistic effect and defects present in the C microspheres contributed to this high microwave absorption performance of C@PANI microspheres. In addition, relatively low electrical conductivity owing to the amorphous structure of C@PANI could be favourable in the impedance matching. The variation of 3 D reflection loss of C@PANI microspheres with the sample thickness in the range of 2–3 mm showed the shifting of the RminL peak from the high to low-frequency region. Based on the observations, the absorption mechanism of C@PANI microsphere has also been proposed. In another study, PANI shell fabricated on the surfaces of CNTs (CNT/aniline mass ratio = 1
:
2) acted as an excellent microwave absorber (RminL: ∼41.5 dB at 9.5 GHz and EB for RL ≤ –10 dB: 5.1 GHz for 2 mm thickness) as a result of the microwave dissipation ability of CNTs and good impedance matching.371
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| Fig. 19 (a) Reflection loss of samples with the thickness of 2.2 mm; (b) impedance matching ratio of samples; (c) three-dimensional reflection loss of C@PANI micro-spheres with different thickness.370 Reproduced with permission from Elsevier. | ||
Liu et al.372 reported excellent microwave absorption performance (RmaxL: −38.1 dB at 11.6 GHz) in the frequency range of the X-band for the pyrrole as the shell on the core of carbon microspheres. The microwave absorption studies were made on core shell-type PEDOT (outer shell) nanocomposite with barium ferrite (center) synthesized by in situ emulsion polymerization in the frequency range of 12.4–18 GHz.373 The subsequent findings on microwaves have shown its absorption value (SEA) of 22.5 dB (>99% attenuation) owing to the higher dielectric and magnetic loss contributions. The effective electromagnetic shielding performance (EMI SE: 28.8 dB) has also been achieved in a core–shell heterostructure comprising polyaniline-coated bagasse fiber.374 According to Saini et al.,375 TEM studies established the coating of PANI deposited via in situ polymerization on the surface of individual MWCNT that contributed towards the absorption-dominated total shielding effectiveness (−27.5 to −39.2 dB) in the frequency range of (12.4–18.0 GHz). In another study, Polyaniline@Helical CNTs with dual chirality exhibited enhanced microwave absorption synergistically.376
Manna and Srivastava,383 motivated by the role played by the dual interface in microwave absorption and shielding performance, reported the fabrication of Fe3O4@C@PANI according to the scheme in Fig. 20(a) by varying the aniline
:
Fe3O4@C as 9
:
1, 8
:
2, 7
:
3 with the aniline monomer under identical reaction conditions, and the products were designated as PFC-10, PFC-20 and PFC-30, respectively. HRTEM imaging of the trilaminar PFC-10 composite in Fig. 20(b) clearly shows the formation of the highest outermost thickness of nonmagnetic polyaniline shell (∼30 nm) on Fe3O4@C corresponding to the aniline
:
Fe3O4@C ratio of 9
:
1. Further investigations revealed the decrease in complex permittivity and increase in complex permeability on encapsulation of Fe3O4@C by PANI due to impedance matching. Fig. 20(c) shows the highest shielding efficiency for the PFC-10 composite predominantly due to absorption (SEA: ∼47 dB) rather than reflection (SER: ∼15 dB) in the frequency range of 2–8 GHz. Such findings in Fe3O4@C@PANI are unique owing to the dual interfaces compared with Fe3O4@C and Fe3O4/PANI due to their applicability limited to a discrete frequency. In addition, such remarkable EM wave attenuation in the Fe3O4@C by PANI trilaminar core@shell composite was also supported by impedance matching and dielectric and magnetic loss.
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Fig. 20 (a) Schematic presentation of the fabrication of Fe3O4@C@PANI ternary composite (aniline : Fe3O4@C (FC) = 9 : 1, 8 : 2, 7 : 3 with aniline monomer under identical reaction conditions and procedure and designated as PFC-10, PFC-20 and PFC-30, respectively), (b) HRTEM images of PFC-10, and (c) frequency vs. EMISE of PFC composites.383 Reproduced with permission from ACS. | ||
Motivated by this, they extended their work on core@shell@shell-type Fe3O4@SiO2@PPy, anticipating that the aggregation of Fe3O4 in the PPy matrix could be prevented by introducing SiO2 as first shell (dielectric) between the interfaces of Fe3O4 and PPy in comparison to Fe3O4 alone.384 Their findings indicated Fe3O4@SiO2@PPy (Fe3O4@SiO2/pyrrole wt/wt = 1
:
9) exhibited the highest total shielding efficiency (SET: ∼32 dB) in the frequency range of 2–8 GHz (Fig. 21(a)) following reflection as the dominant shielding mechanism. This was attributed to role played by dual interfaces, poor impedance matching between the PPy (conducting)/SiO2 (insulating) and high electrical conductivity of Fe3O4@SiO2@PPy and interfacial polarization, and reflection/scattering of EM waves. These findings clearly established that switching of the dominating shielding mechanism from absorption to reflection could be achieved by tuning C@ PANI compared with SiO2@PPy shells in Fe3O4@C@PANI and Fe3O4@SiO2@PPy trilaminar composites, respectively (Fig. 21(b)). Such switching over of the shielding mechanism was also supported by the impedance mismatch and impedance matching in Fe3O4@ SiO2@PPy and Fe3O4@C@PANI.
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Fig. 21 (a) Plot of frequency versus SET of Fe3O4@SiO2@PPy (PFS) nanocomposites (Pyrrole/Fe3O4@SiO2 (PS) = 9 : 1, 8 : 2, and 7 : 3) with the aniline monomer under identical reaction conditions and procedures, and the samples were designated as (PFS-10, PFS-20, and PFS-30, respectively), and (b) tuning of shells in trilaminar Fe3O4@SiO2@PPy and Fe3O4@C@PANI core@shell nanocomposites in controlling electromagnetic interference through switching of the shielding mechanism.384 Reproduced with permission from ACS. | ||
Ji et al.385 synthesized hollow γ-Fe2O3@PEDOT (FP) and γ-Fe2O3@SiO2@PEDOT (FSP) core–shell nanocomposites. The corresponding SEM images of FSP and FP clearly established the removal of the SiO2 layer from γ-Fe2O3@SiO2@EDOT to form hollow γ-Fe2O3@PEDOT. Further investigations on the frequency (2–18 GHz) dependence of reflection loss revealed remarkable microwave absorption properties of hollow γ-Fe2O3@PEDOT (RminL: −44.7 dB: 12.9 GHz, EAB: 4.3 GHz in 10.8–15.1 GHz range) compared with the γ-Fe2O3@SiO2@PEDOT (RminL: −21.3 dB: 14.1 GHz, EAB: 3.8 GHz: 12.6–16.4 GHz range) for thickness 2.0 mm. This was ascribed to the synergistic effect between the magnetic and dielectric components and the core–shell structure. Reports are also available on enhanced electromagnetic wave absorption of Co@Hollow carbon nanospheres @PANI386 and FeNi@C@PANI.387 Panigrahi and Srivastava388 fabricated rubber (EPDM, NBR, and NR)@Polystyrene@Polyaniline blends and observed high shielding efficiency (>30 dB:1–8 GHz). Such high performance of rubber blends was attributed to the trapping of EM waves through enhanced internal reflection due to the typical core–shell morphology of PS@PANI. PPy nanotubes/NR/NBR389 core–shell composites also displayed excellent electromagnetic wave absorption properties.
γ-Fe2O3/(SiO2)2−SO3H/PPy composite (thickness: 2.0 mm) core/shell/shell microspheres displayed substantially improved microwave absorption properties (RmaxL: −43.1 dB) (15.1 GHz), EAB: 6.1 GHz (11.9–18.0 GHz) (Fig. 22(a)).390 This was ascribed to impedance matching, unique core/shell/shell structures, synergistic interaction, dielectric loss (SiO2 and PPy layers) and magnetic loss (γ-Fe2O3). A model has been proposed in Fig. 22(b) to account for the effects of core/shell/shell structures on microwave absorption. Core/shell/shell-structured Ni/C/PANI nanocapsules prepared by a two-step process involving modified arc-discharge and chemical polymerization exhibited an optimal RL value of −9.3 dB at 6.2 GHz (thickness: 3 mm) with broad −5 dB (3.4–18 GHz) bandwidth.391 Wang et al.392 prepared hierarchical Fe3O4@Graphene@PANI following hydrothermal and in situ polymerization. The composite exhibited favourable microwave absorption properties, as evident from RmaxL of –43.7 dB (at 10.7 GHz) and the EAB <10 dB of 5.4 GHz (6.8–12.2 GHz) with a matching thickness of 3 mm. These findings were explained on the basis of impedance matching, enhanced interfacial polarization and orientation polarization.
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| Fig. 22 (a) Variation of RL of γ-Fe2O3/(SiO2)x–SO3H/polypyrrole (referred to as FSxHP, where x = 0,1,2,3,4) core/shell/shell microspheres and FS2H-P (physical blend of FS2H and PPy) with the frequency (d = 2 mm), and (b) physical model of the effects of core/shell/shell structures on the microwave absorption.390 Reproduced with permission from Springer. | ||
Ding et al.393 fabricated core@shell hierarchical cable-like TiO2@Fe3O4@PPy (Thickness: 3.2 mm) and observed maximum reflection loss of −61.8 dB owing to the magnetic–dielectric synergy. CoNi@SiO2@Polypyrrole nanocomposites displayed enhanced microwave absorbing capacity as evident from their minimum reflection loss of −34.19 dB at 9.59 GHz (thickness: 2.12 mm) and the EAB with RL < −10 dB in the entire X-band.394 In another study, core–shell SiCNWs@MnO2@PPy prepared through a multistep process showed the minimum reflection loss of −50.59 dB (matching thickness: 2.41 mm) and the effective absorption bandwidth of 6.64 GHz (matching thickness: 2.46 mm).395 This excellent electromagnetic wave absorption performance was ascribed to the advantage of the interfacial polarization and dipole polarization displayed by core–shell SiCNWs@MnO2@PPy. Several other ternary composites have also been reported as efficient microwave absorbers, such as Ni/PANI/RGO,396 Fe3O4@PEDOT microspheres/RGO,397 NiCo2O4 (hollow)@PPy nanofibers/RGO,398 encapsulation of γ-Fe2O3-decorated RGO in PANI core–shell tubes,399 RGO/Fe3O4/PANI,56 N-doped Graphene@PANI nanorod modified by Fe3O4 nanoclusters,400 polyaniline/graphene oxide/Fe3O4,401 magnetite nanoparticles decorated CNT/PANI,402 PANI/CIP/Fe3O4,403 and Fe3O4@SiO2@PPy.404 Shukla405 prepared dual core–shell structured Fe3O4/C/PPy (Fe3O4/C
:
PPy:2
:
8 wt/wt) composites via a hydrothermal and chemical oxidative polymerization method and observed their absorption-dominated excellent EMI shielding efficiency (>28) dB in the range of 1 to 8.5 GHz (Fig. 23(a)). The probable mechanism in Fig. 23(b) shows the attenuation of electromagnetic waves by the trilaminar Fe3O4/C/PPy composite. It was also suggested that spin motion plays a decisive role in this performance. In addition, excellent electromagnetic absorption properties have also been reported in PANI@Natural graphite flakes (NGF)/MWCNT406 and PEDOT/RGO/Co3O4.407
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Fig. 23 (a) Plots of frequency versus SET Fe3O4/C/PPy core/shell composites with pyrrole: (Fe3O4/C = 9 : 1, 8 : 2,7 : 3) with pyrrole monomer under similar reaction situations, referred to as10, 20 and 30, respectively, and (b) schematic diagram of EMI attenuation mechanism.405 Reproduced with permission from Springer. | ||
According to the available literature, a very limited amount of work has been reported on quaternary core–shell composites in general, or their applications in microwave absorption. In one such study quaternary MWCNT/CuO/Fe3O4/PANI nanocomposites following the weight ratio of CuO/Fe3O4/PANI to MWCNT in the 1
:
3, 1
:
4 and 1
:
5 showed minimum reflection losses −45.7, −85.4, and −87.4 dB, respectively.408 The corresponding absorption bandwidths (RL ≤ −10 dB) of MWCNT/CuO/Fe3O4/PANI nanocomposites were found to be 6, 7.6, and 6 GHz. The higher value of loss constant (α) of MWCNT/CuO/Fe3O4/PANI nanocomposites indicated both magnetic and dielectric loss tangent playing key roles in influencing the microwave absorption efficiency.
Wang et al.409 fabricated a 3D heterostructure of Graphene@Fe3O4@WO3@PANI using a hydrothermal method and chemical oxidation polymerization and studied its performance in microwave absorption. In addition, the presence of WO3 decreased permittivity, facilitating better impedance matching. The synthesized quaternary nanocomposite displayed a maximum RL value (−46.7 dB) at 9.4 GHz and the maximum absorbing bandwidth exceeding −10 dB at 1.8 GHz (12.4 to 14.2 GHz) corresponding to the thickness of 4 mm and 1.5 mm, respectively. The EM wave absorption mechanism involved contributions originating from enhanced interfacial polarization, better impedance matching, multiple reflection, and a synergistic effect. In another study, Liu et al.410 investigated the electromagnetic wave absorption properties of graphene (GN@Fe3O4@PANI) decorated with TiO2 prepared by a hydrothermal method and in situ polymerization, as described in Fig. 24(a). The corresponding TEM image in Fig. 24(b and c) indicated TiO2 nanosheets oriented perpendicular to GN@Fe3O4@PANI and TiO2 nanosheets forming hierarchical structures. The EM wave absorption properties of graphene@Fe3O4@PANI@TiO2 nanosheets loaded in 50 wt% paraffin are displayed in Fig. 24(d). According to this, GN@Fe3O4@PANI@TiO2 nanosheets showed RmaxL of −41.8 dB at 14.4 GHz (thickness: 1.6 mm) and absorption bandwidth of RL < −10 dB at ∼3.5 GHz. The attenuation of EM waves was attributed to the interfacial polarization and improved impedance matching of the nanocomposites. Table 1 records the microwave absorbing properties of hollow ICPs, hollow ICP nanocomposites and ICP based core–shell nanocomposites.
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| Fig. 24 (a) Schematic illustration of the fabrication of the GN@Fe3O4@PANI@TiO2 nanosheets, (b and c) TEM images of graphene GN@Fe3O4@PANI@TiO2 nanosheets, and (d) reflection loss curves of GN@Fe3O4@PANI@TiO2 nanosheets.410 Reproduced with permission from Elsevier. | ||
| Conducting polymer/nanocomposites | Method of preparation | Filling (wt%) in the matrix selected | Frequency range | Shielding performance (sample thickness) | Maximum bandwidth (<10 dB) (GHz) | Ref. |
|---|---|---|---|---|---|---|
| Hollow polyaniline/Ag | Emulsion polymerization | — | 100 kHz–20 GH | SET: 19.5 dB | — | 203 |
| Hollow polypyrrole/Ag | Via in situ chemical oxidative copolymerization | — | 100 kHz–20 GHz | SET: 34.5 dB | — | 204 |
| Fe3O4 (core: ∼100 nm)/PPy (shell: ∼70 nm) | In situ polymerization | 50 wt% in paraffin | 2–18 GHz | RminL: −22.4 dB at 12.9 GHz (thickness: 2.3 mm) | ∼5 GHz in the range of 4–18 GHz (thickness: 1.5–5.0 mm) | 329 |
| Fe3O4 microsphere@PANI | Two step oxi. polymerization | 50 wt% in paraffin wax bn | 2–16 GHz | RmaxL: −31.3 dB at 9.0 GHz (thickness: 3 mm) | 4.0–18 GHz (thickness: 1.5 to 5.0 mm) | 330 |
| Graphene@Fe3O4@SiO2@PANI | Dilute polymerization | 25 wt% in paraffin wax | 2–18 GHz | RmaxL: −40.7 dB at 12.5 GHz (thickness: 2.5 mm) | 5.8 GHz (10.5–16.3 GHz) | 331 |
| 3D helical hollow superstructure of PANI | Co-self-assembly process combined with emulsion droplets | 20 wt% in paraffin | 2–18 GHz | RminL: −51.60 dB at 13.95 GHz (thickness:2.0 mm) | 5.12 GHz (12.03–17.15 GHz) | 337 |
Hollow PPy nanofibers based self-assembled aerogel (seeds and Py proportion = 1 : 0.5) |
Self-assembly | 8% in paraffin | 2–18 GHz | RminL: −58.73 dB at 16.48 GHz (thickness: 2.30 mm) | 7.28 GHz (thickness: 2.69 mm) | 338 |
| Hollow PPy nanorods | Via self-assembly template sacrificial strategy | 10 wt% in paraffin | 2–18 GHz | RminL: −54.94 dB at 13.2 GHz (thickness: 3.4 mm) | 7.36 GHz | 339 |
| PANI microtubes | Via a self-assembly process assisted by excess APS | — | 0 to 6000 MHz. | RL: −15.5 dB | — | 342 |
| PANI hierarchical microtubes | SDS/HCl (7.5 mM) assisted oxidative polymerization method | 50% in paraffin | 2–18 GHz | −43.6 dB: absorption (thickness: 1.55 mm) | 5.84 GHz | 343 |
| Polyaniline 3D hollow spheres integrated milled carbon fibers (MCF) | PANI 3D hollow spheres are synthesized by removing the polystyrene (PS) core from PS/PANI composites | 4 wt% MCF + 1 wt% PANI in epoxy | 8–12 GHz | Max. absorption −49.3 dB (thickness: 1.8 mm) | 1.7 GHz (thickness: 1.8 mm) | 344 |
| Polyaniline-mediated N and S co-doped carbon nanoflakes | In situ polymerization method and carbonization process with oxygen limitation | Paraffin wax (80 wt%) and samples (20 wt%) | 2–18 GHz | RminL: −53.5 dB at 10.2 GHz (thickness: 2.9 mm) | 4.5 GHz at 2.9 mm | 345 |
| Hollow PANI /CNF in the surface layers and MXene/CNF in the intermediate layer | Alternating vacuum-assisted filtration method | MXene: 8 wt% and Hollow PANI : 24 wt% in CNF matrix | 8–12.4 GHz | EMI SE: 35.3 dB | — | 346 |
| Hollow Fe3O4 (7.33 wt%)@PANI (magnetic fluid: 15 ml) | Hollow PANI prepared by using PS microspheres as hard template and decorating Fe3O4 on its surface. | Paraffin filled with with a sample (loaded with 7.33 wt% Fe3O4) content of 75% | 2–18 GHz | RmaxL: −15.6 dB | 8.0 GHz | 347 |
| Fe3O4@PPy | In situ polymerization method | 60 wt% of composites blended with paraffin wax | 2–18 GHz | RmaxL: −52.01 dB in 25 wt% of paraffin wax loaded sample of 3.1 mm thickness | 2.72 GHz (thickness: 3.1 mm) | 348 |
| Fe3O4/PPy double-carbonized core–shell-like composite | Rapid microwave assisted carbonization process | — | 2–18 GHz | RminL: −26 dB at 16 GHz (thickness: 1.6 mm) | 4.64 GHz (thickness: 1.6 mm) | 349 |
| Hollow core–shell Fe3O4@PPy | Solvothermal process, followed by in situ polymerization (aniline monomer: 170 μL) | 50% of nanocomposite by wt in paraffin | 2–18 GHz | RminL: −84.92 dB at 3.87 mm | 4.20 GHz at 2.38 mm | 350 |
| Fe3O4–PE@PANI hollow sphere | Electrostatic self-assembly approach | 50 wt% in paraffin | 0.5–15 GHz | RminL: −6.5 dB at 14.3 GHz | Frequency bandwidth at less than −5 dB (12.5 to 15 GHz) | 352 |
Hollow structure Fe3O4/PANI microspheres (aniline : PS = 1 : 6) |
Three-step synthesis 1.5 and 2.0 mm, the bandwidth below and 4.64 GHz (11.04–15.68 GHz) | 50 wt% in paraffin | 2–18 GHz | RminL: −24.3 dB at 18 GHz (thickness: 1.6 mm) | 2.48 GHz (15.52–18 GHz) for 1.5 mm thickness, 4.64 GHz (11.04–15.68 GHz) for 2 thickness | 353 |
| Hollow poly(aniline-co-pyrrole)–(0.6 g Fe3O4) | Oxidized polymerization of aniline and pyrrole in the presence of Fe3O4 (0.06 g) using non-ionic surfactant as a template | 50 wt% in paraffin | 0.5–10 GHz | RminL : −3 dB at 9 GHz and 10 GHz (thickness: 2 mm) | — | 354 |
| Fe3O4/PANI (hollow 0D/1D) | Hydrothermal treatment and chemical oxidative polymerization | 40% in wax | 2–18 GHz | RminL: −55.03 dB (thickness: 1.84 mm) | 4.88 GHz (thickness: 1.84 mm) | 355 |
| Fe3O4/polyaniline core/shell microspheres (PANI shell thickness: 100 nm) | In situ polymerization method | 50 wt% in paraffin | 1–18 GHz, | RmaxL: −37.4 dB at 15.4 GHz | — | 356 |
| Fe3O4-PEDOT microspheres (EDOT/Fe3O4 vol. fraction: 20%) | Two-step method | Paraffin wax | 2–18 Ghz | RminL: ∼−30 dB at 9.5 GHz (thickness: 4 mm) | — | 357 |
| Core–shell Fe3O4−polyaniline | In situ polymerization of aniline in the presence of dodecyl benzenesulfonic acid | 40% Fe3O4−polyaniline in paraffin wax | 0.03–18 GHz | RoptimalL: −35.1 dB at 16.7 GHz (thickness: 1.7 mm) | — | 358 |
| Core–shell Fe3O4@Polypyrrole | Process comprising etching (time: 5 min), polymerization and replication | 50 wt% filler in paraffin | 2–18 GHz | RmaxL: −41.9 dB (99.99%) at 13.3 GHz (thickness: 2.0 mm) | 6.0 GHz (12.0–18.0 GHz). | 359 |
| Core–shell Fe3O4@Polypyrrole microspheres (pyrrole/Fe3O4 ratio = 20) | Chemical oxidative polymerization in the presence of polyvinyl alcohol and p-toluenesulfonic acid | 50% filler in paraffin wax | 2–18 GHz | RmaxL: −31.5 dB (99.99%) at 15.5 GHz (thickness: 2.5 mm) | 5.2 GHz (12.8–18 GHz) | 360 |
| Core–shell structure BaFe12O19@PANI | 30 vol% paraffin wax and 70 vol% powdered filler | In situ polymerization method (aniline: 400 μL) | 2–18 GHz | RmaxL: −65.354 dB at 17.28 GHz (thickness: 1.47 mm.) | 2.3 GHz | 361 |
| Polythiophene nanofibers coated on MnFe2O4/Fe3O4 (core–shell) | Co-precipitation and in situ polymerization | — | 8.0–12.0 GHz | RminL: −21 dB at 12 GHz (thickness: 1.5 mm) | Whole X-band | 362 |
| CoSe2@Polythiophene core–shell | Hydrothermal followed by in situ polymerization | 10 wt% mixed with PVDF | 2–18 GHz | RminL: −55.40 dB (thickness: 1.76 mm) | 5.8 GHz (thickness: 1.76 mm) | 363 |
| rGO/Ni0.5Co0.5Fe2O4@PEDOT | In situ oxidative polymerization | — | 12.4–18.0 GHz | SET: 38.79 dB | Broad absorption bandwidth | 364 |
| 3D graphene-supported Fe3O4-coated by polypyrrole | One-step chemical reduction method (GO to Fe3O4@PPy) wt ratio = 1 : 3 |
Composites soaked into molten paraffin | 2–18 GHz | RminL: −40.53 dB at 6.32 GHz (thickness:2.5 mm) | 5.12 GHz (thickness: 2.5 mm) | 365 |
| Prism-shaped hollow carbon decorated with polyaniline | Carbonization and in situ polymerization | 30 wt% filler in wax | 2–18 GHz | RminL: −64.0 dB at 11.1 GHz (thickness: 2.5 mm) | 5.0 GHz (9.5–14.5 GHz) | 366 |
| Core–shell PPy@MoS2 | Combining chemical oxidative polymerization and hydrothermal process | 40 wt% filler in paraffin | 2–18 GHz | RoptimalL: −49.1 dB at 6.1 GHz (thickness: 2.5 mm) | 6.4 GHz (11.5–17.5 GHz) at 2.5 mm | 367 |
| PPy@PANI | Polymerization of aniline on the surface of PPy microspheres | 50 wt% filler in paraffin | 2–18 GHz | RmaxL: −34.8 dB at 13.9 GHz (thickness: 2 mm) | 4.7 GHz (11.9–16.6 GHz) | 368 |
| Hollow ZnxFe3−xO4@Polyaniline | Solvothermal followed by in situ chemical oxidation polymerization (ZnxFe3−xO4 : aniline ratio = 0.5 : 1) |
50 wt% filler in paraffin wax | 2–18 GHz | RminL: −59.44 dB at 11.04 GHz (thickness: 2.31 mm) | 4.65 GHz (13.35–18.0 GHz) for thickness of 1.72 mm. | 369 |
| Waxberry-like Carbon@Polyaniline microspheres | Via dilute polymerization | 30 wt filler in paraffin wax | 2–18 GHz | RminL: −59.6 dB at 15.5 GHz (thickness : 2.2 mm) | 5.4 GHz (12.6 to 18 GHz) for thickness of 2.2 mm. | 370 |
| CNTs/polyaniline (shell) | Hybrid powders with wax at 10 wt% loading | In situ polymerization (mass ratio of CNTs/PANI:1 : 2) |
2–18 GHz | RminL: −41.5 dB at 9.5 GHz (thicknesses: f 2 mm) | 5.1 GHz at thicknss of 2.0 mm. | 371 |
| PPy (shell)@Carbon microsphere (CMC) | In situ polymerization | 40 wt% of composite corresponding to 0.6 g of CMC in paraffin wax | 2–18 GHz. | RmaxL: −38.1 dB at 11.6 GHz (thickness: 3.00 mm) | 11.17 to 12.26 GHz (thickness of 3.00 mm) | 372 |
| Core shell PEDOT/barium ferrite | In situ emulsion polymerization | — | 12.4–18 GHz | SEA: 22.5 dB at 15 GHz with minimal reflection loss of 2 dB | — | 373 |
| PANI-coated bagasse fiber (BF) core–shell heterostructure | One-step in situ polymerization of aniline in the dispersed system of BF | Mass ratio of BF/PANI to paraffin = 40 : 60 |
8.2–12.4 GHz | EMI SE: 28.8 dB (thickness: 0.4 mm) | — | 374 |
| Polyaniline-coated MWCNT | In situ polymerization | — | 12.4–18.0 GHz | SET: −27.5 to −39.2 dB | — | 375 |
| Polyaniline@Helical-CNTs with dual chirality | In situ polymerization | Mass ratio of the samples to wax: 3 : 7 |
2–18 GHz. | RmaxL: −32.5 dB at 8.9 GHz (thickness: 3.7 mm) | 5.1 GHz (from 7.1 to 11.2 GHz). | 376 |
| Hollow PPy microspheres@Fe3O4/CNTs | Spray-dry method | Mass ratio of powder with paraffin: 1 : 4 |
2–16 GHz | RmaxL: −51.8 dB at 8.8 GHz (thickness: 2.38 mm) | 2.24 GHz (7.76 GHz to 10 GHz) | 377 |
| Hollow PPy/Ni/PVDF microspheres | Spray phase inversion method | Mixing samples with paraffin wax in a 1 : 8 wt ratio |
18–40 GHz | RminL: −47.2 dB at 25.36 GHz and −39.8 dB at 31.30 GHz | 18–40 GHz (thickness: 1.0–3.5 mm) | 378 |
| PPy@FeCo@PPy nanotubes | Combination of electroless plating and oxidative polymerization | Mass fraction of 15 wt% dispersed in the paraffin | 2–18 GHz | RminL: −50.5 dB (thickness: 2.0 mm) | 5.7 GHz (thickness: 2.0 mm) | 379 |
| 1D double-shell PPy@Air@MnO2 nanotubes | 50 wt% in paraffin | Dispersion and self-assembly method | 2–18 GHz | RmaxL: −52.49 dB at 8.88 GHz (thickness: 2.94 mm) | 3.84 GHz (thickness: 2.94 mm) | 380 |
Hollow-spherical composites of PANI/CoS/carbon nanodots (molar ratio of 3 : 1 : 1) |
30 wt% in paraffin wax | Via in situ polymerization in the presence of magnetic field | 2–18 GHz | RmaxL: −24 dB at 14 GHz under external applied field of 0.5 T (thickness: 3 mm) | 1.92 GHz | 382 |
Fe3O4@Carbon@PANI (Fe3O4@C: Aniline = 1 : 9 wt/wt) |
Multiple steps | — | 2–8 GHz | RL: ∼33 dB SET: ∼65 dB | — | 383 |
| Fe3O4@SiO2@PPy | Multistep | Mass ratio of products and paraffin = 3 : 7 |
2–18 GHz | SET: ∼32 dB (thickness: 1 mm) | — | 384 |
| γ-Fe2O3@PEDOT | Reaction of hydrofluoric acid and and γ-Fe2O3@SiO2@PEDOT | Mass ratio of γ-Fe2O3@PEDOT and paraffin = 3 : 7 |
2–18 GHz | RminL: −44.7 dB at 12.9 GHz with a matching layer thickness of 2.0 mm | 4.3 GHz (10.8–15.1 GHz) | 385 |
| Co@Hollow carbon nanospheres@Polyaniline | Mixed with paraffin in mass ratio of 1 : 2 |
Soft template, switching liquid phase transport and in situ polymerization method | 2–18 GHz | RminL: −43.63 dB (matching thickness: 2.8 mm) | 9.75 GHz (8–17.5 GHz) at a matched thickness of 2.8 mm | 386 |
| FeNi@C@Polyaniline | Combining the arc-discharge process and an in situ chemical oxidative polymerization reaction | FeNi@C@Polyaniline (40 wt%) mixed with paraffin | 2–18 GHz | RminL: −49.2 dB at 16.6 GHz for a thickness of 1.3 mm | 5 GHz (13–18 GHz) for the thickness of 1.4 mm | 387 |
| PS@PANI | Solution mixing | — | 100 kHz–20 GHz | EMI SE: ∼32 dB at 8 GHz (thickness: 0.5 mm) | — | 388 |
| PPy nanotubes/NR/NBR (90/10) | 5.24 wt% in paraffin | Mixing technology | 8.2–12.4 GHz | RminL: −56.67 dB (thickness:2.9 mm) | 3.7 GHz (thickness:2.9 mm) | 389 |
| γ-Fe2O3/(SiO2)x–SO3H/polypyrrole core/shell/shell microspheres | Sol–gel process and an in situ polymerization | 70% in paraffin wax | 2–18 GHz | RmaxL: −43.1 dB (15.1 GHz), (thickness: 4 mm) | 6.1 GHz (11.9–18.0 GHz) | 390 |
| Core/shell/shell-structured Ni/C/polyaniline | Modified arc discharge method and a chemical polymerization method | 40 wt% in paraffin | 2–18 GHz | RoptimalL: −9.3 dB at 6.2 GHz (thickness: 3 mm) | 5 dB (3.4–18 GHz) | 391 |
| Fe3O4 microsphere@Graphene nanosheets@PANI nanorods | Hydrothermal and in situ polymerization methods | 30% in paraffin | 2–18 GHz | RmaxL: −43.7 dB at 10.7 GHz with a thickness of 3 mm | 5.4 GHz (from 6.8 to 12.2 GHz) | 392 |
| TiO2@Fe3O4@PPy | Sequential process of solvothermal treatment and polymerization | — | 2–18 GHz | RmaxL: −61.8 dB (thickness: 3.2 mm) | 6.0 GHz (X and Ku band) at 2.2 mm thickness | 393 |
| CoNi@SiO2@PPy | Three-step reaction: | — | 8.2 to 12.4 GHz | RminL: −34.19 dB at 9.59 GHz (thickness 2.12 mm) | Entire X-band (8.2–12.4 GHz) | 394 |
| SiCNWs@MnO2@PPy heterostructures | Chemical vapor deposition and two-step electrodeposition process | — | 2–18 Ghz | RminL: −50.59 dB (Matching thickness: 2.41 mm) | 6.64 GHz (matching thickness: 2.46 mm) | 395 |
| Ni/PANI/RGO | Hydrothermal followed by in situ polymerization | — | 2–18 GHz | RmaxL: −51.3 dB at 4.9 GHz with 3.5 mm thickness | 3.1 GHz (3.3 to 6.4 GHz) | 396 |
| Fe3O4@PEDOT microspheres/RGO | Multiple steps | 50 wt% in paraffin | 2.0–18.0 GHz | RmaxL: −48.8 dB at 9.12 GHz (matching thickness:2.9 mm) | 4.32 GHz (matching thickness:2.9 mm) | 397 |
| Core–shell NiCo2O4@Polypyrrole nanofibers/RGO | 50 wt% in paraffin | Combination of multiple steps | 2.0–18.0 GHz | RminL: −61.20 dB at 14.26 GHz a (thickness:1.56 mm) | 4.90 GHz at 1.57 mm | 398 |
| γ-Fe2O3 decorated RGO in PANI core–shell tubes | Aniline to Fe2O3-decorated rGO weight ratios = 1 : 3 |
Multiple steps | 8.2–12.8 GHz | SET: ∼51 dB) (thickness: 2.5 mm) | — | 399 |
| N-doped graphene@PANI nanorod arrays modified with Fe3O4 | Hydrothermal reaction | 25 wt% of the sample in paraffin | 2–18 GHz | RmaxL: −40.8 dB at 14.8 GHz with thickness of 2.7 mm | 5.1 GHz (10.4 to 15.5 GHz) | 400 |
| PANI/GO/Fe3O4 | In situ polymerization | 50% in paraffin wax | 2–18 GHz | RmaxL: −53.5 dB at 7.5 GHz (thickness: 3.91 mm) | 2.8 GHz (thickness: 3.91 mm) | 401 |
| PANI/carbonyl iron powder (CIP)/Fe3O4 | Mechanical mixing PANI/CIP composite with PANI/Fe3O4 composite with mass ratio of 7 : 3 |
— | 0.5–18 GHz | RmaxL: −48.3 dB at 9.6 GHz (thickness: 1.76 mm) | — | 403 |
| Fe3O4@SiO2@PPy | Microemulsion polymerization method | Composites mixed paraffin with 15 wt% | 2–18 Ghz | RminL: −40.9 dB at 6 GHz (thickness: 5 mm) | 6.88 GHz (11.12–18 GHz) | 404 |
Fe3O4/C/PPy (Fe3O4/C : PPy: 2 : 8 wt/wt) |
Hydrothermal and chemical oxidative polymerization method | — | 1–8.5 GHz | EMI SE: >28 dB (thickness: 0.8 mm) | — | 405 |
| PANI@Natural graphitic flakes (NGF)/MWCNT | In situ by ball milling | 10 wt% of MWCNTs | 12.4–18.0 GHz | EMI SE: −98 dB | — | 406 |
| PEDOT@RGO/Co3O4 | Two-step method | 50 wt% of paraffin | 2–18 GHz | RmaxL: −51.1 dB (10.7 GHz) at thickness of 2.0 mm | 3.1 GHz (9.4–12.5 GHz) | 407 |
| MWCNT/CuO/Fe3O4/PANI (wt ratios of CuO/Fe3O4/PANI to MWCNT = 1.5) | Step by-step approach | 25% filler in paraffin | 8.2–18 GHz | RminL: −87.4 dB (thickness: 3 mm) | 6 GHz (12–18 GHz) | 408 |
| Graphene@Fe3O4@WO3@PANI | Simple hydrothermal method and chemical oxidation polymerization | Composite blended with 70 wt% wax | 2–18 GHz | RmaxL: −46.7 dB at 9.4 GHz (thickness: 4 mm) | 1.8 GHz (12.4–14.2 GHz) at thickness of 1.5 mm | 409 |
| Graphene@Fe3O4@PANI@TiO2 | Hydrothermal method and in situ polymerization | 50 wt% in paraffin | 2–18 GHz | RmaxL: −41.8 dB at 14.4 GHz (thickness: 1.6 mm) | 3.5 GHz | 410 |
| Heavy metal | Sources | Health effects | |
|---|---|---|---|
| Essential heavy metal | Zinc (Zn) | Oil refining plumbing, brass manufacturing | Gastrointestinal disorders, kidney and liver abnormal functioning |
| Copper (Cu) | Copper polishing plating, printing | Abdominal disorders, metabolic activity abnormalities | |
| Iron (Fe) | High intake of iron supplements & oral consumption | Vomiting, diarrhea, abdominal pain, dehydration & lethargy | |
| Cobalt (Co) | Hip alloy replacement case | Haematological, cardiovascular hepatic, endocrine | |
| Non essential heavy metal | Chromium (Cr) | Steel fabrication, electroplating textile | Lung disorders, (bronchitis, cancer), renal and reproductive system |
| Lead (Pb) | Batteries, coal combustion, paint industry | Serious effects on mental health (Alzheimer's disease), nervous system | |
| Arsenic (As) | Atmospheric deposition, mining, pesticides | Highly effects dermal region (cancer), brain & cardiac problems | |
| Mercury (Hg) | Coal combustion, fish, mining, paint industry, paper industry, volcanic eruption | Sclerosis, blindness, Minamata disease, deafness, gastric problems, renal disorders | |
| Cadmium (Cd) | Plastic, fertilizers, pesticides | Osteo related problems, prostate cancer, lung diseases, renal issues |
In view of this, heavy metal ions can be removed from wastewaters/aqueous solution by using different adsorbents. Intrinsically conducting polymers, especially polyaniline and polypyrrole, have played an excellent role as adsorbents in the removal of different heavy metal ions from contaminated aqueous solutions.81–85,413 This is ascribed to their several advantages, such as simple synthesis, excellent environmental stability, chemical versatility, biocompatibility, low cost, the presence of functional groups that facilitate their modification, and functionalization by doping and composite formation to favor the adsorption process by tuning their properties.85,414 Furthermore, the hollow morphology of ICPs, especially polyaniline, can be effective for the adsorption of various pollutants such as heavy metals and dyes due to a large surface area. In addition, hollow ICP-based composites and core–shell nanomaterials have been reported as good adsorbents for removing heavy metal pollutants from wastewater due to their unique physical and chemical properties.
C– groups through sharing of their lone pair of electrons. In addition, polyacrylonitrile/polyaniline core/shell nanofiber mat,422 sulfonated poly(arylene ether nitrile)/polypyrrole core/shell nanofibrous mat,423 Ag-P/Ppy core–shell composite,424 polypyrrole-wrapped oxidized MWCNTs,425 polyaniline-coated ethyl cellulose,426 and polypyrrole-coated halloysite nanotube clay nanocomposite427 have also been used as adsorbents in the efficient removal of toxic Cr(VI) from aqueous solution.Fe3O4/PANI microspheres were fabricated through the interfacial polymerization and used as adsorbent in removing about 94% of Cr(VI) ions from water.428 The adsorption isotherm followed the Langmuir isotherm mode (qm: 200 mg g−1), and pseudo-second-order kinetics. Fe3O4/PANI microspheres. In addition, Fe3O4/PANI has been evaluated for its regenerability and reusability to remove adsorbed Cr(VI) ions using NaOH aqueous solution. These studies have shown the adsorption capacity of Fe3O4/PANI microspheres retained 90% of the initial value after reusing five times. It may be interesting to mention that the regeneration of Fe3O4/PANI microspheres using hydrochloric acid is not possible as it degrades the polyaniline and dissolves the Fe3O4. In another study, Fe3O4/polypyrrole nanotubes prepared by a one-pot process exhibited a Cr(VI) adsorption capacity of ∼451.45 mg g−1.429 This suggested that the adsorption process takes place due to ion exchange and chelation. Furthermore, the existence of −NH+ on the Fe3O4/PPy nanotubes partially reduced Cr(VI) to Cr(III). Fe3O4/PPy nanotubes also retained about 90% of the initial removal efficiency after 5 adsorption/desorption cycles. According to this, adsorption of Cr(VI) on the Fe3O4/PPy nanotubes involved ion exchange and chelation. As a result, Cr(VI) was partially reduced to Cr(III) due to the existence of −NH+ on the Fe3O4/PPy nanotubes.
In another study, Fe3O4-coated polypyrrole (initial concentration: 200 mg L−1) showed 100% adsorption for 200 mg L−1 Cr(VI) aqueous solution corresponding to pH 2.430 The proposed mechanism for the removal of Cr(VI) was guided by ion exchange and reduction on the surface of the nanocomposite. The kinetics studies indicated a pseudo-second-order rate model and Langmuir model predicted from the fitting of isotherm data. The maximum adsorption capacity of Polypyrrole/Fe3O4 magnetic nanocomposite increased from 169.4 to 243.9 mg g−1 corresponding to the temperature change from 25 °C to 45 °C, respectively. The possible mechanism was elucidated based on XPS studies. According to this, the possible mechanism for Cr(VI) removal by the PPy/Fe3O4 could be due to ion exchange and reduction on the surface. Several other adsorbents comprising magnetite arginine-functionalized polypyrrole,431 magnetic particle-coated PPy and PANI,432 polypyrrole-coated Fe3O4,433 polypyrrole-modified natural corncob-core sponge,434 polyaniline-coated protonic titanate nanobelt,435 and MnO2-coated polyaniline nanofibers436 also successfully removed hexavalent chromium from water.
Du et al.437 synthesized core–shell polypyrrole/hollow mesoporous SiO2 particles by in situ polymerization to study the removal of Cr(VI) from aqueous solution that exhibited the maximum adsorption capacity of Cr(VI) of ∼322 mg g−1 at 25 °C following the quasi-second-order kinetic model and the Langmuir isotherm model. In another study, deposition of PANI on the surface of ThO2 has been validated by TEM analysis.438 Further investigations revealed the adsorption of Cr(VI) on this core shell composite to be dependent on the solution pH. The kinetic model and adsorption process fitted well with the pseudo-second-order and Langmuir model (qm: 141 mg g−1). Polyacrylonitrile/polypyrrole core/shell nanofiber mat exhibited high selectivity for Cr(VI) compared with the Ni(II) and Cu(II) ions in the solution.439 The high removal efficiency of hexavalent chromium has also been reported on L-cystine-doped glucose carbon spheres (GCS)@PPy,440 PANI@Nano hollow carbon spheres,441 Polypyrrole@Attapulgite,442 copper slag@polyaniline,443 polyaniline@Ni(OH)2,444 PPy@MgFe2O,445 polypyrrole/graphene oxide,446 and PANI@Almond shell biocomposite.447
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| Fig. 25 (a) Effect of initial concentration of Cr(VI) at a different temperature (PPY PANI@RHA dose: 0.8 g L−1; contact time: 300 min; agitation speed: 200 rpm; pH∼2), (b) effect of adsorbent dose at pH 2 and without pH (∼6.8) adjustment (initial Cr(VI) concentration: 50 mg L−1; contact time: 300 min; agitation speed: 200 rpm; temperature: 303 K), (c) effect of initial solution pH on % removal of Cr(VI) by PPY–PANI@RHA, PPY–PANI and RHA adsorbents (Initial Cr(VI) concentration: 50 mg L−1; contact time: 300 min; agitation speed: 200 rpm; temperature: 303 K), and (d) variation of zeta potential of PPY–PANI@RHA at different pH.448 Reproduced with permission from RSC. | ||
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| Fig. 26 Representation of possible Cr(VI) adsorption by PPY–PANI@RHA.448 Reproduced with permission from RSC. | ||
In another study, the adsorption of Cr(VI) in aqueous solution on a polypyrrole-decorated graphene-silica (Graphene/SiO2@Polypyrrole) composite exhibited the maximum adsorption capacity corresponding to 429.2 mg g−1 (298 K) at pH 2.449 The adsorption of Cr(VI) on graphene/SiO2@ polypyrrole fitted well with the pseudo-second-order kinetic and Langmuir isotherm model. The simultaneous removal of methyl orange and Cr(VI) from water has also been evaluated based on PPy@Magnetic chitosan adsorbent.450 Da Rocha et al.451 reported the formation of a layer of PPy chains on the PMMA/rice husk ash (RHA) fibers and observed a Cr(V) removal capacity qe of 363.63 mg g−1 (after 150 min) at pH 2. In another study, core–shell PS/PANI-Fe3O4 adsorbent removed 100% Cr(VI) corresponding to pH: 2, adsorbent: 0.05 g, initial concentration of Cr(VI): 5 mg L−1, total volume: 30 mL and 120 min, respectively.452 The removal of hexavalent chromium from water has also been studied using a polyaniline/wood sawdust/polyethylene glycol composite.453 Yao et al.454 prepared Fe3O4@Polypyrrole nanospheres with a hierarchical porous structure anchored on graphene nanosheets and noted the excellent adsorption capability in Cr(VI) removal (qm: ∼348.4 mg g−1) due to the synergic effect between graphene and Fe3O4@polypyrrole. The adsorption kinetics was explained on the basis of pseudo-second-order kinetics. In addition, the fabricated adsorbent was found to be stable and retained ∼72.2% removal efficiency after six cycles.
The large specific surface area of γ-Fe2O3@Chitosan@PPy accounted for the maximum Cr(VI) adsorption capacity of 301.2 mg g−1.455 The magnetic nanocomposite removed 100% Cr(VI) in aqueous solution, and this was described as based on exchange and chelation as the dominant interaction mechanisms.
Vatani and Eisazadeh460 coated polythiophene on polystyrene and poly(vinyl chloride) to investigate the role they play as adsorbents in the removal of Pb(II) from aqueous solution. They observed the higher removal efficiency of PTh/PVC compared with PTh/PS nanocomposites under the optimum conditions (pH: 2, initial concentration of cations 100 mg−1, equilibrium time: 30 min). Chen et al.461 prepared a PTh/MnO2 composite with MnO2 as the core and PTh as the shell for the selective adsorption towards Pb2+, Zn2+ and Cu2+ from industrial wastewater in the aqueous medium. These findings showed the adsorption capacities of Pb2+, Zn2+ and Cu2+ (within 30 min) were found to be 82.10, 30.72 and 60.79 mg g−1, respectively. These findings have been explained on the basis of a synergistic effect between PTh and MnO2.
Binary composites have been prepared following the coating of polyaniline for their applications in the removal of Pb(II) ion in water. Fe3O4 particles coated with polyaniline showed the maximum lead adsorption capacity of Pb(II) as 114.9 mg g−1.462 Pb(II) ions were found to be almost completely removed under the optimum conditions (initial concentration of lead(II): 50 ppm, adsorbent dosage: 3 mg, pH: 9.3).
According to Shakhsari et al.,463 CoFe2O4@PANI removed 98% of Pb at 25 °C from water under the optimum condition of initial concentration of metal ions (17 mg L−1), adsorbent dose (1 g), pH (7) and time (120 minutes). The adsorption kinetics followed the quasi-first-order model, and data fitted well with the Freundlich isotherm. Polypyrrole-coated ZnO-NiO nanocomposites have also been investigated as adsorbents for enhanced removal of Pb(II) from aqueous solution and wastewater.464 The possible mechanism of Pb(II) adsorption on the PPy/ZnO-NiO adsorbent has been explained based on ion exchange, electrostatic attraction, and the formation of metal complexes. The reusability and regeneration experiments after six adsorption–desorption cycles have shown a decrease in the adsorption and desorption of Pb(II) from 98.7% to 77.8% and 92% to 67%, respectively. Naphthalene sulfonic acid-doped polyaniline@Ni0 composite (0.5 g L−1) achieved 90.9% removal efficiency of Pb(II) ions in aqueous solution (pH: 5).465 The findings based on the isotherm data supported the Langmuir isotherm model, with maximum Pb(II) removal capacity of 414.6 mg g−1 at 25 °C. Fe3O4/polyaniline hollow microspheres have been fabricated and used as adsorbent in the uptake of Pb2+ from aqueous solution.466 It followed the pseudo-second-order kinetics and adsorption data agreed well with the Langmuir isotherm.
Zare et al.467 used a poly(aniline-co-3-aminobenzoic acid)-based magnetic core–shell nanocomposite and observed the maximum adsorption capacity of Pb(II) to be 138.31 mg g−1 in an aqueous solution. The findings were also found to be in agreement with the pseudo-first order and Freundlich isotherm. Pomegranate-like MnO2@PANI using 0.1 mol L−1 of KMnO4 has been successfully synthesized according to the procedure described in Fig. 27(a).468 Subsequently, the variation of removal ratios (q) of Pb(II) ions with PANI nanoflowers (NF), commercial MnO2, PANI spheres prepared with cavities and pomegranate-like MnO2@PANI spheres as adsorbents has been studied, and the findings are displayed in Fig. 27(b and c). It is noted that respective removal ratios (q) values correspond to 36.1%, 54.9%, 71.2%, and 99.2%, respectively. MnO2@PANI showed the maximum sorption capacity of 309.6 mg g−1. Such excellent adsorbability of MnO2@PANI spheres was ascribed to the presence of mesoporous structures of PANI spheres with more exposed adsorption sites towards Pb(II) ions. Alternatively, enhancing the sorption ability of Pb(II) ions could be ascribed to the interaction (chelation/physisorption) between MnO2 and PANI contributing synergistically. The removal ratios of different heavy metal ions on PANI and PANI@MnO2 as adsorbents were also tested for Ni(II), Cd(II), Cu(II), Zn(II) heavy metal ions. Subsequent findings revealed higher removal ratios of these heavy metals for the MnO2@PANI hybrids compared with PANI nanospheres and also agreed well with the earlier results on Pb(II) ion adsorption. Chemically modified polythiophene with copper nanoparticles and polyvinylpyrolidine-sulfonic acid469 and polypyrrole-iron oxide–seaweed470 exhibited the adsorption capacity of lead from aqueous solution of 111 mg g−1 and 333.33 mg g−1, respectively.
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| Fig. 27 (a) Schematic representation of the preparation of pomegranate-like MnO2@PANI sub-microspheres, (b) removal ratios of Pb(II) ions with PANI(NF), MnO2, PANI sphere and MnO2@PANI as adsorbent, (c) removal ratios of Pb(II) ions with MnO2@PANI-1, to MnO2@PANI-2, MnO2@PANI and MnO2@PANI-4 as adsorbent. Adsorption conditions: [Pb(II)] = 60 mg L−1, [adsorbent] = 0.5 g L−1, pH = 5.0 ± 0.1, T = 25 °C, 12 h.468 Reproduced with permission from Elsevier. | ||
PANI/Jute fiber composites exhibited effective Cr(VI) and Cd(II) ion decontamination from water.471 The core/shell like structure of the PTh/SiO2 composite exhibited superior selectivity to separate and recycle Zn2+ among multiple ions (Pb2+, Zn2+, Cu2+) in wastewater due to the synergistic effect.472 Sun et al.473 studied the adsorption of Cu(II), Pb(II) and Ni(II) on PANI@Aminopropyltriethoxysilane (APTS)-Fe3O4/Attapulgite composite and observed the maximum adsorption capacity of 189.03, 270.27 and 142.86 mg g−1, respectively. The reusability performance of PANI@APTS-Fe3O4/Attapulgite after 5 times of use showed a slight decrease for all the heavy metals (Cu(II): 84% to 79%, Pb(II): 87% to 81%, Ni(II): 63% to 56%). SiO2-coated magnetic graphene oxide modified with a pyrrole-thiophene copolymer showed a maximum adsorption capacity for Cu(II), Pb(II), Zn(II), Cr(III) and Cd(II) in aqueous solution corresponding 201, 230, 125, 98 and 80 mg g-1, respectively.474 High-temperature hydrothermally prepared polypyrrole-derived N-doped carbon nanotubes decorated with fish scale-like MoS2 nanosheets showed a significantly much higher removal capacity for Pb(II) (qm: 381.87 mg g−1) in waste water.475 Based on XPS studies, the following possible mechanism for the adsorption of Pb(II) on the C-Ppy@MoS2 has been proposed:
| Mo(IV) + 2H+ + 4e− + 4H2O (aq) → 5H2 (g) + MoO42−(VI) |
| MoO42−(VI) + Pb2+ + S → PbMoO4−xSx (s) |
It is believed that the protons produced in the above reaction may have a driving effect on the adsorption process. The unique structure of the fish scale-like MoS2 nanosheets on the C-PPy nanotubes accounts for the adsorption of Pb(II).
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| Fig. 28 (a) Effect of adsorbent dose (Experimental conditions: C0: 1000 μg L−1; pH∼7; contact time: 240 min; T: 300 ± 3 K), (b) effect of contact time (Experimental conditions: adsorbent dose: 1 g L−1; C0: 1000 μg L−1; pH ∼7; T: 300 ± 3 K), (c) influence of initial solutions pH (Experimental conditions: adsorbent dose: 1 g L−1; C0: 1000 μg L−1; contact time: 240 min; T: 300 ± 3 K) on As(III) and As(V) removal efficiency using PNHM/Fe3O4-40, (d) ζ-potential of PNMH/Fe3O4-40 under various pH conditions.476 Reproduced with permission from Nature Publication. | ||
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| Fig. 29 Schematic representation of arsenic adsorption mechanism in aqueous solution.476 Reproduced with permission from Nature Publication. | ||
Further studies have shown an increase in the adsorption of As(III) and As(V) on the surface of PNHM/Fe3O4-40 on increasing the temperature from 293 K to 313 K.477 In another study, Fe3O4/PANI was prepared by the chemical polymerization method.478 SEM studies confirmed the formation of PANI on the surface of Fe3O4 grains. This core–shell structure of Fe3O4/5%PANI exhibited the highest arsenic adsorption ability at pH 7 and 300 K. According to Muhammad et al.,479 the Fe3O4/PANI core–shell composite can be applied as an effective adsorbent for the removal of hexavalent chromium and divalent nickel from water. Polyaniline/Fe0 (ref. 480) and iron-functionalized polythiophene (PTh@Fe)481 were also reported as excellent adsorbents for the removal of arsenic from aqueous solutions. In addition, heavy metals from aqueous solution have also been removed by polyaniline coated on sawdust,482 Fe3O4-embedded poly(thiophene),483 PAN/PANI-Nylon,484 2-aminopyridine functionalized magnetic core–shell Fe3O4@Polypyrrole composite,485 and Fe3O4/SiO2/PANI-SDBS nanocomposite.486 Fe3O4@PPy core–shell functionalized with tetrakis (4-carboxyphenyl) porphyrin (TCCP) prepared in multiple steps displayed 100% efficiency for Hg(II) removal in water.487 Investigations have also been reported on the adsorptive removal of Hg2+ by polyaniline/attapulgite.488 Ren et al.489 prepared Fe3O4@Polypyrrole@Sodium dodecyl sulfate core@shell composite and observed the selective removal of Mn(VII) and other dyestuffs from wastewater (Table 3).
| Metal ions | Adsorbent used | Water type | Preparative method | Experimental conditions on removal of metal ions | qm (mg g−1) | Removal isotherm fitted to | Kinetics data fitted to (k) | Ref. |
|---|---|---|---|---|---|---|---|---|
| Cr(VI) | Hollow PANI micro/nano sphere | Waste water | Monomer polymerization in alk solution with Triton X-100 as soft templates | Cr(VI): 1.2 m mol L−1 (20 mL), dosage: 10 mg, pH 3.0, qe (time): ∼79 mg g−1 (180 min) | 127.88 | Langmuir | Pseudo sec. order | 417 |
| Cr(VI) | Amino acid-doped PANI nanotubes | Aqueous solutions | In situ chemical polymerization | Temp.: 25 °C Cr(VI): 30 mg L−1 (10 mL), dosage: 0.25 g, pH: 7, removal (time): ∼100% (120 min) | 60 | Langmuir | Pseudo sec. order | 419 |
| Cr(VI) | Bamboo-like PPy nanotubes | Aqueous solution | Reactive-template vapor phase polymerization method | Cr(VI): 1.95 mmol L−1 (20 mL), dosage: 3 mg, pH: 3, adsorption capacity (time): ∼9 mmol g−1 (1400 min) | 9.281 mmol g−1 | Langmuir | Pseudo sec. order (0.0031 g mmol−1 min−1) | 420 |
| Cr(VI) | Core–shell polyaniline/polystyrene | Aqueous solutions | Microemulsion polymer of polystyrene followed by in situ polymer of aniline monomer | Temp.: 20 °C Cr(VI): 100 mg L−1 (50 mL), dosage: 250 mg, pH: 2, removal (time): ∼95% (30 min) | 19 | Temkin | Pseudo sec. order (k: 6.27 × 10−3 mg L−1 min−1) | 421 |
| Cr(VI) | Polyacrylonitrile/polyaniline core/shell nanofiber mat | Aqueous solution | Via electrospinning followed by in situ polymerization | Temp.: 25 °C, Cr(VI): 207 mg L−1 (30 mL), dosage: 100 mg, pH: 2, qt (time): 53.4 mg g−1 (12 h) | 71.28 | Langmuir | Pseudo sec. order (k: 7.20 × 10−3 g mg−1 min−1) | 422 |
| Cr(VI) | Sulfonated poly(arylene ether nitrile)/polypyrrole core/shell | Aqueous solution | Electrospinning technique followed by in situ polymerization | Temp.: RT, Cr(VI): 50 ppm (50 mL), dosage: 20 mg, pH: 2, removal (time): 56.5% (4 h) | 165.3 | Langmuir | Pseudo-second order (k: 6.9 × 10−4 g mg−1 min−1) | 423 |
| Cr(VI) | Ag-P/PPy core–shell | Water | In situ chemical oxidative polymerization | Temp.: RT, Cr(VI): 50 mg L−1 (50 mL), dosage: 0.05 g, pH: 2, removal (time): 99.4% (55 min) | 138.5 | Temkin and Redlich Peterson | Pseudo-second order | 424 |
| Cr(VI)C | Polypyrrole-wrapped oxidized MWCNTs | Aqueous solution | In situ chemical polymerization | Temp.: 25 °C Cr(VI): 200 mg L−1 (50 mL), dosage: 0.5 g L−1, pH: 2, removal (time): 100% (300 min) | 294 | Langmuir | Pseudo sec. order (k: 0.0028 g mg−1 min−1) | 425 |
| Cr(VI) | PPy-coated Halloysite nanotube (HNT) clay | Deionized water | In situ polymerization of pyrrole in the dispersion of HNTs | Temp.: 25 °C, Cr(VI): 100 mg L−1 (50 mL), dosage: 1.5 g L−1, pH: 2.0, removal (time); ∼100% (24 h) | 149.25 | Langmuir | Pseudo sec. order (k: 0.019 g mg−1 min−1) | 427 |
| Cr(VI) | Core–shell Fe3O4/PANI microspheres | Water | Interfacial polymerization | Temp.: RT, Cr(VI): 100 mg g−1 (60 mL), dosage: 0.1 g 1, pH: 2, removal (time); ∼86% (180 min) | 200 | Langmuir isotherm | Pseudo sec. order | 428 |
| Cr(VI) | Fe3O4/PPy nanotubes | Aqueous solution | One-pot process | Temp.: 25 °C, Cr(VI): 20 mg L−1 (50 mL), dosage: 0.01 g, pH:1, removal (time); 94.62% (24 h) | 451.45 | Langmuir | Pseudo sec. order | 429 |
| Cr(VI) | Fe3O4-coated PPy | Aqueous solution | In situ polymerization of pyrrole monomer | Temp.: 25 °C, Cr(VI): 200 mg L−1 (50 mL), dosage: 2 g L−1, pH: 2, removal (time); 100% (24 h) | 169.5 | Langmuir | Pseudo-sec. order (k: 0.037 g mg−1 min−1) for [Cr(VI)]: 150 mg L−1 | 430 |
| Cr(VI) | Fe3O4@ arginine-functionalized PPy | Deionised water | In situ polymerization | Temp.: 25 °C. Cr(VI): 200 mg L−1 (50 mL), dosage: 0.05 g, pH: 2, removal (time); ∼100% (1 h) | 322.58 | Langmuir | Pseudo sec. order (k: 6.67 × 10−3 g mg−1 min−1) | 431 |
| Cr(VI) | PPy/γ-Fe2O3 | Aqueous media | Emulsion polymerization | Temp.: RT, Cr(VI): 2.5 mg L−1 (10 mL), dosage: 2 mg, pH: 2, removal (time); ∼100% (1 h) | 208.8 | Langmuir | Pseudo sec. order (k: 2.0 × 10−2 g mg−1 min−1) | 432 |
| Cr(VI) | PANI/γ-Fe2O3 | Aqueous media | Emulsion polymerization | Temp.: RT, Cr(VI): 2.5 mg L−1 (10 mL), dosage: 2 mg, pH: 2, removal (time); ∼100% (1 h) | 195.7 | Langmuir | Pseudo sec. order (k: 7.5 × 10−4 g mg−1 min−1) | 432 |
| Cr(VI) | PPy-modified corncob-core sponge | Aqueous solution | Solution polymerization | Temp.: 25 °C, Cr(VI): 100 mg L−1, dosage: 3 g L−1, pH: 3.5, removal, (time);∼100% (180 min) | 84.7 | Langmuir | Pseudo sec. order (k: 0.0023 g mg−1 min−1): [Cr(VI)]: 50 mg L−1 | 434 |
| Cr(VI) | MnO2-coated polyaniline nanofibers | Aqueous solution | In situ oxidative polymerization | Temp.: 298 K, Cr(VI): 10 mg L−1 (50 mL), dosage: 10 mg, pH: 1, removal (time); ∼96% (60 min) | 158.2 | Freundlich | Pseudo-sec. order (k: 0.0751 g mg−1 min−1) | 436 |
| Cr(VI) | PPy/hollow mesoporous silica | Aqueous solution | In situ polymerization | Temp.: 25 °C, Cr(VI): 400 mg L−1 (25 mL), dosage: 80 mg, pH: 2, removal (time);∼100% (24 h) | 322 | Langmuir | Quasi-second-order | 437 |
| Cr(VI) | Polyacrylonitrile/PPy core/shell nanofiber mat | Aqueous solution | Electrospinning followed by in situ polymerization of pyrrole monomer | Temp.: 25 °C Cr(VI): 200 ppm (30 mL), dosage: 0.20 g, pH: 2, removal (time); 84.5% (12 h) | 61.80 | Langmuir | Pseudo sec. order (k: 1.77 × 10−3 g mg−1 min−1) | 439 |
| Cr(VI) | L-Cystine-doped glucose carbon sphere @PPy | Water | In situ growth method | Temp.: RT, Cr(VI): 100 mg L−1 (100 mL), dosage: 0.050 g, pH: 1, adsorption capacity, qe (time); 209.18 mg g−1, (24 h) | 108.41 | Langmuir | Pseudo sec. order (k: 0.0014 g mg−1 min−1) | 440 |
| Cr(VI) | PANI@Nano hollow carbon sphere | Wastewater | In situ polymerization method | Temp.: 298 K, Cr(VI): 100 mg L−1 (25 mL), dosage: 10 mg, pH: 1, removal (time);100% (300 min) | 250 | Langmuir | Pseudo sec. order (k: 0.284 × 10−3 g mg−1 min−1) | 441 |
| Cr(VI) | PPy/attapulgite core–shell | Aqueous solutions | In situ polymerization on the surface of attapulgite | Temp.: 298 K Cr(VI): 50 mg L−1 (100 mL), dosage: 0.2 g, pH: 3, removal (time): 99.27% (10 min) | 48.45 | Langmuir | Pseudo sec. order (k: 1069 × 10−5 mg−1 s−1) | 442 |
| Cr(VI) | Cu slag@PANI | Aqueous solution | In situ polymerization | Temp.: 303 K Cr(VI): 300 mg L−1 (20 mL), dosage: 0.01 g, pH: 2, absorption capacity (time): 357.68 mg g−1 (24 h) | 343.23 (303 K) | Langmuir | Pseudo sec. order (k: 0.00409 g mg−1 min−1) | 443 |
| Cr(VI) | PANI nanotubes@Ni(OH)2 | Aqueous solution | By depositing Ni(OH)2 on 2-naphthalene sulfonic acid-doped PANI nanotubes surface | Temp.: 25 °C, Cr(VI): 100 mg L−1 (50 mL), dosage: 0.03–0.05 g (50 mL), pH: 4.0, removal (time): ∼100% (24 h) | 625 (25 °C) | Langmuir | Pseudo-sec. order (k: 0.03008 g mg−1 min−1) | 444 |
| Cr(VI) | PPy@5% MgFe2O4 | Water and wastewater | Oxidation method | Temp.: 25 °C., Cr(VI): 100 mg L−1 (10 mL), dosage: 1 g L−1, pH: 3–6, removal (time): ∼93 mg g−1 (600 min) | 138.6 | Langmuir | Pseudo sec order (0.00 21 g mg-1 min−1) | 445 |
| Cr(VI) | PANI@Almond shell | Aqueous solutions | In situ chemical polymerization | Temp.: 298 K, Cr(VI): 50 mg L−1, dosage: 0.5 g L−1, pH: 7, removal (time): 95.86% (120 min) | 335.25 | Freundlich | Pseudo sec. order (k: 0.0273 mg g−1 min−1) | 447 |
| Cr(VI) | PPy–PANI-coated rice husk ash | Aqueous solutions | In situ chemical polymerization | Temp.: RT, Cr(VI): 50 mg L−1 (100 mL), dosage: 0.8 g L−1, pH: 2, removal (time): ∼98% (300 min) | 769.15 | Freundlich | Pseudo sec. order (k: 0.009 mg g−1 min−1) | 448 |
| Cr(VI) | Graphene/SiO2@PPy | Deionized water | In situ polymerization | Temp.: 298 K, Cr(VI): 100 mg L−1 (250 mL), dosage: 100 mg, pH: 2, qe (time): ∼240 mg g−1 (5000 min) | 429.2 | Langmuir | Pseudo sec. order (k: 1.852 × 10−5 min−1) | 449 |
| Cr(VI) | PPy/Fe3O4/chitosan | Water | Co-precipitation followed by in situ polymerization | Temp.: 25 °C, Cr(VI): 100 mg L−1 (50 mL), dosage: 100 mg, pH: 2, q (time): ∼84% (40 min) | 105 | Langmuir | — | 450 |
| Cr(VI) | PMMA/rice husk/PPy membrane | Water | Electrospinning and chemical polymerization | Temp.: 283 K, Cr(VI):10 mg L−1, dosage (membrane): 0.02, mx0.02 m (wt: 0.6 mg), pH: 2.0, removal (time): ∼95% (24 h) | 363.63 | Langmuir | Pseudo sec. order (k: 49.90 mg g−1 min−1) | 451 |
| Cr(VI) | PS/PANI/Fe3O4 | Water | Simultaneous chem. oxidation polymerization and precipitation | Temp.: 303 K, Cr(VI): 5 mg L−1 (30 mL), dosage: 0.05 g, pH: 2.0, efficiency (time): 100% (120 min) | 23.753 | Freundlich | Pseudo sec. order | 452 |
| Cr(VI) | PANI/wood sawdust/PEG | Water | Oxidation polymerization | Temp.: RT, Cr(VI): 50 ppm (50 mL), dosage: 40 g L−1, pH: 5, removal (time): ∼98% (30 min) | 3.2 | Langmuir | — | 453 |
| Cr(VI) | γ-Fe3O4/chitosan/PPy | Aqueous media. | Coprecipitation method + in situ polymerization | Temp.: RT, Cr(VI): 10 mg L−1 (10 mL), dosage: 2 mg, pH: 2, removal (time): 100% (720 min) | 301.2 | Freundlich | Pseudo sec. order (k: 7.12 × 10−5 min−1) | 455 |
| Cr(VI) | PANI/jute fiber | Deionized water | In situ polymerization | Temp.: 25 °C, Cr(VI): 100 mg L−1 (200 mL), dosage: 1.0 g, pH: 2, removal (time): 98% (120 min) | 50 | Langmuir | Pseudo sec order (k: 0.0023 mg g−1 min−1) | 471 |
| Pb(II) | Amino acid-doped PANI nanotubes | Aqueous solutions | In situ chemical polymerization | Temp.: 25 °C [Pb(II):]:30 mg L−1 (10 mL), dosage:0.25 g, pH: 7, removal (time): ∼68% (120 min) | — | — | — | 419 |
| Pb(II) | Hollow polyaniline nanosphere | Deionized water | Chemical polymerization | Temp.: 30 °C, Pb(II): 20 mg L−1 (25 mL), dosage: 20 mg, pH: 7, absorptivity (time): 97% (24 h) | 1589 | Freundlich | — | 456 |
| Pb(II) | Fe3O4/@Py yolk–shell | Water | Multi step | Pb(II): 1 mg L−1 (100 mL), dosage:15 mg, pH: 6, removal (time): ∼96% (30 min) | 65.093 | Langmuir, Freundlich | Pseudo sec. order (k: 0.004 g mg−1 h−1) | 458 |
| Pb(II) | PTh coated on PS | Deionized water | Chemical oxidative polymerization | Temp.: RT, Pb(II): 100 mg L−1 (25 mL), dosage: 0.25 mg, pH: 2, removal (time): ∼85% (30 min) | — | — | — | 460 |
| Pb(II) | PTh coated on PVC | Deionized water | Chem. oxi. polymerization | Temp.: RT, Pb(II): 100 mg L−1 (25 mL), dosage: 0.25 mg, pH: 2, removal (time): ∼85% (30 min) | — | — | — | 460 |
| Pb(II) | PANI/Fe3O4 | Wastewater | In situ polymerization | Temp.: 25 °C, Pb(II): 50 ppm (100 mL), dosage: 3 mg, pH: 9, removal (time): 93% (60 min) | 114.9 | Langmuir | Pseudo sec. order (k: 0.0074 g g−1 min−1) | 462 |
| Pb(II) | CoFe2O4@PANI | Water | Aniline polymerization | Temp.: 25 °C, Pb(II): 17 mg L−1 (50 mL), dosage: 1 g, pH: 7, removal (time): 98% (120 min) | 23.31 | Langmuir | Quasi first order | 463 |
| Pb(II) | PPy-coated ZnO-NiO | Wastewater | Chemical polymerization | Temp.: 298 K, Pb(II): 100 mg L−1 (100 mL), dosage: 25 mg, pH: 5, removal (time): 98.7% (240 min) | 436.48 | Langmuir | Pseudo sec. order (k: 0.00013 mg g−1 min−1) | 464 |
| Pb(II) | PANI nanotubes/Ni0 | Aqueous solution | Immobilisation | Temp.: 25 °C, Pb(II): 100 mg L−1 (20 mL), dosage: 0.5 g L−1, pH: 5.1, removal (time): ∼90% (24 h) | 414.6 | Langmuir | Pseudo sec. order (k: 0.00798 mg g−1 min−1) | 465 |
| Pb(II) | MnO2@PANI | Water | Oxidation polymerization | Temp.: 25 °C, Pb(II): 60 mg L−1 (20 mL), dosage: 0.5 g L−1, pH: 5, removal (time): ∼98% (12 h) | 309.6 | Langmuir | Pseudo sec. order (k: 17.52 g mg−1 min−1) | 468 |
| Pb(II) | PTP/polyvinylpyrolidine (PVP)/sulfonic acid/Cu | Aqueous solution | In situ co-polymerization | Temp.: 298 K, Pb(II): 30 mg L−1 (10 mL), dosage: 3.0 g L−1, pH: 7, removal (time): ∼28 mg g−1 (180 min) | 111.11 | Langmuir | Pseudo sec. order (k: 3.62 × 10−4 g g−1 min−1) | 469 |
| Pb(II) | PPy/Fe3O4/seaweeds | Aqueous solution | In situ chemical oxidative polymerization | Temp.: 40 °C, Pb(II): 100 mg L−1 (50 mL), dosage: 10 mg, pH: 5, removal (time): 97.25% (20 min) | 333.33 | Langmuir | Pseudo sec. order (k: 0.005535 g mg−1 min−1) | 470 |
| Pb(II) | Carbon–PPy@MoS2 | Wastewater | Template method involving five steps | Temp.: 25 °C, Pb(II): 54.26 ppm (100 mL), dosage: 50 mg, removal (time): 100% (10 min) | 381.87 | Langmuir | Pseudo sec order (k: 1.75 × 10−4 g mg−1 min−1) | 475 |
| Pb(II) | Fe3O4/SiO2/PANI-SDBS | Wastewater | Polymerization of aniline | Temp.: 30 °C. Pb(II): 15 mg L−1 (50 mL). dosage: 30 mg, pH: 7.0, removal (time): 94.1% (120 min) | 72.20 | Freundlich model | Pseudo sec. order | 486 |
| As(V) | γ-Fe2O3@PANI | Deionized water | In situ polymerization | Temp.: 298 K, As(V): 20 mg L−1 (100 mL), adsorbent: 0.5 g L−1, pH: 5, qe (time): 0.354 mg g−1 (5 h) | 37.61 | Langmuir | Pseudo sec. order (k: 1.733 g mmol−1 min−1) | 457 |
| As(III) | Hollow PANI microsphere-Fe3O4 (Fe3O4: 40 wt%) | Water | Multiple steps | Temp.: 300 K, As(III): 1000 mg L−1 (100 mL), dosage: 5 g L−1, pH:7, removal (time): 98% (240 min) | 28.27 | Freundlich | Pseudo sec order (k: 0.363 g mg−1 min−1) | 476 |
| As(V) | Hollow polyaniline microsphere/Fe3O4 (Fe3O4: 40 wt%) | Water | Multiple steps | Temp.: 300 K, As(V): 1000 mg L−1 (100 mL), dosage: 2 g L−1, pH:7, removal (time): 100% (240 min) | 83.078 | Freundlich | Pseudo sec order (k: 0.733 g mg−1 min−1) | 476 |
| As(V) | PANI/Fe0 | Aqueous solutions | Polyaniline nanofiber in polymerization media + NaBH4 | Temp.: RT, As(V): 1 mg L−1 (20 mL), dosage: 1 mg L−1, pH: 7, removal (time): 100% (60 min) (24 h) | 227.3 | Langmuir isotherm | Pseudo sec. order (k: 0.01343–0.01714 g mg−1 min−1) | 480 |
| As(III) | PANI/Fe0 | Aqueous solutions | Polyaniline nanofiber in polymerization media + NaBH4 | Temp.: RT, As(III): 1 mg L−1 (20 mL), dosage: 1 g L−1, pH: 7, removal (time): 100% (60 min) | 232.5 | Langmuir isotherm | Pseudo sec. order (k: 0.0332 g mg−1 min−1) | 480 |
| Cd(II) | PANI/jute fiber | Deionized water | In situ polymerization | Temp.: 25 °C, Cd(II): 100 mg L−1 (200 mL) (750 mL), dosage: 1.0 g, pH: 5, removal (time): 99% (120 min) | 140 | Langmuir | Pseudo sec. order (k: 0.0039 mg g−1 min−1) | 471 |
| Cd(II) | PANI-coated sawdust | Wastewater | Mixing method | Temp.: 20.5 °C, Cd(II): 40 mg L−1 (750 mL), dosage: 0.75 g, pH: 6, qe (time): ∼500 mg g−1 (35 min) | 430 | Freundlich | Pseudo sec. order | 482 |
| Cd(II) | Fe3O4/SiO2/PANI-SDBS | Waste water | Polymerization of aniline | Temp.: 30 °C, Cd(II): 15 mg L−1 (50 mL), dosage: 30 mg, pH: 7.0, removal (time): 77.47% (120 min) | 67.84 | Freundlich model | Pseudo sec. order | 486 |
| Mn(VII) | Functionalized-Fe3O4@PPy | Aqueous solution | In situ polymerization of pyrrole monomer on Fe3O4 | Temp.: 20 °C, Mn(VII): 150 mg L−1 (50 mL), dosage: 20 mg, pH: 2, contact time: ∼90% (240 min) | 781.25 | Freundlich | Pseudo sec. order (k: 4.8 × 10−4 g mg−1 min−1) | 485 |
| Mn(VII) | Core@Shell Fe3O4@Polypyrrole@Sodium Dodecyl Sulphate | Complex wastewater | Hydrothermal + in situ polymerization methods | Temp.: 20 °C, Mn(VII): 60 mg L−1 (50 mL), dosage: 10 mg, pH: 7, removal (time): ∼93.14% (60 min) | 175.75 | Langmuir | Pseudo sec. order (k: 2.93 × 10−5 g mg−1 min−1) | 489 |
| Cu(II) | PPy/γ-Fe2O3 | Aqueous media | Emulsion polymerization | Temp.: RT, Cu(II): 2.5 mg L−1 (10 mL), dosage: 2 mg, pH: 2, qe (time): ∼165 mg g−1 (2 h) | 170 | Langmuir | Pseudo sec. order (k: 4.7 × 10−2 g mg−1 min−1) | 432 |
| Cu(II) | PANI/γ-Fe2O3 | Aqueous media | Emulsion polymerization | Temp.: RT, Cu(II) 2.5 mg L−1 (10 mL), dosage: 2 mg, pH: 2, qe (time): ∼165 mg g−1 (2 h) | 106.8 | Langmuir | Pseudo sec. order (k: 6.1 × 10−3 g mg−1 min−1) | 432 |
| Cu(II) | Fe3O4@PPy yolk–shell | Water | Multistep | Cu(II): 1 mg L−1 (100 mL), dosage:15 mg, pH:6, removal (time): ∼95% (30 min) | 25.179 | Langmuir, Freundlich | Pseudo sec. order (k: 0.035 g mg−1 h−1) | 458 |
| Ni(II) | Amino acid-doped PANI nanotubes | Aqueous solutions | In situ chemical polymerization | Temp.: 25 °C Ni(II):30 mg L−1 (10 mL), dosage:0.25 g, pH: 7, removal (time): ∼68% (120 min) | — | — | — | 419 |
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| Fig. 30 Sources and pathways of dyes in the environment.88 Reproduced with permission from RSC. | ||
In this regard, polyaniline has been reported as one of most studied and cost-effective adsorbents in the decontamination processes of wastewater treatment, owing to its easy synthesis with a possibility of doping, exhibiting environmental stability, mechanical flexibility and good physicochemical properties and the presence of amine and imine groups.64,489 However, conventional PANI powder has a low surface area that limits its ability to adsorb dye. In this regard, hollow and core–shell-structured conducting polymers, especially polyaniline, have been used for the effective adsorption of dyes owing to their high surface area and other properties.
From this perspective, hollow-structure polyaniline is more advantageous for the removal of dye due to its high surface area and porous structure. In addition, core–shell-structured polyaniline also offers several advantages that include enhanced adsorption capacity, improved selectivity, better stability, and achieving increased surface area and the ability to incorporate different materials for specific interactions with the dye molecule.64,68 Accordingly, the adsorption performance of hollow conducting polymers, hollow conducting polymer composites and conducting polymer-based core–shell composites has been reviewed below for the removal of different dyes from water.490–550
In another study, the maximum adsorption capacity values of rhodamine B, methylene blue, malachite green, and crystalline violet present on Fe3O4@polypyrrole@2-acrylamido-2-methyl-1-propanesulfonic acid composite in aqueous solution were found to be 215.054 mg g−1, 183.486 mg g−1, 144.718 mg g−1 and 194.175 mg g−1, respectively.502 The trilaminar composite maintained a removal efficiency exceeding 95% after going through 5 cycles. The kinetic, adsorption isotherm and thermodynamic studies indicated pseudo-second-order, Langmuir model and an endothermic spontaneous adsorption process, respectively. In addition, a mechanism has also been proposed on the adsorption of dyes by Fe3O4@PPy@AMPS composite based on the electrostatic interactions between dyes and adsorbent, formation of hydrogen bonding involving O (in AMPS) and H (dyes), π–π interactions between the benzene rings (AMPS) and in dye including the hydrophobic interactions. Sayed et al.503 prepared a PANI/C hybrid by an in situ chemical oxidation method under ultrasonic vibration. Scanning electron microscopy of the composite revealed the PANI network formation of intersecting nanorods. They also reported that the uptake of rhodamine B by the free form of the employed polyaniline took place due to hydrogen bonding, electrostatic interactions, and pi–pi interaction.
Varghese et al.504 prepared a PEG-capped PANI/TiO2/CuO composite by in situ chemical oxidative polymerization to study its adsorption performance in the removal of rhodamine B and other organic dyes in water. TEM studies of the trilaminar composite confirmed the incorporation of TiO2/CuO into the tubular-shaped fibrous network of PANI. The adsorption efficiency of MB, MG, CR, RhB, and CV on PANI/TiO2/CuO after 120 minutes corresponded to the removal efficiency of 98%, 67.7%, 95.1%, 64.4%, and 97.3%, respectively (Fig. 31(a)). The effect of a variety of materials on the adsorption of RhB dye has also been studied and the corresponding findings are displayed in Fig. 31(b). These findings revealed the superior removal performance by PANI/TiO2/CuO (PTC) (89.7%) compared with PANI, (64.9%) TiO2 (63.9%), CuO (44.3%), PANI/TiO2 (PT): (72.9%), PANI/CuO (PC): 60.4%, and TiO2/CuO (TC): 52.7% in 240 min due to its more negative zeta potential value. Fig. 31(c) shows the effect of adsorbent (PANI/TiO2/CuO) amounts on the adsorption of RhB for 120 min. According to this, the maximum adsorption efficiency was inevitable at 0.2 g of adsorbent. The variation of initial dye concentration in Fig. 31(d) indicated the maximum removal efficiency of 89.7% (adsorbent: 0.2 g, dye: 5 mg L−1). The temperature dependence of the adsorption studies in Fig. 31(e) showed the removal efficiency decreasing from 89.7% (25 °C) to 78% (50 °C). The dependence of the pH, displayed in Fig. 31(f), showed the removal efficiency of RhB increasing from 78.5% to 89.7% on increasing pH from 4 to 6. Furthermore, the adsorption process followed the Langmuir adsorption isotherm (qm: 3.53 mg g−1) and pseudo-second-order kinetics. Fig. 32 shows the effect of pH on the adsorption efficiency of PANI/TiO2/CuO.
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| Fig. 31 (a) Adsorption efficiency of various dyes using PANI/TiO2/CuO at 120 min, (b) efficiency of RhB using different catalysts at 240 min, (c) effect of amount of adsorbent on RhB adsorption using PANI/TiO2/CuO for 120 min, (d) RhB adsorption at different dye concentrations using PANI/TiO2/CuO for 240 min, (e) effect of RhB adsorption using PANI/TiO2/CuO at different temperatures, and (f) effect of pH on the adsorption of RhB using PANI/TiO2/CuO.504 Reproduced with permission from Elsevier. | ||
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| Fig. 32 The effect of pH on the adsorption efficiency of PANI/TiO2/CuO.504 Reproduced with permission from ACS. | ||
Teng et al.510 observed 89.62% removal of CR from aqueous solution on PANI-coated Fe3O4 nanoparticles (PANI/Fe3O4: 70/30). These studies also indicated slightly enhanced dye removal by PANI/Fe3O4 compared with PANI alone. The adsorption of CR on the PANI/Fe3O4 adsorbent could be ascribed to the possible bond formation between the –OH functional group (Fe3O4) and CR, electrostatic interactions between the –NH+ of PANI (emeraldine salt form) and anionic sulfonic group of CR dye, and hydrogen bonding interaction between CR and the PANI/Fe3O4 surface. The regeneration studies showed 77.4% removal retained after the fifth cycle of adsorption–desorption. Singh et al.511 confirmed the coverage of in situ-prepared PANI over the zinc titanate surface by FESEM. This showed dramatically enhanced Congo red adsorption (qm: 64.51 mg g−1) compared with that of PANI and zinc titanate.
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| Fig. 33 Effect of pH on (a) MG and (b) CR dye removal efficiency (inset: change of wavelength of the dye solutions at different solution pH); (c) zeta potential of PNHM/MnO2/Fe3O4 with the variation of pH, effect of (d) adsorbent dose, (e) contact time and (f) initial dye concentration on MG and CR dye removal efficiency.513 Reproduced with permission from ACS. | ||
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| Fig. 34 Schematic representation of plausible adsorption mechanism of MG and CR dye on the surface of PNHM/MnO2/Fe3O4 at pH ∼6.75.513 Reproduced with permission from ACS. | ||
A PANI@ZnO-SiO2 hybrid material displayed good adsorption efficacy for CR (83.82 mg g−1) and MB (71.19 mg g−1) in aqueous solution.514 According to Weng et al.,515 ultrathin Mg silicate nanosheets were grown on Fe3O4@PPy and subsequently used as adsorbent to remove Congo red from aqueous solution. These findings revealed the applicability of the Langmuir isotherm model with maximum monolayer adsorption capacities of 540.5 mg−1 and kinetic data fitting to the pseudo-second-order model (k: 0.9030 g mg−1 min−1). Adsorptive removal of CR on L-cysteine/rGO/PANI nanocomposite was done at room temperature to find out the optimum conditions.516 These findings indicated the data fitted well with the Langmuir model (qm: 56.57 mg g−1) and kinetics validating pseudo-second-order. Furthermore, the adsorption process was found, guided via intra-particle diffusion and thermodynamic studies that indicated the adsorption process of CR was endothermic and spontaneous.
El-Sharkaway et al.524 synthesized a transparent layered and wrinkled wavy structure of GO covered with PANI and used it subsequently in the preparation of PANI-RGO, and used this to study the adsorption ability for MB in water. The kinetic studies of the PANI/GO and PANI/RGO indicated pseudo-first-order kinetics and the adsorption data best suited the Langmuir model. The estimated maximum dye adsorption capacity values of MB on PANI/GO and PANI/RGO adsorbents were found to be 14.2 and 19.2 mg g−1, respectively. These findings affirmed PANI/RGO to be more effective compared with PANI/GO for the removal of MB. Ayad et al.525 prepared a coating of polypyrrole on a cotton textile by in situ oxidative polymerization of pyrrole monomer and subsequently used this as adsorbent of methylene blue in alkaline solutions. The adsorption process followed the Freundlich isotherm model and the adsorption kinetics fitted well with pseudo-second order. They also extended their work on the removal of Acid Green 25 in acidic medium and observed some affinity.
Polypyrrole/GO@Fe3O4 has been prepared by a one-step method and used as magnetic adsorbent in the removal of methylene blue dye from aqueous solution (pH: 8).528 This adsorbent exhibited an adsorption capacity of 323.2 mg g−1 for MB. A super-paramagnetic architecture comprising Fe3O4@PPy@RGO ternary nano-adsorbents was fabricated to remove methylene from wastewater.529 The choice of Fe3O4 hollow spheres, polypyrrole layers and graphene sheets was guided by the role they play in contributing towards the abundant hydrophilic groups, protecting hollow spheres from acid corrosion/surface oxidation and in enhancing the removal performance of Fe3O4@PPy. HRTEM studies of Fe3O4@PPy@RGO established the formation of a ternary nano-architecture comprising wrapping of Fe3O4@PPy by RGO sheets. Fig. 35(a) shows Fe3O4@PPy@RGO exhibiting a superior removal efficiency for MB compared with Fe3O4 and Fe3O4@PPy in neutral solution (pH: 7). Furthermore, Fe3O4@PPy@RGO retained about 96% removal efficiency after five cycles of the adsorption–desorption process Fig. 35(b). In addition, the removal efficiency of these adsorbents in acidic solution (pH: 2) and alkaline solution (pH 10) are also displayed in Fig. 35(c and d), respectively. Graphene-modified magnetic polypyrrole530 and Fe3O4/polypyrrole/phytic acid531 also efficiently removed methylene blue from aqueous solution.
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| Fig. 35 (a) Removal efficiency of magnetic adsorbents in neutral solution (pH 7); (b) removal efficiency of Fe3O4@PPy@RGO in five cycles, neutral solution (pH 7); (c) removal efficiency of magnetic adsorbents in acidic solution (pH 2) and (d) alkaline solution (pH 10).529 Reproduced with permission from Elsevier. | ||
Zhang et al.538 fabricated halloysite nanotubes/polypyrrole nanocomposites by in situ polymerization of pyrrole monomer in the presence of HNTs. Subsequently, its adsorption efficiency was evaluated in the removal of methyl orange as a function of adsorbent dose, contact time, initial concentration MO, and temperature on the adsorption efficiency. The adsorption kinetics fitted the pseudo-second-order and adsorption isotherms validated by Langmuir (qm: 2
146 mg g−1) and Freundlich models. The thermodynamic investigations pointed to an adsorption process of methyl orange onto HNTs/PPy that was spontaneous and exothermic. Furthermore, regeneration experiments have shown the reusability of HNTs/PPy nanocomposites at least three times in removing methyl orange in aqueous solution.
Yao et al.539 prepared core–shell Fe3O4@C@polyaniline composite microspheres as a separable adsorbent for the removal of MO dye from aqueous solution. The TEM images of the product confirmed the core–shell structure of the Fe3O4@C@PANi composite microspheres. The adsorption isotherms and kinetics data supported the Langmuir and pseudo-second-order models, respectively. The trilaminar core–shell composite also exhibited excellent adsorption capability (qm: 120.2 mg g−1), and retained excellent adsorption capability (∼81%) after five adsorption–desorption cycles.
Table 4 presents the removal of the various dyes in aqueous solution based on hollow intrinsically conducting polymers, nanocomposites comprising hollow intrinsically conducting polymers and core–shell based ICP nanocomposites as adsorbents.
| Dye | Adsorbent | Water type | Preparative method | Experimental conditions and findings | qm (mg g−1) | Removal isotherm fitted to | Kinetics data fitted to | Ref. |
|---|---|---|---|---|---|---|---|---|
| a qm: maximum adsorption capacity. AG: acid green, AR: acid red, AR1: acid red 1, AYR: alizarin yellow R, BB: brilliant blue, BG: brilliant green, CR: Congo red, CV: crystal violet, E102 (tartrazine: TTz), EB: Evans blue, EY: eosin Y, OG: orange green, IC: indigo carmine, MG: malachite green, MO: methyl orange, MB: methylene blue, MR: methyl red, OG: orange green, Rh: rhodamine, RhB: rhodamine B, Rh6B: rhodamine 6B. Rh6G: rhodamine 6G, SY: sunset yellow. | ||||||||
| CR | Amino acid-doped PANI nanotubes | Aqueous solutions | In situ chemical polymerization | Temp.: 25 °C CR:30 mg L−1 (10 mL), dosage:0.25 g, pH: 7, removal (time): ∼110 mg g−1 (90 min) | 112 | Langmuir | Pseudo first-order | 419 |
| OG | PANI@Almond shell | Aqueous solutions | In situ chemical polymerization | Temp.: 298 K, OG: 50 mg L−1, dosage: 0.5 g L−1, pH: 5, removal (time): 94.69% (120 min) | 190.98 | Freundlich | Pseudo sec. order (k: 0.0008 mg g−1 min−1) | 447 |
| MO | PPy/Fe3O4/chitosan | Water | Co-precipitation and in situ polymerization | Temp.: 25 °C, MO: ∼100 mg L−1 (50 mL), adsorbent: 100 mg, pH: 3, removal efficiency (time): 67 mg g−1 (40 min) | 95 | Langmuir | — | 450 |
| IC | PMMA/rice husk/PPy membrane | Water | Electrospinning and chemical polymerization | Temp.: 283 K, IC: 30 mg L−1, dosage (membrane): 0.02m × 0.02 m (wt: 0.6 mg), pH:2.0, qe (time): 142.9 mg g−1 (70 min) | 144.93 | Langmuir | Pseudo sec. order (k: 0.002 g mg−1 min−1) | 451 |
| E102 | PMMA/rice husk/PPy membrane | Water | Electrospinning and chemical polymerization | Temp.: 283 K, TZ:60 mg L−1, dosage (membrane): 0.02 m × 0.02 m2 (wt: 0.6 mg), pH: 2.0, qe (time): 165.7 mg g−1 (60 min) | 171.23 | Langmuir | Pseudo sec. order (k: 0.002 min−1) | 451 |
| RhB | Fe3O4@PPy@Sodium dodecyl sulphate | Complex wastewater | Combination of a hydrothermal method in situ polymerization | Temp.: 20 °C, RhB:40 mg L−1 (50 mL), adsorbent: 10 mg, pH: 7, removal (time): 94.83% (7 h) | 127.55 | Langmuir | Pseudo sec. order (k: 3.027 × 10−3 g mg−1 min−1) | 489 |
| CR | Fe3O4@PPy@Sodium dodecyl sulphate | Complex wastewater | Combination of hydrothermal method and in situ polymerization | Temp.: 20 °C, CR:40 mg L−1 (50 mL), adsorbent: 10 mg, pH: 7, removal (time): 96.45% (7 h) | 101.63 | Langmuir | Pseudo sec. order (k: 2.75 × 10−4 g mg−1 min−1) | 489 |
| MB | Fe3O4@PPy@Sodium dodecyl sulphate | Complex wastewater | Combination of a hydrothermal method in situ polymerization | Temp.: 20 °C, MB:40 mg L−1 (50 mL), adsorbent: 10 mg, pH: 7, removal (time): 93.27% (400 min) | 135.50 | Langmuir | Pseudo sec. order (k: 1.71 × 10−4 g mg−1 min−1) | 489 |
| MG | Fe3O4@PPy@Sodium dodecyl sulphate | Complex wastewater | Three-step process | Temp.: 20 °C, MG:40 mg L−1 (50 mL), adsorbent: 10 mg, pH: 7, removal (time): 96.03% (7 h) | 182.82 | Langmuir | Pseudo sec. order (k: 8.93 × 10−4 g mg−1 min−1) | 489 |
| AR1 | Fe3O4@PPy@Sodium dodecyl sulphate | Complex wastewater | Combination of a hydrothermal method in situ polymerization | Temp.: 20 °C, AR1:40 mg L−1 (50 mL), adsorbent: 10 mg, pH: 2, removal (time): 92.99% (7 h) | 181.16 | Langmuir | Pseudo sec. order (k: 2.66 × 10−4 g mg−1 min−1) | 489 |
| RhB | Hollow spherical PANI | Aqueous solution | In situ polymerization on functionalized polystyrene template | RhB: 100 mg L−1 (50 mL), adsorbent: 5 mg, qe (time): 61.75 mg g−1 (72 h) | 61.75 | — | — | 491 |
| CR | Hollow spherical PANI | Aqueous solution | Chemical polymerization | CR: 5 mg (50 mL), Adsorbent: 100 mg L−1, qe (time): 46.91 (72 h) | 46.91 | — | — | 491 |
| Rh6G | Hollow PANI helical nanobelts | Aqueous solution | Chemical oxidation of aniline | Temp.: RT, Rh6G: 50 mg (100 mL), adsorbent: 479 mg L−1, removal (time): ∼249 mg L−1 (120 min) | 0.42 mg mg−1 | Langmuir | Pseudo sec. order (k: 1.28 mg mg−1 min−1) | 492 |
| RhB | Coating of PANI onto carbonized tea waste | Aqueous solutions | Coating of polyaniline onto carbonized tea waste material | Temp.: 30 °C, RhB: 50 mg L−1 (100 mL), adsorbent: 100 mg, pH: 8.0, removal (min): 95.21% (60 min) | 34.93 | Langmuir | Pseudo-second-order (k: 0.0035 g mg−1 min−1) | 495 |
| RhB | α-MoO3/PANI | Water | Chemical oxidative polymerization using camphor sulfonic acid as dopant | Temp.: 20 °C, RhB: 2.1 × 10−5 mol L−1 (50 mL), adsorbent: 50 mg, pH:3, Removal (time): 91% (60 min) | 36.36 | Langmuir | — | 497 |
| CR | α-MoO3/PANI | Water | Chemical oxidative polymerization using camphor-10 sulfonic acid as dopant | Temp.: 15 °C, CR: 1.5 × 10−5 mol L−1 (1000 mL), adsorbent: 50 mg, pH: 5, removal (time): 94.6 (60 min) | 76.22 | Langmuir | — | 497 |
| RhB | PPy/coffee grounds waste | Aqueous solution | Pyrrole polymerization | Temp.: 15 °C, RhB: 200 mg L−1 (150 mL), adsorbent: 125 mg, pH: 9, removal (time): 32 mg g−1 (80 min) | 50.597 | Redlich–Peterson and Langmuir | — | 498 |
| RhB | Fe3O4@PPy@4-Vinylpyridine | Wastewater | Multiple steps | Temp.: 20 °C, RhB: 50 mg L−1 (30 mL), adsorbent: 10 mg, pH = 7, removal (time): ∼97% (500 min) | 58.72 | Langmuir | Pseudo sec. order (k: 9.728 × 10−4 g mg−1 min−1) | 499 |
| MB | Fe3O4@PPy@4 vinylpyridine | Wastewater | Multiple steps | Temp.: 20 °C, MB: 50 mg L−1 (30 mL), adsorbent: 10 mg, pH = 7, removal (time): ∼100% (500 min) | 85.98 | Langmuir | Pseudo sec. order (k: 3.704 × 10−3 g mg−1 min−1) | 499 |
| MG | Fe3O4@PPy@4-vinylpyridine | Wastewater | Multiple steps | Temp.: 20 °C, MG: 50 mg L−1 (30 mL), adsorbent: 10 mg pH = 7, removal (time): ∼98% (600 min) | 36.114 | Langmuir | Pseudo sec. order | 499 |
| AR | Fe3O4@PPy@4-vinylpyridine | Wastewater | Multiple steps | Temp.: 20 °C, AR: 200 mg L−1 (30 mL), adsorbent: 10 mg pH = 7, removal (time): ∼90% (600 min) | 55.90 | Freundlich | Pseudo sec. order (k: 2.270 × 10−4 g mg−1 min−1) | 499 |
| MB | PANI/attapulgite-supported nanoscale zero-valent Fe | Aqueous solution | Liquid-phase chemical reduction method | Temp.: 298 K., MB: 60 mg L−1 (50 mL), adsorbent: 0.05 g, pH: 11, removal (time): 30% (30 minutes) | 23 | Langmuir | — | 500 |
| AYR | PANI/attapulgite-supported nanoscale zero-valent Fe | Aqueous solution | Liquid-phase chemical reduction method | Temp.: 298 K, AYR: 60 mg L−1 (50 mL), adsorbent: 0.05 g, pH:3, removal (time): 99.56% (10 min) | 72 | Langmuir | — | 500 |
| RhB | Polyaniline magnetic nanoparticles/dicationic ionic liquid | Tap/industrial and lake water | Coating aniline and dicationic ionic liquids on magnetic nanoparticle | Temp.: 298 K, RhB:10 mg g−1 (10 mL), adsorbent: 20 mg, pH: 1, removal (time); ∼94% (60 min) | 109.90 | Temkin | Pseudo sec. order (k: 0.4172 g mg−1 min−1) | 501 |
| RhB | Magnetite@PPy@2-acrylamido-2-methyl-1-propanesulfonic acid microspheres | Aqueous solutions | Two-step process | Temp.: 293 K., RhB: 60 mg L−1, adsorbent: 7 mg, pH: 7, removal (time): >90% (300 min) | 215.054 | Langmuir | Pseudo sec. order (k: 2.441 × 10−3 g mg−–1 min−1) | 502 |
| MB | Magnetite@PPy@2-acrylamido-2-methyl-1-propanesulfonic acid microspheres | Aqueous solutions | Two-step process | Temp.: 293 K. MB: 50 mg L−1, adsorbent: 7 mg, pH: 7, removal (time): ∼100% (240 min) | 183.486 | Langmuir | Pseudo sec. order | 502 |
| CV | Magnetite@PPy@2-acrylamido-2-methyl-1-propanesulfonic acid microspheres | Aqueous solutions | Two-step process | Temp.: 293 K, CV: 50 mg L−1, adsorbent: 7 mg, pH: 7, removal (time): ∼100% (300 min) | 194.175 | Langmuir | Pseudo sec. order (k: 3.156 × 10−3 g mg−1 min−1) | 502 |
| RhB | PEG capped PANI/TiO2/CuO | Water | In situ polymerization of aniline in the presence of TiO2/CuO | Temp.: 300 K. RhB: 5 mg L−1 (50 mL), adsorbent: 0.2 g, pH: 6, removal (time): 89.7% (240 min) | 3.53 | Langmuir | Pseudo sec. order (k: 0.809 g. mg−1 min−1) | 504 |
| CR | PANI@ZnO | Deionized water | In situ oxidation chemical process | Temp.: 298 K, CR: 150 mg L−1 (25 mL), adsorbent: 10 mg, pH: 5, Removal (time):∼70% (60 min) | 76.92 | Langmuir | Pseudo sec. order (0.0004 g mg−1 min−1) | 507 |
| MO | 3D PANI@Activated SiO2 gel | Aqueous solution | In situ polymerization | Temp.: 298.15 K, MO: 50 mg L−1 (30 mL), adsorbent: 0.25 g, pH: 3, removal efficiency (time): ∼100% (200 min) | 161.29 | Langmuir | Pseudo sec. order 0.036 g mg−1 min−1 | 508 |
| BG | 3D PANI@Activated SiO2 gel | Aqueous solution | In situ polymerization | Temp.: 298.15 K. BG: 50 mg L−1 (30 mL), adsorbent: 0.025 g, pH: 8, removal (time): 100% (200 min) | 136.98 | Langmuir | Pseudo sec. order (k: 1.34 g mg−1 min−1) | 508 |
| CR | PANI-ZnTiO3 | Aqueous solutions | Polymerization of aniline in the suspensions of ZTO | Temp.: RT, CR:50–150 ppm (100 mL), adsorbent: 200 mg, pH: natural pH, removal (time): 90% (15 min) | 64.51 | Langmuir | Pseudo sec. order (k: 0.000509 g s−1 mg−1) | 511 |
| CR | Fe3O4/PPy/carbon black | Aqueous solution | Encapsulating Fe3O4 nanoparticles in PPy/carbon black | CR: 120 mg L−1 (40 mL), adsorbent: 0.5 g L−1, pH: 7, removal (time): 95% (240 min) | 500 | Langmuir | Pseudo sec. order (k: 0.007 × 10−2 g mg−1 min−1) | 512 |
| MB | Fe3O4/PPy/carbon black | Aqueous solution | Encapsulating Fe3O4 nanoparticles in PPy/carbon black | MB: 40 mg L−1 (40 mL), adsorbent: 0.5 g L−1, pH: 7, removal (time): 95.9% (120 min) | 90.9 | Langmuir | Pseudo sec. order (k: 0.14 × 10−2 g.mg−1 min−1) | 512 |
| CR | PANI microsphere/MnO2/Fe3O4 | Aqueous solution | In situ deposition | Temp.: 303 ± 3 K, CR: 20 mg L−1, adsorbent: 1 g L−1, pH: ∼6.75, removal (time): 98% (1500 min) | 599.49 | Elovich | Pseudo sec. order (k: 0.25 g mg−1 min−1) | 513 |
| MG | PANI microsphere/MnO2/Fe3O4 | Aqueous solution | In situ deposition | Temp.: 303 ± 3 K, MG: 20 mg L−1, adsorbent: 1 g L−1, pH: ∼6.75, removal (time ): 88% (1500 min) | 1142.13 | Freundlich | Pseudo sec. order (k: 0.012 g mg−1 min−1) | 513 |
| CR | L-Cysteine/rGO/PANI | Aqueous solution | rGO + 0.1M L-cysteine solution + aniline monomer + APS | Temp.: RT, CR: 30 mg L−1 (10 mL), adsorbent: 0.025 g, pH: neutral, removal (time): 98% (10 min) | 56.57 | Langmuir | Pseudo sec. order | 516 |
| MB | Polyaniline nanotubes | Aqueous solutions | In situ polymerization | Temp.: 25 °C, MB: 3.1 mg L−1 (100 mL), adsorbent: 0.05 g, pH: qe/time: ∼0.6 mg g−1 (150 min) | 9.21 | Langmuir | Pseudo sec. order (k: 0.03595 g mg−1 min−1) | 518 |
| MB | Polyaniline hollow nanotubes | In situ synthesis | In situ polymerization | Temp.: RT, MB: 6.2 mg L−1 (100 mL), Adsorbent: 10 mg, pH: 11, Removal/time: ∼92% (600 min) | 69.4 | Langmuir | Pseudo sec. order (k: 0.001 g mg−1 min−1) | 519 |
| AG | PANI hollow nanotubes | Aqueous media | Using acid green as a structure-directing agent and soft template | Temp.: 298 K, AG:6.1 mg L−1 (100 mL), adsorbent: 10 mg, pH: 3.0, removal (time): 52% (6 h) | 57.8 | Langmuir | Pseudo sec. order (k: 8.9 × 10−4 g mg−1 min−1) | 519 |
| MB | Polyaniline nanotubes | Aqueous medium | Aniline oxidation in the presence of methyl orange | Temp.: 298 K, MB = 8.8 mg L−1 (0.1 L), adsorbent: 20 mg, pH: 9, removal (time): > 90% (300 min) | 91.1 | Langmuir | Pseudo sec. order (k: 0.00117 g mg−1 min−1) | 520 |
| AG | PANI nanotubes | Aqueous medium | Green approach via the aniline, oxidation | Temp.: 25 °C, AG: 20 mgL−1 (100 ml), adsorbent: 8 mg L−1, pH: 3, removal (time): 67% (320 min) | 58 | Langmuir | Pseudo sec.-order (k: 0.002 g mg−1 min−1) | 520 |
| CR | PPy@MoS2 hollow microtubes | Aqueous medium | Hydrothermal process, in situ polymerization and sulfidation | Temp.: RT, CR: 60 mg L−1 (5 mL), adsorbent: 50 mg L−1, pH: neutral, removal (time): 84,14% (120 min) | 598.7 | Freundlich | Pseudo sec. order (k: 0.0030 g mg−1 min−1) | 521 |
| MB | PPy@MoS2 hollow microtubes | Aqueous medium | Hydrothermal process and in situ polymerization and sulfidation | Temp.: RT, MB:150 mg L−1 (5 mL), adsorbent: 50 mg L−1, pH: neutral, removal (time): 41.1% (120 min) | 121.3 | Langmuir | Pseudo sec. order (k: 0.0003 g mg−1 min−1) | 521 |
| MB | PANI nanotubes base/silica | Distilled water | In situ polymerization | Temp.: 25 °C, MB: 0.95 mg L−1 (100 mL), adsorbent: 0.05 g, removal (time): 100% (10 min) | 10.31 | Langmuir | Pseudo sec. order (k: 0.09 g mg−1 min−1) | 522 |
| MB | PANI/TiO2 hydrate | Distilled water | One-pot chemical oxidative polymerization | Temp.: 298 K, MB:100–200 mg L−1 (10 mL), adsorbent: 2 g L−1, pH: 3–11, removal (time): ∼100% (12 h) | 458.10 | Freundlich model | Pseudo sec. order (k: 0.0009 g mg−1 min−1) | 523 |
| MB | PPy-coated cotton textile | Aqueous solution | In situ oxidative polymerization of cotton textiles | Temp.: 25 °C, MB: 3.9 mg L−1 (50 mL), adsorbent: 0.05 g, pH: 7, removal (time): 96% (24 h) | 6.83 | Freundlich | Pseudo sec. order (k: 0.083 g mg−1 min−1) | 525 |
| MB | Fe3O4@PPy@SDBS | Aqueous solutions | Through hydrothermal, in situ polymerization, and surface modification | Temp.: 20 °C, MB: 20–30 mg L−1 (30 mL), adsorbent: 10 mg, pH: 7, removal (time): ∼97% (500 min) | 124.07 | Langmuir | Pseudo sec. order (1.213 × 10−3 g mg−1 min−1) | 527 |
| MG | Fe3O4@PPy@SDBS | Aqueous solutions | Through hydrothermal, in situ polymerization, and surface modification | Temp.: 20 °C, MG: 20 mg L−1 (30 mL), adsorbent: 8 mg, pH: 7, removal (time): ∼96% (500 min) | 73.10 | Langmuir | Pseudo sec. order (1.445 × 10−3 g mg−1 min−1) | 527 |
| MB | PPy/GO@Fe3O4 | Aqueous solutions | One step | Temp.: RT, MB: 100 mg L−1 (40 mL), adsorbent: 10 mg, pH: 8, removal (time): ∼80% (140 min) | 323.2 | Langmuir | Pseudo second, order (k: 0.00172 g mg−1 min−1) | 528 |
| MB | Fe3O4@PPy/RGO | Aqueous solutions | Chemical route | Temp.: 30 °C. MB:100 mg L−1 (30 mL), adsorbent: 0.333 g L−1, pH: natural, removal (time): ∼95% (60 min) | 270.3 | Langmuir isotherm | Pseudo-second-order (k: 0.0154 g mg−1 min−1) | 530 |
| MB | Fe3O4/polypyrrole/phytic acid | Water | In situ polymerization | Temp.: 35 °C, MB: 100 ppm (50 mL), adsorbent: 80 mg, pH: 10, removal (time): ∼86.4% (120 min) | 153.84 | Langmuir | Pseudo sec. order (k: 0.001 g mg−1 min−1) | 531 |
| CV | Fe3O4/polypyrrole/phytic acid | Water | In situ polymerization | Temp.: 35 °C, CV: 100 ppm (50 mL), adsorbent: 80 mg, pH: 10, removal (time): ∼85% (120 min) | 181.82 | Langmuir | Pseudo sec. order (k: 0.001 g mg−1 min−1) | 531 |
| MO | PANI nanotube-filled sodium alginate | Distilled water | Mixing of PANI nanotubes in water + CaCl2 | Temp.: 35 °C, MO: 20 mg L−1 (50 mL), adsorbent: 0.05 g, pH: 2, removal (time): ∼76% (90 min) | 370.4 | Langmuir | Pseudo sec. order (k: 0.001 g mg−1 min−1) | 534 |
| MO | PANI-MWCNT | Water | In situ oxidative polymerization | Temp.: 30 °C, MO: 30 mgL−1 (100 ml), adsorbent: 8 mg L−1, pH: neutral, removal (time): ∼94% (60 min) | 149.25 | Langmuir | Pseudo sec. order (k: 5.265 × 10−4 g mg−1 min−1) | 535 |
| MO | PANI (skin)/polyamide 6 (core) | Aqueous solution | In situ oxidation polymerization | Temp.: 298 K, MO:10 ppm, adsorbent: 0.03g, pH: 6, removal (time): 58.7 mg g−1 (120 min) | 58.7 | Langmuir | Pseudo sec. order | 536 |
| MO | Waterborne poly vinyl pyrrolidone-stabilized PANI core–shell | Tap water | Waterborne PVP-stabilized PANI core–shell | Temp.: 28 °C, MO: 32.73 mg L−1 (20 ml), adsorbent: 5 mg, pH 7.02, removal (time): 100% (15 min) | — | Langmuir | — | 537 |
| MO | Halloysite nanotubes/PPy | Aqueous solution | In situ polymerization | Temp.: 25 °C, MO: 90 mg L−1 (50 mL), adsorbent: 0.15 g, pH: natural, removal (time): 98.6% (120 min) | 214.6 | Langmuir and Freundlich | Pseudo sec. order (k: 0.0037 g mg−1 min−1) | 538 |
| RB | PANI@TiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. RB: 100 mg L−1 (100 mL), adsorbent: 50 mg, pH: 6.7, qt (time): ∼80 mg g−1 (120 min) | — | Langmuir and Freundlich | First order (k: 0.007 min−1), pseudo sec. order (k: 0.00008 g mg−1 min−1/2) | 540 |
| RB | PANI@SiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. RB: 100 mg L−1 (100 mL), adsorbent: 50 mg, pH: 6, qt (time): ∼30 mg g−1 (120 min) | — | Langmuir and Freundlich | First order (k: 0.024 min−1), pseudo sec. order (k: 0.00029 g mg−1 min−1/2) | 540 |
| R6G | PANI@TiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. R6G: 50 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time): ∼90 mg g−1 (120 min) | 94 | Langmuir and Freundlich | First order (k: 0.023 min−1), pseudo sec. order (k: 0.00 069 g mg−1 min−1/2) | 540 |
| R6G | PANI@SiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. R6G: 5 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time): ∼60 mg g−1 (120 min) | 61 | Langmuir and Freundlich | First order (k: 0.011 min−1), pseudo sec. order (k: 0.00 006 g mg−1 min−1/2) | 540 |
| CR | PANI@TiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. CR: 100 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time): ∼93 mg g−1 (120 min) | 93 | Langmuir and Freundlich | First order (k: 0.020 min−1), pseud sec. order (k: 0.00048 g mg−1 min−1/2) | 540 |
| CR | PANI@SiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. CR: 100 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time): ∼70 mg g−1 (120 min) | 71 | Langmuir and Freundlich | First order (k: 0.0253 min−1), pseudo sec. order (k: 0.00034 g mg−1 min−1/2) | 540 |
| MB | PANI@TiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. MB: 100 mg L−1 (100 mL), adsorbent: 50 mg, pH: 6.7, qt (time): ∼90 mg g−1 (120 min) | 89 | Langmuir and Freundlich | Pseudo first order (k: 0.024 min−1), pseudo sec. order (k: 0.00050 g mg−1 min−1/2) | 540 |
| MB | PANI@SiO2 | Deionized water | Sonochemical method | Temp.: 28 °C, MB: 50 mg L−1 (100 mL), adsorbent: 50 mg, pH: 6.7, qt (time): ∼73 mg g−1 (120 min) | 74 | Langmuir and Freundlich | First order (k: 0.037 min−1), pseudo sec. order (k: 0.00056 g mg−1 min−1/2) | 540 |
| EB | PANI@TiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. EB: 100 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time) ∼55 mg g−1 (120 min) | — | Langmuir and Freundlich | First order (k: 0.008 min−1) pseudo sec. order (k: 0.00011 g mg−1 min−1/2) | 540 |
| EB | PANI@SiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. EB: 100 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time) ∼55 mg g−1 (120 min) | — | Langmuir and Freundlich | First order (k: 0.013 min−1) pseudo sec. order (k: 0.00012 g mg−1 min−1/2) | 540 |
| BB | PANI@TiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. BB: 100 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time):∼42 mg g−1 (120 min) | — | Langmuir and Freundlich | Pseudo first order (k: 0.011 min−1), pseudo sec. order (k: 0.00013 g mg−1 min−1/2) | 540 |
| BB | PANI@SiO2 | Deionized water | Sonochemical method | Temp.: 28 °C. BB: 100 mg L−1 (100 mL), adsorbent: 5 mg, pH: 6.7, qt (time): ∼42 mg g−1 (120 min) | 86 | Langmuir and Freundlich | Pseudo first order (k: 0.038 min−1), pseudo sec. order (k: 0.00060 g mg−1 min−1/2) | 540 |
| MG | Graphene/Fe3O4/PANI | Aqueous solutions | Multiple steps | Temp.: 25 °C, MG: 16 mg L−1 (50 mL), adsorbent: 30 mg, pH: 6.5, removal (after cycle 1): 97.72% | 196.10 | Langmuir | Pseudo sec. order (k: 0.0022 g mg−1 min−1) | 541 |
| AR1 | Graphene/Fe3O4/PANI | Aqueous solutions | Multiple steps | Temp.: 25 °C, AR1: 16 mg L−1 (50 mL), adsorbent: 30 mg, pH: 6.5, removal efficiency (after cycle 1): 97.013% | 150.27 | Langmuir | Pseudo sec. order (k: 0.0021 g mg−1 min−1) | 541 |
| MG | CNT/PANI | Aqueous solution | Static interfacial polymerization technique | Temp.: 20 °C, MG: 8–12 mg L−1 (100 mL), adsorbent: 0.1 g, pH: 7, removal (time): ∼95% (120 min) | 15.45 | Langmuir | Pseudo sec- order (k: 5.0 × 10−3 mg g−1 min−0.5) | 542 |
| AR1 | PPy/Mn0.8Zn0.2Fe2O4/GO (PMG50) | Wastewater | In situ Py polymerization | Temp.: 298 K, AR1:10 mg L−1 (10 mL), adsorbent: 100 mg, pH: 2, removal (time): 98.8% (120 min) | — | — | Pseudo sec. order (0.320 g mg−1 min−1) | 545 |
| BG | Cross-linked PANI/chitosan-graphene oxide-oxidized SWCNT | Aqueous solution | Chemical oxidative copolymerization | Temp.: 22 °C, BG: 5 mg L−1 (25 mL), adsorbent: 12.5 mg, pH 6, removal efficiency (time): ∼98.4% % (120 min) | 21.27 | — | Pseudo-second-order (k: 9.2 × 10−4 mg g−1 min-0.5) | 546 |
| AR1 | Cross-linked PANI/chitosan-graphene oxide-oxidized SWCNT | Aqueous solution | Chemical oxidative copolymerization | Temp.: 22 °C, AR1: 20 mg L−1 (25 mL), adsorbent: 12.5 mg, pH 2, removal efficiency (time): 99.7% (120 min) | 90.91 | — | Pseudo-second-order (k: 3.4 × 10−4 mg g−1 min−0.5) | 546 |
| BG | Core–shell polythiophene/ZnO/MWCNTs | Aqueous solutions | In situ chemical polymerization (two-way method) | Temp.: 25 °C. BG: 5 mg L−1 (20 mL), adsorbent: 30 mg, pH: 6, removal efficiency (time): 94% (90 min) | 8.3 | — | Pseudo second-order (k: 1.9 × 10–3 mg g−1 min−1) | 547 |
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| Fig. 36 Charge storage mechanism of supercapacitors, (a) EDLCs, (b) pseudocapacitors and (c) hybrid supercapacitors.551 Reproduced with permission from RSC. | ||
| Materials | Advantages | Disadvantages |
|---|---|---|
| Carbonaceous materials | High specific surface area | Low energy density |
| High electrical conductivity | Poor cyclability | |
| Inexpensive | ||
| Eco-friendly | ||
| High electrochemical stability | ||
| Conducting polymers | High specific capacitance | Low conductivity |
| Tunable electrical conductivity Unique solution processability | Poor electrochemical stability | |
| High flexibility | ||
| Easy fabrication | ||
| Transition metal oxide | High specific capacitance | Low conductivity |
| Wide potential window | Poor electrochemical stability | |
| High energy density |
In this regard, intrinsically conducting polymers are favoured in supercapacitor applications due to their simple synthesis, tunable conductivity, large surface area, high flexibility, and pseudocapacitive properties.7 These features enable them to store and release energy quickly, thereby making conducting polymers an ideal candidate for high-power applications. The superior electrochemical performance of these ICPs is greatly guided by their morphology. In view of this, hollow-structured material electrodes can be better alternatives by offering higher specific surface area to facilitate the large electrode/electrolyte interface favorable for the fast transport of charges and ions as well as act as the ion reservoir to benefit the accumulation of ions. Therefore, ICPs are considered as promising electrode materials due to their low production cost and their ability to possess redox pseudocapacitance and double-layer capacitance. However, the application of ICPs is limited due to their inferior stability; therefore, ICP is combined with other active materials to overcome this intrinsic disadvantage. Accordingly, the performance of ICP for hollow-structured ICPs, their composites and core–shell-based materials is discussed below.
Polyaniline hollow microspheres (dia: 410 nm, thickness: 72 nm) doped by (poly(2-acrylamido-2-methylpropane sulfonic acid)) (PAMPS) synthesized by a self-assembly method have shown excellent promise in the field of supercapacitors.554 Li et al.555 fabricated Ce3+-doped polyaniline hollow microspheres by a self-assembly method; it exhibited a high specific capacitance of 248.2 F g−1 (1 mA cm−2) due to its enhanced conductivity compared with PANI (201.6 F g−1). In another approach, hollow PANI nanospheres prepared by in situ chemical oxidative polymerization of aniline in the presence of uniform poly(methyl methacrylate-butyl methacrylate-methacrylic acid) latex microspheres (self-sacrificial template) demonstrated specific capacitance (485.5 F g−1 at 1 A g−1) and performance after 500 cycles (69%).556
Polypyrrole hollow nanospheres prepared using polystyrene (PS) as a template that was subsequently removed by dissolving it in DMF displayed high specific capacitances (350 F g−1 at 1 A g−1).557 The corresponding symmetric supercapacitor has shown the maximum energy density of 40 Wh kg−1 at a power density of 490 W kg−1. Electrochemical studies were also performed on hollow polypyrrole films prepared by depositing polypyrrole on a 3D colloidal crystal template.558 According to Li et al.,559 hollow capsular polypyrrole nanofibers with porous capsule acted as a flexible, binder-free, self-supported supercapacitor electrode exhibiting specific capacitance of 203 F g−1 at 2 mV s−1 and excellent capacitance retention (>90% after 11
000 charge–discharge cycles @10 A g−1). This was attributed to the availability of enough free space in the capsular walls of the hollow PPy film to facilitate the volume variation during doping/de-doping. Zhang et al.244 synthesized PEDOT hollow nanospheres by expulsion of SiO2 from the SiO2@PEDOT nanospheres by dissolving it hydrofluoric acid. The PEDOT hollow sphere film fabricated in this manner showed a high specific capacitance (121.6 F g−1) at the current density of 0.5 A g−1 and sustained 65.7% of its initial specific capacitance at a current density of 8.0 A g−1.
000 cycles). This suggested that the carbon-coated PANI electrode acted as a constraint layer to prevent the tubular-structured PANI from expanding outward during the charge–discharge process. ZnO nanorod arrays (sacrificial templates) were used to fabricate polyaniline nanotube arrays and their electrochemical polymerization was studied for supercapacitor applications (Fig. 37(b)).561 Jyothibasu and Lee562 fabricated polypyrrole tubes using curcumin (template), as schematically shown in Fig. 37(c) and combined it with functionalized carbon nanotubes (f-CNTs) to form freestanding electrodes (referred to as PPyC3T2/f-CNT). It showed excellent areal capacitance of 11
830.4 mF cm−2 at a current density of 2 mA cm−2 in a thick freestanding PPyC3T2/f-CNT-electrode at a high mass loading of 30 mg cm−2. Furthermore, a symmetric supercapacitor assembled by using the PPyC3T2/f-CNT displayed an areal capacitance, cycling stability, high energy density and maximum power density of 2732 mF cm−2 at 2 mA cm−2, 118.18% retention after 12
500 cycles, 242.84 μW h cm−2 and 129.35 mW cm−2, respectively.
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| Fig. 37 (a) Schematic presentation on the preparation procedure of PANI(HNTs) and PANI(HNT)s/C.560 Reproduced with permission from Elsevier. (b) The illustration for the formation of PANI nanotubes via a sacrificial ZnO nanorods template route.561 Reproduced with permission from RSC. (c) Schematic representation of the preparation of polypyrrole tubes using curcumin as template.562 Reproduced with permission from RSC. (d) Schematic diagram of the synthesis of PPy hollow nanospheres.565 Reproduced with permission from RSC. | ||
Hollow PANI nanotubes (inner dia: 80 nm, outer dia: 180 nm) prepared via one-step polymerization attained specific capacitance of 436 F g−1 (0.5 A g−1) in H2SO4 (1 mol L−1) solution with good cycling stability (89.2%: 500 cycles at a current density of 0.5 A g−1).563 Crystalline tetragonal hollow polyaniline nanotubes prepared by using methyl orange as self-degrading template showed a specific capacitance of 590 ± 36 F g−1 at a scan rate of 5 mV s−1.564 The assembled symmetrical device exhibited maximum energy density and power density of 14.56 Wh kg−1 and 250 W kg−1, respectively. Ahn et al.565 prepared PPy hollow nanoparticles with controlled diameters through surfactant-templated chemical oxidation polymerization (Fig. 37(d)). The specific capacitance of PPy hollow nanoparticles (326 F g−1) fabricated in this manner was found to be approximately twice as large as that of solid PPy nanospheres. High-performance supercapacitor performance has also been displayed by PANI nanofibers, nanotubes, and nanospheres,566 and hollow polyaniline nanofibers fabricated by electrospinning.312 Hryniewicz and Vidotti567 for the first time electrodeposited PEDOT nanotubes onto stainless steel mesh electrodes in the presence of methyl orange template and observed enhanced supercapacitive and electrocatalytic properties. Wan et al.568 observed high specific capacitance (290 F g−1 at 1 A g−1) and outstanding cyclic stability (capacitance retention: 83% even after 1000 cycles) for the polyaniline hollow nanofibers supercapacitor electrode exhibiting 3D porous network architecture.
000 cycles at 10 A g−1) and energy density (20.4 Wh kg−1) at a power density of 194 W kg−1. Wang and others570 investigated the electrochemical performance of mesoporous MnO2/polyaniline composite with a unique morphology of hierarchical hollow submicron spheres synthesized by an interfacial approach. Electrochemical studies revealed its superior electrochemical properties, as indicated by its specific capacitance (262 F g−1) and higher capacitance retention (93% of its initial capacitance after 800 cycles) owing to its microstructure and polyaniline/MnO2 coexisting together.3D hollow balls of graphene–polyaniline hybrids were prepared through the self-assembly of graphene oxide and PMMA followed by the polymerization of polyaniline, and demonstrated high specific capacitance and good cycling stability.571 Luo et al.572 used layer-by-layer assembly for the preparation of a graphene–polyaniline hollow microsphere for supercapacitor application. It displayed excellent specific capacitance (381 F g−1: 4.0 A g−1) and good cycling stability (83% after 1000 cycles) in 1 M H2SO4 solution due to a synergistic effect. The hierarchical Ti3C2/PANI nanotubes have shown excellent specific capacitance performance (596 F g−1 at 0.1 A g−1) with 94.7% retention after 5000 cycles (at 1 A g−1).573 Furthermore, a symmetric supercapacitor device based on this showed excellent performance (energy density: 25.6 Wh kg−1 at 153.2 W kg−1, power density: 1610.8 W kg−1 at 13.2 Wh kg−1, capacitance retention 81.1% after 4000 cycles).
Devi and Kumar574 prepared nanocomposites of reduced graphene oxide/polyaniline nanotubes in the presence as well as the absence of irradiated high energetic ions and performed electrochemical investigations as a supercapacitor. They observed the relatively enhanced specific capacitance (482 F g−1 at 0.5 A g−1) and cycling stability (92%) compared with the unirradiated nanocomposite. This was ascribed to the increased surface energy and porosity as a result of irradiation. Yang et al.575 tested the electrochemical performance of a polypyrrole hollow nanosphere intercalated graphene-based flexible supercapacitor and observed its area specific capacitance and capacitance retention of 381.54 mF cm−2 (at 2 mA cm−2) and 93.94% after 1000 cycles, respectively. Graphene–polypyrrole hollow sphere,576 hollow polypyrrole nanosphere embedded in N-doped graphene layers,577 3D-arrayed polyaniline hollow nanospheres encaging RuO2 nanoparticles,578 polyaniline hollow fibers decorated by graphene,579 graphene–polypyrrole nanotubes,580 3D metal−organic frameworks with conductive polypyrrole tubes,581 and hollow PPy nanospheres decorated on the CNT582 have been synthesized and also used as electrode materials for electrochemical supercapacitor applications.
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| Fig. 38 (a) Schematic diagram for the synthesis of core–shell PPy@PANI nanospheres. (b) SC values’ plot of the scan rates and (c) charge/discharge cycling of the core–shell PPy@PANI-0.008, individual PPy, and the PANI electrode carried out at 5 A g−1 in H2SO4 aqueous electrolyte (1 M). The insert is the SEM images of the core–shell@PANI-0.008 before and after 1000 cycles.585 Reproduced with permission from ACS. | ||
Li et al.586 fabricated hollow microsphere (MS) and microtubes (MT) of PPy using polystyrene microspheres and methyl orange as hard and soft templates, respectively. Subsequently, they prepared composites of MS and MT with poly(1,5-diaminoanthraquinone) (referred as PDAAQ) and observed the following order for specific capacitance at a current density of 1 A g−1:
PPy@PDAAQ MTs (533 F g−1) > PPy@PDAAQ MSs (471 F g−1) > PDAAQ, (348 F g−1) >PPy MTs (322 F g−1) > PPy (MSs 235 F g−1).
The hollow morphology of PPy could account for the observed high specific capacitance of PPy@PDAAQ MTs.
The specific capacitance retention after 10
000 cycles followed the following trend:
PDAAQ (146.0%) > PPy@PDAAQ MTs (107.4%), PPy@PDAAQ MSs (98.0%), PPy MTs (43.6%), and PPy MSs (27.3%).
Fan et al.587 prepared a core–shell hybrid comprising PS@PANI, polyaniline hollow spheres (PANI-HS)@GO and PANI-HS@ ERGO (electrochemically reduced graphene oxide) according to the procedure as illustrated in Fig. 39(a). The morphology and structure of the PANI-HS36@GO (36: shell thickness of PANI-HS) hybrid was studied by SEM and is displayed in Fig. 39(b). The PANI-HS36@ERGO hybrid indicated its significantly high specific capacitance corresponding to 614 F g−1 at 1 A g−1 current density (Fig. 39(c)) and maintained 90% after 500 charging/discharging cycles at a current density of 1 A g−1 (Fig. 39(d)) due the synergistic effect.
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| Fig. 39 (a) Schematic illustration on the preparation of PANI-HS36@ERGO hybrids (36 here refers to shell thickness in nm), (b) SEM images of PANI-HS36@GO hybrids, (c) galvanostatic charge−discharge curves of ERGO, PANIHS36, and PANI-HS36@ERGO hybrids within a potential window of 0–0.80 V at a current density of 1 A g−1 (modified), and (d) plots of specific capacitance for PANI-HS36 and PANI-HS36@ERGO hybrids at various current densities (modified).587 Figure reproduced with permission from ACS. | ||
Du et al.588 used MnO2 nanotubes as the reactive template for the preparation of PANI nanotubes using an in situ polymerization process, that exhibited excellent specific capacitance (455.7 F g−1 at 0.5 A g−1), rate capability of 63.2% even up to 30 A g−1. However, it showed poor cycling stability due to the swelling and shrinking of PANI during intercalating/deintercalating. Therefore, they fabricated hierarchical carbon layer-encapsulated PANI nanotubes by a hydrothermal method and observed its superior performance compared with the PANI nanotubes. In addition, the assembled symmetric supercapacitors based on this delivered high energy density (42.32 Wh kg−1) and power density (16.44 kW kg−1) and had good cycling stability. Mini and Devendrappa589 prepared a core/shell polyaniline/NiO nanocomposite and studied its electrochemical performance as an electrode in supercapacitor applications. These findings revealed its specific capacitance, energy density, power density and coulombic efficiency corresponding to 362 F g−1 (1 A g−1), 50.2 Wh kg−1, 0.50 kW kg−1 and 99% (at 4 Ag−1), respectively. The enhanced specific capacitance performance was ascribed to the nanosized effect of NiO and the synergic effect between NiO and PANI.
Polypyrrole nanosphere (dia: ∼70 nm)/graphene oxide synthesized via in situ surface-initiated polymerization exhibited specific capacitance of 370 F g−1@0.5 A g−1, and capacitance retention of 91.2% even after 4000 cycles owing to the core–shell structure and synergistic effect.590 Qi et al.591 reported the preparation of core–shell-structured tubular graphene nanoflake-coated polypyrrole nanotubes and observed its large capacitance, high capacitance retention and stable cycling performance. The energy density and cycling stability of the symmetric supercapacitor device based on this correspond to 11.4 μWh cm−2 at 720 μW cm−2 and over 80% capacitance retention after 5000 cycles, respectively.
In recent years, there has been considerable interest in studying the capacitive properties of MoS2 for its application in supercapacitors.592–597 However, despite many advantages, the aggregation, poor electrical conductivity and specific capacitance of MoS2 limit its practical application in energy storage electrode materials.592 As a result, MoS2 is combined with conducting polymers to overcome this problem. In view of this, Chen et al.593 prepared urchin-like MoS2@PANI (MoS2: 25 wt%) by a hydrothermal method and observed its maximum capacitance of 645 F g−1 at 0.5 A g−1 due to the synergistic effect. In addition, excellent cycling stability (89% capacitance retention) was observed after 2000 cycles at a current density of 10 A g−1.
Zhang et al.594 fabricated core/shell microspheres comprising hollow MoS2/PANI-5 (5 represents the mass ratio of aniline to hollow MoS2 microspheres). The electrochemical studies of this electrode material displayed the specific capacitance of 633 F g−1 @0.5 A g−1 and retention of the capacitance up to 86.0% after 1000 cycles at 10 A g−1, benefitting from polyaniline confined firmly on the microspheres of MoS2. In addition, in the MoS2/PANI-5 composite the energy density could deliver 31.7 W h kg−1 at the power density of 0.3 kW kg−1.
A template-assisted method was employed to synthesize the MoS2/PANI (mass ratio = 1
:
2) hollow microsphere and used as a promising electrode for a supercapacitor.595 SEM images clearly established the coating of PANI on the surface of the hollow structure of MoS2 microspheres (dia: ∼2 μm). The specific capacitance was found to be 299 F g−1 at a scan rate: 10 A g−1 and was attributed to the synergistic effect of MoS2 core and PANI coating shell. MoS2/PANI microsphere electrode materials also delivered excellent cycling stability, as evident from its retention of 84.3% after 8000 cycles. The investigations also indicated the energy density reaching 23.1 Wh kg−1 at a power density of 8320 W kg−1. The specific capacitances of the fabricated symmetric supercapacitor based on MoS2/PANI microspheres electrodes corresponded to 231, 139, 97, 79 F g−1 at the current density of 0.2 A g−1. Furthermore, the assembled symmetric supercapacitor also exhibited high cycling stability (80.4% after 5000 cycles at 1 A g−1). These findings highlighted the potential application of MoS2/PANI hollow microspheres for supercapacitors.
Ansari et al. reported596 the formation of a mechanically exfoliated MoS2 sheet coupled with polyaniline. TEM studies of the product indicated PANI was coated on the MoS2 sheet and displayed the specific capacitance of 510.12 F g−1 at a current of 1 A g−1 due to the synergistic effect and interfacial interaction. The hierarchical PEDOT@MoS2 showed high specific capacitance (2540 mF cm−2 at 1 mA cm−2) and excellent capacitance retention (98.5%) after 5000 cycles at a high current density of 100 mA cm−2.597 This was ascribed to the hierarchical core/shell structure of the electrode material and the synergic effect. In addition, the assembled asymmetric supercapacitor delivered a high energy density (937 Wh m−2) at 6500 W m−2 and excellent cycling stability with capacitance retention of 100% (5000 cycles).
According to Liang et al.,598 V2O5@PPy displayed high conductivities and the synergic effect accounted for the specific capacitance of 307 F g−1 and good cycling life (82% capacity retention up to 1000 cycles). Such performance of V2O5@PPy benefited from the enhanced conductivity, synergistic effect, and the stability of the composite. The symmetric V2O5/PPy device exhibited a maximum energy density of 37 Wh Kg−1 at a power density of 161 W kg−1. In addition, polyaniline-carbon nanotube core–shell,599 pistil-like MnCo2O4.5@PANI,600 and high-performance electrodes for supercapacitors.601 Ni ferrite@Polypyrrole,602 core/sheath structured ultralong MnOx/PPy nanowires,603 and CuS@PANI604 also displayed superior performance as electrodes in supercapacitor applications. The performance of MWCNT coated with PANI (core dia: ∼80–150 nm) has also been evaluated for supercapacitor application.605 The findings showed maximum specific capacitance (552.11 F g−1 at 4 mA cm−2) for PANi/MWCNT (10 wt%) in 1 M H2SO4.
Xia et al.606 prepared a core–shell PANI/CNTs nanostructured hybrid by chemical vapor and electrochemical deposition methods according to Fig. 40. Subsequent findings based on galvanostatic charge/discharge (GCD) curves of CNTs and PANI/CNTs with and without the addition of 0.02 M Fe3+/Fe2+ are displayed in Fig. 41(a). It was inferred that discharge time was extended on the addition of the Fe3+/Fe2+ redox couple. The following order for discharge time was observed: PANI/CNTs (0.02 M Fe3+/Fe2+) > PNI/CNTs > CNT (0.02 M Fe3+/Fe2+) > CNTs. GCD curves of PANI/CNTs at different current density in 1 M H2SO4 in Fig. 41(b) confirmed the ideal capacitive mechanism of the core–shell hybrid. GCD curves of PANI/CNTs in 1 M H2SO4/0.02 M Fe3+/Fe2+ electrolyte at different current densities are displayed in Fig. 41(c). These findings affirmed a non-ideal triangular pattern corresponding to the redox reaction behavior of the Fe3+/Fe2+ redox couple. The specific capacitance curves of PANI/CNTs at different current densities in Fig. 41(d) showed improvement in the specific capacitance of PANI/CNTs (1005 F g−1) on adding 0.02 M Fe3+/Fe2+ (1547 F g−1) at 2 A g−1 in 1 M H2SO4. This superior performance was attributed to the synergistic effect originating from the contribution of the Fe3+/Fe2+ redox couple and the PANI/CNTs core–shell structure. In addition, the specific capacitance of the assembled symmetric architecture device was calculated and found to be 412 F g−1 at 0.5 A g−1. In addition, the energy density (22.9 Wh kg−1) at a power density of 700.1 W kg−1 and the capacitance retention of 97% (2000 charge–discharge cycles) was reached using PVA/H2SO4/Fe3+/Fe2+ gel as redox electrolyte. These findings supported the role played by the core–shell PANI/CNT hybrid electrode and Fe3+/Fe2+ redox additive electrolyte in achieving this enhanced electrochemical performance.
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| Fig. 40 Illustrations of the fabrication process for PANI/CNTs on carbon cloth (CC).606 Reproduced with permission from Springer. | ||
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| Fig. 41 (a) GCD curves of CNTs and PANI/CNTs at 1.5 mA cm−2 in 1 M H2SO4 with and without the addition of 0.02 M Fe3+/Fe2+. (b) GCD curves of PANI/CNTs testing in 1 M H2SO4 electrolyte at different current densities. (c) GCD curves of PANI/CNTs testing in 1 M H2SO4/0.02 M Fe3+/Fe2+ electrolyte at different current densities. (d) Specific capacitance curves of PANI/CNTs at different current densities.606 Reproduced with permission from Springer. | ||
An enhanced electrochemical performance has been reported for the hierarchical NiCo2S4@PANI core–shell nanowires grown on a carbon filter.607 The specific capacitance of the electrode fabricated in this manner showed enhanced areal capacitance of 4.74 F cm−2 (1823 F g−1) at 2 mA cm−2 and a capacitive retention of 86.2% (5000 cycles) compared with NiCo2S4/CF due to the availability of the more electrochemically active sites and faster ionic diffusion. The excellent cycling stability of NiCo2S4@PANI/CF was suggested to be induced by the presence of the PANI shell. The assembled asymmetric supercapacitor (positive electrode: NiCo2S4@PANI/CF, negative electrode: graphene/CF) delivered a high energy density of 64.92 Wh kg−1 at a power density of 276.23 W kg−1. This was found to be significantly higher compared with the asymmetric and symmetric supercapacitors based on NiCo2S4 and was ascribed to the core/shell heterostructure of NiCo2S4@PANI/CF.
Pan et al.608 displayed more surface capacitive contribution and enhanced electrochemical performance benefiting from the unique heterostructure in NiCo2O@Polyaniline nanotubes anchored on carbon. Their finding showed a specific capacitance of 720.5 C g−1 at 1 A g−1, found to be much better than that of NiCo2O4. In addition, cycling performance and coulombic efficiency was also investigated for the NiCo2O4@PANI electrode. These findings showed the sample retaining 99.64% of its initial gravimetric capacity following 10
000 cycles with 100% coulombic efficiency due to the high efficiency of rapid electron transfer for charge storage and delivery. They also suggested that unique coaxial structure of NiCo2O4@Polyaniline increases the interface area of the electrode/electrolyte and facilitates a shorter diffusion path for ions and electrons.
Mu et al.609 used polystyrene sulfonate microspheres as a template to fabricate graphene/polyaniline hybrid hollow microspheres in two steps involving the layer-by layer assembly technique followed by in situ oxidative chemical polymerization. Subsequent studies have indicated a specific capacitance of graphene/polyaniline hybrid hollow microspheres of ∼633 F g−1 in a 1.0 M H2SO4 electrolyte as well as excellent cycling stability (with 92%) of its original specific capacitance, in all probability due to the synergistic effect. Alternatively, the contribution of the unique structure facilitating the reduced transport lengths for both mass and charge transport also cannot be ruled out. The energy density has also been calculated and found to be 382.97 Wh kg−1 at a current density of 10 mA cm−2.
In another study, the hierarchical polyaniline/NiCo-layered double hydroxide (PANI/NiCo-LDH) core–shell composite nanofiber network was prepared by a two-step strategy (in situ oxidative polymerization and electrochemical deposition) on carbon cloth.610 The choice of a LDH nanosheet shell grown on the PANI network in this work was guided by the role it plays in facilitating ion and electron transport and also in relieving the strain change of the electrode during redox reaction. The electrode fabricated in this manner delivered a specific capacitance of 1845 F g−1 at 0.5 A g−1 and excellent cycling stability (82% after 5000 cycles at 10.0 A g-1), benefiting from rapid electron transport and ion diffusion. In addition, the assembled asymmetric device (positive electrode: PANI/NiCo-LDH, negative electrode: activated carbon) displayed excellent energy density (46.0 Wh kg−1) at a power density of 351.6 W kg−1 and good cycling performance. Polyaniline/graphene nanosheets,611 Co(OH)2–polyaniline,612 polyaniline/NiCo2S4,613 carbon nanotube@polypyrrole core–shell,614,615 and a Janus-type α-Fe2O3/PEDOT nanoparticles core/shell616 also functioned as high-performance supercapacitive electrode materials.
Moreno et al.622 recorded the cyclic voltammetry (CV) of vertically aligned ZnO@CuS@PEDOT core@shell nanorod arrays decorated with MnO2 nanoparticles at different scan rates in 1 M LiClO4 aqueous electrolyte. The appearance of a more-or-less quasi-rectangular with symmetric shape of CV indicated the fast reversible reaction and an ideal capacitor-type behaviour. Furthermore, ZnO@CuS@PEDOT exhibited excellent electrochemical performance, as evident from its high specific areal capacitance of 19.85 mF cm−2, good rate capability and cycling stability. This promising capacitive behavior was attributed to the unique hierarchical core–shell hybrid nanorod configuration and synergistic effects. A core@shell hollow Bi2O3−x@Carbon fiber@PEDOT electrode fabricated through a multistep process exhibited specific capacitance of 460 F g−1 (1 A g−1) and reasonably good cycling stability.623 It was also noted that energy density, power density and remarkable cycling performance in the assembled symmetric supercapacitor corresponded to 16.4 Wh kg−1, 500.34 W kg−1 and 99% capacitance retention after 8500 cycles.
The coaxial core–sheath shaped supercapacitor based on polypyrrole-functionalized graphene/carbon nanotubes hollow fibers exhibited ultrahigh length specific capacitance and energy density.624 According to Ghosh et al.,625 an asymmetric supercapacitor comprising 3-D urchin shaped coaxial MnO2@PANI composite and a self-assembled 3-D pillared graphene foam exhibited an energy density of 37 Wh kg−1 at a power density of 386 W kg−1 and stable cycling performance. In another report, graphene carbon sphere@PANI@RGO composites reached specific capacitance of 446.19 F g−1 (scan rate: 5 mV s−1) in 1 M H2SO4 solution with 93.4% capacitance retentions after 1000 cycles.626 Wang et al.627 prepared a core–shell MoS2/PPy/PANI ternary hybrid with a ‘pizza-like’ nanostructure. It achieved a high specific capacitance (1273 F g−1 at 0.5 A g−1) with good cycling performance (83% after 3000 charge/discharge cycles). This was ascribed to the synergistic effect, improved electrical conductivity and enhanced electrolyte/electrode interaction. Recently, Liu et al.628 synthesized poly(3,4-propylenedioxythiophene)-OH/CoNi-SeS@Hollow carbon sphere via a sulfurization/selenization ion exchange method and in situ oxidation, and showed excellent electrochemical performance (mass specific capacity: 775.1 C g−1 at 1 A g−1). The assembled asymmetric supercapacitor device possessed a good energy density (84.8 Wh kg−1) and excellent power density (8000 W kg−1), and the capacity retention rate of 82.85% at 4 A g−1 (after 20
000 cycles). It was suggested that a synergistic effect of the conductive polymer, the hollow structure, and modified electronic structure contributed to achieving the better capacitance performance.
Polypyrrole-coated low-crystallinity Fe2O3 supported on carbon cloth,321 graphene/polyaniline/MnO2,322 GO/α-MnO2/PANI,323 (CoCrFeMnNi)3O4@CC-PPy,324 LaMnO3@CC-PPy,325 PPy/black phosphorus oxide/CNT,326 PANI/GO/CuFe2O4629 and PANI-coated CuO–ZnO–MnO630 have also been investigated as electrodes for their supercapacitor performance.
Table 6 shows the electrochemical performance of various supercapacitors fabricated based on polyaniline electroactive material.
| Electrode material | Method of preparation | Electrolyte | Specific capacitance (current density) | Cycling stability | Energy density (ED) | Power density (PD) | Ref. |
|---|---|---|---|---|---|---|---|
| Ppy1%/DBSA2%/NiO97%-GS | Electrodeposition at 4 mA cm−2 for 10 min | 0.1 M LiClO4 | 679 at 1 A g−1 | 83.9% (1000 cycle) at 1 A g−1 | 94.4 Wh kg−1 | 94.4 W kg−1 | 154 |
| MnO2@PPy | Hard template (PS) method. | 1 M Na2SO4 | 295 F g−1 at of 1 A g−1 | 100% (20 000 cycles) 10 A g−1 |
42 Wh kg−1 | 1100 W kg−1 | 239 |
| Core–shell nanorod arrays with PANI deposited into NiCo2O4 | Electrochemical polymerization | 1 M H2SO4 | 901 F g−1 at1 A g−1 | 91% (3000 cycles) at 10 A g−1 | 81.77 Wh kg−1 at a PD of 399.3 W kg−1 | — | 320 |
| D-Fe2O3@PPy/CC | Chemical reduction and electrodeposition methods | 1 M Na2SO | 640 F g−1 at 1 mA cm-1 | 79.3% of its (10 mA cm-2) after 5000 cycles | — | — | 321 |
| (CoCrFeMnNi)3O4@CC-PPy | Two-step electrodeposition | 2 M H2SO4 | 791 F g−1 at 0.5 A g−1 | 63% (5000 cycles) at 10 A g−1 | 49.2 Wh kg−1 (PD: 800 W kg−1) | — | 324 |
| LaMnO3@CC-PPy | Two-step electrodeposition | 862 F g−1 at 1 A g−1 | 66% (3000 cycles) at 10 A g−1 | 73 Wh k−1 | — | 325 | |
| Hollow polyaniline helical nanobelts | By chemical oxidation of aniline | — | 688 F g−1 at 5 mV s−1 | 81.6% (1000 cycles) | 14.37 Wh kg−1 at PD of 500 W kg−1 | — | 492 |
| Hollow polyaniline microspheres | In situ chemical oxidative polymerization with SPS spheres as the template | 1 M H2SO4 | 421 F g−1 | 45% (500 cycles) at 10 mA cm−2 | — | — | 552 |
| Hollow polyaniline nanocapsules | Interfacial polymerization method | 1 M H2SO4 | 502 F g−1 at 5 mA cm−2 | 83.1% (1000 cycles) at 10 mA cm−2 | — | — | 553 |
| Ce3+-doped polyaniline hollow microspheres | Self-assembly method | H2SO4 | 248.2 F g−1 at 1 mA cm−2 | 41.6% (5000 cycles) at 5 mA cm−2 | — | — | 555 |
| Hollow polyaniline nanospheres | Self-sacrificial templates and emulsion polymerization | 1 M HCl | 485.5 F g−1 at 1 A g−1 | 69% (500 cycles) at 5 A g−1 | — | — | 556 |
| Polypyrrole hollow nanospheres | Hard template method | 1 M H2SO4 | 350 at 1A g−1 | — | 40 Wh kg−1 | 490 W kg−1 | 557 |
| Hollow polypyrrole films | Electrochemical oxidative polymerization of pyrrole | ∼300 F g−1 at 3 A g−1 | No decrease in capacitance (1000) | — | — | 558 | |
| Hollow capsular polypyrrole nanofiber | Vapor-phase polymerization | 1 M H2SO4 | 203 F g−1 at 2 mV sec−1 | >90% (11 000 cycles) at 10 A g−1 |
— | — | 559 |
| Nanotubular-polyaniline | Using natural tubular halloysite as hard template | 1 M H2SO4 | 654 F g−1 at 1 A g−1 | 120% (until 2000 cycles) and 87% (10 000) at 100 mV s−1 |
— | — | 560 |
| Polyaniline nanotube arrays | Electrochemical polymerization using ZnO nanorod arrays as sacrificial templates | 1 M H2SO4 | 675 F g−1 at 50 mV sec−1 | Decrease in ∼30% of Csp value (100) at 50 mV s−1 | — | — | 561 |
| Polyaniline nanotubes (inner dia: 80 nm, outer dia: 180 nm) | One-step polymerization and acrylic acid in aqueous solution | 1 mol L−1 H2SO4 | 436 F g−1 at 0.5 A g−1 | 89.2% (500 cycles) at 0.5 A g−1 | — | — | 563 |
| Crystalline tetragonal hollow PANI nanotubes | MO (self-sacrificial template) in acidic solutions to facilitate the growth of PANI nanotubes | 1 mol L−1 H2SO4 | ∼590 ± 36 1 F g−1 at 5 mV s−1 | Capacitance loss of 49.6% (1000 cycles) at 10 A g−1 | 14.56 Wh kg−1 at PD of 250 W kg−1 | — | 564 |
| PPy hollow nanoparticles | Surfactant-templated chemical oxidation polymerization | 1 M Na2SO4 | 326 F g−1 at A g−1 | 86% (10 000 cycles) |
— | — | 565 |
| Hollow polyaniline nanofiber | Chemical oxidation polymerization | 1 M H2SO4 | 290 F g−1 at 1 A g−1 | 83% (1000 cycles) at 3 A g−1 | — | — | 568 |
| MnO2/polyaniline hollow sphere | Interfacial synthesis | 0.5 M Na2SO4 | 262 F g−1 at 1.5 mA cm−1 | 93% (800 cycles) at 9 mA cm−1 | — | — | 570 |
| 3D-hollow balls of graphene-polyaniline | Self-assembly method | 1 M H2SO4 | 331 F g−1 at 1 A g−1 | 14% loss of capacitance (500 cycles) at 1 A g−1 | — | — | 571 |
| 3D-graphene–polyaniline hybrid hollow spheres | Layer-by-layer assembly | 1 M H2SO4 | 381 F g−1 at 4.0 A g−1 | 83% (1000 cycles) at 0.5A g−1 | — | — | 572 |
| Hollow polyaniline nanotubes supported on Ti3C2 MXene | By exfoliating Ti3C2 followed by in situ polymerization | 1 M H2SO4 | 596.6 F g−1 at 0.1 A g−1 | 94.7% (5000 cycles) at 1 A g−1 | 25.6 Wh kg−1 at PD of 153.2 W kg−1 | 1610 Wkg−1 at ED of 13.2 Wh kg−1 | 573 |
| RGO/polyaniline nanotubes | In situ reduction | 1 M-H2SO4 | Unirradiated: 448 F g−1 at 0.5 A g−1 | Unirradiated: 89% (1000) | Unirradiated: 30.52 Wh kg−1 | Unirradiated: 174.96 W kg−1 | 574 |
| RGO/polyaniline nanotubes | In situ reduction | 1 M-H2SO4 | Irradiated: 482 F g−1 at 0.5 A g−1 | Irradiated: 92% (1000 cycles) | Irradiated: 32.81 Wh kg−1 | Irradiated: 174.98 W kg−1 | 574 |
| Graphene–polypyrrole hollow sphere | Pickering emulsion polymerization | 1 M H2SO4 | 238 F g−1 at 1 A g−1 | 90.7% (1500 cycles) at 1 A g−1 | — | — | 576 |
| N-doped graphene (NG)/hollow PPy | Hollow PPy nanospheres prepared by using a sacrificial template and embedded in NG layers | 1 M HCl | 575 F g−1 at a current density of 1 A g−1 | 90.1 (500 cycles) at 1 A g−1. | 47.92 Wh kg−1 at 1 A g−1 | — | 577 |
| Polyaniline hollow nanospheres encaging RuO2 nanoparticles | Polymerizing aniline monomers on 3D-arrayed PS nanospheres | 1.0 M aqueous HClO4 | 1570 F g−1 at 10 mV s−1 | 77.6% (1000 cycles) at 10 mV s−1 | — | — | 578 |
| Polyaniline hollow fibers (PANI-HF) | In situ polymerization of aniline in the presence of electrospun PAN nanofibers | 1 M H2SO4 | 425 F g−1 at 20 mV s−1 | 72% (500 cycles) at 100 mV s−1 | — | — | 579 |
| PANI-hollow fiber decorated by RGO | Self-assembling of GO sheets on PANI-HF followed by electrochemical reduction of GO | 1 M H2SO4 | 449 F g−1 at 20 mV s−1 | 91% (500 cycles) at 100 mV s−1 | — | — | 579 |
| Graphene–polypyrrole nanotube | Multi steps | 2 M H2SO4 aqueous solution | 324 F g−1 at 1.5 A g−1 | 88% (200 cycles) at 1.5 A g−1 | — | — | 580 |
MOF-PPy tubes (mass ratio % of PPy : 28) |
Dispersion and mixing method | 1 M Na2SO4 | 554.4 F g−1 at 0.5 A g−1 | 90.7% (10 000 cycles) at 20 A g−1 |
0.0113 mW h cm−2 with PD of 0.12 mW cm−2 | — | 581 |
| Hollow PPy nanospheres decorated on CNTs | Via in situ chem. oxid. emulsion interfacial polymerization | 1.0 M aqueous NaNO3 | 33.9 F g−1 at 20 mV s−1 | 71% (500 cycles) | — | — | 582 |
| Polyaniline nanowires wrapped on the polypyrrole nanotubes | Chemical synthesis method | 1 M H2SO4 | 765 F g−1 at a scan rate of 10 mV s–1 | 86.3% (1000 cycles) at 10 mV s−1 | — | — | 583 |
| Core–shell polyaniline-functionalized carbon quantum dots (CQDs) | Via adsorption of CQDs on PANI to be produced PANI | 1 M H2SO4 | 264.6 F g−1 at 2.5 A g−1 | High stability (5000 cycles) | — | — | 584 |
| PPy@PANI nanosphere | By dilute solution polymerization | H2SO4 | 510 F g−1 at 10 mV s−1 | 87.6% (1000 cycles) at 5 A g−1 | — | — | 585 |
| Polypyrrole@poly(1,5-diaminoanthraquinone) | Dispersion and sonication | 1.0 M H2SO4 | 533 F g−1 at 1 A g−1 | 107.4% (10 000 cycles) at 100 mV s−1 . |
7.5 Wh kg−1 (at a PD of 96.1 W kg−1) | 1124.9 W kg−1 (at ED of 4.0 Wh kg−1) | 586 |
| Graphene-wrapped polyaniline hollow spheres | Solution-based coassembly process | 1 M H2SO4 | 614 F g−1 at 1 A g−1 | 90% (500 cycles) 1 A g−1 | — | — | 587 |
| Carbon layer-encapsulated polyaniline nanotubes | In situ polymerization + hydrothermal method | 1 M H2SO4 | 410.5 F g−1 at 1 A g−1 | 63% (2000 cycles) | 42.32 Wh kg−1 | 16.44 kW kg−1 | 588 |
| Polyaniline/nickel oxide core/shell | In situ polymerization in the presence of NiO nanoparticles | 1 M H2SO4 | 372 F g−1 at 20 mV s−1 | — | 50.2 Wh Kg−1 at 1 Ag−1 | 0.50 kW Kg−1 at 1 Ag−1 | 589 |
| Core–shell nanospherical polypyrrole/graphene oxide | In situ surface-initiated polymerization method | 1.0 M H2SO4 | 370 F g−1 at 0.5 A g−1 | 91.2% (4000 cycles) | — | — | 590 |
| MoS2@PANI (wt% of MoS2 in: 71.2% for sample react 24 h) | Chemical polymerization | 0.5 M H2SO4 | 669 F g−1 at 1 A g−1 | 91% (4000 cycles) at 10 A g−1 | 106 Wh kg −1 at a power density of 106 kW kg−1 | — | 592 |
| MoS2@Polyaniline (with 25 wt% MoS2) | One-pot hydrothermal method, energy density was 25.7 Wh kg | 1 M H2SO4 | 645 F g−1 at 0.5 A g−1 | 89% (2000 cycles) at 10 A g−1 | 25.7 Wh kg−1 at PD of 779.9 W kg−1 | — | 593 |
| Hollow MoS2/PANI core/shell microsphere | In situ oxidative polymerization | 1 M H2SO4 | 633 F g−1 at 0.5 A g−1 | 86.0% (1000 cycles) at 10 A g−1 | 31.7 W h kg−1 at 0.3 kW kg−1 | — | 594 |
| MoS2/polyaniline hollow microsphere | Template-assisted method | 1 M H2SO4 | 364 F g−1 at a scan rate of 5 mV s−1 | 84.3% (8000 cycles) at 10 A g−1 | 32 Wh kg−1 at PD of 320 W kg−1 | — | 595 |
| Mechanically exfoliated MoS2 sheet coupled with polyaniline | In situ chemical oxidative polymerization | KOH | 510.12 F g−1 at 1 A g−1 | ∼80% (2500 cycles) | — | — | 596 |
| PEDOT@MoS2 | Electrochemical co-deposition of EDOT and MoS2 | 1 M H 2SO4 | 2540 mF cm−2 at 1 mA cm−2 | 98.5% (5000 cycles) at 100 mA cm−2 | 937 Wh m−2 at PD of 6500 W m−2 | — | 597 |
V2O5@Polypyrrole (V2O5 Sol : Pyrrole : SDBS = 40 ml : 0.1 ml : 20 mg) |
Sol–gel with in situ polymerization method | 1 M Na2SO4 | 307 F g−1 at 1 A g−1 | ∼60% (2000 cycles) at 3 A g−1 | 37 Wh Kg−1 at PD of 161 W kg−1 | — | 598 |
| 3D core–shell pistil-like MnCo2O4/polyaniline | Electrochemical deposition polymerization | 2 M KOH | 1098 F g−1 at 1 A g−1 | 83.2% (5000 cycles) at 10 A g−1 | — | — | 600 |
| Nickel ferrite/polypyrrole core–shell | In situ chemical oxidation containing sodium dodecyl sulfate | 0.1 N H2SO4 | 721.66 F g−1 at 1 A g−1 | No significant change (1–1000 cycles) | 51.95 Wh kg−1 | 6.18 kW kg−1 | 602 |
| Core/sheath-structured ultralong MnOx/polypyrrole nanowires | In situ polymerization | 1.0 M Na2SO4 | 1091.4 F g−1 at 1 A g−1 | 97.4% (10 000 cycles) at 10 A g−1 |
144 Wh kg−1 at PD of 1100 W kg−1 | — | 603 |
| CuS@Polyaniline microspheres | Chemical oxidative polymerization | Li2SO4 | 308.1 F g−1 at 0.5 A g−1 | 71.6% (1000 cycles) at 1 A g−1 | __— | — | 604 |
| Polyaniline/CNT core–shell | Chemical vapor deposition and electrochemical deposition | 1 M H2SO4 electrolyte | 823 F g−1 at 5.0 A g−1 | — | 22.9 Wh kg−1 at PD of 700.1 W kg−1 | — | 606 |
| Hierarchical NiCo2S4@Polyaniline grown on carbon fiber | Hydrothermal method and potentiostatic deposition | 6 M KOH | 1823 F g−1 at 2 mA cm−2 | 86.2% (5000 cycles) | 64.92 Wh kg−1 at PD of 276.23 W kg−1 | — | 607 |
| NiCo2O4@PANI nanotubes anchored on C | Electrodeposition method | — | 720.5 C g−1 at 1 A g−1 | 99.64% (10 000 cycles) |
— | — | 608 |
| Graphene/polyaniline hybrid hollow microspheres | Combination of layer-by layer assembly and in situ chemical oxidative polymerization | 1.0 M H2SO4 | 633 F g−1 at 10 mA cm−2 | 92% (1000 cycles) at at 80 mV s−1 | 382.97 Wh kg−1 at 10 mA cm−2 | — | 609 |
| PANI/NiCo-LDH core–shell composite | Electrochemical deposition method | 2.0 M KOH | 1845 F g−1 at 0.5 A g−1 | 82% (5000 cycles) at 0.5 A g−1 | 46.0 Wh kg−1 at PD of 351.6 W kg−1 | — | 610 |
| Graphene nanosheets coating with polyaniline | In situ polymerization | 6 M KOH | 261.4 F g−1 at 100 mA g−1 | Capacitance decreased to 161.2 F g−1 after 500 cycles at 0.1 A g−1 | — | — | 611 |
| Polyaniline-coated NiCo2S4 | Chemical oxidative polymerization | PVA-KOH gel | 1879 F g−1 at 1 A g−1 | 91.1% (2000 cycles) at 8 A g−1 | 54.06 Wh kg−1 at PD of 0.79 kW kg−1 | 27.1 Kw kg−1 at ED of 15.9 Wh kg−1 | 613 |
| Hierarchical core/shell Janus-type a-Fe2O3/PEDOT | Multistep process | PVA–H2SO4 Hydrogel | 252.8 F g−1 at 0.1 A g−1 | 92% (1000) at 0.6 A g−1 | 136.3 Wh kg−1 | 10 526 W kg−1 |
616 |
| Core/double shell PANI/chitosan/cobalt oxide | In situ chemical oxidation method | 1 M H2SO4 | 1253 F g−1 at 5 mV s−1 | 91% (5000) at of 1 A g−1 | 95.42 Wh kg−1 at 1 A g−1 | 1549 W kg−1 at 3 A g−1 | 617 |
| Polyaniline-Ag-MnO2 nanorod | Two-step process | 2 M KOH | 1028.6 F g−1 at 1 A g−1 | 93.7% (5000 cycles) at 10 A g−1 | 49.77 Wh kg−1 | 1599.75 W kg−1 | 618 |
| Polyaniline@CNTs–MnO2 | Hydrothermal and in situ oxidative polymerization of aniline | 0.1 M KOH | 143.26 C g−1 at 3 mV s−1 | 119% (3500 cycles) at 3.0 A g−1 | 27.17 Wh kg−1 at 0.3 A g−1 | 298.00 W kg−1 at 0.3 A g−1 | 619 |
| MWCNTs@MnO2@Polypyrrole | Multiple steps | — | 272.7 F g−1 | 60% after 300 cycles | — | — | 620 |
| ZnO NRs@CuS@PEDOT@MnO2 | Multiple steps | 1 M LiClO4 | 19.85 mF cm−2 at 5 mV s−1 | 18% loss of initial value (1500) at 100 mV s−1 | — | — | 622 |
| Hollow Bi2O3@Carbon fibre@PEDOT | Electrospinning technique using stabilization, pyrolyzation and polymerization | PVA-KOH g | 460 F g−1 at 1 A g−1 | 93.6% (10 000 cycles) at 2 A g−1 |
16.4 Wh kg−1 | 500.34 W kg−1 | 623 |
| Hierarchical graphene/polyaniline hollow microsphere | Multiple steps | 1 M H2SO4 | 446.19 F g−1 at 5 mV s−1 | 93.4% (1000 cycles) at 2 A g−1, 8.7% (5000 cycles) at 2 A g−1 | — | — | 626 |
| “Pizza-like” MoS2/polypyrrole/polyaniline architecture | Multistep process | 0.5 m H2SO4 | 1273 F−1 g at 0.5 A g−1 | ∼83% (3000 cycles) at 2 A g−1 | — | — | 627 |
Electromagnetic interference creates electronic pollution that is very harmful to human health and the functioning of electronic devices and remains a critical challenge for researchers.9 The practical application of electromagnetic interference/microwave absorption materials is limited by complex synthetic procedures and expensive raw materials. In this regard, lightweight hollow ICPs and their binary and ternary composites and core–shell structured materials are reported in trapping/absorbing electromagnetic waves to enhance dielectric loss, multiple internal reflection, and scattering of EM waves.9 However, challenges require researchers to develop thermally and mechanically stable hollow-structured ICPs, their composites, and core–shell-based materials with superior electrical conductivity, dielectric/magnetic, and corrosion-resistance properties, for applicability to a wide range of frequencies and absorption bandwidth.54 The conducting blends with simultaneously enhanced mechanical properties could also be interesting for future applications in EMI shielding and microwave absorption.388
The removal of heavy metals and organic dyes in wastewater remains a critical challenge for researchers.84,88 In this regard, polyaniline and polypyrrole have attracted considerable attention as promising adsorbents in the separation of dyes and metal ions from wastewater. In view of this, hollow conducting polymers60–64 and core–shell materials66,67 hold great promise in the adsorptive removal of metal ions from wastewater due to their enhanced surface area, tunability, and potential for synergistic effects.88 Challenges exist in developing low-cost, high-performing adsorbents with significantly enhanced activity and long-term stability for the separation of the mixture of individual dyes, metal ions, dye/metal ions and other types of pollutants present in wastewater. Furthermore, regeneration of the spent adsorbents is still challenging and needs more attention in developing cost-effective regeneration methods for their reusability with high economic viability and environmental sustainability.631 Furthermore, safe disposal or reuse of spent/exhausted adsorbents also needs to be considered.
Hollow ICPs have emerged as a promising electrode material in supercapacitor applications. Their larger surface area and shorter ion diffusion path facilitate faster charging and discharging.72,73 However, the future scope of hollow conducting polymers as an electrode material is limited due to their poor structural stability, which results in lower cyclability and capacity retention of the assembled supercapacitor.632 This problem can be mitigated by fabricating nanocomposites by integrating different components, such as carbonaceous, metal oxides, metal chalcogenides, and MXene base materials through an inexpensive and facile synthesis approach. Attention is also focused on achieving enhanced mechanical stability of hollow ICPs to prevent degradation during repeated charging and discharging cycles. In addition, the fabrication of hollow copolymers of ICPs remains another area not well addressed so far.633 In addition, core–shell nanostructured electrode materials fabricated by the coating of ICPs on a conducting core have been very promising due to the short ion transport pathways and abundant active sites. Recently, the electrodeposition method has also received more attention, though there exist several challenges in real-world applications.
Future research also needs to be focused on the development of new cost-effective synthetic core–shell methods. This can be realized by utilizing naturally driven green and sustainable biomass,634 plant waste,635 marine bio-waste,636 marine plastic waste,637 biomass waste,638–642 cotton,643 fly ash of coal waste644 and agricultural by-products645 as a source of carbon in realizing the fabrication of conducting polymer-coated core–shell materials across the three distinct application fields.
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