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Review  |  Open Access  |  7 Nov 2024

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

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Energy Mater 2024;4:400079.
10.20517/energymater.2024.34 |  © The Author(s) 2024.
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Abstract

The rechargeable alkali metal-ion batteries (RAMIBs) are highly promising candidates for next-generation efficient energy storage devices, owing to their outstanding theoretical specific capacities and extremely low electrochemical potentials. However, RAMIBs possess unsuitable lifespans, low mechanical durability and inevitable side reactions attributable to their inherent severe volumetric/structure alteration during the charge-discharge cycles. These hitches could be solved using porous multimetallic alloy-based anodes, due to their impressive specific capacities, low working potential, low cost, and earth-abundance, which can meet sustainability and practical application needs. Meanwhile, great surface area, electrical conductivity, structural stability, and ability to accommodate the generated alkali metal ions can yield satisfactory coulomb efficiency and long durability. Immense efforts are dedicated to rationally designing porous multimetallic alloy-based anodes for RAMIBs, so it is essential to provide timely updates on this research area. Herein, we reviewed recent advances in porous multimetallic alloy-based anodes (i.e., Sn, Mn, Mo, Co, V, and Fe) for RAMIBs (i.e., lithium-ion batteries, sodium-ion batteries, and potassium-ion batteries. This is rooted in the engineering approaches (i.e., template-based, hydrothermal/solvothermal, chemical reduction, electrochemical deposition, sol-gel, and electrospinning) to fundamental insights (i.e., mechanisms, key parameters, and calculations) and precise evaluation for structural changes, and mechanisms by various experimental, theoretical, and in-situ analysis to optimizing their performance. Also, advances in RAMIBs recycling and circular economy were discussed. Eventually, we highlighted the current drawbacks and provided proposed perspectives to solve these issues and enable practical utilization of such anodes for large-scale applications.

Keywords

Alkali metal-ion batteries, porous multimetalllic alloy-based anodes, lithium-ion, sodium-ion, and potassium-ion batteries, battery recycle

INTRODUCTION

There are global concerns regarding environmental threats (i.e., global warming) and nonrenewable fossil fuel exhaustion, which raise the need for gas conversion reactions[1,2] and developing green energy sources[3-8]. Lithium-ion batteries (LIBs) with their trustworthy power source are the most common and efficient energy storage devices widely used in various portable devices and electric cars, but the high cost and earth-rarity of Li are crucial issues in the sustainable future[9-12]. The efficiency and performance of LIBs are shaped by the anode (i.e., shape and composition) and electrolytes[11-13]. Rechargeable alkali metal-ion batteries (RAMIBs) emerged as a promising alternative to traditional Li-batteries, owing to their tolerable cost, reliable theoretical specific capacities (Li = 3,860 mAh/g; Na = 1,166 mAh/g; K = 685 mAh/g), and low electrochemical redox voltage [i.e., Li = 3.04 V, Na = 2.71 V, and K = 2.93 V vs. Standard Hydrogen Electrode (SHE)][14]. However, the alkali metal-ion batteries are still not up to the level of commercial scale, owing to their viability to dendrite growth, repetitive breakage or regeneration of the solid electrolyte interphase, causing subsequent unreliable safety, low energy efficiency, and low durability. Immense efforts devoted to solving these barriers lie in the development of controlled size, composition, and morphology of the anodes, new electrolytes (i.e., ether-based electrolytes, solid-state electrolytes, and multifunctional electrolyte additives), and the design of new hierarchical supports[10,15-18]. These solutions led to decreasing the local current density, controlling alkali-metal deposition, enhancing mechanical properties, increasing the ionic conductivity, ceasing dendrite growth, and stabilizing alkali metal anodes from corrosion. However, the intrinsically great activity of alkali metals and the significant volume alteration during plating or stripping are critical barriers for practical applications of RAMIBs[19,20].

Another promising solution is the rational formation of porous multimetallic alloy-based anodes (PMMAs), especially porous transition metals, which are the most promising to solve the current hitches in RAMIBs, owing to their impressive specific capacities and low working voltage[16,21,22]. This is in addition to the low cost and abundance of transition metals, which can meet the requirements of both sustainability and practical application[23,24]. Moreover, PMMA anodes act as a protective layer, which enhances the cyclic durability, rate capability, and plating/stripping Coulombic efficiency (CE) of RAMIBs[25]. Besides, PMMAs are endowed with enhanced specific capacity (SC), alkaline metal (Li+/Na+/K+) ion diffusion/kinetics, stable architectural integrity, negligible volume expansion and pulverization in RAMIBs, compared to their monometallic analogous[26,27]. Notably, using at least one alkali metal with PMMAs decreases the high reactivity of alkali metal, provides abundant channels for quick ion transfer, and acts as mechanical supports, hence preferring quick and orderly metal plating and stripping[23]. Additionally, direct use of PMMAs with their interphases can plausibly serve as an artificially protective layer to tailor the ion flux, increase rapid ion diffusion, and inhibit the side reactions between the electrolyte and electrode. This has led to an exponential increase in publications (i.e., 100 articles, cited ~1,500 times) [Figure 1A], with much attention on the rational design of PMMAs for alkali metal-ion batteries; hence, it is important to provide timely updates on this research area. Although there are various recent excellent reviews on alkali metal batteries and metal anodes [Supplementary Table 1], the PMMA anodes for LIBs, sodium-ion batteries (SIBs), and potassium-ion batteries (PIBs) have not yet been reviewed to the best of our knowledge[14,27,28].

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 1. (A) Database literature survey using keywords "multimetallic alloy anodes for batteries" according to the "Web of Science" and (B) review focus.

This review summarized the progress in the fabrication methods (i.e., template-based, hydrothermal/solvothermal, chemical reduction, electrochemical deposition, sol-gel, and electrospinning) of PMMAs (i.e., Sn, Mn, Mo, Co, V, and Fe) for RAMIBs (i.e., LIBs, SIBs, and PIBs) [Figure 1B]. These are classified and grouped according to the active atoms/elements in their compositions, whose physicochemical merits and electrochemical performance are robustly discussed in detail. This is in addition to the fundamental issues (i.e., mechanisms, key parameters, and calculations) of such batteries, along with deep discussions on the key descriptors of these batteries (i.e., lifespans, energy density (ED), structural changes, and mechanisms). A lot of experimental data, theoretical simulations, and in-situ analysis were provided to optimize the performance of PMMAs in LIBs, SIBs, and PIBs. Meanwhile, a conclusion and perspectives/outlooks are provided to underline the current challenges and propose solutions for such anodes and batteries.

FUNDAMENTAL AND MECHANISMS OF RECHARGEABLE ALKALI-ION BATTERIES

The RAMIBs, including LIBs, SIBs and PIBs, comprise four basic parts: anodes, cathodes, electrolytes and separators. The electrodes (anodes and cathodes) are good electrical conductors, while electrolyte functions as an ionic conductor, as briefly explained below.

• Anode: This is a negative electrode (metal or alloy) where negatively charged ions migrate.

• Cathode: This is a positive electrode (layered structure of metallic oxide, sulfides, and/or carbon materials) where positively charged ions migrate.

• Electrolyte: This is a solution containing dissociated salts that allows the movement of ions between the anode and cathode.

• Separator: This is a permeable or porous membrane that keeps the anode and cathode apart to eschew electrical short circuits but allows the movement of ionic charge carriers required for the passage of current in the battery.

The anode and cathode are often made up of different conducting materials, kept apart by the separator and immersed in the electrolyte solution. A typical RAMIB is shown in Figure 2 with similar mechanisms. For example, in LIBs, charging and discharging ensues via the movement of A+-ions between the cathode and anode, coupled with exchange of electrons (e-s). Particularly, the charging Li/Na/K is delithiated/desodiated/depotassiated from the cathode (i.e., Li-based compound) and the interlayer anode [i.e., metal alloys (MAs) or carbon] are lithiated/sodiated/potassiated with Li/Na/K, and vice-versa during the discharge process, as given in Eqs. 1 and 2, where A represents Li+ or Na+ or K+ ions and MAs are metal alloys.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 2. Schematic illustration of rechargeable alkali metal-ion battery.

$$ \begin{equation} \begin{aligned} \mathrm{Initial~charge:}~~ \mathrm{ACoO}_{2}+\mathrm{C} \rightarrow \mathrm{A}_{1-\mathrm{x}} \mathrm{CoO}_{2}+\mathrm{A}_{\mathrm{x}} \mathrm{MA} \end{aligned} \end{equation} $$

$$ \begin{equation} \begin{aligned} \mathrm{Discharge}:~~\mathrm{A}_{1-\mathrm{x}} \mathrm{CoO}_{2}+\mathrm{A}_{\mathrm{x}} \mathrm{C} \rightarrow \mathrm{A}_{1-\mathrm{x}-\mathrm{dx}} \mathrm{CoO}_{2}+\mathrm{A}_{\mathrm{x}-\mathrm{dx}} \mathrm{MA} \end{aligned} \end{equation} $$

Parameters of indicator and calculations

In addition to the materials’ cost, toxicity and safety of the components of RAMIBs, their performance can be assessed by various parameters of indicators, including cell voltage, C-rate, SC, capacity retention (CR), ED, power density, CE, voltage efficiency and energy efficiency, which aid in the rational design and fabrication of suitable intercalation electrodes for high ED batteries[29-31]. These are briefly discussed below:

• Cell voltage: This is the driving force for the movement of alkali metal ions and electrons from one electrode to the other. Thermodynamically, it is the electrochemical potential difference, which is proportional to Gibb’s free energy (∆G), as given in

$$ \begin{equation} \begin{aligned} \Delta G=-n F V \end{aligned} \end{equation} $$

Here, n represents the total number of electrons, Faraday’s constant F = 96,485.3 (C/mol), and V refers to the cell voltage.

Discharge rate or C-rate: This is the rate at which a battery is discharged/charged in relation to its capacity. For instance, 1C-rate indicates that a battery is fully discharged in 60 min (1 h), and 10 Ah capacity of a battery gives a 1C-rate equivalent to 10 A.

• Specific capacity (SC): This is the amount of electrons intercalated/deintercalated per unit mass of the electrode during cycling. The SC is reported with mass or volume of an active electrode, called gravimetric SC (GSC, mAh/g) or volumetric SC (VSC, mAh/cm3), respectively, and calculated using

$$ \begin{equation} \begin{aligned} \mathrm{SC}=\frac{n F}{3600 M} \end{aligned} \end{equation} $$

Here, the number of available sites for active Mn+ ions intercalated into the host matrix of the battery’s capacity. Also, the storage capacity can be measured with respect to unit area, called areal capacity (mAh/cm2). The VSC is particularly crucial when designing batteries for high energy applications, such as electric vehicles and grid storage.

• Capacity retention (CR, cyclability/stability): This is the number of times a battery can be discharged/charged at both fixed and various current densities. For practical application in industries, a good battery should retain at least 80% of its initial SC after multiple cycles (charged/discharged).

• Energy density (ED): This is the overall energy stored in a battery, which is calculated by multiplying the working voltage (V) and reversible capacity (C), as given in

$$ \begin{equation} \begin{aligned} E=V \times C=V \times \mathrm{i} \times t \end{aligned} \end{equation} $$

Here, i indicates the current, and t represents time. Electrodes having higher potential (voltage), which is a function of the amount of alkali metal ion intercalated, and layered structure with various compositions facilitate higher ED. The ED can be expressed as gravimetric (Wh/kg) or volumetric (Wh/L).

• Power density: This is the optimal power delivered by a battery with regard to its electrode mass or volume. It shows how fast work is done with the availed energy in the battery, as given in

$$ \begin{equation} \begin{aligned} P=(i \times V)=\left(i^{2} \times R_{\text {int }}\right) \end{aligned} \end{equation} $$

Here, i, V, and Rint denote the current, voltage, and internal resistance, respectively. The Rint is a function of ionic conductivity of the alkali metal ions, electrical conductivity of electrodes and reaction kinetics during cycling. The power density can be reported per unit mass [i.e., gravimetric power density (W/kg)] or unit volume [i.e., volumetric power density (W/L)]. Surface reactivity, conductivity, surface morphology, electrochemical, chemical and structural stability of electrodes are the contributory factors for optimized power density.

• Coulombic efficiency (CE): This is the ratio of energy withdrawn from a battery during discharge and energy restored during charging, as given in

$$ \begin{equation} \begin{aligned} \mathrm{CE}=\frac{\text { Specific capacity of discharging }}{\text { Specific capacity of charging }} \times 100 \end{aligned} \end{equation} $$

A good battery should have close to 100% CE.

• Voltage/voltaic efficiency: This is the ratio of mean discharging voltage to charging voltage. High active surface area and electrical conductivity of electrodes enable increased voltage efficiency.

• Energy efficiency: This is the ratio of energy densities during discharge and charge process.

The cyclability, ED, power density, and rate capability are dependent on the ionic and electrical conductivities of the electrodes. Hence, a battery must maintain low internal resistance and higher conductivities to obtain excellent performance. Meanwhile, low molar mass electrodes enable higher capacity and rate capability.

ENGINEERING METHODS FOR POROUS MULTIMETALLIC ALLOY-BASED ANODES

The PMMA anodes are controllably synthesized by various methods, including template-based, hydrothermal/solvothermal, chemical reduction, electrodeposition, sol-gel, co-precipitations and electrospinning.

Template-based methods

The PMMAs are mostly and best prepared via the template-based methods, i.e., hard-templates or soft-templates[3,27]. The hard-template is appropriate to tailor the preparation of well-ordered PMMAs, initiated by the infiltration of metal precursors into the template by co-deposition or in-situ deposition or self-assembly, and then removal of the template by etching (i.e., NaOH or HF) and/or heating, thereby replicating the exact porosity of the template. Zeolites, mesoporous silica (i.e., MCM-41, MCM-48, KIT-6 and SA-15), alumina membranes and colloidal crystals [i.e., crystal latex, salt-like (KCl)] are typical examples of the hard-templates[3,27], for the preparation of nanotube-like PMMAs [Figure 3A]. Similarly, soft-templates utilize lyotropic liquid crystals, such as block copolymers (i.e., 3,4-dihydroxy-D-phenylalanine, 3,4-dihydroxy-L-phenylalanine, and (R)-phenylethanol), surfactants (Brij® C10, polyvinylpyrrolidone, and pluronic F127), degradable copolymers [i.e., polystyrene-block-poly(4-vinylpyridine), polystyrene-b-poly(l-lactide), poly(lactic-co-glycolic acid), and polyisoprene-block-polystyrene-block-poly(propylene carbonate)] and micelle assembly (PS-b-P4VP micelles)[27,32]. A typical example of the soft-template method for the synthesis of PMMAs is presented in Figure 3B. Despite the advantages of template methods for the preparation of PMMAs, there is volume collapse during the metal precursors’ reduction and incomplete retention of template shapes and porosity after their removal, which pose a challenge for controlling the morphologies, particularly for powder or film nanostructures on non-conductive substrates. This hitch is often surmounted by combining the template methods with chemical reduction or electrodeposition. This method is often used for the synthesis of PMMA anodes for RAMIBs. These methods utilize the dynamic structures of templates to control the morphologies, porosity, surface area and other physicochemical features of the PMMA anodes.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 3. Schemes of (A) hard-template and (B) soft-template methods of preparing PMMAs.

Hydrothermal/solvothermal method

The synthesis of PMMAs using hydrothermal methods involves the mixing of aqueous metal precursors (i.e., acetate, chloride, nitrate and hydroxide dissolution in water), where a pH modular/additive (i.e., KI, KBr or KOH) serves as a catalyst when magnetically stirred or ultrasonicated, and surfactants (i.e., polyvinylpyrrolidone (PVP), pluronic F127) as structure-directing agents[33,34]. The aqueous solution is sealed in an autoclave and heated at elevated temperature for some time (2-24 h), and then the anticipated product is washed by centrifugation for several cycles and dried in a vacuum oven, prior to calcination [Figure 4A]. Solvothermal method is similar to hydrothermal method, but it uses non-aqueous solvents, such as dimethylformamide, ethylene glycol, isopropanol, ethanol, and butanol, which may act as a structure-directing agent. The fabrication methods of the PMMAs via hydrothermal/solvothermal method entails initial nucleation and subsequently direct attachment growth; meanwhile, the surfactant is adsorbed or interacts with the anion additives (Br-, I-, OH-) and sometimes in-situ etching-induced porous architectures[35-37]. The hydrothermal/solvothermal method is easy, effective and appropriate for the preparation of PMMAs, their oxides, chalcogenides, spinels, perovskites, high entropy alloys, and composites, with or without supports [i.e., carbon, nickel foam (NF)] in various architectures (nanospheres, nanocubes, nanosponges, nanocages, flower-like architectures, etc.).

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 4. Scheme of (A) hydrothermal/solvothermal and calcination, and (B) chemical reduction for the synthesis of PMMAs.

Chemical reduction method

The chemical reduction method uses suitable reducing agents, such as NaBH4, ascorbic acid, PVP, etc.[38-40]. The formation mechanism of the PMMAs follows a burst nucleation of metal with high standard reduction potential, which eventually serve as seeds for other metal(s) atoms to form multiple crystallites with large surface-free energy; then, these crystallites aggregate and undergo continuous direct-attachment/diffusion-limited growth across the interface through Brownian motion [Figure 4B][41]. At rapid reduction rate, the as-formed nuclei grow along the single-crystalline lines to yield polyhedron shapes (i.e., cubes, tetrahedrons, and octahedrons) with Oh and Td symmetry. In contrast, slow reduction rate affords a five-fold twinned nuclei growth into polyhedrons with Ih symmetry (dodecahedrons and icosahedrons). Also, the structures of the PMMAs are a function of the adsorption model of the structure-directing agents[42], including ionic polymers [i.e., cetyltrimethylammonium bromide (CTAB) and cetyltrimethylammonium chloride (CTAC)] and non-ionic polymers (i.e., Pluronic F127, Brig-58, and PVP), on the as-formed nuclei with the respective functional groups. This then leads to self-assembly to yield micelles that serve as in-situ templates during the growth for the formation of porous wire-like, branched and 3D nanocrystals.

Electrochemical deposition method

The preparation of PMMAs via electrochemical deposition is low-cost, rapid, single-step and low energy-intensive (i.e., low potential and room temperature) in the form of thin films, coatings and various shapes/compositions. The fabrication process involves reduction/oxidation of metal ions in an electrolyte (acid, neutral or alkaline), which are deposited on the conductive materials when certain potential is applied, utilizing a 3-electrode configuration, comprising the counter electrode (i.e., Pt wire and graphite), reference electrode (i.e., Ag/AgCl, and SCE) and working electrode (i.e., glassy carbon, carbon paper, carbon cloth sheet) [Figure 5A]. The modulation of the shapes and compositions of the PMMAs are functions of the electrolyte types, applied potential, cell set-up and deposition time. This method is easy and could be combined with other approaches for the synthesis of thin film; however, it requires a lot of precaution and skills for controlled morphologies and compositions.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 5. The illustration of (A) electrodeposition, (B) sol-gel and (C) electrospinning methods for the preparation of PMMAs.

Sol-gel method

Controlled texture, size and surface features of PMMAs in the form of aerogels, xerogels or cryogels are prepared via sol-gel method, which is cost-effective, easy to implement, and provides high quality and large yield[43,44]. The fabrication process of PMMAs through this method follows several steps: hydrolysis, condensation, aging & drying and crystallization [Figure 5B][45]. Hydrolysis involves the mixing of metal alkoxide precursors and solvent, where the nucleophilic oxygen of water attaches to the metal alkoxide to remove it from the formation of the alcohol functional group (M-OH). This is affected by several parameters [nature of R-group, alkoxy functional group steric hindrance, temperature, pH, aqueous or non-aqueous solvents, ratio of solvent to metal alkoxide, and the amounts of catalysts (acid or base)]. These parameters can sometimes make it difficult to control the synthesis and the structure of the obtained gel depending on the catalyst, owing to the rate of hydrolysis. The hydrolysis rate is often faster in alkaline media than in acidic media[46]. The condensation is the formation of a polymer network, composed of metal oxide linkages, due to the removal of solvent (water or alcohol) to form a sol. This step raises the solution’s viscosity during the polymer network growth and forms a porous structure within the gel-phase. Aging is the continuous polycondensation within the solution and precipitation of the gel network, which lowers porosity, but increases thickness of the colloidal nanoparticles. Drying is the evaporation during gelation, whose rate significantly affects the gel structure. The network structure of the gel may be affected by liquids removal: if the structure is retained, an aerogel (high pore volume and surface area) is formed; if it collapses, a xerogel (low pore volume and surface area) is formed; but it is removed at low temperature, a cryogel is formed. The drying of gel requires heat treatment to remove surface OH groups and compress to form crystalline PMMAs[47].

Electrospinning method

The electrospinning is a useful and worthwhile technology for the preparation of 1D nanofibrous materials for nanotechnological applications in biomedicine, fuel cells, energy storage, electronics, and sensors[48,49]. This method involves four main components: a high-voltage power supply, a syringe pump, a spinneret (i.e., a hypodermic needle with a blunt tip) and a conductor collector[50]. It utilizes an electrodynamic process to electrify liquid droplets of metal precursors to produce a jet that is then stretched and elongated to give PMMA nanofibers [Figure 5C]. The fabrication mechanism involves the extrusion of metal precursor liquid from a spinneret to afford a suspended droplet, due to the surface tension; then, the electrostatic repulsion of the surface charges of the same sign deforms the droplet into a Taylor cone, where a charged jet is ejected. The jet is extended initially in a straight line, then subjected to vigorous whipping motions, owing to bending instabilities, stretches to finer diameters, and solidifies rapidly, resulting in deposition of solid porous PMMA nanofibers on the conductor substrate[51,52].

ALKALI METAL-ION BATTERIES

Lithium-ion batteries

In the last decade, numerous studies have explored the use of MA anodes for rechargeable Lithium-ion batteries (LIBs). Nevertheless, research on PMMA anodes has been relatively limited. PMMA anodes are considered preferable because of their superior specific capacities relative to carbon anodes. However, during cycling, these anodes are conspired with large capacity irreversibility at the 1st cycle and meager cycling performance, owing to volume variation. These hiccups are being surmounted by tailoring the nanostructures of the alloys and/or supporting them with porous conducting materials [i.e., carbon, NF, and copper foam (CF)]. Hence, the PMMAs for LIB anodes are classified according to the main active atoms/elements in the alloy compositions: (i) tin (Sn)-based alloy anodes; (ii) cobalt (Co)-based alloy anodes; (iii) manganese (Mn)-based alloy anodes; and (iv) other alloy anodes-containing active elements/atoms (i.e., Fe, V, Ni, Zn, Ti, Si).

Porous multimetallic tin (Sn)-based alloy anodes

The high theoretical capacity, cheap nature and suitable working conditions of Sn have positioned it as a capable anode for imminent LIBs. The practical application of Sn anodes is limited by the huge volume change during Li+-ions lithiation and delithiation, which results in massive irreversible capacity loss and poor life cycle. Alloying of Sn to other metals/composites with carbon having tailored morphologies and augmented synergism is desirable for boosted electrochemical properties of energy storage systems[53,54], particularly improving the anodic performance of porous multimetallic Sn-based alloy anodes in LIBs[55]. For example, the construction of Sn on a porous Cu foam substrate (Sn-Cu6Sn5/Cu foam) was achieved by electrodeposition. This configuration exhibited superior performance as a LIB anode at higher initial SC (821.5 mAh/g@0.1 A/g) compared to Sn/Cu foil (655.5 mAh/g); besides, CR = 58% after 50 cycles, due to the formation of porous Cu6Sn5 interface that eschewed volume expansion and pulverization/delamination[56]. This study revealed that Cu foam is a preferred substrate to Cu foil. Template-like electrodeposition/annealing was used to form Sn-Sb on a Cu foil (Sn-Sb/Cu) with a sponge-like porous membrane alloy on the Cu foil through a mixed phase inversion process and tested as a LIB anode[57]. In the 1st cycle, Sn-Sb/Cu anode delivered impressive SC (651.9 mAh/g@0.5 A/g), CR (82.9%) and rate performance, attributable to the co-existence of alloy on meshwork conducting polymers, unfilled pores and intermediate Cu3Sn alloy. Although this method proves promising, more robust research is needed for directing the structures of the PMMAs with improved energy storage capacity and stability.

Sb-doped SnO2 nanoparticles grown on N-doped graphene-carbon nanotubes hydrogels (ATO/N-GCH) were prepared by a hydrothermal method and then freeze-drying to obtain the aerogel counterpart (ATO/N-GCA) [Figure 6A], with endowed 3D spherical Sb-SnO2 on sheet-like nanotube proved by scanning electron microscopy (SEM, Figure 6B), high porosity and electrical conductivity to afford good LIB anode performance at increased initial SC (942 mAh/g@1.0 A/g), CR (73%) and rate capability than ATO/G (~940 mAh/g; 59%) and SnO2/N-GCA (~940 mAh/g; 35%) [Figure 6C-E][58]. Indeed, metal doping and/or composite with metal influences the electrical conductivity of Sn-based anodes for enhanced electrochemical energy storage capability. CoSn2 and FeSn2 tetragonal nanocrystals, proved by the transmission electron microscope (TEM, Figure 6F), were separately prepared by a chemical reduction method[59]. The CoSn2 possessed higher average SC (650 mAh/g@1.984 A/g) and excellent cycling stability, relative to an equivalent mixture of metals (Co + Sn, 380 mAh/g) and Sn (520 mAh/g) [Figure 6G], due to the presence of Co domains that buffered the volumetric change during cycling, eschewed Sn aggregation and amorphization. However, amorphous CoSn2Ox nanoparticles with spherical morphology, proved by TEM [Figure 6H] prepared by chemical reduction and ball milling in air, displayed better mean SC (525 mAh/g@2.0 A/g) and cycling performance than crystalline CoSn2 (462 mAh/g; 82%) [Figure 6I-K][60]. This was ascribable to the inhibition of Li alloy formation, the buffering effect of inactive Co matrix on the volume change, and the prevention of Sn agglomeration during lithiation/delithiation. The modulated physicochemical merits such as defects and oxygen vacancies of amorphous anodes are beneficial for enhanced energy storage.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 6. (A) Hydrothermal synthesis, (B) SEM, (C) rate capability and (D and E) cyclic performance of ATO/N-GCA, ATO/G and SnO2/N-GCA. This figure is quoted with permission from Ref.[58] Copyright 2017 Elsevier. (F) TEM and (G) galvanostatic charge/discharge curves of CoSn2, Co + Sn and Sn. (H) TEM, (I and J) galvanostatic charge/discharge and (K) cycling stability of CoSn2Ox, CoSn2 and Sn NPs. This figure is quoted with permission from Refs.[59,60] Copyright 2018 the Royal Society of Chemistry.

Porous multimetallic cobalt (Co)-based alloy anodes

In recent times, Co-based materials (i.e., oxides, phosphides, nitrides, sulfides and alloys) are receiving huge attention as impressive anodes and electrocatalysts for LIBs and other electrochemical applications, owing to their excellent electrochemistry[61]. Despite this, the anode is still affected with volume variations triggered by the lithiation/delithiation that lead to the pulverization and detachment, thereby causing capacity fading[62]. This issue could be circumvented by rational nanoarchitecture design and alloying with or without conductive materials in facilitating the rapid Li+ ions diffusion and enduring strain induced by the volume enlargement, thereby augmenting the electrochemical activity and cyclability[63,64]. For instance, NiCo2O4 anchored reduced graphene oxide (rGO/NiCo2O4) was systematically synthesized by citrate-assisted hydrothermal/annealing techniques, which enabled interconnected nanosheets on hierarchical porous wrinkled film to give high initial SC (1,697.9 mAh/g@0.2 A/g), notable CR and rate capability[65]. The high capacity was traced to contributory effects of the hierarchical porous support that optimized electrode/electrolyte interface for rapid Li+-ions flux/diffusion. Appropriate hierarchical nanocomposites are excellent materials for outstanding reversible Li+-ion storage. Hard-template annealing was utilized to construct CuO/CoO core/shell arrays on Cu foams [Figure 7A], which gave very good LIB anode performance at initial SC (1,216 mAh/g@0.1 A/g). Then, this capacity increased to 1,364 mAh/g after 50 cycles, with a CE of 69% [Figure 7B][66], due to the unceasing polymeric gel/oxide layer formation on the nanosized metal oxides. Meanwhile, the high SC and impressive CR (93.8%) after 1,000 cycles [Figure 7C] were ascribed to the unique porous 3D hierarchical tubular core/shell structure, as proved by SEM [Figure 7D], and potent hybridization. The fabrication of hollow heterostructures is amongst the most practicable strategies for high-performance energy storage systems.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 7. (A) Hard-template fabrication method, (B) charge/discharge curves, (C) cyclic performance at 0.1 A/g and (D) SEM of tubular CuO/CoO core/shell arrays on Cu foam. This figure is quoted with permission from Ref.[66] Copyright 2015 Elsevier. (E) Field emission scanning electron microscopy (FESEM), (F) charge/discharge curves for 1st, 3rd, 50th and 100th cycles, and (G) cycling performance of NiCo2O4/NiO-HD at 0.2 A/g. This figure is quoted with permission from Ref.[32] Copyright 2015 the Royal Society of Chemistry. (H) charge/discharge curves of 1st, 2nd and 100th cycles at 1.0 A/g, and (I) FESEM of NiCo2O4. Reproduced with permission from Ref.[68] Copyright 2016 Elsevier.

Various self-supported hierarchical porous multimetallic oxides (ZnCo2O4, NiCo2O4, CuxCo3-xO4, MnxCo3-xO4, ZnxNiyCo3-x-yO4, Co3O4, NiO, Fe2O3 and ZnO) on Ni foam (NF) were developed by hard-template/calcination[67]. The ZnCo2O4/NF had improved interfacial Li+-ion storage, numerous interconnected flower-like nanosheets and reversible polymeric gel-film formation/dissolution to deliver a higher LIB anode at initial SC (1,544 mAh/g@0.1 A/g), CR (82%) and cycling performance, than NiCo2O4/NF (1,500 mAh/g; 70%); MnxCo3-xO4/NF (1,300 mAh/g; 73%), Co3O4/NF (1,280 mAh/g; 70%) and NiO/NF (1,250 mAh/g; 65.6%). Mesoporous multimetallic alloy oxides are promising anodes with high yields for outstanding Li+-ion storage capacity. Porous NiCo2O4/NiO hollow dodecahedron (HD), proved by FESEM [Figure 7E], was prepared from a zeolitic imidazolate framework-67 (ZIF-67) sacrificial template via solvothermal/calcination[32]. The NiCo2O4/NiO-HD demonstrated high SC (1,622 mAh/g@0.2 A/g) at the 1st cycle, incredible CR (97.2%) and cycling performance [Figure 7F and G], compared to Co3O4-HD, owing to its unique hierarchical nanostructures, high surface area, acceptable volume increase, high electron mobility and rapid Li+-ions diffusion. However, chemical reduction synthesis of NiCo2O4, utilizing PVP as a structure-directing agent, gave lower initial SC (1,282 mAh/g@1.0 A/g), but moderate irreversible capacity fading (6%) [Figure 7H], which was traced to its endowed porous rose flower-like nanosheets, as proved by FESEM [Figure 7I], which provided enough void space for easy electrolyte penetration and rapid electron mobility[68]. These studies proved the superiority of metal-organic framework (MOF)-templated anodes for excellent Li+-ion storage performance, owing to the tailored nanoarchitectures and porosity.

Mesoporous FeCo2O4 was synthesized via sol-gel/calcination, which favorably utilized its multicomponent effect, octahedral architectural stability and meso-porosity for superb LIB anode performance at increased initial SC (2,436 mAh/g@0.2 A/g) and CR (95.2%)[69]. The 3D Zn-Ni-Co oxide enclosed graphene nanosheets (ZNCO/GNS) were prepared by chemical reduction/hard-template annealing [Figure 8A][70]. This was based on the wrapping of ZNCO microspheres within the GNS to form core/shell architectures, evidenced by SEM [Figure 8B], that prevented agglomeration of active ZNCO, volume variations, and boosted electrons/Li+-ions mobility, which resulted in good Li+-ion storage at initial SC (1,429 mAh/g@0.1 A/g) and CR (95%) [Figure 8C]. Adopting synthesis method for preparing core/shell composites with micro-/nanostructures are preference for boosted Li+-ion storage. The fabrication of 3D porous ZnCo2O4 thin films on NF (ZnCo2O4 thin film/NF) via hard-template annealing gave high discharge capacity (1,726 mAh/g@0.4 A/g) and cycling performance[71]. This was due to the capability of the 3D porous ZnCo2O4 architectures in facilitating abundant reactive sites, effective void space to volume change during cycling, increased contact with electrolyte and boosted electron mobility. Core/shell Te@ZIF-8 (Zn,Co) nanofibers were prepared by hydrothermal methods and explored as sacrificial templates via annealing to afford 1D hierarchical Te@ZnCo2O4 nanofibers, proved by TEM [Figure 8D] with fascinating compositional and morphological merits to deliver great LIB anodes at high SC (1,364 mAh/g@0.1 A/g), eminent cycling durability (~100%) and rate capability [Figure 8E and F][72]. Also, the fabrication of Zn-Co-S embedded N,S-codoped carbon polyhedral (Zn-Co-S@NS-CP), prepared from the annealing of ZIF-8@ZIF-67 template, was endowed with hierarchical hollow polyhedron architectures with interconnected conductive network, more reactive active sites, Li+-ion mobility and phase separation of lithiated intermediates that enabled LIB anodes with high reversible capacity at SC (1,298.1 mAh/g@0.57 A/g) and long-term stability[73]. The SC could be affected by changing the annealing temperature during the anode preparation. Thereby, lower SC (975.2 mAh/g@0.2 A/g) and CR (81.6%) were recorded for spherical CoO-ZnO@NC-450, prepared by hydrothermal/calcination of CoZnBTC@NC precursors at various temperatures (350-550 °C in Ar for 2 h), owing to the disordered structure at 450 °C that reduced the permeation energy barrier and abundant active sites of Li+-ions[74].

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 8. (A) Chemical reduction/annealing synthesis, (B) SEM, and (C) charge/discharge curves at 0.1 A/g for 1st-3rd and 50th cycles of ZNCO/GNS. (D) TEM, (E) Charge-discharge, cycling life and Columbic efficiency, and (F) rate capability of Te@ZnCo2O4 nanofibers. This figure is quoted with permission from Refs.[70,72] Copyright 2015 Wiley-VCH. (G) TEM, (H) 1st-3rd charge/discharge profiles and (I) Cyclic performance at 0.5 A/g of CoMoO4-CoO/S@rGO and analogs. This figure is quoted with permission from Ref.[75] Copyright 2022 the Royal Society of Chemistry.

Hierarchical porous CoMoO4-CoO/S@rGO, prepared from MOF-template via S-doped hydrothermal/annealing method, had core/shell polyhedron structures, proved by TEM [Figure 8G] to deliver better LIB anode at increased initial SC (1,672 mAh/g@0.5 A/g), and excellent cyclic performance superior to CoMoO4-CoO@rGO, CoMoO4-CoO/S, CoS/S@rGO and rGO [Figure 8H and I][75]. This study revealed that S-doping enlarged the interplanar distance, improved conductivity and charge storage capacity, which were beneficial for high-performance LIB anodes. The fabrication of a porous Cu shell uniformly glazed on CoO nanowires core (CoO/Cu) was achieved by hard-template/pulsed electrodeposition[76]. The constructed CoO/Cu heterostructured arrays exhibited impressive performance as anodes in LIBs at higher initial SC (1,215 mAh/g@0.5 A/g) and CR (68.15%) than CoO (1,053 mAh/g; 53.8%), due to their improved electron/ion transport, conductivity, surface area, and lower polarization.

Porous multimetallic manganese (Mn)-based alloy anodes

Manganese oxide (MnxOy)-based materials possess inimitable outer valence electrons, physical and chemical features that makes it amazing LIB anodes[77,78]. Besides their low cost, environmental benignity, ease of preparation and high theoretical capacity (1,232 mAh/g). Nevertheless, large volume change during cycling and low electrical conductivity of MnxOy anodes are the drawbacks that lead to low rate capability and cycling durability[79,80]. These drawbacks are solved by deliberately fabricating porous nanostructured MnxOy alloy and/or carbon composites with controlled sizes and morphologies[81-83]. For instance, solvothermal/annealing methods were utilized to fabricate porous quasi-mesocrystal ZnMn2O4, following oriented attachment and Ostwald ripening mechanisms for the formation of distinct twin-microsphere structures, 3D hierarchical porosity and Li alloying reaction, beneficially utilized for good LIB anodes at initial SC (1,100 mAh/g@0.5 A/g), CR (77.8%), rate capability and long-standing cycling durability[84]. However, porous ZnMnO3 spherulite, prepared by co-precipitation/annealing, had inner atomic synergism of Zn-O and Mn-O that decreased its LIB anode performance at lower initial SC (1,294 mAh/g@0.5 A/g), but improved CR (67.9%) than ZnO-MnO2 equimolar power mixture (1,333 mAh/g; 60.4%) and nano-sized MnO2 (1,553 mAh/g)[85]. This study showed that the synergistic effect of inner atoms of Zn-O and MnO2 could lead to significant initial capacity fading of ZnMnO3, but improved rate capability and cyclability. The construction of 3D porous CoMn2O4 on NF (CoMn2O4/NF) was achieved by hard-template/annealing, with greater initial discharge SC (1,833 mAh/g@0.4 A/g) and CR (74.5%), compared to un-annealed CoMn2O4/NF (1,540 mAh/g, 60.6%)[86]. Thus, annealing enabled high synergism in CoMn2O4/NF for improved initial SC via enhanced reaction sites, electrode-electrolyte contact and electron mobility, nullified volume change and improved growth/dissolution of polymeric gel film attachment on the CoMn2O4 anode. However, annealing had suppressing effect on ZnMn2O4/NF, thereby un-annealed ZnMn2O4/NF displayed better initial discharge SC (2,211 mAh/g@0.4 A/g), but lower CR (94%) than annealed ZnMn2O4/NF (1,789 mAh/g; 96%)[87]. The studies confirmed that effects of annealing are ambiguous for boosting the SC of Mn2O4-based anode/NF anodes but definitely augments their CR and cycling stability.

Controlled synthesis of multi-shelled nanostructured Ni-Co-Mn oxides by self-templated hydrothermal/annealing method [Figure 9A] that enabled various architectures, including quadruple-shelled hollow microspheres (QS-HS), triple-shelled hollow microspheres (TS-HS) and double-shell hollow microspheres (DS-HS), proved by TEM [Figure 9B-D][88]. The QS-HS afforded abundant interfacial electrode-electrolyte interaction, numerous active sites, and favorable Li+-ions transfer and volume accommodation to deliver high LIB anodes at initial SC (1,761.8 mAh/g@0.2 A/g), rate capability (1,073.6 mAh/g@5 A/g), gravimetric energy densities (1,261.7 Wh/kg) and good cyclability, compared with TS-HS and DS-HS [Figure 9E-G]. Rational design of multi-shelled PMMA oxides with tailored morphology and compositions is an appropriate recipe for the practicality of LIB anodes. A double-shelled NiO nanoparticles-doped MnO grown on NF (np-Ni@NiO/MnO/NF), prepared by an induction melting/dealloying/annealing, gave impressive initial reversible SC (960 mAh/g@0.1 A/g), remarkable CR (105%), CE and rate capacity [Figure 9H and I], due to its interconnected shell nanoporous architectures with vigorous defects and roughness, evidenced by SEM [Figure 9J], that allowed high ions/electrons mobility and shielded volume expansion[89]. Dealloying and oxidation of PMMAs allow a sporadic distribution of core-shell nanocrystals on conductive support for excellent LIB anodes. Solvothermal/annealing strategy was used to prepare porous Zn1.67Mn1.33O4 microspheres anchored GNS (Zn1.67Mn1.33O4/GNS), where the GNS eschewed aggregation of the cubic spinel-type oxide, enhanced its electrical conductivity and alleviated volume change to deliver superior cyclability, (99.95%), retentive capacity (670 mAh/g@0.1 A/g) after 200 cycles, lower than Zn1.67Mn1.33O4 (99.81%; 518 mA/g)[90]. The fabrication of well-dispersed spinel-oxides incorporated GNS is effective for buffering the volume variations.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 9. (A) Controlled hydrothermal/annealing synthesis, (B-D) TEM, (E) specific capacity and coulombic efficiency, (F) rate performance, and (G) gravimetric energy densities of Ni-Co-Mn oxides QS-HS, TS-HS and DS-HS. This figure is quoted with permission from Ref.[88] Copyright 2017 the American Chemical Society. (H) capacity retention at 0.1 A/g after 200 cycles and coulombic efficiency, (I) rate capacity at various current densities, and (J) SEM of np-Ni@NiO/MnO/NF. (K-M) charge/discharge profiles of MN-1/P, MN-1, and MN-2. This figure is quoted with permission from Refs.[89,91] Copyright 2019, 2023 Elsevier.

A series of NiMn hydroxides modified with [p-phthalic acid (PTA)] and/or activated carbon (AC) [i.e., Ni(OH)2/Mn(OH)2 (MN-1), NiO/Mn3O4 (MN-2), MN-1/P, Ni(OH)2/Mn(OH)2/AC) (MN-1/C), Ni(OH)2/Mn(OH)2/PTA/AC (MN-1/PC), NiO/Mn3O4/PTA (MN-2/P), NiO/Mn3O4/AC (MN-2/C), and NiO/Mn3O4/PTA/AC (MN-2/PC)] were synthesized by in-situ electro-conversion/calcination and studied as LIB anodes[91]. The MN-1/P showed higher initial discharge SC (1,554 mAh/g) than MN-1/PC (1,518 mAh/g), MN-1 (1,386 mAh/g), Mn-2/P (1,128 mAh/g) and MN-2 (1,068 mAh/g) [Figure 9K-M], besides its CR (100%), owing to the successful wrapping of NiMn nanosheets by the PTA, dissolved by alkaline medium (-OH), without changing the MN-1 structure and content (1:1). The facile in-situ electrosynthesis of NiMn-MOF for the development of LIB anodes is viable for large-scale application of LIBs. Microsphere 3D Cu/Mn3O4@SC composite, made from thermolysis of Cu-Mn/MOF template, had an impressive anodic performance for Li+-ion storage at good SC (766.2 mAh/g@0.2 A/g), and CR (66.3%), attributable to the heterojunction synergism[92]. The synergetic effect of the components of multimetallic alloy anodes is significant for their increasing conductivity and Li+-ion diffusion rate.

Other porous multimetallic-based alloy anodes

Other PMMAs with main active atoms/elements, including Fe, Mo, Ni, Si, Ti, V, and Zn, and their composites have been demonstrated as inspiring anodes for LIBs because of their excellent features (i.e., chemical stability, high ionic/electrical conductivity and lithiophilicity) that facilitate facile Li+-ions mobility and inhibit Li dendrite growth and volume expansion[93-95]. For example, the fabrication of TiO2 on Fe3O4/CNTs (TFCs) was achieved by hydrothermal/calcination [Figure 10A], based on the bottom-up assembly mechanism with TiO2, carbon nanotubes (CNTs) and FexOy as buffer material, conducting network/effective anchorage and active nanoteeth, respectively, proved by HRTEM [Figure 10B][96]. The TFCs exhibited higher initial SC (1,589 mAh/g@0.5 A/g) than FexOy/CNTs (FCs, 771 mAh/g) and CNTs (309 mAh/g) [Figure 10C-E], and its superb rate capability and cycling performance, due to its highly porous hierarchical structural integrity. The scalable synthesis of hybrid anodes with specific morphologies/architectures and compositions is crucial in high-performance LIBs.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 10. (A) Hydrothermal/calcination, (B) HRTEM and (C-E) galvanostatic charge/discharge curves of TFCs, FCs and CNTs at 0.05 A/g. This figure is quoted with permission from Ref.[96] Copyright 2014 the Royal Society of Chemistry. (F) TEM, (G) charge/discharge curves at 0.2 A/g and 1st cycle, and (H) cycling performance and CE of 3D-OHP-a-VOx/MoOy, VOx/MoOy, a-VOx, and a-MoOy. Adapted with permission from Ref.[97] Copyright 2016 the American Chemical Society. (I and J) SEM, (K) charge/discharge profiles, and (L) rate performance of Zn3V2O8 hollow nanocages and solid nanospheres. (M) SEM and (N) cycling performance of CoFe2O4 and Mn3O4/Fe2O4. This figure is quoted with permission from Ref.[98,99] Copyright 2017 Elsevier.

The 3D ordered hierarchical porous amorphous vanadium and molybdenum oxides (3D-OHP-a-VOx/MoOy), prepared by freeze-drying/annealing, showed remarkable Li+-ion storage[97]. The 3D-OHP-a-VOx/MoOy exhibited amorphous architectures and 3D hierarchical sheets, proved by TEM [Figure 10F], and strong synergism that facilitated enhanced initial discharge SC (1,705 mAh/g@0.1 A/g) relative to crystalline VOx/MoOy (721 mAh/g), a-VOx (1,600 mAh/g), and a-MoOy (1,270 mAh/g), besides good cycling durability (82.1%) and rate capability [Figure 10G and H]. This study established the significant benefits of amorphous nanostructures with well-defined structures and compositions for high-performance anodes in LIBs. Solvothermal/annealing methods were exploited to develop porous Zn3V2O8 hollow nanocages and solid nanospheres, evidenced by SEM [Figure 10I and J] and comparatively tested as LIB anodes[98]. The hollow nanocages displayed superior Li+-ion storage at higher initial discharge SC (1,906 mAh/g@0.1 A/g) [Figure 10K], which was 1.5-folds of solid nanospheres (1,285 mAh/g), good rate capability [Figure 10L] and CR (80%). This was ascribable to the rapid Li+-ions/electrons diffusion, facile electrolyte permeability and optimal volume change alleviation by the hollow nanocages. Hence, hollow cages are preferred architectures to solid nanospheres for excellent LIB anodes. CoFe2O4 and Mn3O4/Fe2O4 were fabricated by melt spinning/dealloying, where CoFe2O4 with interconnected nanoplates/sheet-like architectures and porosity, evidenced by SEM [Figure 10M], high contact surface for Li+-ion mobility, rapid diffusion and smaller size that gave outstanding LIB anodes at higher initial discharge SC (2,134.7 mAh/g@0.1 A/g) and CR (83.5%), relative to Mn3O4/Fe2O4 (1,942.9 mAh/g; 66.9%) [Figure 10N][99]. Well-constructed PMMA composition and dealloying is a possible approach for large production of LIB anodes with amazing performance.

Inverse spinel-type NiFe2O4 anchored porous carbon fibers (NFO@C), synthesized by electrospinning/calcination, delivered superior LIB anodes to NFO, which was attributable to exclusive mesoporous fibrous structures, high surface area, fast Li+-ions diffusion, and improved electrical conductivity that eventually eschewed pulverization and agglomeration[100]. The physicochemical merits of mesoporous fibrous supports could significantly boost the electrochemical storage capacity of PMMA oxides. Facile evaporation-solidification/annealing was adopted to prepare vacancy-enriched Ni3ZnC0.7 nanohybrids, with much focus on stoichiometric and non-stoichiometric ratios, where the latter gave higher Li+-ion storage capacity (1,100 mAh/g@0.05 A/g), rate capability and cycling stability than the former (400 mAh/g)[101]. This study proved that a non-stoichiometric ratio of PPMA alloy carbides induces vacancies/defects that increased capacitive and diffusion-controlled charge-storage features, and Li+-ions adsorption, relative to the stoichiometric counterparts. A series of porous transition metal-Si-carbon composites (i.e., NiSix/Si/C, CoSix/Si/C, and TiSix/Si/C) were fabricated by ball-milling/annealing. Among the composites, NiSix/Si/C had higher initial SC (1,060 mAh/g@0.1 A/g), rate capability and CR than CoSix/Si/C (930 mAh/g) and TiSix/Si/C (832 mAh/g), due to its porosity and high specific area[102]. However, NiFe-NiFe2O4/rGO composites with adjustable mass ratios, synthesized by chemical reduction/calcination at various time (2-10 h)[103]. The optimized NiFe-NiFe2O4/rGO-8 anode at calcination time (8 h) gave impressive initial discharge SC (1,362 mAh/g@0.1 A/g) and CR (79.4%), amongst others, owing to its distinct composition, hollow microstructure, and optimal synergism. Optimizing the preparation conditions of binary MA oxide composites is necessary to tune the Li+-ion storage. The 3D porous ternary Ni-Co-Fe oxides (NiO/Co3O4/Fe3O4) hollow nanostructures were made by solution-precipitation/calcination and tested as a LIB anode[104]. The NiO/Co3O4/Fe3O4 exhibited superior initial discharge SC (1,052 mAh/g@0.5 A/g), CR (92.4%) and CE, compared to Co3O4/Fe3O4(~920 mAh/g; 85.7%), ascribable to the improved synergistic effect of Ni-Co-Fe ternary hollow nanocage architectures that boosted the transportation efficiency, amplified interfacial capacitance, and decreased contact barrier. Synergism of ternary PMMA oxides significantly changes the physicochemical merits advantageously used for improving the Li+-ion storage, relative to binary counterparts. MOF templates were utilized for the construction of 3D NiCo2O4@Fe2O3, with flower-like cross channel and surface crumpled structures, which delivered more reliable LIB anodes at high initial discharge SC (1,640 mAh/g@1.0 A/g) that was three folds of NiCo2O4 (1,261.5 mAh/g; 52.9%)[105]. However, CoNiSe2/C-700 fabricated from MOF templates exhibited outstanding Li+-ion storage at superior initial discharge SC (2,125.5 mAh/g@0.1 A/g), CE (98%) and long-term cycling performance, due to the synergism of the binary metal selenides, well-defined nanododecahedral architectures, improved electronic structure and fast charge transport at the electrolyte interface[106]. The enhanced LIB anode of the NiCo2O4@Fe2O3 was related to better conductivity, lower electrode interfacial barrier, porous channel structure and synergy between Ni-Co petal-like and crumpled Fe2O3 coating.

Sodium-ion batteries

The abundance and low cost of sodium (Na) have spurred the Sodium-ion batteries (SIBs) among the most auspicious energy storage technology[107,108]. The practicability of the SIBs lies largely on robust fabrication of electrodes with high SC and long cyclability. The development of suitable anodes is more thought-provoking; in this regard, the PMMA anodes have great potential for SIBs with high energy because of their high gravimetric/volumetric SCs and easy Na+-ion insertion/ejection[109-111]. The utilization of PMMA anodes for viable SIBs is conspired with enormous capacity fading, irreversible capacity, rate capability, low coulombic efficiency and poor cycling durability that lead to volume expansion[112,113]. This hitch is solved by incorporating conductive materials with their unique physicochemical merits that could accelerate the reaction kinetics and alleviate capacity fading[114-116]. Hence, the modulated physicochemical features of the PMMA anodes result in improved Na+-ion storage and stability. For example, a hydrothermal method was exploited to prepare Sb-doped SnO2 nanoparticles grown on N-doped graphene-carbon nanotubes aerogels (ATO/N-GCA) with spherical Sb-SnO2 on sheet-like nanotubes, high porosity and electrical conductivity that delivered increased initial SC (409 mAh/g@0.1 C), CR (74%) and lower charge transfer resistance (Rct = 314 Ω) than ATO/G (124 mAh/g; 59%, 475.6 Ω)[58]. This was traced to the rapid Na+-ions diffusion, instead of electrons, on SnO2 and macroporosity for easy contact and sodiation/desodiation during cycling. However, ultra-small SnSb nanocrystals embedded N-rich porous carbon nanowires (SnSb/N-PCNWs), synthesized by electrospinning/calcination [Figure 11A], were endowed with enhanced electronic properties, plentiful edges/defects for rapid Na+-ions adsorption, robust spherical metals on nanowires, proved by SEM and TEM [Figure 11B and C], crystalline-phase reservation and highly reversible alloying/dealloying behavior that facilitated its boosted SIB anode at superior rate capability, CR (100%) and cycling performance, compared to counterpart without urea (SnSb/CNWs), PCNWs and bulk SnSb [Figure 11D and E][117]. Distinctive nanoarchitectural design of PMMA anodes with alloying/dealloying nature allows an extremely long lifespan for SIBs.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 11. (A) Electrospinning/annealing synthesis, (B) SEM, (C) TEM, (D) rate performance, and (E) ultra-long cyclability of SnSb/N-PCNWs. This figure is quoted with permission from Ref.[117] Copyright 2019 Elsevier. (F) SEM, (G) charge/discharge curves at 0.2 A/g for 1st-5th cycles, (H) rate capability, and (I) long-term cyclability and coulombic efficiency of ZMS@FCs. This figure is quoted with permission from Ref.[120] Copyright 2022 Wiley-VCH.

The construction of bimetallic metals core-shells (SnSe2/CoSe2@C), achieved by selenization/carbonization and tested as SIB anodes, showed higher initial SC (455 mAh/g@0.1 A/g), rate capability and CR (77.6%) than SnSe2/CoSe2 (300.31 mAh/g) and mechanically-mixed SnSe2-CoSe2 (29 mAh/g)[118]. This study proved that the addition of carbon to SnSe2/CoSe2 improved the conductivity, retained the architectural design, and prevented capacity fading. Also, poor chemical bonding in multiple metal selenides results in capacity fading and structural damage. A self-adaptive Sn-Bi@C composite, prepared by hydrothermal/annealing, had Bi-core with Sn shell that exhibited uniform stress circulation, alleviated structural strain, improved electrical conductivity and Na+-ions diffusion kinetics, advantageous to deliver high SC (462 mAh/g@0.1 A/g) superior to Bi@C (232 mAh/g), Sn@C (374 mAh/g) and pure Sn (219 mAh/g), besides its outstanding CR (86.9%) and cycling performance[119]. This study proved the merits of biphase mixing of metal atoms in PMMA anodes for efficient Na+-ion storage.

Porous carbon-supported Zn-Mn selenides (ZMS@FC) were constructed by solvothermal/calcination, and examined as SIB anodes[120]. The ZMS@FC was endowed with flower-like metal selenides on flakes support, proved by SEM [Figure 11F] that enabled outstanding initial SC (494.8 mAh/g@0.2 A/g), great rate capability, and CR (74.7%) [Figure 11G-I], compared to MnSe@C (230.9 mAh/g) and ZnSe@C (343.2 mAh/g). This was ascribed to the synergism of the flower-like binary selenides and porous carbon flakes. This study revealed that multimetallic chalcogenides are promising anodes for Na+-ion storage and stability.

Also, ultrathin Cu4Mo6Se8 grown on carbon skeleton (CMSe/C), achieved by chelation/annealing and tested as SIB anode, exhibited exceptional rate capability, initial discharge SC (514 mAh/g@0.5 A/g) and CR (107.7%), relative to MoSe2 (203 mAh/g), ascribable to its copious void space, homogeneous morphology, ultrathin nanosheet arrays and improved conductivity[121]. Moreover, a series of rod-shaped CoSb2Se4@Sb2Se3, i.e., 1CSS, 2CSS and 4CSS at varied Co amounts (0.1, 0.2 and 0.4 mmol), synthesized by hydrothermal, where the optimized Co amount coating in 2CSS anodes of SIB suppressed volume expansion, enhanced structural integrity and cycling stability, and resulted in high CR (81.4%)[122]. This work confirmed the benefits of multimetallic chalcogenide alloy anodes with suitable/appropriate metal atoms coating for excellent Na+-ions diffusion and storage. Chemical reduction/calcination was utilized to construct NiCoSe2 on N,Se codoped carbon (NiCoSe2@NSC) and demonstrated as superior SIB anode at higher SC (572.5 mAh/g@0.2 A/g) and CR (85.1%), relative to CoSe2/NSC (252.7 mAh/g; 82.1%)[123]. This was traced to the synergism, electronic effects, and ions transport of multimetallic selenide alloys, following the probed reaction mechanism by in-situ X-ray diffraction (XRD) and theoretical calculations [Figure 12A-E].

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 12. (A) In-situ XRD during 1st and 2nd charge-discharge cycles, (B) atomic structure model, (C) density of states, (D) Na+ ions adsorption energies, and (E) diffusion energy barriers of Na+ ions of NiCoSe2 and CoSe. (F) Top/side view of most stable adsorption sites, (G) charge density differences of each structure and (H) simulated density of states of VS4/SnS2/MXene, VS4/MXene and SnS2/MXene. This figure is adapted from Ref.[123,124] Copyright permission 2024 Elsevier.

VS4/SnS2 confined MXene (VS4/SnS2@MXene), prepared by hydrothermal/etching/self-assembly, was demonstrated as an anode for Na+-ion storage, proven experimentally and theoretically[124]. The VS4/SnS2@MXene exhibited outstanding SC (2,508.4 mAh/g@0.1 A/g), CR (82.8%) and rate capability, compared to VS4@MXene and SnS2@MXene, owing to the heterogenous interfacial interaction that facilitated rapid Na+-ions, electron mobility, and reduced volume expansion, evidence by the theoretical calculations [Figure 12F-H]. This work proved that construction of heterostructures on conducting 2D network augments the physicochemical merits for high-performance RAMIBs. The influence of partial Mn ion replacement, at various contents (5%-15%), in NiCoS nanosheets, i.e., NCMS-5, NCMS-10 and NCMS-15, was investigated as SIB anodes[125]. This revealed that the NCMS-10 was the optimized ratio with unique structures and more accessible active sites to mitigate the volume expansion and enhance stability, thereby enabling high SC (662.6 mAh/g@0.3 A/g), CR (85.4%), rate capability and long-term cycling stability, amongst others. The appropriate addition of metal atoms in PMMAs is beneficial for excellent Na+-ion storage. Indeed, the PMMAs are excellent SIB anodes, but only a few studies were reported. There is a need for further exploration of PMMA anodes for SIBs with outstanding performance, cyclability and rate capability.

Potassium-ion batteries

The Potassium-ion batteries (PIBs) are recently drawing so much interest as an alternative to LIBs and SIBs because of their chemical and economic merits[126]. Their chemical quality is traced to low potential of K+/K (-2.88 V vs. SHE) in carbonate ester electrolytes[127], which infers a high ED with K+-ions as the charge carrier and a low risk of potassium (K) plating[128]. Also, K+-ions boost the ionic conductivity and rapid diffusion rate. The economic advantage is due to the essentially limitless and worldwide distribution of K reserve at low cost [i.e., potassium carbonate (K2CO3, $1,281/tonne) compared to lithium carbonate (Li2CO3, $6,500)][129]. Also, PIBs allow the use of extremely cheap electrode materials and facilitate an easy transition to commercialization with the existing LIB industry. Amongst the commonly used PIB anodes, PMMA anodes are promising with higher capacity and/or power than carbon-based anodes[130]. However, only a few studies reported the performance of PMMA anodes for PIBs. For example, a 3D nanoporous CuBi (NPCuBi) anode was fabricated via melt-spinning/dealloying [Figure 13A], which enabled interconnection of Bi as an active phase and Cu ornamented as a highly conductive matrix with bicontinuous ligament-channel architecture, proved by SEM [Figure 13B], abundant porosity, synergistic effect, and conductivity of CuBi that surmounted slow K+-ion diffusion kinetics and volume expansion during cycling, and resulted in superior PIB anodes at initial discharge SC (1,045 mAh/g@0.05 A/g), CR (> 93.0%) and rate capability to nanoporous Bi (~650 mAh/g) [Figure 13C and D][131]. Dealloying of Bi-based alloys is an effective strategy for boosting K+-ion storage and stability.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 13. (A) Melt-spinning/chemical dealloying synthesis, (B) SEM, (C) cycling and (D) rate performance for 50 cycles of NPCuBi and NPBi. This figure is quoted with permission from Refs.[131] Copyright 2020 Wiley-VCH. (E) SEM, (F) 1st-3rd charge/discharge curves and (G) cycling performance at 0.1 A/g of FeCo@PAZ-C. (H) galvanostatic charge/discharge curves for 1st-3rd, 50th and 100th at 0.1 A/g, (I) rate capability, and (J) long-term cyclability of ZCS@NC@C@rGO, ZCS@NC@C and ZCS@NC. This figure is quoted with permission from Ref.[132,133] Copyright 2024, 2023 Elsevier.

Flower-like porous carbon-embedded Zn-Mn selenides (ZMS@FC), made via solvothermal/calcination, demonstrated exceptional performance as PIB anodes. They exhibited a great initial SC (494.8 mAh/g@0.2 A/g), CR (74.7%) and rate capability, compared with MnSe@C (230.9 mAh/g) and ZnSe@C (343.2 mAh/g), due to the contributory effects of flower like shape with hierarchical porosity and rich accessible metal active sites besides high electrical conductivity of FC and synergism of ZMS[120]. Controlled synthetic strategies enable the easy tuning of physicochemical merits of PMMA selenides as efficient anodes for commercialization of PIBs. N-doped carbon-based composite with FeCo nanoalloys (FeCo@PAZ-C) was constructed from MOF-template annealing and tested as a good PIB anode[132]. FeCo@PAZ-C had spherical nanoalloys core-nanosphere shell morphology, proved by SEM [Figure 13E], that enabled excellent initial SC (1,232.0 mAh/g@0.1 A/g), CE and CR (95%) [Figure 13F and G], due to its capability to boost K+-ion storage by lowering its diffusion routes and increase electron mobility. Incorporation of PMMAs on both surface and interior of conductive materials needs to be further explored for improved K+-ion storage. N-doped carbon (NC), resorcinol-formaldehyde-derived carbon (C) and rGO confined ZnSe/Co0.85Se (ZCS@NC@C@rGO) was synthesized by co-precipitation/selenization/annealing and examined as a good PIB anode[133]. The ZCS@NC@C@rGO had superior initial SC (422.2 mAh/g@0.1 A/g) to ZCS@NC (340 mAh/g) and ZCD@NC@C (345 mAh/g), besides its good rate capability and cycling performance [Figure 13H-J]. This was due to the porous carbon microcubes and carbon shell that provided rich channels for rapid electron mobility and K+-ions intercalation/deintercalation and prevented agglomeration of the bimetallic selenides and volume change. Notably, multilevel spatial confinement of PMMA selenides is an efficient strategy to enhance the K+-ion storage and stability.

Germanium-based alloy anodes (GeV4S8) were rationally fabricated by physical mixing/annealing to incorporate Ge atoms into V-S framework with loosely packed and metallic media that facilitated rapid K+-ion/electron diffusion and reduced volume expansion, shown by theoretical calculations [Figure 14A-F], as a good PIB anode at SC (400.0 mAh/g@0.5 A/g), and CR (80%), compared to most state-of-the-art anodes[134]. The dual functions of multimetallic alloy selenides and fast K+-ions intercalation enable high capacity and kinetics of PIB anodes. Vulcanization annealing was explored to incorporate CoS2/SnS2 into S-doped carbon (CoS2/SnS2@SC), which gave excellent K+-ion storage at high initial discharge SC (1,026.0 mAh/g@0.1 A/g), CR (76%), and cycling performance[135]. This was due to the internal voids in the CoS2/SnS2 core and enhanced electron transport with alleviated polysulfide dissolution. Selective morphological and structural designs of multimetallic alloy anodes are significant for excellent K+-ion storage. A 3D composite microsphere (CoFe)Sex-rGO-CNT) was synthesized by spray pyrolysis and the effect of electrolyte (dimethyl ether (DME)- and ethylene carbonate (EC)/DEC-based) on its PIB anodic performance was explored[136]. The structural stability of (CoFe)Sex-rGO-CNT allowed higher CE, rate capability, K+ ions diffusion and cycling stability than (CoFe)Sex-rGO, besides improved K+-ion storage in DME-based electrolyte, relative to EC/DEC-based electrolyte. This was attributed to the formation of a thin stable solid-electrolyte layer (SEI) in DME-based electrolyte. Suitable electrolytes with appropriate SEI layers that allow rapid ions/electron transport are considerable parameters for the assembly of high-performance PIBs. A 3D microflower BiFeO3 (BFO-MF), assembled from its nanosheets precursors via solvothermal method, exhibited impressive performance as a PIB anode at good SC (606.0 mAh/g), great cycling performance, CR (98.2%) and power/energy densities (2,152.8 W/kg; 177.1 Wh/kg)[137]. This was traced to its favorable affinity/diffusion for K+-ions with rapid electrochemical kinetic and contracted voltage-hysteresis, proved by theoretical calculations [Figure 14G-J]. This work proposed the possibility of extensive research in developing advanced Bi-based alloy anodes for high ED and durable PIBs.

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 14. (A) Density of state (DOS), (B) K+-ions adsorption energies, (C) K+-ions diffusion energy barriers of GeV4S8, V5S8, GeS2 and Ge, and (D-F) charge density difference maps with side views of K/GeV4S8, K/V5S8, and K/GeS2. (G and H) Structural models and corresponding charge density differences for the adsorption of K+ ions on {110} and {111} facets, (I and J) energy and diffusion barrier of BiFeO3. This figure is reproduced with permission from Ref.[134,137] Copyright 2024 Wiley-VCH.

Solvothermal/calcination methods were explored for the construction of FeS2/MoS2 on N-doped carbon (FMS@NC) with spherical flower-like morphology, synergistic effect to alleviate volume expansion and conductivity to give good PIB anodic performance at SC (585.0 mAh/g@0.05 A/g), CR (93.9%) and cycling capability[138]. Systematic construction of heterostructure alloys with conductive materials is viable for high-performance PIB anodes and stability. Although PMMAs are promising anodes for PIBs, only very few studies have been reported as far as we found. The in-situ construction of PMMAs with Cu substrate revealed the best K+-ion storage capacity and long-term durability. Thus, there is a need for this area of research to be extensively exploited and optimized.

RAMIBs RECYCLING AND CIRCULAR ECONOMY

The recycling of RAMIBs is pivotal for developing a sustainable circular economy, mitigating environmental hazards, and promoting a sustainable future, but it remains a significant challenge[139]. This is attributed to the complex chemistry and the need for specific processes to recover rare metals (i.e., Li, Ni, Al, and Co)[140,141], which offer an alternative way to decrease the consumption of these metals besides reducing wastes. Life cycle assessments, including all steps from the extraction of anode materials to end-of-life treatment, are needed to estimate the environmental footprint of RAMIBs recycling processes to determine areas that require prompt improvements to enhance sustainability[142]. For example, unveiling the trade-offs between the environmental benefits of material recycling and the encumbrances of collection and treatment can direct the process towards more eco-friendly practices[142]. Also, the rational design of advanced recycling technologies and life cycle thinking in managing RAMIBs is vital to attain a circular economy[143-145].

Considering the widespread applications of the RAMIB devices for portable electronics, electric vehicles and renewable energy systems, their environmental impact assessment, including (i) raw materials mining and resources extraction; (ii) production stage; (iii) usage phase; and (iv) end of life and recycling, is a crucial area of concern. The extraction of the anode materials (Li, Na, K) from mineral ores and brine deposits could result in water depletion, contamination and environmental disorders. For instance, the mining of cobalt, manganese and nickel results in total emission of 8.1 GtCO2 equivalent in 2050[146], which causes considerable environmental degradation, such as soil and water pollution, deforestation and harmful consequences on the immediate localities. Also, the manufacturing of RAMIBs (LIBs, SIBs and PIBs) requires high energy consumption, which contributes to greenhouse gas emissions and carbon footprint, which are highly concentrated in three countries: China (45%), Indonesia (13%) and Australia (9%)[146]. Besides, the use of various chemicals during the production of RAMIBs could pose the risks of hazardous chemical spillage and pollution if not optimally managed. However, during their use for electric vehicles and renewable energy systems, the RAMIBs are highly effective in reducing the overall greenhouse gas emissions, as no pollutants are emitted, making them cleaner than fossil fuel-based systems[147]. After complete usage (i.e., end of life stage), the RAMIBs are either disposed of or recycled: inappropriate disposal of the RAMIBs could result in water and soil pollution with toxic materials such as heavy metals and pose fire hazards with environmental and safety concerns; meanwhile recycling of valuable materials in spent RAMIBs is complex and not economically viable[148]. Hence, the current recycling rate of RAMIBs is extremely low. Significant enhancement of the technology and infrastructures is a necessity for sustainability. Although there are environmental concerns associated with the production of RAMIBs, the devices still significantly reduce the emissions of greenhouse gas by 38% in 2050[146], particularly for transportation and renewable energy systems. Their sustainability efforts are directed toward improving the RAMIB technology with much focus on reducing total reliance on essential raw materials, advancing recyclability and devising more mining sustainable and manufacturing processes, implementing stricter policy regulations, and promoting sustainable practices in the RAMIB lifecycle.

The policymakers who can promote a circular economy for RAMIBs recycling need proper and clear policy measures to drive sustainable practices and enhance resource efficiency through various processes[149]. This includes material management (i.e., supply chain traceability, material transport/storage/recovery), awareness (i.e., stakeholder engagement and educational campaigns), incentivizing circular business models (i.e., financial incentives, and market signals), and worldwide cooperation[149].

The market size and growth of RAMIBs recycling are noteworthy, indicating the growing importance of sustainability in the battery industry. Mainly, the global market size of battery recycling is nearly 1.83 billion USD in 2023 and is expected to grow by about 37.6% from 2024 to 2030[150]. The market share of RAMIBs is about 75% of the global battery market share[150]. Some successful examples of battery recycling occurred in China, which leads the global battery recycling with over 500,000 metric tons, compared with the USA and Europe, both of which had a recycling capacity of nearly 200,000 metric tons[151,152]. The leading technologies for recycling batteries in China include recycling electric-vehicle batteries and utilization of spent vehicle batteries, which could reach a market size of (3.59 billion Euros) by 2025, and reusing electric-vehicle batteries operate below 70%-80% capacity after 4-6 years in slower light electric vehicles and stationary energy storage application[153,154]. In Europe, the recycling market for batteries will reach 130GWh by 2030, which is about 700 kilotons of recycling capacity required, and will increase by three times by 2040[152].

CONCLUSION AND OUTLOOK

In brief, this article reviews the rational design of PMMA (i.e., Sn, Mn, Mo, Co, V, and Fe) anodes using various approaches (i.e., template-based, hydrothermal/solvothermal, chemical reduction, electrochemical deposition, sol-gel, dealloying and electrospinning) for the RAMIBs (i.e., LIBs, SIBs, and PIBs). This is besides the fundamental aspects (i.e., mechanisms and calculations), along with the deep discussions on the key descriptive factors of RAMIBs (i.e., lifespans, ED, structural changes, and mechanisms) corroborated with the summary tables, schemes, and figures. The results discussed above warranted that the performance of PMMAs in LIBs is significantly superior to SIBs and PIBs, respectively, as shown in the higher SC, CR and cycling durability [Tables 1-3]. Meanwhile, the most active anodes in LIBs were FeCo2O4 octahedral (SC = 2,436@0.2 A/g) prepared by the sol-gel method[69], 3D reticular-like and ZnMn2O4/NF (SC = 2,211@0.4 A/g) obtained using hard-template/annealing[87], FeCo2O4 (SC = 2,436@0.2 A/g), and CoFe2O4 nanoplates (SC = 2,134.7@0.1 A/g) by melt spinning/dealloying[99]. The sol-gel method is the most promising for tailoring morphology and compositions of RAMIBs. Despite the advances in PMMA anodes for the RAMIBs, the current challenges could be thwarted via the following proposed potential research directions [Figure 15]:

Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries

Figure 15. Summary of the outlook highlighting the recent advances, challenges and solutions proffered for future research.

Table 1

Comparative porous transition metal alloy anodes for LIBs

AnodesSynthesis methodMorphologyElectrolyteCapacity/mAh/g@current density (A/g)CyclesCapacity retention/%Ref.
Sn/Cu foamElectrodepositionGrape-like foam 1 M LiPF6 in EC/DMC (1:1)821.5@0.15058.0[56]
Sn-Sb/CuTemplate-like electrodeposition/annealingSponge-like foam1 M LiPF6 in EC/DMC/DEC (1:1:1)651.9@0.53082.9[57]
ATO/N-GCAHydrothermalSpherical metals on sheet-like nanotube1 M LiPF6 in EC/DMC (1:1)942@1.01,00072.7[58]
CoSn2Chemical reductionTetragonal1 M LiPF6 in EC/DMC (1:1)/FEC(3%)650@2.05,000-[59]
CoSn2OxChemical reduction/ball millingSpherical 1 M LiPF6 in EC/DMC (1:1)525@2.01,50092.0[60]
rGO/NiCo2O4Hydrothermal/annealingNanosheets on porous wrinkled films1 M LiPF6 in EC/DMC (1:1)1,697.9@0.25061.0[65]
CuO/CoO core/shell array on Cu foamHard-template and annealingNanosheets on nanotubes1 M LiPF6 in EC/DMC/DEC (1:1:1)1,216@0.11,00093.8[66]
ZnCo2O4/NFHard template/calcinationFlower-like nanosheets1 M LiPF6 in EC/DMC/EMC (1:1:1)1,544@0.110082.0[67]
NiCo2O4/NiO-HDSolvothermal/calcinationHollow dodecahedron1 M LiPF6 in EC/DMC (1:1)1,622@0.210063.5[32]
NiCo2O4Solvothermal/annealingRose flower-like nanosheets 1 M LiPF6 in EC/DEC (1:1)1,282@1.010094.0[68]
FeCo2O4Sol-gel/annealingOctahedral1 M LiPF6 in EC/DMC/DEC (1:1:1)2,436@0.220095.2[69]
ZNCO/GNSHard-template/calcination/chemicalreductionMicrospheres core/nanosheet shell 1 M LiPF6 in EC/DMC/EMC (1:1:1)1,429@0.15095.0[70]
ZnCo2O4 film/NFHard-template/annealing3D porous networks1 M LiPF6 in EC/DEC (1:1)1,726@0.410063.0[71]
Te@ZnCo2O4Templated/annealingCore-shell nanofibers1 M LiPF6 in EC/DEC (1:1)1,364@0.1100~100[72]
Zn-Co-S@NS-CPTemplate pyrolysisHollow polyhedron1 M LiPF6 in EC/DMC/DEC (1:1:1)1,298.1@0.57400-[73]
CoO-ZnO@NC-450Hydrothermal/annealingSpherical nanoparticles1 M LiPF6 in EC/DMC (1:1)975.2@0.210081.6[74]
CoMoO4-CoO/S@rGOTemplated hydrothermal/AnnealingSpherical metals on polyhedron sheets1 M LiPF6 in EC/DEC (1:1)/FEC (5 wt.%)1,672@0.515062.1[75]
CoO/CuHard-template/pulsed electrodepositionNanowire core/spherical shell1 M LiPF6 in EC/DEC (1:1)1,215@0.525068.1[76]
ZnMn2O4solvothermal/annealingTwin-microspheres1 M LiPF6 in EC/DMC/DEC (1:1:1)1,106@0.513077.8[84]
ZnMnO3Co-precipitation/annealingSpherulites1 M LiPF61,294@0.515067.9[85]
CoMn2O4/NFHard-template/annealing3D reticular-like1 M LiPF6 in EC/DMC (1:1)1,833@0.410074.5[86]
ZnMn2O4/NFHard-template/annealing3D reticular-like1 M LiPF6 in EC/DMC (1:1)2,211@0.410094[87]
Ni-Co-Mn oxide QS-HSSelf-templated hydrothermal/annealingHollow microspheres1 M LiPF6 in EC/DMC (1:1)1,761.8@0.225079.5[88]
np-Ni@NiO/MnO/NFInduction melting/dealloying/annealingCoarsened grains1 M LiPF6 in EC/DMC/DEC (1:1:1)960@0.1200105[89]
ZMO-G500Solvothermal/calcinationSpherical metal on nanosheets1 M LiPF6 in EC/DMC (1:1)1,100@0.120099.95%[90]
MN-1/P In-situ electroconversion/calcinationFlower-like nanosheets1 M LiPF6 in EC/DMC (1:1)1,554@0.11,000~100[91]
Cu/Mn3O4@SCTemplate annealingMicrospheres1 M LiPF6 in EC/DEC (1:1)766.2@0.21,00066.3[92]
TFCsHydrothermal/calcinationSpherical metals on nanotubes1 M LiPF6 in EC/DMC/DEC (1:1:1)1,589@0.545058.0[96]
3D-OHP-a-VOx/MoOyFreeze-dried/annealing(3D) ordered hierarchical porous sheets1 M LiPF6 in EC/DMC/DEC (1:1:1)1,705@0.15082.1[97]
Zn3V2O8Solvothermal/annealingHollow nanocages1 M LiPF6 in EC/DMC/DEC (1:1:1)1,906@0.120070.7[98]
CoFe2O4Melt spinning/dealloyingNanoplates 1 M LiPF6 in EC/DMC (1:1)2,134.7@0.120099.1[99]
NFO@CElectrospinning/annealingSpherical metals on fibers1 M LiPF6 in EC/DMC/DEC (1:1:1)1,030@0.110072.3[100]
Ni3ZnC0.7Evaporation-solidification/annealingIrregular spheres1 M LiPF6 in EC/DEC (1:1)1,100@0.051,000100[101]
NiSix/Si/CBall milling/annealingIrregular spheres1 M LiPF6 in EC/EMC (1:1)1,060@0.120072[102]
NiFe-NiFe2O4/rGO-8Chemical reduction/annealingSpherical metals on wrinkled sheets1 M LiPF6 in EC/DMC (1:1)1,362@0.113079.4[103]
NiO/Co3O4/Fe3O4Precipitation/calcinationHollow nanocages1 M LiPF6 in EC/DMC/EMC (1:1:1)1,052@0.540085.7[104]
NiCo2O4@Fe2O3Hydrothermal/calcinationFlower-like porous channels1 M LiPF6 in EC/DEC (1:1)1,640@1.040057.6[105]
CoNiSe2/C-700Template annealingNanododecahedral1 M LiPF62,125.5@0.11,00098[106]
Table 2

Comparative porous transition metal alloy anodes for SIBs

AnodesSynthesis methodMorphologyElectrolytesCapacity/mAh/g@current density (A/g)CyclesCapacity retentio/%Ref.
ATO/N-GCAHydrothermalSpherical metals on sheet-like nanotubes1 M NaClO4 in EC/FEC (1:1)/FEC(5%)409@0.150074.0[58]
SnSb/N- PCNWsElectrospinning/annealingSpherical metals in nanofibers1 M NaClO4 in EC/DMC (1:1)/400@0.0510,000100[117]
SnSe2/CoSe2@CSelenization/carbonizationNanobox core/shell1 M NaPF6 in DIGLYME/DOL (1:1)455@0.150077.6[118]
Sn-Bi@CHydrothermal/annealingnanosphere core-shell on layer support 1 M NaPF6 in DME462@0.12,00086.9[119]
ZMS@FCSolvothermal/calcinationFlower-like metals on porous flakes1 M SHCF in DEGDME494.8@0.21,00074.7[120]
Cu4Mo6Se8/CChelation/annealingUltrathin nanosheets polyhedral C skeleton 1 M NaPF6 in DME514@0.52,400107.7[121]
CoSb2Se4@Sb2Se3Hydrothermal Rod-shaped1 M NaCF3SO3 in DEGDME437.9@0.116081.4[122]
NiCoSe2@NSCChemical reduction/annealingSpherical nanoparticles on porous nanosheets1 M NaPF6 in DME572.5@0.2 1,00085.1[123]
VS4/SnS2@MXeneHydrothermal/etching/self-assemblyNanosheets on layered MXene1 M NaPF6 in EC/DEC (1:1)/FEC(5%)2,508.4@0.120082.8[124]
Mn-NiCoS-10Solvothermal/annealingNanosheets1 M NaPF6 in DME662.6@0.31,00085.4[125]
Table 3

Comparative porous multimetallic alloy anodes for PIBs

AnodesSynthesis methodMorphologyElectrolytesCapacity/mAh/g@current density (A/g)CyclesCapacity retention/%Ref.
NPCuBiMelt-spinning/chemical dealloyingNanospheres with bicontinuous open channel1 M KFSI in DME1,045@0.0550> 93.0[131]
ZMS@FCSolvothermal/calcinationFlower-like metals on porous flakes1 M KPF6 in EC/DEC (1:1)494.8@0.21,00074.7[120]
FeCo@PAZ-CTemplate/annealingSpherical nanoparticle core on nanosphere shell1 M KPF61,232.0@0.1 50095[132]
ZnSe/Co0.85Se@NC@C@rGOCo-precipitation/selenization/annealingMicrocubic core-shell1 M KFSI in DME422.2@0.12,00055.5[133]
GeV4S8Physical mixing/annealingNanocubes3 M KFSI in DME400.0@0.51,00080.0[134]
CoS2/SnS2@SCVulcanization annealingCore-shell1.5 M KFSI in EC/DEC (1:1)1,026.0@0.11,50076.0[135]
(CoFe)Sex-rGO-CNTSpray pyrolysisMicrospheres on hierarchical supports1 M KFSI in EC/DEC600.0@0.5200˃ 90.0[136]
BiFeO3-MFHydrothermalFlower-like spheres3 M KFSI in DME606.0@0.55,00098.2[137]
FMS@NCSolvothermal/calcinationSpherical flower-like1.5 M KFSI in EC/DEC (1:1)585.0@0.053,00093.9[138]

• Many studies have addressed storage mechanisms, but PMMA anode failure mechanisms in RAMIBs are rarely reported, necessitating further investigation alongside ambiguous dendrite suppression and related chemical reactions[27]. This goal can be achieved by initially examining electrochemical merits of custom full cells, using experimental, theoretical, and in-situ studies to address problems in future electrode design[21].

• The preference for synergetic or strain effects in PMMAs, particularly with active alkali metals, remains unclear. Some reports indicate that synergism can enhance electrode durability and capacity[27]. Systematic studies, proper metal selection, and in-situ characterization techniques [TEM, XRD, X-ray photoelectron spectroscopy (XPS)] are essential to determine the preferred effect and monitor structural changes during the electrochemical reactions.

• Current fabrication methods face barriers such as hazardous chemicals, low yield, and complexity, necessitating new green and simple synthesis methods for atomic-level metal mixing and improved surface features and structure stability[155,156].

• To optimize the performance of PMMA anodes, factors such as electrolyte type, additives, pH, and composition must be considered. Exploring cost-effective and durable electrolytes is crucial, with ionic liquid electrolytes and solid electrolytes being the most promising options[157,158]. Electrochemical impedance spectroscopy (EIS) analysis can estimate electrolyte resistance and provide insights on interfacial interactions[159].

• Interfacial engineering enhances kinetics and chemical durability in alkali metal ions intercalation/deintercalation[25]. Hierarchical porous morphologies with a high surface area-to-volume ratio and support materials, including carbon, improve metal dispersion and stability against aggregation[15,160,161]. Support can be optimized via in-situ fabrication of PMMAs with strong metal-support interaction.

• Encapsulation of low-temperature liquid MAs inside porous MA under high pressure offers a self-healing anode or substrate, preventing dendritic growth of alkali metals. However, new assembly approaches and electrolytes are required[162].

DECLARATIONS

Authors’ contributions

Data collection and writing: Ipadeola AK

Conceptualization, writing, and supervision: Eid K

Review, supervision, and funding: Abdullah AM

Availability of data and materials

The materials are available upon request.

Financial support and sponsorship

This work was supported by (i) the Qatar National Research Fund (QNRF, a Division of the QRDI Council) through the Academic Research Grant (ARG) program, Grant# ARG01-0524-230330, and (ii) Qatar University through an International Research Collaboration Co-Fund program, Grant# IRCC-2023-157.

Conflicts of interest

All authors declared that there are no conflicts of interest.

Ethical approval and consent to participate

Not applicable.

Consent for publication

Not applicable.

Copyright

© The Author(s) 2024.

Supplementary Materials

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Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries
Adewale K. Ipadeola, ... Kamel EidKamel Eid

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Ipadeola, A. K.; Abdullah, A. M.; Eid, K. Recent advances in porous multimetallic alloy-based anodes for rechargeable alkali metal-ion batteries. Energy Mater. 2024, 4, 400079. http://dx.doi.org/10.20517/energymater.2024.34

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