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Effective Transport Properties of Porous Electrochemical Materials — A Homogenization Approach

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Published 3 April 2014 © 2014 The Electrochemical Society
, , Citation A. Gully et al 2014 J. Electrochem. Soc. 161 E3066 DOI 10.1149/2.011408jes

1945-7111/161/8/E3066

Abstract

This study concerns the determination of effective transport coefficients for multiscale composite materials used in various electrochemical systems. The effective transport coefficients are indispensable in macroscale modeling of such systems. We propose an integrated approach which for a given two-phase or three-phase microstructure allows us to systematically determine the exact values of different effective transport coefficients such as diffusivity of a species or electric conductivity. In addition to electron microscopy, this approach combines state-of-the-art techniques of mathematical homogenization, image processing and numerical computation. When only partial information about the microstructure is available, rigorous upper and lower bounds are available on the effective transport coefficients and we demonstrate that the commonly used Bruggeman's formula may in fact violate the lower bound in some regimes. These upper bounds also allow one to quantify how much the transport properties of the material with a given composition could be improved. The proposed approach is illustrated by analyzing a three-phase electrode material of an actual Li-ion battery. We also quantify the uncertainty of the effective transport coefficients resulting from possibly imprecise information about the material properties of the individual phases and address the question concerning the importance of resolving all three phases.

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Mathematical modeling of electrochemical systems is both useful and necessary due to the high material cost associated with building and testing such systems. While the ideas described in this study are applicable to a broad range of electrochemical systems where diffusion in porous media plays a role, the focus of this investigation will be on Li-ion batteries. Their mathematical models are systems of differential and algebraic equations predicting the evolution of critical parameters characterizing the battery, and commonly track changes in lithium concentrations, current densities (both electric and ionic), and temperature. Such models inform the design of the control algorithms used in Battery Management Systems which control battery packs,5,10 for example in electric cars. In order for the mathematical model to predict battery functions of commercial interest, such as cycling performance and temperature distributions, it must be developed on length scales that can assess the battery as a whole (Figure 1(A)). On the other hand, description of the electrochemical processes based on first principles is available at the level of the microstructure only (Figure 1(B)). Given that the length scales characterizing the microstructure and the entire battery usually differ by more than one order of magnitude (the typical battery cathode or anode has a length scale of 50–100 μm, while the details of the corresponding microstructure may have elements smaller than 200 nm), resolving the relevant phenomena simultaneously at the micro- and macro-scale results in an intractable computational problem. This, in turn, necessitates formulating "effective" models, which are defined at the macro level only, where unresolved small-scale effects are represented through suitable effective transport coefficients and source terms in homogenized Partial Differential Equations (PDEs).11,35

Figure 1.

Figure 1. (A) Schematic of the battery at the macroscale where the entire cell is considered; at this level the negative and positive electrodes are viewed as homogeneous materials where effective transport coefficients are used to account for the complicated microstructure illustrated schematically in Figure (B). Here three distinct components are observed, namely, active particle ΩAP, polymer binder doped with carbon particles (binder) ΩB, and electrolyte ΩE. When considered individually, each component has a unique set of material properties which can very significantly between any two different components. For example, the difference of the electric conductivity between the binder and electrolyte is at least eight orders of magnitude.

The effective transport properties are defined such that the homogeneous material carries the same flux as the original composite material under the same imposed gradients. In other words, the effective transport coefficients represent replacing a highly complex heterogeneous composite material with a simple homogeneous material that has the exact same macroscale properties (Figure 2). As indicated schematically in Figure 1(B), a Li-ion battery cathode microstructure has three distinct phases: the electrolyte ΩE, active particles ΩAP, and carbon particle doped binder (binder) ΩB. Further, each of the three phases has a distinct set of individual transport coefficients. Mathematical homogenization as depicted in Figure 2 results in a much simpler homogeneous material, where only one effective transport coefficient is needed instead of three individual transport coefficients combined with the microstructure geometry to describe a transport process. Both the complicated microstructure (Figure 2(A)) and the homogenized equivalent (Figure 2(B)) have the same macroscale properties reflected in the effective transport coefficients, thus allowing much larger length scales to be accurately implemented in computational models.

Figure 2.

Figure 2. (A) An irregular periodic microstructure Ω0 featuring three phases with distinct transport coefficients represented by the subdomains Ω1, Ω2 and Ω3, where the geometry can be constructed with any combination of the three phases. (B) The corresponding homogenized material. From a macroscale point of view, both (A) and (B) have identical transport properties. The homogenized version reflects these transport properties as an effective coefficient.

The main goal of this contribution is to demonstrate how the state-of-the-art mathematical homogenization techniques combined with suitable imaging and computational tools can be employed to determine the effective transport coefficients of a given material with a complex microstructure based on the properties of the individual phases. In contrast to some earlier attempts in this direction,20,36,38 we will consider three-phase electrode materials.

The relevant effective transport coefficients, namely the effective diffusivity D*, electric conductivity σ*, and thermal conductivity k*, can be determined or approximated using a variety of approaches. Perhaps the most widely used approximation in the electrochemical literature is the Bruggeman formula.4 In the case of electric conductivity, it is given by

Equation ([1])

where σ* is the effective conductivity, σ1 is the conductivity of the conductive material, and ν1 is the volume fraction, or porosity, of the conductive material. A nearly identical equation exists to calculate the effective diffusion coefficient. Generally speaking, this approximation is accurate when a number of conditions are satisfied, namely, the volume fraction for the conductive phase is low, the conductive phase is always connected, and the non-conductive phase forms spherical inclusions. However, when volume fractions become larger, or if the connected pathways become complicated, as may happen in a Li-ion battery, accuracy is quickly lost.20,34 An application area where approaches based on Bruggeman's formula clearly are not refined enough concerns modeling Li-ion battery cells. While repeated cycling can significantly change the microstructure geometry and therefore also its transport properties, analysis based on Bruggeman's formula cannot capture such changes because the volume fractions remain essentially unaffected in this process. As a step to improve upon this popular formula, several recent studies on the effective transport coefficients of battery materials8,12,22,24,36-38,40 incorporate the concept of tortuosity which is essentially an estimation of connected path curvature. Tortuosity cannot be directly calculated even if the entire microstructure is known and the situation is further complicated by the fact that this concept is defined multiple ways in the literature. The tortuosity can in principle be calculated indirectly, by first finding the effective transport coefficients through other means and then doing a reverse calculation.22 However, if the objective is to calculate the effective transport coefficients of an electrode material, this then leads to a circular argument and defies the purpose of using the tortuosity to find the effective transport coefficients. Although tortuosity conveniently characterizes how difficult it is to find a pathway across a microstructure, it is the effective transport coefficient together with its dependence on the microstructure that are ultimately important. Systematic assessment of the predictions obtained based on Bruggeman's formula (1) in the light of the rigorous homogenization theory is the second main contribution of this study. We note that some insights concerning this problem were already discussed in 8, 14. Another approach for determining the effective transport coefficients of porous structures is related to the percolation theory and relies on Monte Carlo modeling. It assumes that the microstructure is formed from particles with a prescribed distribution of sizes and random locations. For each such microstructure in the ensemble, the transport problem is solved with standard methods and then the effective coefficients are evaluated using statistical techniques. We refer the reader to 7, 31 for recent work on such approaches.

Here we formulate the problem of calculating the effective transport coefficients of electrochemical materials in terms of modern homogenization techniques. This theory became mathematically uniform in the late 1980's and is well described in several monographs.6,29,39 In particular, we use the analytic continuation method proposed by Bergman, Milton, Golden and Papanicolaou1,17,25,27 which separates geometrical information from material properties in a mathematically precise calculation of the effective transport coefficients. Further, this formulation yields rigorous bounds which provide perspective on how well a given microstructure performs in comparison to optimal geometric configurations.

In addition to homogenization theory whose relevant aspects are reviewed in the section below, implementation of the proposed approach relies on the following key enablers:

  • high-resolution images characterizing the porous microstructure of the electrode material; such images can be obtained using advanced visualization techniques, such as the dual-beam Focused Ion Beam/ Scanning Electron Microscope system,
  • an image processing algorithm for the segmentation of the images into the different phases composing the electrode material, where periodicity may be enforced,
  • numerical technique for the solution of the PDE representing a suitably reformulated transport problem in the porous microstructure domain; this technique computes PDE problems defined on complex geometries obtained as a result of the image segmentation process.

While a detailed description of Focused Ion Beam (FIB) imaging techniques is beyond the scope of this paper, the image processing and numerical algorithms are described in section Enablers for Determination of effective Transport Properties of Composite Materials, and in the Analysis and Results section we apply the proposed methodology to determine the effective transport coefficients of an actual porous battery material and compare our findings with more standard approaches based on Bruggeman's formula. Discussion and final conclusions are deferred to the Conclusions section. Some more technical material concerning derivation of the rigorous bounds on the transport coefficients is collected in Appendix A, whereas in Appendix B we restate the main equations in the component-wise form.

Homogenization-Based Formulation of Diffusive Transport in Multiphase Media

In this section we develop a description of the conduction or diffusion in an inhomogeneous medium, such as a porous battery electrode material, which will allow for:

  • an efficient computation of the effective transport coefficients when complete information about the microstructure geometry is available,
  • derivation of different rigorous upper and lower bounds on the effective transport coefficient when only partial information about the microstructure is available.

Without loss of generality, we will focus here on characterizing the effective electric conductivity σ* (hereafter, an asterisk will denote an effective property). Denoting the electric current j and the potential ϕ, the homogenized Ohm's law can be expressed in the anode or cathode, respectively, in Ω or Ω+, cf. Figure 1(A), as

Equation ([2])

where ⟨ · ⟩ is the spatial average over a periodic microstructure Ω0 and B represents effects that are not related to the electric potential. To clarify, equation (2) only considers electric current, i.e., current induced by the transport of electrons, and does not account for the ionic current induced by the transport of chemical species. We emphasize that the same formalism as described above can be used to characterize other effective transport coefficients relevant for modeling electrochemical systems, such as diffusivity of species or thermal conductivity. We make the following assumptions concerning the microstructure domain Ω0 (see Figure 2).

Assumption 1

  • (a)  
    Ω0 is periodic in all three directions,
  • (b)  
    Ω0 is a union of three subdomains Ω1, Ω2 and Ω3 corresponding to three distinct phases, i.e., Ω0 = Ω1∪Ω2∪Ω3,
  • (c)  
    each of the phases Ωj, j = 1, 2, 3, is isotropic,
  • (d)  
    the individual phases are characterized by non-zero conductivity coefficients σj, j = 1, 2, 3, such that
    Equation ([3])
    where
    Equation ([4])
    is the characteristic function of the j-th phase (" := " means "equal to by definition").

In the case of a Li-ion battery (cf. Figure 1), the three subdomains can be identified with the different phases as Ω1 = ΩB, Ω2 = ΩAP and Ω3 = ΩE.

Exact evaluation of effective transport coefficients

We now develop the mathematics for homogenizing the electric conductivity of a three-phase porous electrode to obtain an effective electric conductivity using the analytic continuation method,2,17,18,26 keeping in mind that the derivation for the effective diffusivity, ionic conductivity, and thermal conductivity are all mathematically identical39 to the one for the effective electric conductivity. Let J and E be the current and electric fields, where E is the negative gradient of the electrical potential ϕ, i.e., . Then, locally, we have following constitutive law

Equation ([5])

where σ(x) is given in (3). We note that, since the electric field is the negative gradient of the electrical potential and there is no free charge, we can write

Equation ([6])

For brevity, hereafter we will not indicate the dependence on the independent variable x. Let

Equation ([7])

where ek is a unit vector in the k-th direction for k = 1, 2, 3. The effective conductivity, which is a diagonal tensor, is then defined to be

Equation ([8])

From this we can write

Equation ([9])

and then define . This allows us to strictly examine the kk-th component of the effective conductivity tensor and simplifies the notation. Thus, using (3) we can rewrite equation (9) as σ* = ⟨eTk1χ1 + σ2χ2 + σ3χ3)E⟩. Due to the homogeneity of the effective transport coefficients, i.e., the property that σ*(λσ1, λσ2, λσ3) = λσ*(σ1, σ2, σ3), σ* only depends on the ratios h1 := σ13 and h2 := σ23, and we define the function

Equation ([10])

Although strictly real values σj, j = 1, 2, 3, will be used to calculate the effective conductivity of the porous electrode, mathematically, we need not make such restrictions and the σj values could in principle be complex numbers. Thus, the two main properties of m(h1, h2) are that it is analytic off the interval ( − , 0] in the h1-plane and h2-plane, and that it maps the upper half plane to the upper half plane,1,15,17 so that it is an example of a Herglotz or Stieltjes function. Therefore, to be mathematically guaranteed here that the effective conductivity is well defined and unique for real conductivity values, each material phase must be characterized by a positive, non-zero conductivity σj. While in many consistent models, the electrolyte is often assumed to have an electrical conductivity of zero, within the proposed framework an effective conductivity cannot be defined if the conductivity of one of the phases is exactly zero, and therefore we must consider a very small, yet strictly positive conductivity value for the electrolyte. Certain trivial microstructures exist, such as, e.g., parallel slabs, where an effective conductivity tensor can still be uniquely determined if one material has a conductivity identically equal to zero; however, this may not be universally true for all microstructures.

For convenience, let s1 := 1/(1 − h1) and s2 := 1/(1 − h2) and then define

Equation ([11])

which is now analytic off [0, 1] in the s1–plane and s2–plane. From here, we must now obtain a resolvent representation for E corresponding to (7) and obeying conditions (6). First, it is observed that implies that . Then, we let W be a vector field representing the fluctuations in the electric field, such that ⟨W⟩ = 0, and we suppose that E = ek + W. Using (3) we thus obtain

Equation ([12])

After multiple manipulations involving algebraic transformations, application of the operator and the invoking identity χ1(x) + χ2(x) + χ3(x) = 1 true for all x ∈ Ω0, we obtain

Equation ([13])

where the inverse Laplacian Δ− 1 involves periodic boundary conditions. Following 1619, we introduce the operator , defined for an arbitrary vector field z as , which allows us to express the resolvent of the electric field E as

Equation ([14])

in which I is the identity operator. Then, using this representation to express F(s1, s2) we find

Equation ([15])

This formulation for F(s1, s2) now has two purposes. The first is that this provides a way to directly calculate the effective conductivity. Recalling that F(s1, s2) = 1 − σ*/σ3 and that is the kk-th component of the effective conductivity tensor, we see that

Equation ([16])

A quick check indicates that formula (16) collapses to the correct solution if material three and material two occupying, respectively, Ω3 and Ω2 have identical properties, thus making it a composite of two materials, and in the trivial case when all three materials have the same properties. A computationally efficient approach to evaluate this expression for experimentally obtained microstructures (described in terms of functions χ1, χ2 and χ3) will be introduced in the next section. The second purpose behind relation (15) is that, as shown below, it can be used to derive rigorous upper and lower bounds on the effective conductivity applicable when only partial information about the microstructure is available.

Rigorous bounds on the effective transport coefficients

To obtain the bounds for a three-phase material,15 a suitable integral representation and an expansion about a homogeneous material must be obtained for equation (15). Here we simply state the rigorous bounds and defer a more complete derivation to Appendix A.

The Wiener or elementary bounds for a three phase material are found using only information about the volume fractions of the three phases, i.e., p1, p2, and p3, along with the individual conductivities of each phase, which are σ1, σ2, and σ3. Assuming real values for σ1, σ2, and σ3, this results in bounds on σ*, where for a three-phase material we have

Equation ([17])

The microstructure configurations achieving these bounds are discussed in the Analysis and Results section. Since we will also consider two-phase materials in that section, we state here the corresponding rigorous Wiener bounds for the two-phase case, namely

Equation ([18])

where σ1 and σ2 still have real values and p1 + p2 = 1.

If more information about the microstructure geometry is available, namely, it can be further assumed to be statistically isotropic, the Hashin-Shtrikman or isotropic bounds can be found. Assuming σ1 ⩽ σ2 ⩽ σ3, the Hashin-Shtrikman bounds for a three-phase material are

Equation ([19])

which are optimal for certain volume fractions.28 Essentially, the volume fractions of any one phase cannot be extremely small. For a battery microstructure, all phases have volume fractions well within the appropriate range and these bounds (19) are optimal. Although we do not use the rigorous Hashin-Shtrikman bounds for a two-phase material in any subsequent section, we list them here for completeness. For a two-phase material where σ1 ⩽ σ2 and p1 + p2 = 1, the Hashin-Shtrikman bounds are

Equation ([20])

which are optimal for all volume fractions.

Enablers for Determination of Effective Transport Properties of Composite Materials

In this Section we describe the computational tools required to implement the concepts introduced in the previous section to calculate of the effective transport coefficients for a 3D battery microstructure. High-resolution microstructures images can be obtained with the dual-beam focused ion beam (FIB) technique combined with scanning electron microscopy (SEM). This approach is suitable for serial sectioning of, for example, the electrodes in solid oxide fuel cells (SOFC)32 and Li-ion batteries.13 Without loss of generality, hereafter we will focus on analyzing the microstructure of a custom manufactured cathode of a Li-ion battery. With the use of the dual-beam FIB/SEM one can obtain the slice spacing of less than 20 nm which is comparable with the pixel resolution in the 2D image plane.21 This feature is especially important for our study, as it allows us to construct isotropic computational grids (with the same node spacing in different directions). In the present study a Zeiss NVision 40 dual-beam FIB/SEM instrument was used for serial sectioning. A thin layer of Tungsten was initially deposited on the sample surface to protect the sample from preferential thinning of soft phases and to reduce the curtaining effect. High-energy focused Ga ion beam (30 keV incident energy) with small spot size was generated and the localized material was removed by the interaction of these high-energy ions with the target sample. In total, 240 serial images were obtained with 50 nm spacing between each slice from a volume of 14.58 μm × 18.65 μm × 12 μm. The series of images was then processed as described below to separate the components of the microstructure, namely, the active material (LiNi1/3Mn1/3Co1/3O2), the acetylene black with binder, and the voids (normally filled with the electrolyte). The resulting discrete microstructure domains were then used to solve the required PDE problems as explained below in subsection Numerical Solution of PDE problems. Resolution of the FIB imaging technique is certainly a source of possible errors. However, based on our extensive tests, we concluded that these errors are in fact dominated by inaccuracies resulting from other sources, most importantly, the coarsegraining of the microstructure required for the solution of the PDE problem (more information about this aspect is provided below).

Processing of experimentally obtained microstructure images

In order to compute the effective transport coefficients for a battery microstructure, the sequential set of FIB images must be digitally segmented into the three components of a Li-ion battery. A typical FIB image in a cross-sectional plane is shown in Figure 3(A), and the red square (with dimensions 512 × 512 pixels) marks the region on which we will focus. This region is the same for each individual image in the sequential set and truncation of the images to this region ensures that only battery microstructure is captured. Before the images are segmented, we must also consider the boundary conditions imposed by Assumption 1(a) in the previous section that require the battery microstructure to be periodic in all three directions. In principle, a microstructure can always be assumed to be periodic; however, when images are stacked side-by-side, sharp jump discontinuities are observed along the edges (Figure 3(B)). Therefore, as an optional step before segmentation, periodized microstructure images can be smoothed near the edges, reducing the jump discontinuities (point (i) below). Processing of the FIB images is done using an in-house MATLAB code that performs the following sequence of steps:

Figure 3.

Figure 3. (A) A raw two-dimensional slice (one of 240) of the three dimensional battery microstructure (the resolution is 1024 × 768 pixels). The red square has a dimension of 512 × 512 pixels and is then extended periodically in (B), where sharp edge discontinuities are observed. After the optional smoothing step, in (B(i)) the image is smoother along the edges. The results of thresholding used to identify the three phases (step (ii)) are shown in (C), whereas figure (D) represents the effect of downsampling the microstructure to resolution 51 × 51 (step (iii)) performed on the region marked by the red square in (C). After obtaining the numerical solution, suitable post-processing allows the current fields to be observed in the battery microstructure in (E).

Step (i)— smoothing (optional): a 3D image is reconstituted from the sequential set of 2D SEM images and then smoothed near the edges in all three directions; this is accomplished by treating the gray scale of the 3D image as a function of x1, x2, and x3, and then applying the smooth image periodization algorithm of Moisan;30 it is based on Fourier filtering and produces a 3D image with smoothed edges that is closest to the original 3D image in a suitable sense (Figure 3(B(i))); the smoothed 3D image is then again recast as a sequential set of 2D images; the effect of this optional smoothing step on the computed effective transport coefficients will be studied in the Analysis and Results section,

Step (ii)— thresholding: thresholding combined with gradient analysis is performed using the image processing toolbox available in MATLAB,23 and allows one to segment the sequential set of periodized 2D images into three distinct phases, see Figure 3(C); more specifically, the in-house algorithm identifies several key aspects of an electrode microstructure taking advantage of the following features: (a) the active particles are relatively smooth, lighter on a gray-scale threshold, and have distinct vertical groves as a result of the FIB process, (b) the pore space (or electrolyte) has a very distinct low value on the gray-scale, and (c) the carbon-doped binder typically has a medium gray-scale value with a "cobweb" structure that has many sharp edges; although the algorithm includes features such as an analysis of gradient values, it is still critical to choose appropriate gray-scale threshold values and any error produced during segmentation is typically a result of using inappropriate threshold values; in addition, if the FIB process has artificially produced large regions where the carbon-doped binder phase has larger (or brighter) gray-scale value than the active particles, the algorithm still performs quite well, but has to be used with greater care — controlling variances in the FIB imaging process is especially important in this regard,

Step (iii)— compression: the sequential set of 2D segmented periodized images is reconstituted into a 3D image and then compressed into a manageable size ensuring that the resulting computational problem is tractable; this downsampling process is done using a nearest neighbor 3D stencil with the selection based on the component that occurs most frequently (an average value stencil cannot be applied here, because three components are being considered); in the present study the final size is 51 × 51 × 51 voxels and the corresponding slice of the 3D image is shown in Figure 3(D).

Although it does not significantly alter the volume fractions of the different phases, the downsampling introduced in step (iii) above may lead to some loss of information, especially as regards transport in the narrowest pathways. While this can be rather difficult to quantify precisely, our tests indicate that downsampling errors are in fact significantly larger than the errors related to FIB imaging and image segmentation. On the other hand, because it involves spatial averaging, downsampling may in the mean sense cancel errors introduced during image segmentation. Providing an accurate characterization of this effect is an interesting open problem for future research.

Numerical solution of PDE problems

We now present a computational algorithm which will allow us to conveniently evaluate expression (16) for the effective conductivity by employing standard numerical techniques. The idea is to break the process into steps that can be easily implemented using tools of finite-element analysis, such as available in COMSOL.9 Information about the microstructure in the form of the compressed 3D image (Figure 3(D)) is imported as functions χ1, χ2 and χ3 using interpolation routines. Writing the operator out explicitly, equation (14) becomes

Equation ([21])

Introducing an auxiliary variable (potential) , equation (21) can be recast as the following system

Equation ([22a])

Equation ([22b])

which essentially reduces the problem to the solution of an elliptic boundary-value problem (22a). We reiterate that equation (22a) is subject to periodic boundary conditions (cf. Assumption 1(a)). Then, the kk-th component of the effective conductivity tensor can be easily evaluated as

Equation ([23])

(an explicit representation of equations (21)–(23) in x, y, and z coordinates is given in Appendix B). Solution of system (22a) is obtained by employing the interactive mode in COMSOL which discretizes the problem using finite elements on a 51 × 51 × 51 grid with the order of interpolation chosen adaptively. The resulting algebraic system is then solved using the solver MUMPS available in COMSOL which can take advantage of shared-memory multicore architectures. Due to the high variability of the coefficients in system (22a), convergence of iterations needs to be closely monitored. In all results reported in the next section, convergence needed to determine the effective transport coefficients with the required number of the significant digits was typically achieved within 25 iterations. An average run takes approximately two hours using 32 2.4 GHz AMD Opteron processors and requires about 35 Gb of RAM memory.

It is in this fashion that the effective conductivity tensor is found for any geometric configuration that has three phases, each with its own individual conductivity values. This solution is found without having to specifically track the electric and current fields within the composite material; however, these fields can be studied a posteriori via suitable post-processing (cf. Figure 3(E)). We note that while the effective transport coefficients can be computed in a variety of ways, the proposed approach has the advantage of separating the geometric information about the microstructure from the material properties. The expressions used to derive the lower and upper bounds in the section on homogenization also share this property.

Analysis and Results

In this Section we illustrate the approaches developed in our study and compare them with some commonly used classical methods. General considerations are presented below and are followed by an application of these approaches to characterize the effective transport coefficients for an actual Li-ion battery.

Comparison of analytical bounds and bruggeman's formula

Although one of the key novelties of this study is the characterization of three-phase composites, some of the essential features of the proposed approach are already evident in the two-phase case which is easier to illustrate. For clarity, we will thus use the two-phase setting to make some of the key points.

In order to demonstrate the relationship between the microstructure geometry and the corresponding effective transport coefficients, Figure 4 analyzes three hypothetical composite materials in 2D, where each composite has identical volume fractions, but a different microstructure geometry. We see that the corresponding effective conductivities are in fact quite different and span a broad range of values between the rigorous lower and upper bounds, which are the corresponding Wiener bounds (18) for a two-phase composite. These bounds on the achievable range of effective transport coefficients are, in turn, quite different from the conductivities of the two materials. We also emphasize that two of the microstructures yield effective transport coefficients quite different from the constant value predicted by Bruggeman's formula (1).

Figure 4.

Figure 4. Comparison of the effective transport coefficients of three two-phase composite materials having different microstructures with Bruggeman's formula (1) and the corresponding rigorous two-phase Wiener bounds (18). Transport is assumed in the horizontal direction.

While the results presented in Figure 4 correspond to a fixed contrast h = σ12 = 10, it is also interesting to evaluate how the allowed range of effective transport coefficients varies with contrast h. To illustrate this, Bruggeman's formula (1) together with the upper (17) and lower (18) two-phase Wiener bounds can be rewritten as functions of the contrast h in the general form σ* = σ2f(h) as follows

Equation ([24])

Equation ([25])

Equation ([26])

These relations are shown in Figure 5(A) for arbitrary volume fractions of p1 = p2 = 1/2 and conductivity σ2 = 1, and in Figure 5(B) corresponding to volume fractions from our sampled electrode (Table I) and an approximate electrolyte conductivity from the literature (Table II). Here, phase 1 is assumed to be the combined volume fractions of the active particles and carbon-doped binder, whereas phase 2 is the volume fraction of the electrolyte. Thus, p1 = 0.5953 and p2 = 0.4047, respectively, and σ2 = 1.0 × 10− 8 S · cm− 1. In Figures 5(A) and 5(B) we see that the gap between the upper and lower Wiener bounds increases in proportion to h and, as expected, the two bounds collapse for h = 1, which corresponds to the homogeneous material (σ1 = σ2). We also note that for large contrasts, the predictions of Bruggeman's formula are quite close to the upper bound. On the other hand for low contrasts, these predictions deviate from the upper bound and, for certain values of σ1 > σ2, become incorrect as they drop below the lower bound. Predictions of Bruggeman's formula remain unfeasible when σ1 ⩽ σ2, which is a consequence of the assumption underlying Bruggeman's formula that phase 1 is dominating.4,39

Table I. Volume fractions of the original segmented microstructure (Figure 3(C)) and the compressed segmented microstructure (Figure 3(D)) with and without smoothing.

 Electrolyte Volume FractionBinder (with carbon) Volume FractionActive Particle Volume Fraction
Original0.40470.25350.3418
Original (smoothed)0.40120.26610.3327
Compressed0.40910.24290.3480
Compressed (smoothed)0.40540.25330.3413

Table II. Transport coefficients characterizing the individual phases in the different cases considered, with and without smoothing of the periodized microstructure.

 Li-ion DiffusionElectrical ConductivitySmoothed Microstructure?
 [cm2 · s− 1][S · cm− 1][yes/no]
CASE A   
Electrolyte1.4 × 10− 51.0 × 10− 8 
Binder (with carbon)1.0 × 10− 80.50no
Active Particle1.0 × 10− 70.20 
CASE B   
Electrolyte1.4 × 10− 51.0 × 10− 8 
Binder (with carbon)1.0 × 10− 130.50no
Active Particle1.0 × 10− 70.05 
CASE C   
Electrolyte1.4 × 10− 51.0 × 10− 10 
Binder (with carbon)1.0 × 10− 130.50no
Active Particle1.0 × 10− 110.05 
CASE D   
Electrolyte1.4 × 10− 51.0 × 10− 8 
Binder (with carbon)1.0 × 10− 80.50yes
Active Particle1.0 × 10− 70.20 
CASE E   
Electrolyte1.4 × 10− 51.0 × 10− 8 
Binder (with carbon)1.0 × 10− 130.50yes
Active Particle1.0 × 10− 70.05 
CASE F   
Electrolyte1.4 × 10− 51.0 × 10− 10 
Binder (with carbon)1.0 × 10− 130.50yes
Active Particle1.0 × 10− 110.05 
Figure 5.

Figure 5. Dependence of two-phase Wiener bounds (25)–(26) and Bruggeman's formula (24) on contrast h = σ12 for (A) arbitrary volume fractions p1 = p2 = 1/2 with σ2 = 1 and (B) volume fractions p1 = 0.5953 and p2 = 0.4047 corresponding to an actual electrode material with σ2 = 1.0 × 10− 8.

Evaluation of effective transport coefficients for a three-phase Li-ion battery

In this Section we use the framework developed above to compute the effective electric conductivity and diffusivity of a porous electrode of an actual Li-ion battery. This battery electrode is assumed to consist of three phases, namely, the electrolyte, active particles and carbon-doped binder. The methodology employed to obtain the microstructure images used in our study was described in the previous section. The volume fractions of the three phases obtained after image processing with and without optional smoothing are listed in Table I. As regards the transport properties of the individual phases, even significant uncertainties are not uncommon in the literature,33 and one of the goals of this study is to quantify the effect of this uncertainty on the effective transport coefficients computed with the homogenization approach. Another objective is to assess the importance of smoothing the periodized microstructure (cf. step (i) in the previous section). To address these issues in a systematic manner, we assume that the transport coefficients of the dominating phase (the electrolyte for the Li-ion diffusion and the binder with carbon for the electric conduction) are known exactly, and a range of different values is considered for the transport coefficients of the remaining phases. The calculations are performed with smoothed and nonsmoothed microstructure which leads to six distinct cases (A,D), (B,E) and

(C,F) corresponding to decreasing values of the transport coefficients in the nondominating phases, in the non-smoothed and smoothed setting. The data characterizing the different cases is collected in Table II, whereas the computed effective transport coefficients are listed in Table III together with the associated lower and upper bounds and the predictions based on Bruggeman's formula (1). As regards the effective electrical conductivity, we also report the results of applying Bruggeman's formula with the assumption that the binder and active particle are combined into one phase, so that

Equation ([27])

in relation (1). Homogenization calculations reported in Table III were performed assuming transport in the direction x1 (i.e., k = 1 in equation (16)). To assess to what extent the microstructure considered here is actually isotropic, in CASE B we performed the calculations assuming independent transport in the three different directions. The obtained standard deviation is less than 6% of the mean, indicating that the microstructure anisotropy does not in fact play a significant role. The results for cases A, B and C are plotted in Figure 6 employing the logarithmic scale, useful to assess how the effective properties compare with the rigorous bounds, and also the linear scale, to emphasize the differences between the different approaches (since the results obtained with the smoothed periodized microstructure differ very little, we do not present separate plots for cases D, E and F).

Table III. The effective Li-ion diffusivity and electrical conductivity obtained for the Li-ion electrode together with the corresponding upper and lower bounds and the predictions of Bruggeman's formula for different cases defined in Table II. Except for CASE B, all homogenization calculations are performed assuming transport in the direction x1.

 Effective Li-ion DiffusionEffective Electrical Conductivity
 [cm2 · s− 1][S · cm− 1]
CASE A  
Homogenization3.4 × 10− 60.12
Bruggeman3.7 × 10− 60.060
Bruggeman (combined, cf. eq. (27))0.056
Elementary Lower Bound3.6 × 10− 82.4 × 10− 8
Elementary Upper Bound5.8 × 10− 60.19
Isotropic Lower Bound7.1 × 10− 85.3 × 10− 8
Isotropic Upper Bound4.5 × 10− 60.16
CASE B  
Homogenization (direction x1)3.4 × 10− 60.072
Homogenization (direction x2)3.0 × 10− 60.077
Homogenization (direction x3)3.2 × 10− 60.068
Bruggeman3.7 × 10− 60.060
Bruggeman (combined, cf. eq. (27))0.044
Elementary Lower Bound4.1 × 10− 132.4 × 10− 8
Elementary Upper Bound5.8 × 10− 60.14
Isotropic Lower Bound1.0 × 10− 125.3 × 10− 8
Isotropic Upper Bound4.5 × 10− 60.11
CASE C  
Homogenization3.3 × 10− 60.070
Bruggeman3.7 × 10− 60.060
Bruggeman (combined, cf. eq. (27))0.044
Elementary Lower Bound4.1 × 10− 132.4 × 10− 10
Elementary Upper Bound5.7 × 10− 60.14
Isotropic Lower Bound9.9 × 10− 135.3 × 10− 10
Isotropic Upper Bound4.4 × 10− 60.11
CASE D  
Homogenization3.2 × 10− 60.13
Bruggeman3.6 × 10− 60.064
Bruggeman (combined, cf. eq. (27))0.057
Elementary Lower Bound3.5 × 10− 82.5 × 10− 8
Elementary Upper Bound5.7 × 10− 60.20
Isotropic Lower Bound6.8 × 10− 85.4 × 10− 8
Isotropic Upper Bound4.4 × 10− 60.16
CASE E  
Homogenization3.2 × 10− 60.075
Bruggeman3.6 × 10− 60.064
Bruggeman (combined, cf. eq. (27))0.045
Elementary Lower Bound3.9 × 10− 132.5 × 10− 8
Elementary Upper Bound5.7 × 10− 60.14
Isotropic Lower Bound9.8 × 10− 135.4 × 10− 8
Isotropic Upper Bound4.4 × 10− 60.11
CASE F  
Homogenization3.1 × 10− 60.075
Bruggeman3.6 × 10− 60.064
Bruggeman (combined, cf. eq. (27))0.045
Elementary Lower Bound3.9 × 10− 132.5 × 10− 10
Elementary Upper Bound5.7 × 10− 60.14
Isotropic Lower Bound9.4 × 10− 135.4 × 10− 10
Isotropic Upper Bound4.4 × 10− 60.11
Figure 6.

Figure 6. Results from Table III for cases A, B and C (cases D, E, and F differ very little and are not shown). In order to assess the effect of different material properties of the individual phases (cf. Table II), the logarithmic and linear plots span the same ranges of the effective conductivity and diffusivity.

In Table III and Figure 6 we observe that the computed effective diffusivities and conductivities are in the different cases within 20%–30% of saturating the isotropic upper bounds, meaning that the microstructure sample considered in our study is close to having optimal transport properties. As regards the effect of the uncertainty characterizing the properties of the individual phases, we note that even though the diffusivities of the binder and the active particle are allowed to vary by several orders of magnitude, the resulting effective diffusivity changes only by less than 5%. On the other hand, this effect is more pronounced in regard to the effective electrical conductivity which changes by more than 40% when the conductivities of the electrolyte and the binder are decreased (cf. Table II). Smoothing of the periodized microstructure has a small effect decreasing the effective Li-ion diffusivity (by about 5%) and increasing the effective electrical conductivity (by about 6%). Finally, concerning comparison with Bruggeman's formula (1), we observe that this formula tends to overestimate the effective Li-ion diffusivity by up to 14% and underestimate the effective electrical conductivity by up to 50%, with lumped formula (27) yielding even worse results.

Conclusions

In this study we have developed a systematic framework for the characterization of the effective transport properties of composite materials used in electrochemical applications. It relies on integration of state-of-the-art methods of electron microscopy (FIB), applied mathematics (homogenization theory) and scientific computing (image processing and numerical PDEs). The approach proposed is rigorous which distinguishes it from the heuristic Bruggeman's formula typically used in electrochemical applications, and in our example in the previous section we highlight the differences between the predictions of the two methods. In relying on the mathematical theory of transport processes, our approach does not make any reference to the rather imprecisely defined concept of tortuosity. We demonstrated that the effective transport coefficients obtained with the proposed approach are rather weakly affected by the uncertainty of the transport properties characterizing the individual nondominating phases. We also showed that Assumption 1(a) about the periodicity of the microstructure, although essential to the formal derivation of our approach, does not play a significant role in practice.

The main application of the proposed framework is to systematically quantify the impact of different microstructures on the performance of electrochemical systems. For example, one can assess how close the actual transport properties of a given porous microstructure are to the maximum achievable limits represented by the rigorous upper bounds. In addition, it is well known that repeated cycling of a Li-ion battery may irreversibly change its microstructure. By analyzing microstructure images before and after cycling our method will allow us to rigorously quantify the impact of these microstructural changes on the transport properties of the material, and hence also on the performance of the battery. We emphasize that, since volume fractions remain virtually unaffected during such microstructural changes, these effects cannot be in fact captured by Bruggeman's formula. Investigations along these lines are already underway and results will be reported in the near future. In addition, the effective transport coefficients computed as proposed in this investigation will play an important role in the multiscale simulation studies of the performance of an entire battery cell. This work is already in progress and comparison with actual experimental data will allow us to validate the new method with regard to traditional approaches.

At present, the main factor limiting the accuracy of the proposed approach is the need to downsample the miscrostructure, so that the PDE problem is computationally tractable. We emphasize, however, that this limitation is not fundamental and arises when one solves the problem using commonly available computational resources such as a high-end multiprocessor workstation. Downsampling may not be required when the PDE problem is solved on a suitably large "supercomputer", in which case however software tools other than COMSOL would be needed. Another technical aspect of the proposed framework requiring further study is the sensitivity of the results to the possible under-resolution of the FIB images.

Acknowledgments

The authors are grateful to Gianluigi Botton, Gillian Goward and Ion C. Halalay for assistance and many stimulating discussions. The electron microscopy data included in this paper was acquired at the Canadian Centre for Electron Microscopy, a national facility supported by the Natural Sciences and Engineering Research Council of Canada (NSERC) and McMaster University. Funding for this research was provided by Automotive Partnership Canada (APC) and General Motors of Canada.

: Appendix A

Appendix. Derivation of Rigorous Bounds

To obtain the bounds for a three phase material,15 let us first consider the function analogous to (11) for a two-phase material,1 namely G(s) := 1 − m(h), where s := 1/(1 − h) and h := σ12, which is analytic off [0, 1] in the s–plane. Here we briefly consider a two-phase material, because the integral representation is easier to define and can then be easily extrapolated to a three-phase material. It was proven1,17 that G(s) has the following representation

Equation ([A1])

where μ is a positive measure on [0, 1]. Formula (A1) separates the information about the material properties encoded in s from information about the microstructure geometry contained in μ, a spectral measure of the operator . Information about the geometry, expressed though a number of statistical assumptions, is incorporated into μ via its moments μn = ∫10zndμ(z) which can be calculated from the correlation functions of the composite medium as . This integral representation will now be adapted below to find bounds for a three-phase material.

For simplicity, we now assume that the σj values are strictly real (derivation of the general complex-valued case can be found in Ref. 15). When |s1| > 1 and |s2| > 1, F(s1, s2) has the following expansion about the point s1 = and s2 = , which characterizes a homogeneous medium,

Equation ([A2])

in which the coefficients are given in terms of the correlation functions and where q = 0, 1, 2, 3 and w = 0, 1, 2, 3 such that q + w = 3. Rewriting this expression to separate terms containing only s1 and χ1, or s2 and χ2, we get

Equation ([A3])

where

Equation ([A4])

Thus, F1(s1) and F2(s2) have the integral representations, similar to equation (A1),

Equation ([A5])

where μ1 and μ2 are positive measures on [0, 1]. Similar to the two-component material version (A1), these integral representations (A5) separate the information about the material properties contained in s1 and s2 from information about the composite geometry contained in μ1 and μ2, which are spectral measures of the operators and , respectively. Again, statistical assumptions about the geometry are incorporated into μ1 and μ2 via their moments μ1, n = ∫10zn1μ1(dz1) and μ2, n = ∫10zn2μ2(dz2), which can be calculated based on the correlation functions of the composite medium, with and .

Wiener Bounds

To obtain the elementary bounds for a three-phase material, only the volume fractions of the three components need to be known along with the material properties incorporated into s1 and s2. Letting p1, p2, and p3 = 1 − p1p2 be the volume fractions of the three materials, with the properties ⟨χ1⟩ = p1 and ⟨χ2⟩ = p2, we observe that F(s1, s2) is known only to first order, and the second order terms, including the cross-term, in equations (A2) and (A3) cannot be evaluated. Thus, F(s1, s2) to first order is strictly expressed by the first-order truncations of F1(s1) and F2(s2). To find the upper bound on σ*, we now minimize F(s1, s2) with respect to all admissible geometries, cf. (10)–(11), and since for fixed p1 and p2 it is known to first order, then F(s1, s2) is minimized by separately minimizing the first-order truncations of F1(s1) and F2(s2) with respect to all admissible geometries represented by measures dμ1 and dμ2

Equation ([A6])

The minimums for F1(s1) and F2(s2) are then obtained by letting μ1 = p1δ0 and μ2 = p2δ015 in relations (A5). Thus,

Equation ([A7])

To find the lower bound, consider the auxiliary function1

Equation ([A8])

which has the same analytical properties as F(s1, s2), where t1 := 1 − s1 and t2 := 1 − s2. Similar to F(s1, s2), has the first-order truncated expansion of

Equation ([A9])

and thus using the same argument as before

Equation ([A10])

Putting these bounds together results in the elementary, or Wiener, bounds on σ* for a three component material

Equation ([A11])

The microstructure configurations achieving these bounds are discussed in the Analysis and Results section.

Hashin-Shtrikman Bounds

If more information about the microstructure geometry is available, namely, it can be further assumed to be statistically isotropic, additional correlation terms can be found in expansion (A2) for F(s1, s2) which then becomes15

Equation ([A12])

where d is the space dimension (for a battery microstructure d = 3) and again where q = 0, 1, 2, 3 and w = 0, 1, 2, 3 such that q + w = 3. Since the expansion truncated at the second order now has the non-zero cross-term (2p1p2)/(ds1s2), it is more convenient to consider the relation

Equation ([A13])

where H(s1, s2) again has the same analytic properties as F(s1, s2), but now has the expansion

Equation ([A14])

in which the cross-term with the denominator (ds1s2) has been eliminated under this transformation. Thus, similar to before, H(s1, s2) = H1(s1) + H2(s2) + ... and the minimum of H(s1, s2) is achieved when both H1(s1) and H2(s2) separately achieve minimums. A convenient way of including the second-order expansion terms so that minimums can be found3 is to use the transformations J1(s1) := 1/p1 − 1/(s1H1(s1)) and J2(s2) := 1/p2 − 1/(s2H2(s2)) which again have the same analytic properties as H1(s1) and H2(s2). Therefore, under these transformations, the second-order terms reduce to first-order terms only, and

Equation ([A15])

Then, using the analogous integral representations as in equation (A5), the minimum for J1(s1) and J2(s2) with respect to all admissible geometries are then obtained with the measures δ0/(dp1) and δ0/(dp2).15 Finally, mapping back to H1(s1) and H2(s2), we observe that

Equation ([A16])

To obtain the other bound, we use another auxiliary function ,1 where y2 := 1/(1 − σ21) and y3 := 1/(1 − σ31). Then, in analogy to the argument above, the following relation is found

Equation ([A17])

In this way, when σ1 ⩽ σ2 ⩽ σ3, the Hashin-Shtrikman bounds for a three component material are found

Equation ([A18])

which are optimal for certain volume fractions.28 Essentially, the volume fractions of any one phase cannot be extremely small. For a battery microstructure, all phases have volume fractions well within the appropriate range and these bounds (A18) are optimal.

: Appendix B

Appendix. Component-wise Representation of Equations (21)–(23)

For completeness, an explicit representation of equations (21)–(23) is given below in terms of their x, y, and z components. Rewriting operator in terms of its components, letting C := (s− 11χ1 + s− 12χ2), and denoting δα, k = 1 when α = k and zero otherwise, vector equation (21) can be recast as the following system of three scalar equations

Equation ([B1a])

Equation ([B1b])

Equation ([B1c])

where E = [Ex, Ey, Ez]. Introducing an auxiliary variable (potential) ψ := ( − Δ)− 1[∂x(CEx) + ∂y(CEy) + ∂z(CEz)], equations (B1) can be rewritten as the following system of four equations

Equation ([B2a])

Equation ([B2b])

Equation ([B2c])

Equation ([B2d])

Finally, the diagonal components of the effective conductivity tensor can be evaluated as

Equation ([B3a])

Equation ([B3b])

Equation ([B3c])
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