 Open Access Article
 Open Access Article
      
        
          
            Gregory 
            Beaucage†‡
          
        
        
        
      *a and 
      
        
          
            Siddharth V. 
            Patwardhan‡
          
        
       *b
*b
      
aDepartment of Chemical and Materials Engineering, University of Cincinnati, OH 45221, USA. E-mail: beaucag@ucmail.uc.edu
      
bDepartment of Chemical and Biological Engineering, University of Sheffield, Sheffield S1 3JD, UK. E-mail: s.patwardhan@sheffield.ac.uk
    
First published on 27th October 2025
Significant research is focused on improving the performance of Li ion batteries (LIBs) by using Si in anodes due to its ten times higher theoretical capacity when compared with that of graphite, and it is also naturally abundant. However, there are many issues in using high Si content due to nearly threefold expansion of Si upon lithiation, leading to mechanical breakdown and loss of performance within a few cycles. This leads to the challenge of simultaneously optimising the stability, capacity, lithiation rates and solid electrolyte interphase (SEI) formation. It is unclear what the ideal porous structure is to meet the desired performance specifications. This perspective article proposes quantitative governing equations to correlate structural features with performance, which can provide guiding principles to design (meso)porous silicon (p-Si) structures. The structural features include nano-scale primary particles, and their meso-scale connectivity, degree of aggregation and tortuosity. We hypothesize that hierarchical aggregates of sub-micron networked particles will have an enhanced rate of lithiation yet with mechanical stability to withstand swelling via accordion expansion or disinterspersion (D.I.). Preliminary evaluation of these principles is presented, and future research avenues are outlined. To test these hypotheses, experimental investigations are needed to identify and compare various hierarchical structures that can maximise the criteria described above. These guiding principles will prove valuable for developing Si for LIB anodes, thereby accelerating their commercial uptake.
Graphite is the preferred anode for LIBs and makes up 48 mass percent of a cell and about 27% of the total EV battery pack making it the largest single component by mass.2 However, an alternative is needed in order to meet growing demands such as higher energy density and lower costs while improving sustainability.3,4 Furthermore, there have been recent issues pertaining to graphite availability and the supply chain, mainly driven by securing future access to meet the 8–10 times increase in the demands of energy storage using batteries.5,6 Si provides 10 times higher theoretical capacity compared to graphite and is naturally abundant. Substitution of silicon for graphite could reduce the mass of anodes by a factor of 10 due to greater Li+ specific capacity and higher cell potential. Silicon anode research has sought enhancement of specific capacity, lithiation/delithiation rates, and cycle life. As such, adding Si to graphite anodes has become common recently, with certain manufacturers using up to 10% Si. However, higher Si content is required to achieve the desired improvements. The increase in performance is complicated by up to a tripling of the silicon volume during the charging cycle,7 which leads to decrepitation (Fig. 1 and 2) and formation of a new solid electrolyte interphase (SEI) which permanently depletes anode capacity. To accommodate silicon anodes in batteries, the volumetric breathing with charge cycles, associated with the greater specific capacity, must be included in the structural design.
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| Fig. 1 Schematic representation of various mechanisms for decrepitation of silicon during lithiation. Image reproduced from ref. 9. | ||
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| Fig. 2 (a–e) Lithiation of a 620 nm crystalline silicon particle with decrepitation. Red arrows indicate cracks. (f) Electron diffraction indicating the formation of polycrystalline Li15Si4 upon lithiation. Images reproduced from ref. 10. | ||
Silicon also has a lower electrical conductivity (about 1/10![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) 000) compared to graphite which reduces the charge/discharge rates. Further impacting the rates, the process of lithiation of silicon involves formation of an interstitial or a substitutional alloy which is slower than intercalation.8 The formation of an SEI that irreversibly consumes Li+ provides a further barrier to transport of Li+ and electrons. Decrepitation of silicon particles from cyclic swelling and contraction exacerbates the SEI problem leading to drastic capacity fade. Furthermore, the increase in Si loading in anodes is challenged by expensive manufacturing of anode-grade Si at the desired scale.5
000) compared to graphite which reduces the charge/discharge rates. Further impacting the rates, the process of lithiation of silicon involves formation of an interstitial or a substitutional alloy which is slower than intercalation.8 The formation of an SEI that irreversibly consumes Li+ provides a further barrier to transport of Li+ and electrons. Decrepitation of silicon particles from cyclic swelling and contraction exacerbates the SEI problem leading to drastic capacity fade. Furthermore, the increase in Si loading in anodes is challenged by expensive manufacturing of anode-grade Si at the desired scale.5
• Engineering particle geometries (particle sizes, microstructure, crystallinity and morphology),
• Using Si-composites (including coatings and prelithiation),
• Developing formulations with suitable binders and electrolytes.
Generally, a common approach is to use sub-micron silicon particles such as reduced clay platelets, and rod structures with minor sizes smaller than the critical flaw size preventing breakage (decrepitation).9,11–17 Some of the disadvantages to silicon as an anode material can be overcome through nanoparticles (NPs). There are a variety of ways reported in the literature to engineer particle structures (see Fig. 4 for examples). Particles smaller than the critical flaw size are not subject to cracking. High dilatational strains reduce the critical flaw size from microns to tens of nanometers.18 Nanoparticles can more easily accommodate large volume changes arising from the formation of a swollen LixSi layer with the dilatational stress being alleviated at surfaces (see Fig. 5).7 Diffusion distances are shorter for small particles, making lithiation/delithiation more rapid. The impact of low electrical conductivity is less limiting for shorter distances in nanoparticles embedded in a conductive matrix. Other strategies include creating carbon coatings or Si–C composites which can help mitigate issues arising from low conductivity of Si as well as SEI formation.
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| Fig. 4 Strategies to engineer the particle microstructure (left) and morphology to prevent breakage (decrepitation), right. Images reproduced from ref. 15 and 19. | ||
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| Fig. 5 Lithiation and delithiation of Si nanoparticles (the scale bar = 200 nm): first lithiation cycle (a–c), first delithiation (d–f), and second lithiation (g–i). Images reproduced from ref. 7. | ||
Indeed, there is significant commercial interest in adopting these strategies for designing and developing high performance Si-based anodes. For example, Si deposited on porous carbons to produce Si–C composites are being developed, which are similar to the structures shown in part (e), right panel of Fig. 4.20,21 Technologies for growing nanowires or micro-needles composed of pure silicon as well as Si–C composites have also been developed (such as those shown in part (f), right panel of Fig. 4).22,23 There are also examples of depositing thin layers of Si on metals for direct use in anodes.24
Each of these strategies and combinations thereof has shown the potential to improve the performance of Si and can enable higher loading with graphite; however, 50% Si content and above in anodes is still not within our reach. This is because the strategies noted above provide only incremental improvements in Si performance. Manufacturing some of these complex structures can be very challenging, or at least they are economically prohibitive to manufacture due to multi-step, inefficient and slow processes. For example, Si NPs, while highly desirable for anodes, are notoriously uneconomical to manufacture and are not available on the market at scale.19 Furthermore, there are issues with safety and sustainability of the methods producing desired Si structures. An overarching concern is that most developments have been focusing on one factor/feature (e.g. particle size or morphology or coating), instead of a holistic or an integrated approach which balances performance, scalability, costs and environmental factors.25
Nevertheless, these efforts have highlighted that the most promising structure is (meso)porous Si (p-Si). Experimental and simulation results have shown that porous structures at the nanoscale provide “breathing” space upon expansion during lithiation and hence improve the stability and performance.26,27 This means that p-Si can be used at high Si content, thus overcoming the challenges outlined above, including economical and sustainable manufacture of such materials.28 There are recent reports that such porous structures can be potentially manufactured.23,29–31 As such, there have been many studies on the synthesis and testing of a range of p-Si structures; however, it is unclear what is the ideal porous structure which can simultaneously optimise multiple performance criteria. Guiding principles for designing high-performance Si-structures for LIB anodes are missing. This article aims to identify physics-based governing equations to help define “ideal” Si-structures.
(1) The SEI layer thickness is proportional to primary particle size;
(2) Lithiation/delithiation reaction rates are inversely proportional to the square of the primary particle size;
(3) Disinterspersion (accordion unfolding and folding) of Si aggregates depends on the hierarchical structure and mesoscale properties such as connectivity, the degree of aggregation and tortuosity;
(4) Specific capacity is dependent on the Si aggregate density and mass-fractal dimension.
Below we explain the rationale behind these relationships and their mathematical representations as governing equations.
![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) 000 atm pressure for a 20 nm silicon particle), and because the SEI layer formation involves a decrease in density which is opposed by hydrostatic pressure by Le Chatelier's principle, the SEI thickness depends directly on the primary particle size.33 Therefore, the hypothesis is that smaller silicon particles should show better cycle retention due to more flexible, thin SEI layers.
000 atm pressure for a 20 nm silicon particle), and because the SEI layer formation involves a decrease in density which is opposed by hydrostatic pressure by Le Chatelier's principle, the SEI thickness depends directly on the primary particle size.33 Therefore, the hypothesis is that smaller silicon particles should show better cycle retention due to more flexible, thin SEI layers.| tSEI ∝ dp | (1) | 
| P ∝ 1/dp | (2) | 
We note that as these particles form hierarchical structures, the exposed surface area will reduce depending on the aggregate structures and this may need to be accommodated within the proportionality constant of eqn (1). Furthermore, for lithiation, diffusion of Li from the electrolyte to Si particle surfaces is followed by diffusion and alloying within the Si particles. From Fig. 5, we know that alloying takes on the order of 10 to 100 seconds; hence, the alloying step is rate limiting and the diffusion time, τLi+, depends on the diffusion distance in the particle (dp2), i.e. the lithiation rate (rLi+) increases as Si nanoparticles get smaller (eqn (3) and (4)).
| τLi+ ∝ dp2 | (3) | 
|  | (4) | 
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| Fig. 6 Deformation of titania aggregates in TEM by >200% (from the image on left to the image on right). Image reproduced with permission from ref. 38. | ||
Therefore, it is proposed that through the processes of disinterspersion (D.I.) and elastic expansion, networks of aggregated Si can accommodate large dilatational volume changes that occur during lithiation. The impact of meso- and micro-scale aggregate network structures on anode performance can be considered in relation to a fractal model where aggregates are ramified/branched clusters of primary particles as shown in Fig. 7.40–42
This disinterspersion (D.I.) or expansion can be linked to the structural features of a material if we consider the mass-fractal aggregate in Fig. 7. It shows a ramified mass-fractal aggregate such as p-Si, which can be described with an aggregate size R, a minimum or short circuit path p, and the primary particle size dp. These parameters reflect the tortuosity, and a stick figure structure (lines) that reflects the topology, connectivity, or branching. Using these features, we define disinterspersion (D.I.) or the ability to expand as follows:
|  | (5) | 
Aggregates can be decomposed into a tortuous minimum path from which the aggregate attains elasticity, and a branched connective path which resists expansion due to interconnectivity. This is analogous to a knitted fabric with kinky fibers. The maximum meso-scale expansion occurs with a fully extended minimum path of length p × dp from an original aggregate size R. For a linear structure that is not convoluted (primary particles connected in a straight line without any bends and hence without any possibility of expanding), p × dp = R and disinterspersion (D.I.) = 0, that is, this aggregate structure (a rod) cannot expand through disinterspersion.
It is expected that a higher density aggregate would have a greater interspersion, but the topology (branching) might interfere with the ability to disintersperse or expand on swelling. A linear convoluted but unbranched structure, which can readily expand, will have a substructural minimum (or short-circuit) path, p = (R/dp)dmin based on fractal theory,40–43 where dmin is the minimum dimension that reflects the tortuosity of the aggregate independent of the connectivity, branching, or topology (c) such that the fractal dimension df = c × dmin. Hence, substituting the definition of p in terms of R, dp and dmin, in eqn (5), we get
|  | (6) | 
Furthermore, it is also known from fractal theory40–43 that the degree of aggregation z = (R/dp)df and that df = c × dmin. Substituting z for R/dp in eqn (6) and replacing df with dmin, we get
|  | (7) | 
On the other hand, this new model also indicates that nano-rod silicon or nano-platelet silicon (from clay) does not have the optimum topology/tortuosity for silicon anode materials that are subject to large volumetric expansion on lithiation; however, this needs to be tested. Isolated NPs, while individually can show better performance, possess poor connectivity in an electrode and will have a low density, leading to low specific capacity.16,44,45 Alternatively, if they are closely packed, then there is no possibility of accessing the surface of the nanoparticles and they will not accommodate expansion and contraction.
|  | (8) | 
In summary, it is proposed that aggregates of primary particles composing a network that satisfies the following three criteria can optimize anode performance:
(1) Thin SEI layers (minimize eqn (1)) and high transport rates (maximize eqn (4)),
(2) A high degree of interspersion (maximize eqn (7)), and.
(3) High density for high specific capacity, (maximize eqn (8)).
Based on the equations and the illustrations, we propose that ramified and hierarchical aggregates, that can be produced from various methods, form connected networks in composites,47 which have significant ability to expand without subjecting the links of the branched network to significant stress due to a high degree of disinterspersion.34 They are also known to display elasticity that can accommodate elastic strains greater than 300% (which is similar to the order of volumetric expansion upon full lithiation of Si) depending on the topology of the aggregates.36,37,48–53 Friedlander demonstrated that ceramic and metallic aggregates display similar elasticity.37,51–53 A similar process for solid aggregates in coal was also demonstrated35 and more recently Müller demonstrated disinterspersion for rigid aggregate molecules.39
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| Fig. 9 TEM micrographs of silicon particles showing (a) Type I and (b) Type II particles and (c) associated capacity versus cycle number.54 (d) A summary of the capacity of batteries for type I and type II particles versus cycle number. First three cycles are at C/20, while the remaining are at C/10. Table shows values for some of the features in the plot. | ||
| D, nm | z | P | R/D | d f ln(z)/ln (R/D) | c ln(z)/ln(p) | d min d f/c | Sz (1/dmin) | Disinterspersion z(1/e)(1−1/dmin))−1 | Density z(1−3/df) | Rate of Li+ diffusion (1/D2)/25 × 10−6 | SEI layer thickness (D)/50 | |
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Type I | 200 | 28 | 17 | 8 | 1.60 | 1.18 | 1.36 | 11.5 | 1.11 | 0.054 | 1 | 4 | 
| Type II | 50 | 253 | 70 | 20 | 1.85 | 1.30 | 1.42 | 49.5 | 2.52 | 0.031 | 16 | 1 | 
| Type III elemental | 10 | 25 | 4 | 4 | 2.32 | 2.32 | 1 | 25 | 0 | 0.386 | 10 ![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) 000 | 0.2 | 
Type II aggregates are more branched with a higher value for the connectivity dimension, c. The minimum path through the aggregates is more convoluted in Type II particles (a higher dmin). Using these structural features and applying the governing equations, it is likely that Type I particles will display good capacity retention at a high specific capacity. With lithiation cycles, Type II particles, which have a much higher degree of aggregation, should swell progressively with each new cycle, exposing more accessible surface for lithiation/SEI formation, eventually breaking the clusters apart. Fig. 9c shows the specific capacity change with cycle number for the aggregates (see summary in Fig. 9d). The first three cycles are at C/20 to aid the formation of the initial SEI layer which results in a capacity drop in both cases. The remaining cycles are at C/10. Type II particles have a greater initial specific capacity due to improved access to Si in the smaller primary particle size and high packing density and a greater drop in SEI formation followed by a plateau at a higher capacity. After the first 20–40 cycles, Type II particles show a rapid decline in capacity, potentially due to the primary particle clusters breaking apart and forming new SEI materials, which eventually leads to the observed drastic drop in specific capacity. While there is some matching between the estimated structural features and the observed electrochemical performance, it is not possible to fully predict the behavior due to lack of full structural information of these particles. As such, a detailed and reliable prediction of performance would require in operando measurements and X-ray scattering measurements which can directly determine the 3D structural parameters.40
In our previous work,27 we produced Si nanoaggregates by MTR at 950 °C using silica aggregates. The particles have a bimodal population, composed of smaller (14 nm) and larger particles (170 nm), as shown in Fig. 10a. The small particles are likely to show a low interspersion and high density, df, and connectivity, c, which means that they are topologically unable to structurally expand without breaking. The larger particles show high interspersion and can structurally expand, but low density/capacity. This implies that this material will have high initial capacity arising from the high density of smaller particles, but it would rapidly reduce due to their low interspersion. Subsequent cycling is likely to maintain the (low) capacity, mainly due to the larger particles withstanding the expansion but their low density results in lower capacity. Fig. 10b shows the capacity over 100 cycles, which fully matches the predictions. This closely follows the governing equations, which suggests that capacity retention correlates with interspersion and density, while capacity is related to particle size. Furthermore, this also provides confirmation that MTR is a promising method to produce desired Si structures, with a good control over properties.
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| Fig. 10 Bioinspired silica, reduced at 950 °C; (a) SEM micrograph and (b) capacity versus cycle number, image reproduced with permission from ref. 27. | ||
If we are able to use mass-produced commercial silica or custom silica with the desired structure, then MTR can produce the right types of Si that are suitable for high-performance in LIB anodes. Mass-fractal silica aggregates are often formed by solution (precipitated, colloidal, or silica gel) or flame (fumed) synthesis. Silica can also be produced using base catalysts leading to larger spherical and close to monodisperse particulate aggregates or independent silica spheres by the Stöber process. Fumed silica has extremely small silica primary particles and a typically high degree of aggregation while solution silica generally displays larger primary particle size and a lower degree of aggregation. A range of silica aggregate structures are possible with primary particle sizes from 1 nm to several microns and the degree of aggregation ranging from 1 to about 2000 with variable topologies (branch content and tortuosity).46
Future research should focus on two key aspects. Firstly, identifying and comparing methods to produce various hierarchical structures that maximise the criteria described above is important. While MTR is one such promising method, there are likely others too such as chemical vapor deposition and pyrolysis of silane gas, especially for producing controlled nanoparticles of desired sizes.54 A holistic comparison of these structures and methods of their production should be made on the basis of their multi-criteria performance metrics, scalability/manufacturability, environmental impact and economics.25 Considering a single criterion or not using an integrated approach can lead to unsurmountable hurdles in developing and commercialising promising technologies.57,58 Secondly, in-depth studies are required to understand the structural hierarchy in Si anodes and their performance. Developing links between processing, hierarchical structures and electrochemical performance will help create fundamental design criteria to improve performance. Specifically, a systematic mapping of structural features during the formation of such Si structures and in operando measurements of electrochemical performance is crucial. Examples include the use of a combination of in situ and in operando SAXS and diffraction to study the structures and their lithiation/delithiation, complemented by electron microscopy, spectroscopy and electrochemical testing. SAXS and USAXS can resolve the average structural features over thousands of nanoparticles on a second time scale. This information can be coupled with electrochemical measurements to understand the hierarchical structural basis for anode performance. It has been observed that during the charging/discharging cycles, isolated Si nanoparticles can aggregate and hence the performance changes dynamically. While the governing equations would not change in principle, the inputs based on the characteristics of the Si structures will change dynamically. A combination of in situ and in operando measurements discussed above would be valuable in investigating performance variations as a result of dynamic changes to the Si structure during cycling. Furthermore, Pair Distribution Function (PDF) analysis by X-ray diffraction provides information on chemical bonds (and speciation) from both the crystalline and amorphous components and hence is a powerful tool for in operando measurement of electrochemical processes in LIBs. While in operando PDF is yet to be used over lithiation cycles for hierarchical aggregates of Si, a study published recently on 100 nm Si NPs (not hierarchical aggregates) investigated just one cycle.59 This first in operando study demonstrates that such measurements are possible and contain important kinetic and mechanistic information concerning the lithiation process.
| Footnotes | 
| † Professor Gregory Beaucage sadly passed away in August 2025 while this manuscript was under revision.60,61 | 
| ‡ The authors contributed equally. | 
| This journal is © The Royal Society of Chemistry 2025 |