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Nanomaterial coating for layered lithium rich transition metal oxide cathode for lithium-ion battery

  • Sanjana S. Bhosale , Zhineng Sun and Ruoyu Hong EMAIL logo
Published/Copyright: June 20, 2024
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Abstract

Nowadays, the energy supply market for commercial electrical vehicles and mobiles is highly dominated by Li-ion batteries (LIBs). The layered Li-rich (LLR) oxide MNC (Mn, Ni, and Co)-based cathode is a promising material for next-generation LIBs due to its high energy and power density, cost-effectiveness, and eco-friendliness. However, LLR material’s micrometer-size particles can lead to intergranular cracks during electrochemical cycling at high voltages, resulting in a thick solid electrolyte interphase. Along with this, structural fluctuations, particle agglomeration and non-uniform particles, oxygen loss in initial cycling, Mn dissolution, irreversible cation migration, high internal resistance, and corrosion contribute to issues like low charge–discharge capacities, voltage fade, irreversible capacity loss, poor Coulombic efficiency, and limited rate capability, degrading the electrochemical performance of the LLR cathode. Fortunately, the nanomaterials (NMs) coating, including oxides, phosphates, fluorides, carbon compounds, and polymers, offers solutions through core/shell strategies composed of LLR core and nanoscale shell. This article delves into NM coating advantages and methods for achieving uniform, homogeneous, and ultrathin nanocoatings (less than 40 nm thickness). Additionally, incorporating the ultrathin spinel layer and oxygen vacancies can further enhance the electrochemical activity.

Graphical abstract

1 Introduction

Enormous utilization of petroleum products all over the world causes a serious problem: global warming. Also, dependency on petroleum oil increases production costs while causing petroleum shortages. To address these challenges, there is a significant need for clean and renewable energy transportation systems [1]. Over the past five decades, researchers have been working on environment-friendly power devices, with lithium-ion batteries (LIBs) emerging as a highly advantageous system due to their eco-friendliness, high energy, and high specific capacity [2]. LIBs find extensive use in various devices, from laptops to hybrid electric vehicles and plug-in hybrid electric vehicles.

Recent research by Turrentine and his colleague at ITS-Davis has outlined the remarkable growth in the global market for plug-in electric vehicles, with about 65% of the expansion occurring in 2017 [3]. Bloomberg New Energy Finance predicts that approximately 50% of the global car market will be dominated by electrical vehicles (EVs). However, conventional batteries are unable to meet the rising demand for high-performance power devices [4]. Therefore, extensive research is ongoing to explore advanced materials for various LIB components, including anodes and cathodes, binder, separators, and electrolytes, aiming for higher energy and power density, increased specific capacity, enhanced durability, safety, and cost-effectiveness [58].

The ternary layered lithium-rich (LLR) cathode with the chemical formula of xLi2MnO3·(1−x)LiMO2 or Li1+x M1−x O2 (M = Mn, Ni, Co) offers high energy density (1,000 Wh/kg) and a capacity of around 300 mAh/g compared to conventional cathodes [912]. However, LLR cathodes face issues such as voltage fade [1315], capacity fade [16], irreversible capacity loss (ICL) [17], poor cycle stability [18], rate capability [19], etc. Recent research focused on implementing nanocomposite and nanometer-sized (nm) coating layers for LIB’s anodes and cathodes. These coatings optimize electron and ion diffusion pathways while preventing undesirable, irreversible side reactions and reducing the barrier between the electrode and electrolyte [20]. In 2020, the battery coating market was valued at $169 million and is projected to reach $301 million by 2025, nearly doubling from 2020. It is expected that battery coating technology will garner significant attention from researchers, electronics consumers, and EV companies in the coming years [21].

This review extensively explores LLR-Mn, Ni, and Co (MNC)-based oxide cathode, the advantages and challenges of nanomaterial (NM) coatings, preparation methods for NMs-coated LLR, various materials for nanoscale surface modification of LLR, and the combination of doping and nanoscale surface modification.

2 LLR cathode

The chemical formula of LLR compounds is generally represented by two notations: xLi2MnO3·(1−x)LiMO2 (for two-phase nano-composite; M = Mn, Ni, and Co) and Li1+x M1–x O2 (single-phase solid solution; either Li2MnO3 or LiMO2 phase). The advantage of using layered composite electrode systems like Li2MnO3 and LiMnO2, which are structurally integrated is that they allow lithium extraction and insertion from and into the LiMnO2 component. Li2MnO3 was initially considered electrochemically inactive for lithium insertion and extraction between the voltage range of 2.0–4.5 V vs Li/Li+, becoming electrochemically active beyond 4.5 V. Li2MnO3 aids in lithium-ion transport within the composite structure during charge and discharge [2225]. Lattice oxygen in the LLR structure also plays a vital role in electron participation. Other cathode materials for LIB include lithium iron phosphate (LFP), lithium manganese oxide (LMO), nickel cobalt aluminium oxide (NCAO), and more. Figure 1 summarizes the performance comparison between these cathodes and the LLR cathode [9,2630].

Figure 1 
               Summary of performance of cathode materials.
Figure 1

Summary of performance of cathode materials.

There are three different structural configurations of LLR-MNC: a solid solution with a trigonal system and R-3m space group symmetry, a monoclinic system with C2/m space group symmetry or a nano-composite with both trigonal (R-3m) and monoclinic (C2/m) systems [31]. In 2004, Thackeray and co-workers proposed a nano-composite material, an integrated strategy of LLR cathode that contains two components. Both the components, monoclinic Li2MnO3 species (C2/m space group; also written as Li(Li1/3Mn2/3)O2) and rhombohedral LiMO2 species (R-3m space group; M = Mn, Ni, and Co) have layered α-NaFeO2-type rock-salt structures, where all octahedral sites in their closely packed oxygen arrays are occupied [32]. This integrated nano-composite theory is widely accepted. Other two structural configurations of LLR-MNC represents a solid solution of either R-3m or more commonly a C2/m symmetry. These two symmetries, R-3m and C2/m are structurally very similar. However, resolving the controversy between them is beyond the scope of this article.

In Li2MnO3, the Li+ and Mn4+ ions occupy the transition metal (TM) layer, whereas in LiMO2, only TM ions are present in the TM layers (Figure 2(a) and (b)). The LLR material’s structure is derived from the parent lamellar LiMO2 by gradually substituting excess Li+ for M3+ in the [MO2] layers. The presence of Li+ between the TM layer results in long-range and short-range cation ordering of Li+, with TM (likely Mn4+) ions organizing the Li2MnO3 phase [33]. Both the Li2MnO3 monoclinic phase and LiMO2 trigonal phase have two closely packed layers, (001) and (003) planes, with a distance of approximately 4.7 Å between them. The LiMn6 hexagonal honeycomb structure arises from one LiO6 octahedra surrounded by six MnO6 octahedra, creating a solid solution Li1+x M1−x O2 model that exhibits broad and weakly intense peaks in the X-ray diffraction pattern of LLR material within the 2θ range of 20°–30° [34]. The evolution of LLR cathode from 2001 to present and future prospects is illustrated in Figure 2(c).

Figure 2 
               Structure of LLR composite cathode material containing (a) LiMO2 (M = Co, Mn, Ni) and (b) Li2MnO3 phase. The transition metal layer is occupied by transition metal ions (Mn4+) and Li [1] (Copyright 2014, AIP publishers). (c) An outline of the history and future. (d) Proposed LS transformation mechanism in HE5050 LMR composite oxide via formation of tetrahedral lithium in the lithium layer and migration of Mn from octahedral TM layer to octahedral site of lithium layer. Panels (d) (a–e) correspond to the structural changes during charging [37] (Copyright 2014, ACS).
Figure 2

Structure of LLR composite cathode material containing (a) LiMO2 (M = Co, Mn, Ni) and (b) Li2MnO3 phase. The transition metal layer is occupied by transition metal ions (Mn4+) and Li [1] (Copyright 2014, AIP publishers). (c) An outline of the history and future. (d) Proposed LS transformation mechanism in HE5050 LMR composite oxide via formation of tetrahedral lithium in the lithium layer and migration of Mn from octahedral TM layer to octahedral site of lithium layer. Panels (d) (a–e) correspond to the structural changes during charging [37] (Copyright 2014, ACS).

Metal–oxygen bonding, such as the linear Li–O–Li configuration, relies on unhybridized O2p states that stimulate the electrons from oxygen participation in charge compensation [35]. However, oxygen evolution from the lattice structure can lead to the formation of Li2CO3 impurities on the electrode surface, hindering battery performance [36]. This oxygen evolution is linked to structural arrangements near the surface, potentially causing a phase transformation from layered to spinel structure. Figure 2(d) illustrates this transformation involving intra-layer Li migration from octahedral to tetrahedral sites and interlayer Mn migration from octahedral sites in the TM layer to octahedral sites in the Li layer through Li layer tetrahedral sites [37]. The conversion from a layered to a spinel phase disrupts Li ion diffusion channels, causing voltage decay [38].

Most LLR cathodes are made up of densely packed nano-sized primary particles that combine to generate micro-sized secondary particles. The micro-cracks can easily develop in these secondary particles due to the mechanical stress after electrochemical cycling. The infiltration of electrolyte into these micro-cracks may impede lithium ion transport by promoting the formation of a thick solid electrolyte interphase (SEI) layer at the crack interfaces. This thick SEI layer also contributes to the corrosion and dissolution of TM ions into the electrolyte and degrading overall battery performance [39,40]. These issues are closely linked to structural evolutions and chemical mechanisms within the material, particle concentration and size, and mechanistic reactions associated with the material.

Surface modification has proven to be a successful approach for changing the electrochemical processes within active materials and protecting them from side reactions at the electrode–electrolyte interface over the last two decades. In 2000, Cho and colleagues demonstrated that the sol–gel coating of SnO2 significantly enhanced the structural stability of LiCoO2 [41]. This concept of surface modification has since been applied to various cathodes [4248]. Hu et al. summarized that surface modification is a useful tool for addressing the aforementioned issues, as it can enhance the electronic and ionic conductivities, improve rate capability, suppress voltage fading, and improve initial coulombic efficiency (ICE) [49].

3 Advantages of NM coating on LLR

A thin NM coating layer with thickness less than 40 nm is an effective strategy to address poor electrochemical performance due to the large volume expansion and contraction associated with the phase transformation during cycling, thereby preserving the electrode’s structure and stabilizing cycle performance [5052].

NMs come in various morphologies, including zero-dimensional (0D) (e.g., quantum dots, nanoparticles) [53,54], one-dimensional (1D) (e.g., nanotubes, nanowires, nanorods) [55,56], two-dimensional (2D) (e.g., nanodisks, nanosheets, nanoplates) [57,58], three-dimensional (3D) (e.g., hierarchical nanostructures) [59]. Each morphology offers unique properties that influence electrochemical performance. 0D NMs, for example, have a high surface-to-volume ratio, while 1D NMs like nanorods and nanotubes are notable for their rapid lithium ion transport along their 1D direction. Incorporating 2D nanosheets or nanoplates exposes specific sites involved in electrochemical processes. The 3D hierarchical nanostructures combine the advantages of both nano- and micro-systems [60]. NM coating brings several advantages: (i) the electronic conductive nanolayer coating minimizes the electronic transport length (L e), (ii) it allows fast Li ion diffusion, (iii) it provides a large contact area between electrode and electrolyte, and (iv) it offers a significant lithium ion storage capacity through nanolayer coating.

3.1 Minimization of electronic transport length (L e) with electronic conductive nanolayer coating

To enhance electron transport, the electronic transport length (L e) should ideally be less than or equal to the particle size of the active material. This enables electrons to move back and forth along the material’s surface, and nanolayer coatings can significantly improve electronic transport. Commercialized batteries currently use micrometer-sized particles for electrodes, which offer a low surface area of less than 10 m2 g−1 [61]. However, these larger particles have less contact area for the electrode surface and electrolyte so it exhibit long electronic transport length which is not advantageous. Zhou et al. [62] studied the electrochemical performance of Li2SnO3-coated Li1.2Mn0.54Ni0.13Co0.13O2. Li2SnO3 nanolayer coating decreases R ct, enhancing Li ion diffusion and electronic conductivity of the material. The coating minimizes electronic transport length, allowing electrons to travel shorter distances with fewer obstacles. This creates a more efficient pathway for electron flow, improving overall electronic conductivity. Enhanced electronic conductivity indicates that electrons can move more freely within the material, which is essential for the efficient flow of electrical current in batteries. Consequently, Coulombic efficiency, rate capability, and capacity retention (CR) are improved after Li2SnO3 nanolayer coating.

Nanolayer coatings, with thicknesses ranging from several nanometers to 50 nm, are well-suited for battery application. Figure 3 summarizes the distinction between conventional [63], core/shell [64], and ultrathin nanolayer [65] coatings. Thin nanolayer coatings, thanks to their high surface area, provide more contact area between active material particles and the electrolyte, effectively minimizing the L e value of the electrode material [66].

Figure 3 
                  Comparison between conventional coatings [63] (Copyright 2015, Elsevier), core/shell coatings [64] (Copyright 2005, American Chemical Society), and ultrathin nanolayer coatings [65] (Copyright 2017, Elsevier).
Figure 3

Comparison between conventional coatings [63] (Copyright 2015, Elsevier), core/shell coatings [64] (Copyright 2005, American Chemical Society), and ultrathin nanolayer coatings [65] (Copyright 2017, Elsevier).

3.2 Fast Li ion diffusion

Coatings, particularly those utilizing nanostructured materials, play a pivotal role in enhancing the performance of energy storage systems. The inherent properties of nanostructures, such as their increased surface area and shortened ion diffusion pathways, contribute to more efficient lithium ion transport. This results in quicker charge and discharge rates, ultimately improving the overall conductivity of the system. Additionally, nanostructured coatings facilitate improved interaction between the electrode material and electrolyte, promoting rapid lithium ion adsorption and desorption. These coatings also often act as a preventive measure against dendrite formation, enhancing safety and longevity. Altogether, coating methods, especially those incorporating nanostructures, represent a promising strategy for achieving and optimizing fast lithium ion conductivity in advanced energy storage technologies.

Yang et al. [67] conducted in situ characterization of the grain boundary’s impact on Li-ion diffusion in Li-rich cathodes. Conductive-atomic force microscopy revealed that atoms at grain boundaries are more conductive and have lower activation energy than atoms in the grain interior, allowing for faster Li ion diffusion along the grain boundaries. However, grain boundaries are in fact responsible for phase transformations in the material. This is due to the ease with which metal ions diffuse along grain boundaries, forming nuclei that grow into the trigonal phase at the grain boundary. When nanoscale particles are mixed into the cathode material, they form a zigzag structure along the grain boundaries, blocking the diffusion of metal ions and hence preventing the nucleation and growth of the trigonal phase at these grain boundaries.

In addition to the role of grain boundaries, the concept of “Nanoionics” is vital in nanoelectrodes. Nanoionics involves the study and application of phenomena, properties, and mechanisms associated to rapid ion transport within NMs in all-solid-state batteries. In 2013, Zhu et al. discovered that Li x CoO2 nanograins have low energy barriers for lithium ion mobility, allowing for rapid lithium ion diffusion. When composed of nanograins with large grain boundary areas, Li x CoO2 electrodes operating at optimum voltage demonstrate excellent rate capability and high-power performance in batteries [68]. The comparison between microsized cathode materials and nanolayer-coated cathode materials is shown in Figure 4. Nonetheless, understanding Li-ion transportation in NMs remains incomplete due to a lack of appropriate and effective characterization techniques capable of revealing mechanisms and processes at the molecular level. It is difficult to demonstrate nanoscale mapping of intercalation, charge and ion transport, and dislocation at single grain boundaries.

Figure 4 
                  Comparison between microsized pristine cathode material and nanomaterial-modified microsized cathode material.
Figure 4

Comparison between microsized pristine cathode material and nanomaterial-modified microsized cathode material.

3.3 Large contact area between active material and electrolyte from a nanolayer coating

Because of their fine particle size and large surface area, NMs are ideal for promoting Li ion transport in LIBs, and the charge/discharge process is heavily impacted by the Li surface storage capacity. The NM coating has a large surface area for storing Li ions, which reduces the specific current density of the active material and effectively improves the electrode’s stability at high charge/discharge current densities [51]. The increased surface area allows for a greater interface between the active material and electrolyte. This facilitates more effective and rapid interaction between the electrode and electrolyte ions, promoting improved ion diffusion and charge transfer kinetics. Additionally, a larger surface area can enhance the dispersion of particles within the electrode material, contributing to the maintenance of structural integrity during cycling and reducing the risk of mechanical stress and fracture. Improved structural stability contributes to long-term durability and performance of the electrode.

3.4 Significant benefit of nanolayer coating on lithium ions storing capacity

A nanolayer coating on the cathode material significantly impacts lithium ion storage capacity. The increased surface area facilitates efficient lithium ion diffusion and accelerates charge transfer kinetics. Acting as a protective barrier, the coating prevents undesired side reactions, preserving the cathode’s chemical integrity and ensuring sustained lithium storage capacity. Additionally, by mitigating particle agglomeration and providing mechanical support, the nanolayer enhances structural stability, preventing stress and fracture. This improved stability optimizes overall electrochemical performance, resulting in a higher lithium storage capacity. In summary, nanolayer coatings play a crucial role in enhancing the specific capacity of cathode in advanced energy storage systems.

NM coatings exhibit higher lithium storage capacity than pristine electrode, because previously inactive sites become active and react with lithium ions at the nanoscale. As the particle size of the NMs decreases, the discharge capacity increases since more lithium ions may be stored on the surface, substantially shortening the lithium ion transport length [51]. A conformal nanocoating of La2O3 can effectively boost Li ion diffusion, resulting in a thin SEI layer that facilitates the Li ion storage capacity of the material [69].

4 Challenges and potential solutions related to NM coatings

The following are some issues and potential solutions linked to NM coatings.

4.1 Agglomeration

The uncontrolled growth of nanoparticles is a disadvantage of NMs in a variety of applications. Nanoparticle agglomeration can result in the formation of nanoparticle clusters, which results in a non-uniform NM coating layer and has an impact on the morphological stability of NMs. It is preferable to use a capping agent during the NM synthesis to control nanoparticle growth. To reduce agglomeration, various capping agents, such as surfactants, polymers, and ligands have been utilized in the NM synthesis [70].

4.2 Undesired surface reactions

NMs have the characteristic of high surface area and low density which makes them prone to static charges and rapid dispersion in the air. An unfavourable reaction between active material particles and the electrolyte can lead to the formation of a thick SEI layer, which hinders the transport of lithium ions and electrons. As a result, careful handling of bulk NMs is required, and a glove box can be used for this purpose.

4.3 High cost of production

The production cost can be doubled when using NM-modified cathodes because it involves two steps: (i) preparing the pristine cathode and (ii) modifying NMs onto the pristine cathode. Implementing a one-step synchronous coating process is an effective way to reduce production costs.

4.4 Complex synthesis routes

Highly scalable preparation methods such as co-precipitation and solid-state synthesis are suitable for mass production of the micrometer-sized pristine cathodes because they are simple and effective. However, methods applicable for NM coatings, such as hydrothermal synthesis, sol–gel synthesis, and atomic layer deposition (ALD), are not scalable. Therefore, the scalability of NM-modified cathode synthesis should be carefully analysed.

5 Preparation methods for NMs coated LLR

In terms of the applicability of Li-rich cathodes, surface coating demonstrates to be an effective approach for enhancing the electrochemical properties of LLR oxides. Nanoscale coating can be accomplished using two processes.

5.1 Synchronous coating process

In the synchronous route, the coating material (shell) is directly mixed during the synthesis process of the core cathode material. Synchronous coatings are preferred because, in post-synthesis coatings, the core cathode material and the coating material shell are mixed in the presence of water, which increases the mixture’s alkalinity. This can lead to the formation of Li2CO3 and LiOH impurities due to the reaction of dissolved Li species with water, subsequently reducing the cathode material’s performance [71]. During the synchronous coatings, each particle of the cathode material can be uniformly covered by the coating material, resulting in consistent coating thicknesses and particle sizes. This approach also reduces manufacturing costs and time.

Zhang et al. [72] proposed a synchronous Li2ZrO3 coating strategy on LLR (indicated as LMNO in the original work). Figure 5(a) illustrates two strategies: the synchronous modification route (material named syn-Li2ZrO3@LMNO) and the post-coating method (material named post-Li2ZrO3@LMNO). In synchronous coating, hydrolysis of Zr(OC4H9)4 occurs on the Ni0.25Mn0.75O2 surface. Syn-Li2ZrO3@LMNO comprises bulk Zr4+ doping integrated with Li2ZrO3 coating, whereas bulk Zr4+ doping is absent in post-Li2ZrO3@LMNO. Li2ZrO3 coating serves as a Li-ion conductor, while Zr4+ doping enhances the stability of the layered structure and reduces the voltage fade. The Syn-Li2ZrO3@LMNO showed a capacity of 239.8 mAh/g, surpassing the bare LMNO, which exhibited a capacity of 207.8 mAh/g at 0.1 C. However, the electrochemical performance of bare LMNO and post-Li2ZrO3@LMNO material shows a striking similarity. The modified LLR cathode exhibits superior rate capability and cycle stability compared to the pristine cathode.

Figure 5 
                  (a) Schematic illustration of the preparation process for syn-Li2ZrO3@LMNO and post-Li2ZrO3@LMNO [72] (Copyright 2016, Royal Society of Chemistry), (b) chemical deposition method for preparation of F-doped TiO2 coating on LLR [73] (Copyright 2019, Elsevier), (c) sol–gel preparation of LiAl5O8 coating on LLR [76] (Copyright 2019, Elsevier), (d) hydrolysis-hydrothermal synthesis procedure for the preparation of the LiAlO2-coated LiNi0.8Co0.1Mn0.1O2 composite [79] (Copyright 2018, Springer), and (e) deposition of Al2O3 by atomic layer deposition technique [91].
Figure 5

(a) Schematic illustration of the preparation process for syn-Li2ZrO3@LMNO and post-Li2ZrO3@LMNO [72] (Copyright 2016, Royal Society of Chemistry), (b) chemical deposition method for preparation of F-doped TiO2 coating on LLR [73] (Copyright 2019, Elsevier), (c) sol–gel preparation of LiAl5O8 coating on LLR [76] (Copyright 2019, Elsevier), (d) hydrolysis-hydrothermal synthesis procedure for the preparation of the LiAlO2-coated LiNi0.8Co0.1Mn0.1O2 composite [79] (Copyright 2018, Springer), and (e) deposition of Al2O3 by atomic layer deposition technique [91].

5.2 Post-synthesis process

Various post-synthesis coating processes have been developed, which can be categorized into four groups.

5.2.1 Wet-chemical synthesis

Most LLR modification methods rely on wet chemical techniques due to their ease, effectiveness, and limited use of chemicals for modification. The following are detailed methods within this category.

5.2.1.1 Chemical deposition method

Researchers widely employ the chemical deposition method. In this approach, chemical reactions occur between precursors and solvents under appropriate experimental conditions. The thickness of the nanolayer can be controlled by the amount of precursor used for modification. The method typically involves the following steps: (1) dissolution of the precursor in water or a suitable solvent, (2) preparation of a mixture of the as-prepared cathode material with the precursor solution, (3) stirring the suspension for a specific duration and temperature, (4) evaporation of the solvent from the mixture, and (5) calcination of the dried powder at a proper temperature to obtain the modified cathode material.

The chemical deposition method is favoured for its limited use of chemicals, simplicity, cost-effectiveness, and suitability for large-scale industrial production. It is capable of forming ultrathin and homogeneous coatings with a thickness of about 4–6 nm and good crystallinity (Figure 5(b)) [73]. Various NMs, including oxides, phosphates, and fluorides, can be coated onto LLR material using this technique. However, this method has two limitations: the need for extra drying time to evaporate water or other solvents, and the use of solvents can initiate the extraction of lithium ions, thereby altering the surface stoichiometry of the cathode material.

5.2.1.2 Co-precipitation method

The co-precipitation method is an economical approach commonly used for the industrial production of cathode materials. In this method, metal salt solutions and base solutions are simultaneously added to a reactor under vigorous stirring. The particle size of the coating can be directly influenced by factors such as precursors and base concentration, pH, gradual addition of base, reaction temperature, aging time, and more.

This method offers several advantages, including high crystallinity, small particle size, formation of ultrathin layers, high tap density, and a large pore diameter. Higher tap density can practically increase battery capacity, and uniform spherical particles contribute to achieving high tap density. The co-precipitation of metal salts using a continuous stirred tank reactor can produce Li-rich materials with uniform spherical sizes, effectively leading to higher tap density. For instance, Hu et al. [74] synthesized a hexagonal La0.8Sr0.2MnO3−y (LSM) coating on LLR using this method, resulting in an LSM layer with a thickness of about 5–8 nm. The presence of larger oxygen vacancies is observed as the amount of coating increased. After LSM coating, cycle stability and rate capability are significantly improved, and voltage fading is reduced. However, it is worth noting that while this method is suitable for NM coating, it may not be ideal for producing NMs because achieving particle uniformity during synthesis can be challenging.

5.2.1.3 Sol–gel method

The sol–gel method is a widely employed technique for preparing coatings on battery materials. It is known for its simplicity, cost-effectiveness, and environmentally friendly nature. Typically, acetate and nitrate precursors are used for sol–gel coatings. The sol–gel method offers better adhesion to the pristine material. It generally involves the following steps: (1) formation of a mixture of precursors and a chelating agent, (2) evaporation of the solvent through heating treatment, and (3) calcination of the gel at a specific temperature [7577].

Sol–gel coatings provide advantages such as improved crystallinity, homogeneity, control over particle size, and good porosity. The porosity of the coatings can be adjusted by optimizing the precursor ratio [78]. Figure 5(c) shows high-resolution transmission electron microscopy (HRTEM) image of LiAl5O8 coating on Li1.2Mn0.54Ni0.13Co0.13O2 with a coating layer thickness of 3–5 nm [76]. One cost-related drawback of sol–gel coatings is the extended process time required for complete gel drying.

5.2.1.4 Hydrothermal or solvothermal syntheses

Hydrothermal or solvothermal syntheses are crucial methods for preparing inorganic coatings. In these methods, single-crystalline substances are created in water or organic solvent through low-temperature heating and high vapour pressure within a stainless steel vessel containing a Teflon container. Subsequently, the material to be synthesized undergoes washing, drying, and calcination at high temperatures. For example, Xiao et al. [79] prepared a LiAlO2 coating with a thickness of 8–12 nm on LiNi0.8Co0.1Mn0.1O2 using hydrothermal synthesis (Figure 5(d)). One of the notable advantages of hydrothermal coatings is their ability to produce high-purity powders, as they use high-purity precursors for the synthesis. This high purity contributes to excellent physical properties and, consequently, high electrochemical performance in batteries.

Zheng and colleagues recently compared three methods – hydrothermal, co-precipitation, and sol–gel – for making Li-rich cathode materials. Material synthesized via the hydrothermal method showed a remarkable improvement in the uniform distribution of Ni metal on the material’s surface. This uniform distribution significantly reduces voltage fading during cycling, leading to the conclusion that the hydrothermal method is ideal for achieving uniform structure, offering excellent rate capability and cycling stability [80].

5.3 Dry physical synthesis

Dry physical synthesis is a cost-effective and scalable coating process that requires minimal chemicals. It typically involves the use of dry milling equipment such as planetary ball mills and Nobilta mini bowls [81,82]. In dry chemical synthesis, a coating precursor is mixed with the pristine cathode using ball milling or similar equipment. Subsequently, the powder is sintered at an optimal high temperature, a process referred to as a “solid state reaction.” For instance, Nisar et al. [81] employed this method to coat ZrO2 on Li1.2Ni0.16Mn0.56Co0.08O2 through ball milling and solid-state reaction, resulting in the formation of a thin, uniform coating layer with a thickness less than 10 nm.

Another dry chemical synthesis approach is chemical etching. In this method, the precursor of the desired coating material is mixed with the LLR cathode material to etch the cathode’s surface. Cui et al. employed a similar strategy to modify LLR [83]. They mixed LLR material with ceric ammonium nitrate (CAN) using a microtube homogenizer, resulting in an increase in Mn and Co content and a decrease in Ni content.

5.4 Gas phase chemical synthesis

Gas phase chemical synthesis includes various coating methods such as low-pressure vaporization and ALD [65,84,85].

5.4.1 Low-pressure vaporization method

This is a simple method that operates at low temperatures and low pressure in the gas phase. However, unwanted chemicals can evolve during the synthesis. For example, Xiao et al. [84] used this method to prepare a novel metal-organic framework (MOF) shell with NiCo quantum dots embedded in a thin carbon layer, resulting in a very thin carbon shell (2 nm).

5.4.2 ALD method

ALD is a technique used to prepare ultrathin coatings with a thickness of 0.1 nm. It has shown significant improvements in the electrochemical properties of cathodes with individual layer/spinel structures [86,87]. ALD deposits thin films by sequentially introducing two or more precursors separately onto a substrate under specific reaction conditions. It is extensively used in the battery industry to coat various metal oxides [8890]. The ALD process involves the following steps: (1) placing the substrate in the ALD chamber, (2) purging inert gases to remove undesired gases and moisture from the chamber, (3) introducing precursor gas into the ALD chamber, followed by purging inert gases, and (4) introducing a second reactant gas into the ALD chamber, followed by purging inert gases to remove unreacted reactants and by-products. This process is repeated for each layer. The thickness of the ALD-deposited coating can be precisely controlled by adjusting the number of ALD cycles. The schematic of the ALD process is displayed in Figure 5(e) [91].

ALD coatings are used for advanced cathode materials synthesis because they create ultrathin, crystalline, uniform, homogeneous, and high-purity coatings. However, ALD has some drawbacks, including long, repeatable cycles, extended process time, the need for careful optimization of ALD cycles, complex procedures, and the high cost of precursors. However, ALD’s ability to produce ideal coating layers with uniformity, homogeneity, and controllable thickness makes it highly valuable in the field of nanocoatings [92].

5.5 Advanced physical synthesis

Advanced physical synthesis is an emerging method for preparing the ultrathin and uniform coating layer on the cathode’s surface, which is explained in detail as follows.

5.5.1 RF magnetron sputtering method

The radio-frequency magnetron sputtering (RMS) method is emerging as a promising technique that has the ability to improve cycle stability, rate capability, and specific capacity. In this method, metallic targets are used for direct deposition on the electrode’s surface through reactive sputtering in the presence of reactive gas mixtures. The deposition can be repeated multiple times for the desired coating thickness. Qiu et al. [93] pioneered the use of surface modification via RMS in 2014 when they successfully applied ZnO coatings to a 0.3Li2MnO3–0.7LiNi5/21Co5/21Mn11/21O2 cathode material, creating a 8 nm-thick ZnO coating in just 4 min of deposition. For a summary of different coating techniques and their advantages and drawbacks, refer Table 1.

Table 1

Advantages and drawbacks of different coating techniques

Coating technique Advantages Drawbacks
Synchronous coating process Uniform particle size, less impurities, and reduced production cost and time. Uniformity of thickness cannot be guaranteed.
Chemical deposition method Limited use of chemicals, simple, cost-effective, and homogeneous coatings, no need of specialized equipment. Uniformity cannot be guaranteed, cost may be increased due to use of water or solvents, use of solvent can cause extraction of lithium ions from pristine material.
Co-precipitation method Cost-effective, scalability, high crystallinity, small particle size, ultrathin layer formation, high tap density, and high pore diameter. Many reaction parameters needs to be optimized to control the particle size of coating material.
Sol–gel method Good homogeneity, good porosity, and control over particle size. Cost may be increased due to use of water or solvents, use of solvent can cause extraction of lithium ions from pristine material, long time requirement for drying the gel.
Hydrothermal synthesis High purity powder, uniform particle size, stable structure, and low temperature synthesis. Small-scale production, high purity precursors increases cost of manufacturing.
Dry chemical synthesis Ease of production, scalable, cheap synthesis, and limited use of chemicals. High temperature calcination increases the cost of production, discontinued uniformity in conventional milling.
Atomic layer deposition method Ultrathin, crystalline, uniform, homogeneous, and high-quality and purity coatings. Long repeatable cycles, long process time, careful optimization of ALD cycles, complex process, and high cost of precursors.
Radio frequency (RF) magnetron sputtering method Ultrathin, uniform, good adhesive films, and low temperature synthesis. Cost is high due to radio-frequency waves and reactive gas mixtures.

6 Materials for LLR nanoscale surface modification

Utilizing a thin-layer coating strategy is advantageous because it preserves the total amount of electrochemically active components in the parent oxide, thanks to the thin, uniform outer layer on the active material [94]. Nanolayer coating materials facilitate electrolyte penetration through the thin coating layer to reach the active material. Additionally, nanocoatings offer high electronic conductivity, contributing to good cyclability by providing an ideal Li+ diffusion pathway.

Nanocoating materials vary significantly in their physicochemical properties, which can have different impacts on the electrochemical performance of LIBs. Researchers have explored various nanolayer coatings for lithium-rich cathode materials, including oxides, phosphates, fluorides, carbon compounds, polymers, and more. These nanocoating materials hold promise for enhancing the performance of lithium-rich cathodes in LIBs.

6.1 Oxides

Metal oxides act as effective barriers, inhibiting the formation of SEI by physically separating the electrode and electrolyte. Commonly used metal oxides for coating LLR surfaces include ZnO [65], ZrO2 [81], TiO2 [95], MoO3 [96], and more. The electrochemical performance varies with the choice of metal oxide due to differences in their structures and properties. Coating with metal oxides significantly extends the cycle life of LLR cathodes. These coating materials are cost-effective and readily available. Various methods, such as chemical deposition, sol–gel, ALD, ball milling, and precipitation, have been employed for the modification of oxide coatings on LLR surfaces [65,73,97,98].

The formation of parasitic impurities at the active material–electrolyte interface can negatively impact the electrode performance. This issue is primarily caused by the loss of oxygen from the LLR structure due to irreversible anionic redox activity [99]. To prevent parasitic impurities formation, it is essential to reduce this irreversible anionic redox activity. Some theories suggest that a small amount of ZnO can suppress hydrogen fluoride (HF) formation and improve the electrochemical coupling coefficient, chemical stability, and cycle performance of Mn-based cathode material [100,101]. Yu et al. conducted a post-annealing treatment on ZnO-coated material in an Ar atmosphere [63]. Initially, they prepared Li1.2Mn0.54Ni0.13Co0.13O2 using the sol–gel method and then modified it with ZnO using a wet chemical method. The results showed that the ZnO-coated sample annealed in the Ar atmosphere exhibited more oxygen vacancies compared to the unannealed ZnO-coated sample and the ZnO-coated sample annealed in an O2 atmosphere. These oxygen vacancies played a crucial role in improving electrochemical activities by enhancing the electronic conductivity, reducing resistance to Li-ion intercalation, and suppressing the formation of highly reactive oxygen radicals during charge and discharge processes [102].

Kong et al. [65] recently explored the advantages of achieving a uniform, homogeneous coating of ZnO on pristine LLR material. They opted for the ALD process for this modification. When comparing the findings of Yu et al. [63] and Kong et al. [65], it becomes evident that ALD has the potential to form uniform, ultrathin, and homogeneous nanocoatings when compared to the wet chemical method. In the TEM images, it is clear that ALD can create uniform, ultrathin, and homogeneous nanocoatings (Figure 6(a)–(c) vs (d)–(f)). Figure 6(e), shows a minor change in the voltage plateau at 2.5 V during discharge for ZnO-coated LMNCO material, is attributed to the formation of an ultrathin spinel layer [103]. This suggests that ALD holds significant promise for preparing an ultrathin NM layer on cathode materials.

Figure 6 
                  (a) TEM image of Li1.2Ni0.13Co0.13Mn0.54O2@ZnO particles. (b) The initial charge and discharge curves of Li1.2Ni0.13Co0.13Mn0.54O2 and Li1.2Ni0.13Co0.13Mn0.54O2@ZnO at 0.1 C. (c) Rate capability of bare and ZnO-coated Li1.2Ni0.13Co0.13Mn0.54O2 composite [63] (Copyright 2015, Elsevier). (d) LMNCO coated with 20 ZnO layers. (e) Initial charge–discharge curves of the pristine LMNCO and ZnO-coated LMNCO electrodes at 0.12 C. (f) Rate capability of the pristine and ZnO-coated LMNCO electrodes [65] (Copyright 2017, Elsevier). HRTEM images of (g) and (h) LNCM electrode and (i) and (j) NFO3 electrodes, respectively. All electrodes were operated in a charge/discharge process after 200 cycles at 1 C rate. (k) Schematic of the heterostructural O-sharing bonding of LNCM (104 plane) and NFO (400 plane) [104] (Copyright 2021, American Chemical Society). Cycling performance of P-LLMO, S-LLMO-0.5 wt%, and S-LLMO-1.0 wt% at a current density of 0.5 C between 2.5 and 4.6 V at (l) 25°C and (m) 60°C [105] (Copyright 2019, Springer).
Figure 6

(a) TEM image of Li1.2Ni0.13Co0.13Mn0.54O2@ZnO particles. (b) The initial charge and discharge curves of Li1.2Ni0.13Co0.13Mn0.54O2 and Li1.2Ni0.13Co0.13Mn0.54O2@ZnO at 0.1 C. (c) Rate capability of bare and ZnO-coated Li1.2Ni0.13Co0.13Mn0.54O2 composite [63] (Copyright 2015, Elsevier). (d) LMNCO coated with 20 ZnO layers. (e) Initial charge–discharge curves of the pristine LMNCO and ZnO-coated LMNCO electrodes at 0.12 C. (f) Rate capability of the pristine and ZnO-coated LMNCO electrodes [65] (Copyright 2017, Elsevier). HRTEM images of (g) and (h) LNCM electrode and (i) and (j) NFO3 electrodes, respectively. All electrodes were operated in a charge/discharge process after 200 cycles at 1 C rate. (k) Schematic of the heterostructural O-sharing bonding of LNCM (104 plane) and NFO (400 plane) [104] (Copyright 2021, American Chemical Society). Cycling performance of P-LLMO, S-LLMO-0.5 wt%, and S-LLMO-1.0 wt% at a current density of 0.5 C between 2.5 and 4.6 V at (l) 25°C and (m) 60°C [105] (Copyright 2019, Springer).

The release of active oxygen from pristine LLR can disrupt redox reactions during charge and discharge processes, leading to decreased capacity and increased ICL. Additionally, oxygen release and cation migration in LLR can result in the transformation of the layered structure to spinel in the pristine electrode. To address these challenges, Hu et al. developed a perovskite-type hexagonal LSM material for modifying Li1.2Ni0.13Co0.13Mn0.54O2 (LM) [74]. They observed the formation of strong Mn‒O‒M bonding at the LSM/LM interface, which reduced oxygen release and inhibited the dissolution of Mn. This innovative approach significantly improved CR, with a 48% increase for 2 wt% LSM@LM and 82% ICE for 3 wt% LSM coating. The LSM coating helped to mitigate defects and nanovoid formation during cycling and reduced oxygen release during charging.

Subsequently, the same research group developed an inverse spinel NiFe2O4 (NFO) coating on Li1.2Ni0.13Co0.13Mn0.54O2, offering a cost savings of 36.9% compared to LSM coating [104]. Unlike LSM, NFO contains NO6 octahedra. The M‒O‒N (M = TM ions from LNCM, N = TM ions from NiFe2O4) bonding is established after coating. As seen in Figure 6(g) and (h), the layered to spinel transformation occurred in the LNCM cathode along with structural defects and nanovoids, resulting in the degradation of electrochemical performance. NFO-coated LNCM increased the structural stability, and therefore the electrochemical performance is enhanced (Figure 6(i) and (j)). The mechanism of O-sharing between M and N is illustrated in Figure 6(k). The M‒O‒N bonding mechanism prevented lattice oxygen near the surface from participating in anionic redox reactions and resisted structural collapse during Li ion extraction. As a result, NFO-coated LNCM exhibited enhanced structural stability, improved ICE, and reduced voltage decay.

SiO2 NM coating can show good cycle stability at both room temperature and high temperature. Meng et al. [105] modified Li1.2Mn0.56Ni0.16Co0.08O2 by single shell SiO2, demonstrating enhanced electrochemical performance. The cycle performance for P-LLMO, 0.5 wt% S-LLMO, and 1 wt% S-LLMO is assessed at 0.5 C in a potential range of 2.5–4.6 V at both 25 and 60°C (Figure 6(l) and (m)). The results showed that the SiO2 NM coating improves the thermal stability of the LLR cathode but decreases discharge capacity and rate capability, suggesting it does not reduce oxygen release. α-MoO3/Li2MoO4 modification achieves a superior ICE of 89.6% due to enhanced Li insertion channels and improved electrical conductivity of the interface. Rate capability is also enhanced, though cycle stability remains similar to other oxide coatings. La–Co–O surface modification can suppress the voltage decay [97]. The voltage intervals (ΔV) between La–Co–O coated LLR and pristine LLR increase with higher C-rates, indicating greater polarization for pristine LLR. But the specific capacity and cycle stability of La–Co–O coated LLR are not adequate when compared to surface coatings discussed earlier in this section. From the graphs, it is clear that ICE decreased after La–Co–O coating, implying inefficient Li-ion intercalation.

Metal oxides act as HF scavengers or HF barrier agent. It is investigated that HF barrier agents are more effective than HF scavengers.

Spinel materials offer structural stability and 3D channels for Li-ion diffusion, making them suitable for improving the electrochemical performance of LLR. Researchers have developed a technique where a spinel layer is uniformly coated onto host layered material, resulting in a “heterostructured material” [106109]. The concept of Mn-based integrated layered spinel composites is introduced by Thackeray’s group in 2005 [110], and since then, many researchers have explored this approach. Both post-synthesis modification and one-step modification (synchronous route) techniques have been employed to enhance rate performance [108,111113]. However, a high content of spinel material can reduce the overall capacity, making it essential to modify the host material with an ultrathin layer of the spinel phase to achieve good electrochemical properties. Spinel materials are known for their high ionic and electronic conductivity [114], high voltage window, cost-effectiveness, and lower toxicity. Two different research groups reported Al2O3 nanocoatings on LLR material [85,115]. Comparing these two studies, it is found that 1 wt% Al2O3 coated LLR via the ALD process exhibited ∼147 mAh/g at 1 C, with 84% CR after 200 cycles [85]. No spinel layer is formed in this material. In contrast, LLR nanotubes synthesized via the electrospinning method and coated with 4 wt% Al2O3 using the freeze-drying method exhibited 210 mAh/g at 1 C with 97.6% CR after 90 discharge cycles [115]. An ultrathin spinel layer (2 nm thickness) formed between the LLR nanotubes and the Al2O3 layer, promoting Li ion diffusion and reducing ICL during initial cycling. Therefore, the ultrathin spinel layer has been proven beneficial for electrochemical cycling.

While oxide coatings have shown promise, their specific capacity has room for improvement. This improvement can be achieved by reducing the charge transfer resistance (R ct) and balancing the ratio between cationic and anionic redox reactions. Porous electrode materials have the potential to improve R ct, and enhancing the rate capability of oxide coatings is crucial as it relies on the electronic and ionic conductivity of the material [99].

6.2 Phosphates

Phosphate coatings applied to cathode materials serve to enhance thermal stability by introducing PO4 polyanions [116]. These coatings not only safeguard the cathode surface from HF electrolyte species but also effectively reduce ICL, thereby improving electrochemical properties [117]. The methods used for LLR modification include chemical deposition and sol–gel [118121].

To improve the cycle performance of Li3PO4 coatings, a thin spinel layer can be incorporated between the coating and the LLR surface, as demonstrated by Yang et al. [119]. They treated Li1.2Ni0.2Mn0.6O2 with H3PO4, resulting in the in situ formation of a Li3PO4 layer. Four samples with varying levels of H3PO4 pre-treatment were prepared, namely HPO-0, HPO-2, HPO-4, and HPO-6 (sample pre-treated with 0, 0.02, 0.04, and 0.06 mol L−1 H3PO4 solution). The spinel phase is formed in HPO-4 and HPO-6 samples. Voltage decay, a significant issue in LLR, is primarily caused by oxygen release and irreversible cation migration. Li3PO4 coatings have the potential to mitigate voltage fade in LLR. The voltage decay of four samples HPO-0, HPO-2, HPO-4, and HPO-6 is shown in Figure 7(a)–(d). The graph shows that the voltage decay is effectively reduced for HPO-4. The voltage decay is hindered for HPO-6 because of the production of a high amount of spinel coating. Cycle performance at 1 C for 100 cycles is shown in Figure 7(e). The CR after 100 cycles for HPO-4 reached 92.2%, whereas the pristine sample only retained about 70.9% of its capacity. The transition from layered to spinel structure in Li3PO4-coated LLR is reduced due to the presence of a thin spinel phase in the Li3PO4 coating. However, H3PO4 is acidic and can potentially damage the crystal structure. In contrast, the aqueous solution of the alkaline (NH4)2HPO3 helps maintain the crystallinity of the modified electrode.

Figure 7 
                  Discharge curves of (a) HPO-0, (b) HPO-2, (c) HPO-4, and (d) HPO-6 at 1 C between 2 and 4.8 V, over the course of 100 cycles. (e) Cycling performance for HPO-treated electrode at 1 C in the voltage range 2–4.8 V [119] (Copyright 2019, Springer). (f) Cycling performance at 1 C rate of the pristine and LLO-LP sample, SEM images of electrode sheet, TEM images of active material particle for the pristine (g), (i), and (k) and for LLO-LP sample (h), (j), and (l), (m) SAED patterns from (k), and (n) SAED patterns from (l). Both samples were analysed after 200 cycles at 1 C rate [122] (Copyright 2020, Royal Society of Chemistry).
Figure 7

Discharge curves of (a) HPO-0, (b) HPO-2, (c) HPO-4, and (d) HPO-6 at 1 C between 2 and 4.8 V, over the course of 100 cycles. (e) Cycling performance for HPO-treated electrode at 1 C in the voltage range 2–4.8 V [119] (Copyright 2019, Springer). (f) Cycling performance at 1 C rate of the pristine and LLO-LP sample, SEM images of electrode sheet, TEM images of active material particle for the pristine (g), (i), and (k) and for LLO-LP sample (h), (j), and (l), (m) SAED patterns from (k), and (n) SAED patterns from (l). Both samples were analysed after 200 cycles at 1 C rate [122] (Copyright 2020, Royal Society of Chemistry).

Liu et al. [122] employed a synchronous route with a (NH4)2HPO3 precursor to prepare Li3PO4-modified Li1.18Mn0.52Ni0.15Co0.15O2 (LLO). In this process, the primary particles of LLO were covered by a Li3PO4 layer, referred to as LLO-LP, with a thickness of 2 nm. This Li3PO4 coating significantly improved the material’s cycle performance (Figure 7(f)). After 200 cycles, the CR for 2 wt% Li3PO4-LLO reached 81.3%, compared to just 47.2% for the uncoated LLO. A significant increase in discharge capacity is observed in the (NH4)2HPO3-treated sample compared to the H3PO4-treated sample, relative to their respective discharge capacities of pristine materials. The first cycle discharge capacity also improved from 260.9 to 280.1 mAh/g for (NH4)2HPO3-treated sample (LLO-LP), outperforming the discharge capacity of 262.6 mAh/g for the H3PO4-treated sample. The initial Coulombic efficiencies for H3PO4-treated sample and (NH4)2HPO3-treated sample are 84.4 and 86.3%, respectively. This is because alkaline conditions may influence the electrode/electrolyte interface, promoting enhanced ion mobility and facilitating more efficient electrochemical reactions during discharge. However, the rate capability of H3PO4-treated sample is better than that of (NH4)2HPO3-treated sample. This suggests that the acidic medium treatment may provide superior performance under certain conditions, possibly due to faster charge and discharge kinetics. In summary, the choice between acidic and basic treatments significantly influences the electrochemical performance of the samples. The alkaline treatment appears to enhance discharge capacity and initial Coulombic efficiencies, while the acidic treatment demonstrates superior rate capability. The specific mechanisms behind these effects would require more detailed analysis of the electrochemical processes occurring at the electrode–electrolyte interface under each treatment condition.

To enhance the CR of an electrode, it is essential to minimize charge transfer impedance R ct (Ω), electrolyte decomposition, Mn dissolution, and internal resistance R s (Ω) caused by the electrolyte and other resistive components. SEM and TEM images of pristine and LLO-LP coated electrodes cycled at 1 C for 200 cycles were examined. The SEM and TEM images (Figure 7(g), (i), and (k) for the pristine sample and Figure 7(h), (j), and (l) for the (NH4)2HPO3-treated sample (LLO-LP)) revealed that the pristine electrode, cycled for 200 cycles, exhibited side reactions, and corrosion pits on the electrode surface, and a thick SEI layer. In contrast, the LLO-LP sample featured a clean surface without side reactions or corrosion pits, with visible fringes. Selected area electron diffraction (SAED) patterns demonstrated that the pristine electrode underwent the transition from a layered to a spinel and then to a rock-salt structure, as shown in Figure 7(m) and (n). While Li3PO4 modification did not prevent the formation of a spinel structure, it effectively stabilized the spinel structure and preserved high capacity.

In Table 2, several critical electrochemical parameters are provided, including CR, resistance in series R s (Ω), charge transfer resistance R ct (Ω), and Li+ diffusion coefficient (D Li+). D Li+ can be calculated using the following equation:

(1) D Li + = R 2 T 2 2 A 2 n 4 F 4 C 2 σ 2 ,

where R is the molar gas constant, T is the absolute temperature, A is the active electrode area, n is the number of electrons per molecule during the redox process, F is Faraday’s constant, C is the Li+ concentration in moles, and σ is the Warburg impedance coefficient. The Warburg impedance coefficient σ can be calculated using the following equation:

(2) Z = k + σ w 1 / 2 .

Table 2

CR, R s (Ω), R ct (Ω), and Li+ diffusion coefficient (D Li+) of various phosphate coatings

Coating CR, cycles at 1 C rate R s (Ω) R ct (Ω) D Li+(cm2 s−1) Year & reference
Li3PO4 coating (HPO-6) (0.06 mol/L) 92.2% after 100 cycles 7.2 296.8 7.17 × 10−16 2019 [119]
Li3PO4 coating (LLO-LP) (0.265 mol/L) 72% after 200 cycles 15.72 801 1.1 × 10−12 2020 [122]
LVAP coating (5 wt%) 96% after 100 cycles 34.2 143 2019 [118]
Li1.3Ti1.7Al0.3(PO4)3 coating (LTA0.3) 80% after 170 cycles 103.7 1.641 × 10−11 2021 [120]

Here, the values are determined from the slope drawn on Zversus the square root of frequency ( w 1 / 2 ) ; whereas, k = R s + R ct .

LiTi2(PO4)3 (LTP)-modified LLR does not effectively reduce the transition from a layered to a spinel structure, resulting in similar capacity and voltage decay compared to unmodified LLR [123]. Researchers have introduced a novel material, Li1+y Ti2−y Al y (PO4)3 (LTA-0.3), to enhance Li-ion conductivity in LLR [120]. LTA-0.3 exhibits a discharge capacity of 200 mAh/g after 170 cycles, maintaining 140 mAh/g after 500 cycles at 1 C. The voltage fading decreases with increasing cycle number, and the Li+ diffusion coefficient is calculated as 1.641 × 10−11 cm2 s−1. Another research group worked on the Li1.4Al0.4Ti1.6(PO4)3/polyanilline (LATP@PANI) modification of LLR [121]. While this material showed high ICE (ICE >80% at 0.1 C), its specific capacity, cycle stability, and rate capability were not ideal compared to the work by Yang et al. Vanadium coatings offer excellent chemical and thermal stability, and electrochemical activity at a very low cost [124]. Shi et al. [118] modified LLR with 5 wt% Li3V1.5Al0.5(PO4)3 (LVAP) using a chemical deposition method. LVAP-modified LLMO demonstrated a discharge capacity of 228 mAh/g at 1 C with 96% CR after 100 cycles, outperforming Li3PO4 modification.

Overall, the study of phosphate coatings reveals several insights: (1) controlling the spinel phase layer is crucial, (2) the thickness of NMs should be appropriate, (3) vanadium-containing phosphates can enhance structural and chemical stability while reducing voltage fade, and (4) a small amount of Al3+ doping in LiTi2(PO4)3 structures can strengthen the Ti–O bond in the lattice.

6.3 Fluorides

The reversible extraction of Li+ from lithium oxide (Li2O) offers high capacity and increased ICE. However, irreversibility in Li+ extraction and the formation of Li vacancies are key issues leading to capacity loss and low ICE. Fluorine (F) is highly electronegative and can form strong M‒F bonds (e.g., Li‒F = 684.8 eV), which reduces the irreversibility of Li+ extraction and Li vacancy formation. Various fluoride coatings, including ZrF4, YF3, SmF3, and MnF2 composites, have been demonstrated to enhance LIB performance. Chemical deposition methods are commonly used for depositing fluorides on LLR surfaces [125127].

Niu et al. modified LLR with YF3 and conducted secondary calcination to investigate the effect of F diffusion into the bulk region of LLR [126]. YF3 modification activated the electrochemically inactive component Li2MnO3, while secondary calcination led to the formation of the spinel phase with 3D Li+ channels and F diffusion into bulk regions. Figure 8(a) shows the voltage decay for each sample after 100 cycles. The voltage decay for 0.05-YF3 at 600°C is 331.9 mV, which is comparatively less than pristine material. This indicates that secondary calcination stabilized the material’s structure and reduced voltage decay during cycling. Samarium fluoride (SmF3)-coated LLR showed improved electrochemical performance compared to pristine LLR but it did not outperform coating materials [127]. Zhu et al. [128] studied the performance of an electrochemically active MnF2 coating on LLR. The highest discharge capacity of about ∼300 mAh/g is achieved for the 1.5 wt% MnF2 coating, with good rate capability (150 mAh/g at 1 C rate). However, the cycle performance of this material is unsatisfactory.

Figure 8 
                  (a) Voltage decay of each material after 100 cycles [126], charge–discharge characteristics of pristine LRNCM and LRNCM @CF sample: the (b) first and (c) second cycle curves. The electrochemical property of pristine LRNCM and LRNCM @CF samples. (d) The cycling performance. (e) Discharge capacity above and below 3.5 V vs Li/Li+ during cycling at 1 C [129] (Copyright 2019, Elsevier). (f) Long-term stability test of LNMO, LNMO@AlF3, and LNMO@LiAlF4 electrodes at 5 C for 3,000 cycles [130] (Copyright 2018, American Chemical Society).
Figure 8

(a) Voltage decay of each material after 100 cycles [126], charge–discharge characteristics of pristine LRNCM and LRNCM @CF sample: the (b) first and (c) second cycle curves. The electrochemical property of pristine LRNCM and LRNCM @CF samples. (d) The cycling performance. (e) Discharge capacity above and below 3.5 V vs Li/Li+ during cycling at 1 C [129] (Copyright 2019, Elsevier). (f) Long-term stability test of LNMO, LNMO@AlF3, and LNMO@LiAlF4 electrodes at 5 C for 3,000 cycles [130] (Copyright 2018, American Chemical Society).

Coating Li1.14Ni0.133Co0.133Mn0.544O2 (LRNCM) with a 10 nm thick layer of graphite fluoride resulted in a significant increase in discharge capacity, reaching 325 mAh/g at 0.1 C, which is 22% higher than the pristine electrode within the 2.0‒4.8 V voltage range [129]. During the first discharge, graphite fluoride produced LiF and carbon, improving ICE and capacity by suppressing interfacial side reactions. Figure 8(b) and (c) shows the first and second charge–discharge cycles, respectively. The voltage plateau at 2.4 V during the first discharge cycle is attributed to the reaction between (CF) n and Li+ ions to form LiF. The ICE for pristine LRNCM is 77%, and after modification with 10% CF (LRNMC@10%CF), it improved to 99%. The cycle performance showed that for LRNCM, the discharge capacity decreased from 240.2 to 180 mAh/g after 100 cycles, while for LRNMC@10%CF, it decreased from 273.5 to 203 mAh/g (Figure 8(d)). Figure 8(e) displays the discharge capacities for 100 cycles, plotted separately for low potential (below 3.5 V) and high potential (above 3.5 V). The discharge capacity for all samples in high-potential regions is almost similar, while it is improved in low-potential regions. The rate capability test is conducted at different rates (0.1, 0.2, 0.5, 1, 2, 5, 10 C). LRNMC@10%CF exhibited high rate capability below 2 C, with some reduction in specific capacities at 5 and 10 C due to polarization. The study did not investigate voltage decay for graphite fluoride-modified electrodes, and the reported capacity loss after 100 cycles may be exaggerated. To further enhance the performance, efforts should focus on minimizing internal resistance, electrolyte decomposition, and Mn dissolution.

A Li-rich cathode modified with LiAlF4 showed remarkable electrochemical performance, maintaining a high capacity over many charge–discharge cycles [130]. The presence of a high percentage of unbounded oxygen species and a Li-ion conductive coating layer (LiAlF4) is advantageous for the rapid kinetics of LIBs. The unbound oxygen within the crystal lattice is also attributed to increased charge–discharge efficiency [131]. The discharge capacity of LNMO is 187 mAh/g after 100 cycles. The sample showed 6.4% capacity loss after 3,000 cycles, while LNMO exhibited 14.4% loss (Figure 8(f)). The conversion from layered to spinel structure after 100 cycles, typically observed in LNMO cathode due to TM ion relocation to vacant lithium ions, is diminished for LNMO@LiAlF4 [132].

While fluoride coating still faces challenges in electrochemical performance, it does moderately suppress voltage fading and slightly increase rate capability. The formation of an ultrathin spinel phase beneath the fluoride NM coating can enhance electrode’s discharge capacity. Significant improvements in specific capacity and ICE were observed for graphite fluoride and LiAlF4 coatings, demonstrating exceptional and outstanding performance.

6.4 Carbon compounds

In the electrochemical process of xLi2MnO3 (1−x)LiMO2, the Li2MnO3 component typically acts as an insulator, and the presence of the SEI layer, along with its low electronic conductivity, hinders electrochemical activity [133]. To address practical application requirements, efforts have been made to enhance electrical conductivity and Li-ion diffusion in these cathodes. Carbon, known for its high electrical conductivity and Li diffusion properties, is utilized for cathode modification. Moreover, it can induce HF attack on the LLR cathode’s surface during cycling, significantly improving CR [112]. Various methods are employed for carbon nanolayer modification on LLR, including low-pressure vaporization, solvothermal, and polymerization techniques [84,134,135].

A novel structure involving MOF modification on Li-rich cathode has been developed. Through low-pressure vapour super-assembly, NiCo nanodots are embedded inside a thin carbon shell on LLR [84]. At 0.2 C, LLO@C and NiCo exhibited a CR of 95% with good stability, whereas LLO delivered only 75% retention after 100 cycles. This improvement in rate capability, stability, and ICE is attributed to the suppression of spinel phase formation by LLO@C and NiCo during cycling. The presence of an amorphous carbon layer facilitates fast ion diffusion and acts as a barrier to undesired reactions at the electrode–electrolyte interface. This strategy introduces a new direction where carbon serves as a conducting network and NiCo dots contribute to a stable and robust structure. Recent work has focused on the development of a dopamine-derived carbon spinel layer. Ku et al. [135] prepared a dopamine coating on LLR, followed by carbothermal reduction, resulting in a carbon layer. This layered–spinel material exhibited enhanced electrochemical activity, with a CR of 90.9% after 100 cycles at 0.2 C. At 5 C, the discharge capacity reached 128 mAh/g.

Cai et al. [103] executed surface engineering on hierarchical LLR by carbonizing a dopamine layer. This process introduced oxygen vacancies to the modified LLR surface, leading to structural rearrangement and the formation of a thin spinel layer in situ on the surface. After 200 cycles, the CR reached 85.2% for L@S (spinel layer coating on LLR material) and 77.15% for LMNC at 5 C. The L@S sample exhibited a discharge capacity of 221 mAh/g at 10 C, while the pristine electrode had only 170 mAh/g. The presence of oxygen vacancies activated the electrochemically inactive Li2MnO3 phase and enhanced Li-ion diffusion rates. Additionally, the spinel layer encapsulated on LLR created a 3D Li+ diffusion channel. These findings suggest that both the spinel layer and oxygen vacancies introduced on the surface have the potential to improve the rate capability, ICE, and cycle performance of LLR. Lu et al. also recently developed a glucose-derived spinel layer on the LLR surface [134]. The modified sample, LR@S@C, significantly enhanced the electrochemical activity of pristine LLR (LR). In terms of rate capability, LR@S@C exhibited a discharge capacity of 186.1 mAh/g at 5 C, while LLR achieved only about 100 mAh/g. Both dopamine and glucose-derived spinel nanolayers contributed significantly to the improvement in LLR cathode performance.

In a study by Zhao et al. [136], a novel bi-functional strategy is proposed to achieve fast charging and high volumetric density in LLR cathodes. They synthesized Li-rich MNC semi-hollow microspheres through ultrasonic treatment of porous MnO2 microspheres and metal acetates. This material is then surface treated with lithium and cobalt sources, resulting in ST-MNC. To further enhance its properties, the Li-rich MNC is modified with 2D graphene oxide and 1D carbon nanotubes (CNT), creating GCNT@ST-MNC. Figure 9(a) shows the conventional and bi-functional approaches and their advantages. Both half-cell and full-cell electrochemical measurements were conducted. The Li metal reference electrode is used for half-cell testing, while a pre-lithiated nanographite electrode served as the anode in full-cell tests. Figure 9(b)–(e) displays electrochemical performance for MNC and GCNT@ST-MNC half cells. Figure 9(b) shows the cyclic voltammetry (CV) curve for GCNT@ST-MNC from the first to fourth cycle at 0.1 mV/s. Figure 9(c) shows the charge/discharge curve at 0.1 C. The ICE for MNC and GCNT@ST-MNC is 77.6 and 87.8%, respectively. The rate performance of both electrodes at different current rates are displayed in Figure 9(d). GCNT@ST-MNC demonstrated good CR of 65.5% even at 10 C. This indicates that the dual surface modification strategy provides a fast ion/electron pathway for Li transport. After 1,000 cycles, the CR for the GCNT@ST-MNC electrode is approximately 94.5%. The electrochemical performance for GCNT@ST-MNC/nanographite full-cell is shown in Figure 9(f)–(k). As seen from Figure 9(h), the capacity retained at 0.1 and 2 C is 91 and 82%, respectively, for 1,000 cycles. At 20 C, the capacity for GCNT@ST-MNC is 164 mAh/g (Figure 9(j)). An inset shows a comparison between works carried out by Zhao et al. and other works. Therefore, we conclude that the combination of semi-hollow Li-rich MNC microspheres, surface treatment, and the integration of 1D and 2D NMs created more exposed sites for electrochemical reactions and enhanced Li-ion transport.

Figure 9 
                  (a) Schematic illustration of highlighting the high-conformal structure of the LMR particle. Compared with nanostructured or densely assembled LMR particle that may still suffer structure degradation, integrated advantages enabled by bifunctional strategy can be achieved. Electrochemical performance of MNC and GCNT@ST-MNC half cells. (b) CV curves of GCNT@ST-MNC from first and fourth cycle at 0.1 mV s−1. (c) Galvanostatic charge/discharge curves at 0.1 C. (d) Rate performance at various rates from 0.1 to 10 C (the inset is EIS measurement). (e) Cycling performance at 0.1 C (Coulombic efficiency of GCNT@ST-MNC). Electrochemical performance of GCNT@ST-MNC//nanographite full cell. (f) Schematic of the assembled full cell. (g) Galvanostatic charge/discharge curves with 1st, 2nd, 50th, and 100th cycle at 0.1 C. (h) Cycling performance at 0.1 and 2 C (Coulombic efficiency at 0.1 C). (i) Comparison of specific capacity and cycling performance of our work with other reported full cells. (j) Rate performance at various rates from 0.1 to 20 C (the inset is the comparison of specific capacity at high rate). (k) Ragone plots based on total mass of cathode and anode (the inset is the comparison of energy density) [136] (Copyright 2021, Springer).
Figure 9

(a) Schematic illustration of highlighting the high-conformal structure of the LMR particle. Compared with nanostructured or densely assembled LMR particle that may still suffer structure degradation, integrated advantages enabled by bifunctional strategy can be achieved. Electrochemical performance of MNC and GCNT@ST-MNC half cells. (b) CV curves of GCNT@ST-MNC from first and fourth cycle at 0.1 mV s−1. (c) Galvanostatic charge/discharge curves at 0.1 C. (d) Rate performance at various rates from 0.1 to 10 C (the inset is EIS measurement). (e) Cycling performance at 0.1 C (Coulombic efficiency of GCNT@ST-MNC). Electrochemical performance of GCNT@ST-MNC//nanographite full cell. (f) Schematic of the assembled full cell. (g) Galvanostatic charge/discharge curves with 1st, 2nd, 50th, and 100th cycle at 0.1 C. (h) Cycling performance at 0.1 and 2 C (Coulombic efficiency at 0.1 C). (i) Comparison of specific capacity and cycling performance of our work with other reported full cells. (j) Rate performance at various rates from 0.1 to 20 C (the inset is the comparison of specific capacity at high rate). (k) Ragone plots based on total mass of cathode and anode (the inset is the comparison of energy density) [136] (Copyright 2021, Springer).

Carbon NM coatings have shown promise in improving the electrical conductivity of the LLR cathodes. However, there are challenges associated with their use, such as incomplete combustion of gases such as CO and H2 during high-temperature calcination in inert conditions, which can lead to Mn dissolution [137]. To enhance the electrochemical performance of LLR with carbon NM coatings, several strategies have been proposed: (1) incorporating oxygen vacancies within a thin spinel layer of carbon NM can activate the Li2MnO3 phase in LLR, providing 3D pathways for Li+ diffusion; (2) semi-hollow microspheres can help mitigate volume changes that occur during cycling, contributing to long-term stability; (3) combining different dimensional NMs, such as 1D and 2D materials, offers various properties and benefits that strengthen electrochemical performance; and (4) in the context of full-cell LIBs, pre-lithiation may be required to compensate for the loss of Li ions in irreversible side reactions during initial cycling [138]. This ensures that the cell starts with sufficient capacity and maintains its performance over time.

6.5 Polymer

Certain polymer composites or conductive polymer materials have gained attention for their high conductivity, which is crucial for efficient lithium-ion and electron transportation during charge–discharge cycles. Additionally, they offer the potential to reduce the dissolution of active electrode materials into the electrolyte during battery operation. Common methods for applying polymer coatings include sol–gel and solid-state reaction techniques [139141].

Polymer coating of carboxyl-containing benzene diazonium salt on LLR provides excellent stability under high voltage during cycling. The polymer coating suppresses the electrolyte decomposition on electrode’s surface and TM dissolution. The CR after 350 cycles and 500 cycles is 84.2 and 76.3%, respectively. The X-ray photoelectron spectroscopy results also confirmed that the oxygen vacancies are increased after modification [142]. However, it is worth noting that polymer-modified LLR cathodes tend to exhibit lower Coulombic efficiencies compared to other coating materials. Additionally, their rate capability at high current densities can be relatively poor. Recent work by Liu et al. introduced a double-layer coating of Li2ZrO3 (LZO) and poly(3,4-ethylene dioxythiophene) (PEDOT) on LLR material. The LZO/PEDOT electrode demonstrated an initial discharge capacity of 282.9 mAh/g and an ICE of 79.1% at 0.1 C rate. Furthermore, the LZO/PEDOT-coated LLR exhibited excellent cycle stability, with CR reaching 90.8 and 91.7% after 300 cycles at 0.5 and 2 C rates, respectively. Voltage fading is also reduced with this modification [139]. Another study explored the surface modification of LLR with a germanium-based polymer, conducted by Becker et al. [140]. Unfortunately, the rate capability of this particular coating is found to be extremely poor compared to other coatings. However, the specific thickness of the germanium-based coating is not provided in the discussed literature, which limits a detailed analysis.

Recently, 6–8 nm thin layer of polyaniline is formed on Li1.2Mn0.54Co0.13Ni0.13O2 (LMO) microrod by in situ polymerization of aniline. It provides excellent cycle stability by reducing the electrolyte corrosion. The polymerization process is conducted in acidic media using HCl or (CF3SO2)2NH (HTFSI). The initial discharge capacity of LMO is 235.5 mAh/g, and this capacity is significantly improved after polyaniline modification. The polymerization of aniline in HTFSI (PANI-HTFSI@LMO) exhibited 270.1 mAh/g discharge capacity. However, the polymerization of aniline in HCl (PANI-HCl@LMO) exhibited 251.1 mAh/g discharge capacity. bis(trifluorosulfonyl)imide group (TFSI) positively affects the conductivity and electric stability of PANI [143].

Table 3 summarizes various types of NM coatings (shell), their thickness, the pristine LLR material (core), and their electrochemical performance. Scientists are actively researching polymer coatings for LLR cathodes to improve LIB performance.

Table 3

Different classes of NMs coating (shell), their coating thickness, pristine LLR material (core) and electrochemical performance (int. discharge capacity (mAh/g), CR (in %), cycles at different C rates, int. Coulombic efficiency (ICE in %) before and after coating

Class of coating material Coating material (shell) and thickness (nm) LLR material (core) Electrochemical performance References
Int. discharge capacity (mAh/g), CR (in %), cycles at different C rate, int. Coulombic efficiency (ICE in %)
Before coating After coating
Oxides ZnO – 3.50 Li1.2Mn0.54Ni0.13Co0.13O2 277.8, CR – 85.3%, 100 cycles at 0.1 C. ICE – 78.2% 271.8, CR – 97.5%, 100 cycles at 0.1 C. ICE – 84.3 [65]
TiO2 – 4–6 Li1.2Mn0.54Ni0.13Co0.13O2 278.3, CR – 78.9%, 500 cycles at 1 C. ICE – 82% at 0.1 C 300.1, CR – 91.5%, 500 cycles at 1 C. ICE – 85.6% at 0.1 C [73]
2 wt% La0.8Sr0.2MnO3−y (LSM) – 5–8 Li1.2Mn0.54Ni0.13Co0.13O2 84.4, CR – 48%, 200 cycles at 1 C. ICE – 69% at 0.1 C 202, CR – 94%, 200 cycles at 1 C. ICE – 80% at 0.1 C [74]
2 wt% Li2ZrO3 – 10–40 Li1.2Mn0.54Ni0.13Co0.13O2 186.9, CR – 85.6%, 200 cycles at 0.5 C. ICE – 69.9% at 0.1 C 210.5, CR – 92.6%, 200 cycles at 0.5 C. ICE – 77.2% at 0.1 C [75]
3 wt% LiAl5O8 – 3–5 Li1.2Mn0.54Ni0.13Co0.13O2 211, CR – 82.8%, 100 cycles at 0.5 C. ICE – 67.43% at 0.1 C 240.2, CR – 83.5%, 100 cycles at 0.5 C. ICE – 82.63% at 0.1 C [76]
(3 mol ratio of NH4VO3) LiV3O8 – 2.5 Li1.2Mn0.54Ni0.13Co0.13O2 101.9, CR – 60.7%, 50 cycles at 1 C 156.3, CR – 87.6%, 50 cycles at 1 C [77]
1.5 wt% ZrO2 – 2–3 Li1.2Ni0.16Mn0.56Co0.08O2 205 to 218, CR – 77%, 50 cycles at 0.1 205–218,CR – 95%, 50 cycles at 0.1 C [81]
1 wt% CAN  – 3 Li1.2Mn0.54Ni0.13Co0.13O2 200, CR – 58.7%, 200 cycles at 1 C. ICE – 84.2% at 0.1 C >200, CR – 76.6%, 200 cycles at 1 C. ICE – 83.4% at 0.1 C [83]
AlF3/Al2O3 Li1.2Mn0.54Ni0.13Co0.13O2 147, CR – 25%, 200 cycles, at 1 C 147, CR – 84%, 200 cycles, at 1 C [85]
ZnO/TiO2  – 1.7 ± 0.4 Li1.2Mn0.6Ni0.2O2 104.41, CR – 68%, 80 cycles at 1 C 113.40, CR – 97%, 80 cycles at 1 C [87]
3 wt% MoO3 – 18–25 Li1.2Mn0.54Ni0.13Co0.13O2 242.77, CR – 72%, 200 cycles at 0.1 C. ICE – 75.7% at 0.1 C 261.3, CR – 87%, 200 cycles at 0.1 C. ICE – 89.6% at 0.1 C [96]
2 mol% La–Co–O < 50 Li1.2Mn0.54Ni0.13Co0.13O2 161.3, CR – 66.4%, 100 cycles at 1 C 206.3, CR – 86.2%, 100 cycles at 1 C [97]
1% Al2O3/2% SiO2 – 5–6 Li1.2Mn0.54Ni0.13Co0.13O2 175, CR – 53.6%, 100 cycles at 1 C. ICE – 81.42% at 0.1 C >200, CR – 85%, 100 cycles at 1 C. ICE – 84.69% at 0.1 C [98]
3 wt% NiFe2O4 – 15 Li1.2Mn0.54Ni0.13Co0.13O2 222.33, CR – 51.5%, 200 cycles at 1 C. ICE – 84.3% at 0.1 C 232.5, CR – 91.8%, 200 cycles at 1 C. ICE – 87.2% at 0.1 C [104]
0.5 wt% SiO2 – 2–3 Li1.2Mn0.56Ni0.16Co0.08O2 205, CR – 67%, 200 cycles at 0.1 C. ICE – 75.9% at 0.1 C 194, CR – 82.6%, 200 cycles at 0.1 C. ICE – 77.3% at 0.1 C [105]
Al2O3 – 7–10 Li1.2Mn0.54Ni0.13Co0.13O2 nanotubes 143.03, CR – 78.3%, 90 cycles at 1 C. ICE – 74.9% ∼215, CR – 97.6%, 90 cycles at 1 C. ICE – 85.2% [115]
MgO–20 TiO2–20 0.5Li2MnO3∙0.5LiNi0.5Mn0.3Co0.2O2 240.45, CR – 74.54% after 50 cycles MgO – 202.96, CR – 95.69%, 50 cycles TiO2 – 195.92, 93.10%, 50 cycles [148]
3 wt% Al2O3/LiAlO2 < 10 Li1.2Mn0.54Ni0.13Co0.13O2 ∼210, CR – 53.96%, 300 cycles at 0.5 C. ICE – 75.5% at 0.1 C ∼230, CR – 83.55%, 300 cycles at 0.5 C. ICE – 88.5% at 0.1 C [149]
3 wt% LiCeO2 – 2–3 Li1.2Mn0.54Ni0.13Co0.13O2 ∼230, CR – 60.9%, 200 cycles at 1 C. ICE – 77.4% at 0.05 C ∼230, CR – 84.3%, 200 cycles at 1 C. ICE – 70.5% at 0.05 C [150]
Phosphate 5 wt% Li3V2(PO4)3 (LVP) – 5–10 Li1.12(Ni0.18Co0.07Mn0.57)O2 217.33, CR – 75%, 100 cycles at 1 C. ICE – 82% at 0.1 C 228, CR – 96%, 70 cycles at 1 C. ICE – 93% at 0.1 C [118]
3 wt% Li1+y Ti2−y Al y (PO4)3 – 5 Li1.2Mn0.54Ni0.13Co0.13O2 >260, CR – 62.4%, 100 cycles at 1 C. ICE – 64.9% at 0.5 C ∼250, CR – 62.4%, 100 cycles at 1 C. ICE – 78.7% at 0.5 C [120]
2 wt% Li3PO4 – 2 Li1.18Co0.15Ni0.15Mn0.52O2 212.89, CR – 47.3%, 200 cycles at 1 C 222.16, CR – 81.2%, 200 cycles at 1 C [122]
Fluorides 0.05 wt% YF3 – 2–3 Li1.2Mn0.54Ni0.13Co0.13O2 161.2, CR – 72.71%, 150 cycles at 0.5 C. ICE – 76.94% at 0.2 C 217.6, CR – 85.20%, 150 cycles at 0.5 C. ICE – 87.56% at 0.2 C [126]
3 wt% SmF3 – 8–10 Li1.2Mn0.54Ni0.13Co0.13O2 199.3, CR – 85.2%, 100 cycles at 0.5 C. ICE – 67.9% at 0.1 C 214.2, CR – 91.4%, 100 cycles at 0.5 C. ICE – 74.4% at 0.1 C [127]
1.5 wt% MnF2 – 3–10 Li1.2Ni0.2Mn0.6O2 239.1, CR – 73.60%, 100 cycles at 0.5 C. ICE – ∼74% at 0.1 C 199.3, CR – 72.25%, 100 cycles at 0.5 C. ICE – ∼81% at 0.1 C [128]
10 wt% graphite fluoride (CF) – 10 Li1.14Mn0.544Ni0.133Co0.133O2 281, ICE – 76% at 0.1 C 290, ICE – 99.5% at 0.1 C [129]
LiAlF4 – 5.2 Li1.2Ni0.2Mn0.6O2 <225, CR – 85.1%, 100 cycles at 0.1 C. ICE – 71.3% at 0.1 C ∼250, CR – 85.1%, 100 cycles at 0.1 C. ICE – 81.2% at 0.1 C [130]
Carbon compounds 0.5 wt% NiCo@C – 5 Li1.2Mn0.54Ni0.13Co0.13O2 256, CR – 75%, 100 cycles at 0.4 C. ICE – 66% at 0.4 C 284.21, CR – 95%, 100 cycles at 0.4 C. ICE – 72% at 0.4 C [84]
Dopamine-derived spinel layer – 20 Li1.2Mn0.54Ni0.13Co0.13O2 232, CR – 77.15%, 200 cycles at 5 C 225, CR – 85.2%, 200 cycles at 5 C. ICE – 92.3% at 0.1 C [103]
Glucose-derived spinel layer – 6 0.5Li2MnO3·0.5Li[Mn1/3Ni1/3Co1/3]O2 175, CR – 102.5%, 100 cycles at 1 C 225, – [134]
Dopamine-derived spinel layer – 10 Li1.2Mn0.54Ni0.13Co0.13O2 255, CR – 67.3%, 100 cycles at 0.2 C. ICE – 80% at 0.1 C 270, CR – 90.9%, 100 cycles at 0.2 C. ICE – 87.6% at 0.1 C [135]
Graphene/CNT Li1.2Mn0.54Ni0.13Co0.13O2 250, CR – 82.4%, 1,000 cycles at 0.1 C 275, CR – 94.5%, 1,000 cycles at 0.1 C [136]
Polymers Li2ZrO3/PEDOT – 5 Li1.2Mn0.54Ni0.13Co0.13O2 228.7, 93%, 300 cycles at 0.1 C. ICE – 71.1% at 0.1 C. 272.5, 96.3%, 300 cycles at 0.1 C. ICE – 79.1% at 0.1 C. [139]
Benzene diazomium salt – 2 Li1.2Mn0.54Ni0.13Co0.13O2 ∼300, 70.6%, 120 cycles at 0.2 C. ICE – 75% at 0.2 C ∼300, 83.2%, 120 cycles at 0.2 C [142]
Polyaniline – 6–8 Li1.2Mn0.54Ni0.13Co0.13O2 217.3, 77.4%, 100 cycles at 0.5 C 212.9, 91.98%, 100 cycles at 0.5 C [143]

6.6 Coupling of doping and nanoscale coating

Although nanoscale coatings have shown potential in enhancing LLR cathode performance, it is essential to recognize their limitations in dealing with LLR issues like oxygen evolution, layered to spinel transformation, and Mn dissolution. These issues are rooted in the lattice structure of LLR, making it necessary to consider additional strategies, such as partial doping, to preserve the lattice structure and further enhance the LLR cathode. Despite the improvements achieved through coatings, there is still room for enhancing specific capacity, rate performance, and ICE. The degree of polarization in LLR electrodes remains relatively high and has not been satisfactorily improved by coating alone. As discussed earlier, both doping and coating have their advantages, and combining these strategies synergistically enhances cathode performance by addressing various aspects of LLR electrode behaviour.

One example of successful doping involves the introduction of a small amount of chromium (Cr) into the LLR structure. Cr doping can improve the electrochemical performance by facilitating charge transfer from Cr to Mn, which can reduce Mn dissolution. Additionally, Cr doping can mitigate thermodynamic instability between phases during the delithiation process [144]. Tai et al. [145] explored the effects of Cr doping and Li3PO4 coating on the LLR cathode. While the CR is not optimal, they observed minor voltage decay. Notably, the specific capacity of Cr-doped LLR is higher than that of Cr-doped Li3PO4-coated LLR, highlighting the potential of Cr doping to reduce charge transfer resistance and enhance specific capacity. Li3PO4 coating, on the other hand, contributed to reducing voltage decay. In another study, Lu et al. [125] investigated molybdenum (Mo) doping in ZrF4-modified LLR. Mo, known for its high electrical conductivity, is introduced into the LLR structure. However, this material displayed good discharge capacity while suffering from poor rate capability, cycle stability, and relatively low ICE of less than 78%. While Mo doping enhanced electrical conductivity, the combination with ZrF4 did not satisfactorily address the resistivity of the material, as ZrF4 may counteract the electrical conductivity improvement by Mo.

Researchers have been working on boosting the electrical conductivity of TiO2 by adding the anionic element fluorine, which creates Ti3+ and oxygen vacancies on the coating surface. Rastgoo-Deylami et al. [73] introduced F-doped anatase TiO2 (FATO) as a nanoscale coating layer (4–6 nm thickness) on Li1.2Mn0.54Ni0.13Co0.13O2 (LMNCO) cathodes using a wet chemical method. They compared the electrochemical performance of pristine (LMNCO), 1 wt% (LMNCO-ATO1), 2 wt% anatase TiO2 (LMNCO-ATO2), and 2 wt% F-doped anatase TiO2 (LMNCO-FATO 02) coating. As seen from Figure 10(a) and (d), the initial charge/discharge profiles at 0.1 C for LMNCO-ATO2 and LMNCO-FATO 02 revealed two voltage plateaus in the range of 4.0–4.3 V and above 4.5 V. The first plateau corresponds to the extraction of Li+ ions from the LiNi1/3Co1/3Mn1/3O2 component, accompanied by the oxidation of Ni2+ and Co3+ to form Ni4+ and Co4+, respectively. The second plateau signifies the activation of the Li2MnO3 component, during which Li2O is removed. The ICE values calculated from the data were 83.6% for LMNCO-ATO2 and 85.6% for LMNCO-FATO 02. This suggests that oxygen generated during the initial charging process can be captured by the oxygen vacancies formed in the F-doped anatase TiO2 coating. As seen from Figure 10(b) and (e), LMNCO-FATO 02 exhibited an outstanding rate performance as compared to LMNCO-ATO2, indicating that fluorine doping reduced the polarization at high current densities. The cycle performance over 500 cycles for both samples demonstrated that F-doping in the TiO2 coating enhances both ionic and electrical conductivity, resulting in excellent cycle stability (Figure 10(c) and (f)). The mechanism of oxygen vacancies is displayed in Figure 10(g). During the initial cycling, oxygen vacancies within the FATO nanolayer removed the lattice oxygen. This prevents the formation of thick SEI and contributes to the enhanced electrochemical performance of the LMNCO cathode. Recently, Wu et al. [146] modified Li1.2Mn0.54Co0.13Ni0.13O2 material with Cd doping and CdO surface coating. The Cd doping improves the electrical conductivity and CdO reduces the direct contact between electrolyte and the material and improves structural stability.

Figure 10 
                  (a) Initial cycle charge/discharge curves of Li1.2Mn0.54Ni0.13Co0.13O2 with 2 wt% anatase TiO2 coating in the voltage range between 2.0 and 4.8 V at 0.1 C. (b) Rate performances of 2 wt% anatase TiO2 coating between 2.0 and 4.8 V from 0.1 to 10 C. (c) Cycling performance of all anatase TiO2-coated samples at 1 C. (d) Initial charge and discharge profiles of LMNCO-FATO2. (e) Rate capacities of pristine LMNCO, LMNCO-FATO1, LMNCO-FATO2, and LMNCO-FATO4 electrodes at 0.1 to 10 C. (f) Cycling rate performance of LMNCO-FTO2. (g) Schematic of oxygen vacancies mechanism in FATO coated-Li1.2Mn0.54Ni0.13Co0.13O2 particle [73] (Copyright 2019, Elsevier).
Figure 10

(a) Initial cycle charge/discharge curves of Li1.2Mn0.54Ni0.13Co0.13O2 with 2 wt% anatase TiO2 coating in the voltage range between 2.0 and 4.8 V at 0.1 C. (b) Rate performances of 2 wt% anatase TiO2 coating between 2.0 and 4.8 V from 0.1 to 10 C. (c) Cycling performance of all anatase TiO2-coated samples at 1 C. (d) Initial charge and discharge profiles of LMNCO-FATO2. (e) Rate capacities of pristine LMNCO, LMNCO-FATO1, LMNCO-FATO2, and LMNCO-FATO4 electrodes at 0.1 to 10 C. (f) Cycling rate performance of LMNCO-FTO2. (g) Schematic of oxygen vacancies mechanism in FATO coated-Li1.2Mn0.54Ni0.13Co0.13O2 particle [73] (Copyright 2019, Elsevier).

Ding et al. [147] discovered a novel three-in-one surface treatment approach through the decomposition of urea. This method involved the creation of a carbon nanolayer doped with nitrogen (N) to modify LMNO (Li1.2Mn0.6Ni0.2O2), facilitating the integration of a spinel phase between the N-doped carbon layer and LMNO. The N-doped carbon layer crucially reduces electrolyte corrosion and initiates the formation of oxygen vacancies on the modified surface layer. The CV curve displayed oxidation and reduction peaks at 3.02 and 2.85 V, respectively, attributed to the formation of the spinel phase. At 10 C, the CR for the LMNO electrode (P-LMNO) and the modified electrode (M-LMNO) is 143.5 and 173.6 mAh/g, respectively. Impressively, the CR at 1 C for 500 cycles is significantly improved for M-LMNO at about 89.9%; P-LMNO exhibited a retention of only 55.31%. This suggests that the innovative structure effectively reduces the evolution of oxygen from the electrode structure.

In another study, an electrode is prepared by doping Nb5+ into the LLR structure and coating it with poly(3, 4-ethylenedioxythiophene): poly(styrenesulfonate) (PEDOT:PSS). This surface modification led to a slight increase in rate performance compared to an electrode modified with Li2ZrO3 (LZO)/PEDOT. Additionally, the Nb5+-doped PEDOT:PSS-coated electrode exhibited higher cycle stability than the pristine electrode. For various electrode configurations, without Nb5+-doped LLR (pristine), Nb5+-doped LLR (2 wt%), PEDOT:PSS coated, and Nb5+-doped PEDOT:PSS coated (2 wt%) electrodes, the CR values were 84.3, 86.7, 92.2, and 90.8%, respectively. The Nb5+-doped PEDOT:PSS coating not only prevented direct contact between the electrode and the electrolyte but also improved Li+ ion diffusion kinetics [141].

In summary, the three-in-one surface treatment, as well as Nb5+ doping and PEDOT:PSS coating, offer promising strategies to address issues related to oxygen evolution, corrosion, and cycling stability in LLR-based LIBs. The summarized research in this area, including coupling of doping and coating on the LLR surface (shell), the amount of doping and coating, the thickness of the coating layer, pristine LLR material (core), and their electrochemical performance, is presented in Table 4.

Table 4

Coupling of doping and coating on LLR surface (shell), amount of doping and coating, thickness of coating layer, pristine LLR material (core) and their electrochemical performance (int. discharge capacity (mAh/g), CR (in %), cycles at different C rates, int. Coulombic efficiency (ICE in %) before and after coating

Doping/coating material, thickness in nm LLR material (core) Electrochemical performance References
Int. discharge capacity (mAh/g), CR (in %), cycles at different C rate, int. Coulombic efficiency (ICE in %)
Before coating After coating
0.08 Cr doped 1 wt% Li3PO4 coating – 5 nm Li1.2Mn0.54Ni0.13Co0.13O2 255.8, CR – 59%, 200 cycles. ICE – 76.8% at 0.1 C 265.2, CR – 76.5%, 200 cycles. ICE – 80.5% at 0.1 C [145]
0.03 Mo6+-doped 2 wt% ZrF4 coating – 15–35 nm Li1.2Mn0.54Ni0.13Co0.13O2 At 25°C – 198.9, CR – 86.5%, 200 cycles at 0.5 C. At 55°C – 208, CR – 82.9%, 200 cycles at 0.5 C. ICE – 73.9% at 0.1 C At 25°C – 213, CR – 92.4%, 200 cycles at 0.5 C. At 55°C – 226, CR – 88.7%, 200 cycles at 0.5 C. ICE – 77.2% at 0.1 C [125]
2 wt% F-doped anatase TiO2 – 4–6 nm Li1.2Mn0.54Ni0.13Co0.13O2 278.3, CR – 78.9%, 500 cycles at 0.1 C. ICE – ∼81% at 0.1 C 300.1, CR – 91.5%, 500 cycles at 0.1 C. ICE – 85.6% at 0.1 C [73]
(1 wt% urea utilized) N-doped carbon layer – 2–4 nm Li1.2Mn0.6Ni0.2O2 250.7, CR – 97.9%, 100 cycles at 0.5 C. ICE – 77.9% at 0.1 C 260.2, CR – ∼100%, 100 cycles at 0.5 C. ICE – 81.8% at 0.1 C [147]
0.01 Nb5+-doped 2 wt% PEDOT:PSS – 20–30 nm Li1.2Mn0.54Ni0.13Co0.13O2 249.8, CR – 94.9%, 200 cycles at 0.1 C. ICE – 70.7% at 0.1 C 273.8, CR – 96.2%, 200 cycles at 0.1 C. ICE – 80.2% at 0.1 C [147]

7 Summary and future perspectives

LLR MNC-based oxide is the next-generation cathode material for LIBs. However, LLR suffers from several drawbacks, including ICL, voltage fading, capacity decay, and poor cycle stability and rate capability. To solve these challenges, several NM coatings with thicknesses less than 50 nm have been investigated, providing benefits such as fast Li ion diffusion path, suppression of voltage fading, and better ICE and rate capability.

Nanoscale coatings offer benefits such as fast diffusion paths, large surface areas, and considerable lithium ion storage capacity. Nanoscale coatings, on the other hand, create difficulties such as particle agglomeration, low material density, lower productivity, and complex modification procedures. In real battery systems, striking a balance between benefits and downsides of NMs is critical. This entails using abundant and cost-effective chemicals and electrode preparation procedures. Co-precipitation is an efficient, simple, and scalable process for producing spherical particles with high tap density. The addition of capping agent can improve the homogeneity of spherical particles. ALD coatings provide solutions for substrate homogeneity, controllability, and strong bonding between the coating and substrate. Scaling of ALD coatings for commercialization is a key consideration. Synchronous coatings, which skips the modification step, have gained popularity due to their potential to reduce manufacturing cost and production time.

Oxides and phosphate coatings have proven effective to improve the cycle stability of LLR MNC-based oxide cathodes. Phosphate coating serves good thermal stability compared to other NM coating. These coatings, whether oxide, phosphate, fluoride, carbon, or polymer-based, have all shown a significant increase in the specific capacity of LLR cathodes. This enhancement is mostly due to the decrease in charge-transfer resistance (R ct), which is a key factor in increasing specific capacity. The incorporation of the porous structures on the electrode surface has been successful in lowering R ct and so enhancing rate performance. To improve the rate performance in practical applications after coating, it is essential to reduce polarization at high current densities. The introduction of oxygen vacancies has been shown to be beneficial in activating the electrochemically inert Li2MnO3 phase, decreasing the energy barrier for Li-ion diffusion. Furthermore, the incorporation of a spinel layer has showed potential in improving Li-ion intercalation, resulting in high ICE. The spinel layer can effectively serve as an expressway for Li-ion diffusion. However, it is crucial to recognize that the thermal stability of the layered/spinel heterostructure may not be enough to ensure battery safety. More research is needed to assess the safety performance of these materials. Carbon nanolayer surfaces are of tremendous scientific interest. It is possible to improve rate capability, ICE, and long-term cycling performance by incorporating oxygen vacancies and spinel layers via carbon nanolayers.

Following our thorough examination of several nanocoatings for LLR MNC-based oxide cathodes, we offer many intriguing future research directions:

  1. Combination of two or more multifunctional NMs: Investigating the synergistic effect of combining two or more multifunctional NMs to harness the unique advantages each offers.

  2. Sequential coating strategies: Examining new materials involves substituting the coating material within the LLR bulk, essentially resulting in the doping of the LLR bulk with the coating material and subsequently encapsulating the coated material with another coating material.

  3. Oxygen-deficient NMs: Oxygen-deficient NMs offer unique electrochemical advantages.

  4. Ultrathin spinel layer formation: The formation of ultrathin spinel layers as coatings achieves improved rate performance.

  5. Scaling up nanoscale coating methods: Developing scalable nanocoating techniques suitable for large-volume production while maintaining the desired properties and quality.

  6. Investigate various dimensional nanostructures: Investigating a wide range of different dimensional nanostructures as potential coating materials for LLR, each offering distinct advantages.

In summary, nanoscale coatings have demonstrated significant potential for enhancing the electrochemical performance of LLR cathodes. Further research should delve deeper into the structural and morphological aspects of modified LLR cathodes, including dimensions, uniformity, charge transfer mechanisms, and more. Additionally, as we progress from coin cell configurations to pouch cells and battery packs with NM-modified electrodes, addressing challenges related to particle size control, uniformity, scalable NM synthesis, and cost-effectiveness will be crucial for realizing ideal battery systems.


# These authors contributed equally to this work and should be considered first co-authors.


  1. Funding information: This work was financially supported by the Chinese Government Scholarship (Chinese Scholarship Council – CSC) (No. 2018DFH011142), National Natural Science Foundation of China (NSFC, No. 22278080), Minjiang Scholarship of Fujian Province (No. Min-Gaojiao [2010]-117), Central-government Guided Fund for Local Economic Development (No. 830170778), R&D Fund for Strategic Emerging Industry of Fujian Province (No. 82918001), International Cooperation Project of Fujian Science and Technology Department (No. 830170771), Open Fund of Fujian Key Laboratory of New Energy Generation and Power Conversion (No. KLIF-202102), and Analytical Testing Fund of Qingyuan Innovation Laboratory of Fujian Province.

  2. Author contributions: All authors have accepted the responsibility for the entire content of this manuscript and approved its submission.

  3. Conflict of interest: The authors state no conflict of interest.

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Received: 2023-10-08
Revised: 2024-03-12
Accepted: 2024-05-03
Published Online: 2024-06-20

© 2024 the author(s), published by De Gruyter

This work is licensed under the Creative Commons Attribution 4.0 International License.

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  75. A penta-hybrid approach for modeling the nanofluid flow in a spatially dependent magnetic field
  76. Advancing sustainable agriculture: Metal-doped urea–hydroxyapatite hybrid nanofertilizer for agro-industry
  77. Utilizing Ziziphus spina-christi for eco-friendly synthesis of silver nanoparticles: Antimicrobial activity and promising application in wound healing
  78. Plant-mediated synthesis, characterization, and evaluation of a copper oxide/silicon dioxide nanocomposite by an antimicrobial study
  79. Effects of PVA fibers and nano-SiO2 on rheological properties of geopolymer mortar
  80. Investigating silver and alumina nanoparticles’ impact on fluid behavior over porous stretching surface
  81. Potential pharmaceutical applications and molecular docking study for green fabricated ZnO nanoparticles mediated Raphanus sativus: In vitro and in vivo study
  82. Effect of temperature and nanoparticle size on the interfacial layer thickness of TiO2–water nanofluids using molecular dynamics
  83. Characteristics of induced magnetic field on the time-dependent MHD nanofluid flow through parallel plates
  84. Flexural and vibration behaviours of novel covered CFRP composite joints with an MWCNT-modified adhesive
  85. Experimental research on mechanically and thermally activation of nano-kaolin to improve the properties of ultra-high-performance fiber-reinforced concrete
  86. Analysis of variable fluid properties for three-dimensional flow of ternary hybrid nanofluid on a stretching sheet with MHD effects
  87. Biodegradability of corn starch films containing nanocellulose fiber and thymol
  88. Toxicity assessment of copper oxide nanoparticles: In vivo study
  89. Some measures to enhance the energy output performances of triboelectric nanogenerators
  90. Reinforcement of graphene nanoplatelets on water uptake and thermomechanical behaviour of epoxy adhesive subjected to water ageing conditions
  91. Optimization of preparation parameters and testing verification of carbon nanotube suspensions used in concrete
  92. Max-phase Ti3SiC2 and diverse nanoparticle reinforcements for enhancement of the mechanical, dynamic, and microstructural properties of AA5083 aluminum alloy via FSP
  93. Advancing drug delivery: Neural network perspectives on nanoparticle-mediated treatments for cancerous tissues
  94. PEG-PLGA core–shell nanoparticles for the controlled delivery of picoplatin–hydroxypropyl β-cyclodextrin inclusion complex in triple-negative breast cancer: In vitro and in vivo study
  95. Conduction transportation from graphene to an insulative polymer medium: A novel approach for the conductivity of nanocomposites
  96. Review Articles
  97. Developments of terahertz metasurface biosensors: A literature review
  98. Overview of amorphous carbon memristor device, modeling, and applications for neuromorphic computing
  99. Advances in the synthesis of gold nanoclusters (AuNCs) of proteins extracted from nature
  100. A review of ternary polymer nanocomposites containing clay and calcium carbonate and their biomedical applications
  101. Recent advancements in polyoxometalate-functionalized fiber materials: A review
  102. Special contribution of atomic force microscopy in cell death research
  103. A comprehensive review of oral chitosan drug delivery systems: Applications for oral insulin delivery
  104. Cellular senescence and nanoparticle-based therapies: Current developments and perspectives
  105. Cyclodextrins-block copolymer drug delivery systems: From design and development to preclinical studies
  106. Micelle-based nanoparticles with stimuli-responsive properties for drug delivery
  107. Critical assessment of the thermal stability and degradation of chemically functionalized nanocellulose-based polymer nanocomposites
  108. Research progress in preparation technology of micro and nano titanium alloy powder
  109. Nanoformulations for lysozyme-based additives in animal feed: An alternative to fight antibiotic resistance spread
  110. Incorporation of organic photochromic molecules in mesoporous silica materials: Synthesis and applications
  111. A review on modeling of graphene and associated nanostructures reinforced concrete
  112. A review on strengthening mechanisms of carbon quantum dots-reinforced Cu-matrix nanocomposites
  113. Review on nanocellulose composites and CNFs assembled microfiber toward automotive applications
  114. Nanomaterial coating for layered lithium rich transition metal oxide cathode for lithium-ion battery
  115. Application of AgNPs in biomedicine: An overview and current trends
  116. Nanobiotechnology and microbial influence on cold adaptation in plants
  117. Hepatotoxicity of nanomaterials: From mechanism to therapeutic strategy
  118. Applications of micro-nanobubble and its influence on concrete properties: An in-depth review
  119. A comprehensive systematic literature review of ML in nanotechnology for sustainable development
  120. Exploiting the nanotechnological approaches for traditional Chinese medicine in childhood rhinitis: A review of future perspectives
  121. Twisto-photonics in two-dimensional materials: A comprehensive review
  122. Current advances of anticancer drugs based on solubilization technology
  123. Recent process of using nanoparticles in the T cell-based immunometabolic therapy
  124. Future prospects of gold nanoclusters in hydrogen storage systems and sustainable environmental treatment applications
  125. Preparation, types, and applications of one- and two-dimensional nanochannels and their transport properties for water and ions
  126. Microstructural, mechanical, and corrosion characteristics of Mg–Gd–x systems: A review of recent advancements
  127. Functionalized nanostructures and targeted delivery systems with a focus on plant-derived natural agents for COVID-19 therapy: A review and outlook
  128. Mapping evolution and trends of cell membrane-coated nanoparticles: A bibliometric analysis and scoping review
  129. Nanoparticles and their application in the diagnosis of hepatocellular carcinoma
  130. In situ growth of carbon nanotubes on fly ash substrates
  131. Structural performance of boards through nanoparticle reinforcement: An advance review
  132. Reinforcing mechanisms review of the graphene oxide on cement composites
  133. Seed regeneration aided by nanomaterials in a climate change scenario: A comprehensive review
  134. Surface-engineered quantum dot nanocomposites for neurodegenerative disorder remediation and avenue for neuroimaging
  135. Graphitic carbon nitride hybrid thin films for energy conversion: A mini-review on defect activation with different materials
  136. Nanoparticles and the treatment of hepatocellular carcinoma
  137. Special Issue on Advanced Nanomaterials and Composites for Energy Conversion and Storage - Part II
  138. Highly safe lithium vanadium oxide anode for fast-charging dendrite-free lithium-ion batteries
  139. Recent progress in nanomaterials of battery energy storage: A patent landscape analysis, technology updates, and future prospects
  140. Special Issue on Advanced Nanomaterials for Carbon Capture, Environment and Utilization for Energy Sustainability - Part II
  141. Calcium-, magnesium-, and yttrium-doped lithium nickel phosphate nanomaterials as high-performance catalysts for electrochemical water oxidation reaction
  142. Low alkaline vegetation concrete with silica fume and nano-fly ash composites to improve the planting properties and soil ecology
  143. Mesoporous silica-grafted deep eutectic solvent-based mixed matrix membranes for wastewater treatment: Synthesis and emerging pollutant removal performance
  144. Electrochemically prepared ultrathin two-dimensional graphitic nanosheets as cathodes for advanced Zn-based energy storage devices
  145. Enhanced catalytic degradation of amoxicillin by phyto-mediated synthesised ZnO NPs and ZnO-rGO hybrid nanocomposite: Assessment of antioxidant activity, adsorption, and thermodynamic analysis
  146. Incorporating GO in PI matrix to advance nanocomposite coating: An enhancing strategy to prevent corrosion
  147. Synthesis, characterization, thermal stability, and application of microporous hyper cross-linked polyphosphazenes with naphthylamine group for CO2 uptake
  148. Engineering in ceramic albite morphology by the addition of additives: Carbon nanotubes and graphene oxide for energy applications
  149. Nanoscale synergy: Optimizing energy storage with SnO2 quantum dots on ZnO hexagonal prisms for advanced supercapacitors
  150. Aging assessment of silicone rubber materials under corona discharge accompanied by humidity and UV radiation
  151. Tuning structural and electrical properties of Co-precipitated and Cu-incorporated nickel ferrite for energy applications
  152. Sodium alginate-supported AgSr nanoparticles for catalytic degradation of malachite green and methyl orange in aqueous medium
  153. An environmentally greener and reusability approach for bioenergy production using Mallotus philippensis (Kamala) seed oil feedstock via phytonanotechnology
  154. Micro-/nano-alumina trihydrate and -magnesium hydroxide fillers in RTV-SR composites under electrical and environmental stresses
  155. Mechanism exploration of ion-implanted epoxy on surface trap distribution: An approach to augment the vacuum flashover voltages
  156. Nanoscale engineering of semiconductor photocatalysts boosting charge separation for solar-driven H2 production: Recent advances and future perspective
  157. Excellent catalytic performance over reduced graphene-boosted novel nanoparticles for oxidative desulfurization of fuel oil
  158. Special Issue on Advances in Nanotechnology for Agriculture
  159. Deciphering the synergistic potential of mycogenic zinc oxide nanoparticles and bio-slurry formulation on phenology and physiology of Vigna radiata
  160. Nanomaterials: Cross-disciplinary applications in ornamental plants
  161. Special Issue on Catechol Based Nano and Microstructures
  162. Polydopamine films: Versatile but interface-dependent coatings
  163. In vitro anticancer activity of melanin-like nanoparticles for multimodal therapy of glioblastoma
  164. Poly-3,4-dihydroxybenzylidenhydrazine, a different analogue of polydopamine
  165. Chirality and self-assembly of structures derived from optically active 1,2-diaminocyclohexane and catecholamines
  166. Advancing resource sustainability with green photothermal materials: Insights from organic waste-derived and bioderived sources
  167. Bioinspired neuromelanin-like Pt(iv) polymeric nanoparticles for cancer treatment
  168. Special Issue on Implementing Nanotechnology for Smart Healthcare System
  169. Intelligent explainable optical sensing on Internet of nanorobots for disease detection
  170. Special Issue on Green Mono, Bi and Tri Metallic Nanoparticles for Biological and Environmental Applications
  171. Tracking success of interaction of green-synthesized Carbopol nanoemulgel (neomycin-decorated Ag/ZnO nanocomposite) with wound-based MDR bacteria
  172. Green synthesis of copper oxide nanoparticles using genus Inula and evaluation of biological therapeutics and environmental applications
  173. Biogenic fabrication and multifunctional therapeutic applications of silver nanoparticles synthesized from rose petal extract
  174. Metal oxides on the frontlines: Antimicrobial activity in plant-derived biometallic nanoparticles
  175. Controlling pore size during the synthesis of hydroxyapatite nanoparticles using CTAB by the sol–gel hydrothermal method and their biological activities
  176. Special Issue on State-of-Art Advanced Nanotechnology for Healthcare
  177. Applications of nanomedicine-integrated phototherapeutic agents in cancer theranostics: A comprehensive review of the current state of research
  178. Smart bionanomaterials for treatment and diagnosis of inflammatory bowel disease
  179. Beyond conventional therapy: Synthesis of multifunctional nanoparticles for rheumatoid arthritis therapy
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