Sudeshna
Sen
,
Enrico
Trevisanello
,
Elard
Niemöller
,
Bing-Xuan
Shi
,
Fabian J.
Simon†
and
Felix H.
Richter
*
Center for Materials Research, Institute of Physical Chemistry, Justus-Liebig-Universität Gießen, Heinrich-Buff-Ring 17, 35392 Gießen, Germany. E-mail: felix.h.richter@pc.jlug.de
First published on 20th July 2021
Solid-state batteries have gained increasing attention with the discovery of new inorganic solid electrolytes, some of which rival the ionic conductivity of liquid electrolytes. With the additional benefit of being single-ion conductors, several inorganic solid electrolytes achieve the lithium ion conduction required for solid-state batteries to become the next generation of energy storage device in combination with lithium metal. However, the challenges faced when preparing thin layers and stable interfaces of solely inorganic and brittle materials limit the performance of lithium solid-state batteries that are made purely of inorganic materials. Therefore, the best-performing solid-state batteries also introduce polymers to the system to improve the interfaces, cohesion, manufacture and mechanical properties of the cell as a whole. This article highlights recent developments made with the combination of polymer and inorganic materials in the form of composite electrolytes, interlayers, protective coatings and binders. The role of polymers regarding interface chemistry, interface resistance and lithium transfer is discussed and the importance of polymers for the processing of solid-state batteries is described. Taken as a whole, the article surveys the relevance of polymers at each cell component and discerns how polymers may provide the key to access the full potential of solid-state batteries with inorganic solid electrolytes.
The challenge remains the desire to create a cell with still higher energy and power density by packing materials with exceptional reductive and oxidative potential in an increasingly compact cell format while maintaining safe device operation.2 One of the most prominent emerging alternatives is the lithium solid-state battery (LiSSB), which uses solid electrolytes and a lithium metal anode instead of liquid electrolytes and graphite anode that are typically used in lithium-ion batteries.3 The incentive for their development is based on the expectation that solid electrolytes allow the reversible cycling of a lithium metal anode, which increases the attainable energy density.4
Therefore, the development of a suitable interface of lithium metal and solid electrolyte is one of the central topics in this research field. Most LiSSBs use a lithium foil or film that is added during cell construction, which provides a reservoir of excess lithium that helps with the formation of a stable interface and stable cell cycling.5 Ideally, this would not be required as the lithium to be cycled in the cell is already present in the cathode active material (CAM). If the lithium metal anode can be formed as a uniform layer on the pristine solid electrolyte during charging of the cell this would maximize energy density. The uniform and reversible plating and stripping of lithium metal is at the heart of enabling the lithium metal anode. As already demonstrated with liquid electrolyte,6,7 polymer coatings at the interface between the solid electrolyte and the current collector may prove promising here.
In a LiSSB, the cathode layer determines the attainable cell capacity and potential. This sets a clear target for cathode development, which is to maximize the specific capacity, cathode layer thickness, content of active material and cell potential. These requirements are the same as for lithium-ion batteries, which is why LiSSBs mostly rely on the same types of CAM as lithium-ion batteries: the intercalation-type and conversion-type CAMs. Intercalation-type CAMs are lithium transition metal oxides that can store lithium ions by intercalation in the interstitial layers of the crystal structure.8 They typically have high electrochemical potential, but low specific capacity, which makes them more suited to create LiSSBs with high energy density (by volume).9 The conversion-type CAMs can be transition metal oxides, sulfides, fluorides, phosphides, and nitrides, which react during lithiation to form entirely new products. They typically have intermediate electrochemical potential, but high specific capacity, which makes them more suited to create LiSSBs with high specific energy (by mass).10,11
While it is straightforward to increase the cathode layer thickness and CAM content, theoretical models show that more than about 5 mS cm−1 of lithium ionic conductivity is required for the solid electrolyte in the composite cathode to obtain a competitive LiSSB.12 To date, only few inorganic solid electrolytes (ISEs) exceed this conductivity. Unless, new solid polymer electrolytes (SPEs) with much improved ionic conductivity are discovered, it appears that LiSSBs must rely on ISEs to provide the ion transport in the composite cathode if the cells are to have competitive performance at ambient temperature.
Of course, LiSSBs that use a polymer electrolyte have already been brought to market.13 This demonstrates the key advantage of polymers: processing as solution or melt opens a range of preparative tools not always applicable to inorganic solids. The preparation of thin films of polymer electrolyte is more straightforward than that of inorganic solid electrolytes and can often be carried out at lower temperature. Hence, polymers are expected to facilitate the manufacture of LiSSBs with inorganic solid electrolytes and may provide solutions to the remaining interface challenges.14Fig. 1 depicts a schematic of a LiSSB and highlights how polymers can be employed to improve the performance of LiSSBs with ISEs by acting as protective coatings, interlayers or binders to stabilize the cell.
Fig. 1 Schematic of a solid-state battery with polymer coating, polymer interlayer and binder (CAM: cathode active material, ISE: inorganic solid electrolyte). |
For example, the preparation of thin layers of inorganic solid electrolyte and SSB electrodes over a large area relies on the use of polymer binders.15,16 The SSB with the probably best overall performance published in the academic literature to date (Lee et al.) uses three different binders: polyvinylidene fluoride, polytetrafluoroethylene and a non-aqueous acrylate-type binder in the anode, cathode and solid electrolyte layers, respectively.17 For the successful implementation of polymer functionality, knowledge of the interface and interactions of polymers with inorganic materials is essential. In the following, the types of solid electrolytes and development challenges of LiSSBs with inorganic solid electrolytes are summarized first, after which the role of polymer–inorganic interfaces, composite electrolytes (CEs), interlayers, protective coatings and binders are highlighted.
The best ionic conductivity and mechanical properties are achieved with thiophosphate ISEs.24 Their malleability at ambient temperature facilitates the preparation of model cells by pelletization and creates good contact with the anode and cathode active materials. However, thiophosphate ISEs have only a limited intrinsic electrochemical window of stability and react with most CAMs and lithium metal, resulting in the formation of an interphase layer of decomposition products.25,26 Oxide and phosphate-based ISEs of perovskite, garnet and NASICON structure types have moderate lithium ionic conductivity, high mechanical strength27 and a larger intrinsic electrochemical window of stability.28 However, the need to sinter oxide ISEs at high temperatures to create good ion conduction and contact with the active materials makes cell preparation and cycling very challenging.29 For further reading about ISEs, we refer to a recent review that summarizes fundamentals, challenges and perspectives of SEs.30
In contrast, SPEs comprise good stability with lithium metal while being flexible and cost-efficient to produce.31 Polyethylene oxide (PEO) with lithium bis(trifluoro-methane-sulfonyl)-imide salt (LiTFSI) is arguably the most extensively studied polymer electrolyte due to its low cost, good electrochemical stability and excellent compatibility with lithium salts.21 Their largest impediment is their low room temperature conductivity (<10−4 S cm−1) that necessitates operation temperatures of about 60 °C in order to achieve sufficient ionic conductivity.
Fig. 3 exemplarily summarizes key properties for the most studied solid electrolytes: Li1+xAlxTi2−x(PO4)3 (LATP), Li7La3Zr2O12 (LLZO), Li6PS5Cl (LPSCl) and PEO-LiTFSI solid electrolytes. The ISEs exhibit higher ionic conductivity and elastic modulus than PEO-LiTFSI, but the latter can be prepared easiest as films at low temperature.18,32 Unsurprisingly, Lee et al. use Li6PS5Cl solid electrolyte as it scores reasonably to excellent for all properties: it has high ionic conductivity, cells can be prepared at a temperature of <100 °C and the limited electrochemical stability with anode and cathode can be enhanced with suitable protective coatings (5 nm thick Li2O–ZrO2-coated CAM) and innovative anode concepts (Ag–C nanocomposite).17
Fig. 3 Radar charts of the properties of Li1+xAlxTi2−x(PO4)3 (LATP), Li7La3Zr2O12 (LLZO), Li6PS5Cl (LPSCl) and PEO-LiTFSI solid electrolytes. Data plotted is obtained from the literature.18,23 |
Auvergniot et al. experimentally confirmed the oxidation of LPSCl when contacted with intercalation-type cathode active materials.26 This results in the formation of an interphase predominantly consisting of sulfur, lithium polysulfides, phosphor polysulfides, phosphates, and lithium chloride.36 Walther et al. have located the distribution of decomposition products at the interface of CAM and ISE via 3D secondary-ion mass spectrometry (SIMS).37 In addition, the ISE decomposes at the interfaces with conducting carbon additives and current collectors during cell cycling.38 In order to prevent the decomposition of the ISE, a number of inorganic coatings with superior oxidation stabilities have been developed for CAMs and carbon additives.39,40 For example, Lee et al. use 5 nm thick Li2O–ZrO2 coated high-Ni Li(NixMnyCoz)O2 (NMC) as CAM.17
In the anode, negligible lithium transfer resistance between lithium metal and garnet-type solid electrolyte demonstrates that fast lithium transfer is in principle possible across the interface between two solids.34 However, this relies on an intimate and pristine contact between the two materials, which can be obtained by applying high isostatic pressure. Three caveats of cycling lithium metal with ISEs are non-uniform stripping and plating of lithium, contact loss at the interface, and the formation of short-circuits at a practically relevant current density due to lithium growth through the solid electrolyte.44,45 The application of external pressure on the cell maintains contact at the interface and improves cycling performance.45 However, the requirement for high external pressures poses challenges for the practical application of LiSSBs.
In contrast, CAMs undergo volume change during cycling because the CAM particle volume depends on the lithium content (state of charge). This plays an important role at the interface with the ISE and contact loss can degrade cell performance.46 In addition, polycrystalline CAM particles often sustain cracks within the particle already during the first charge.47 This is less of a concern for lithium-ion batteries as liquid electrolyte can infiltrate these cracks, but for cells with solid electrolytes, infiltration of cracks is impossible, which results in a large resistance contribution from lithium diffusion in the CAM.48 This demonstrates that CAMs and suitable coatings or interlayers need to be tailored to the application in SSBs. Possibly, hybrid interlayers can be developed to circumvent this problem. For further information on degradation mechanisms at LiSSB interfaces, we refer to recent reviews.49–52
Tape casting of slurries is well-known from the manufacturing of lithium-ion batteries and provides electrode sheets with suitable layer thicknesses. It can also be applied to ISEs, however, the as-prepared thin films are fragile and prone to fracture due to the brittleness of the ISEs. Therefore, ISE particles are combined with polymers in the form of composite electrolytes (CEs) resulting in robust and bendable thin films.53 Both insulating polymer binders and ion-conducting polymer electrolytes have been used to help with the preparation of cells. In the case of polymer binders that are not able to conduct lithium ions, larger ISE contents are required to ensure effective ion conduction through the ISE particle network. In contrast, when using polymer electrolytes, lithium ion conduction is possible, independent of the ISE content.
The introduction of composites, polymer coatings and binders creates additional polymer–ISE interfaces. To assess possible applications of polymer-based interlayers and binders, knowledge about the polymer–ISE interface chemistry, mechanics, lithium transfer resistance and possible decomposition reactions is crucial.
The strength of the interactions depends significantly on the chemical composition, morphology and preparation method of the polymer and inorganic materials. In the context of the polymer–ISE interfaces for electrochemical applications, the nature of such interactions is rarely investigated.56 However, such a mechanistic understanding of the phenomena governing the atomic and molecular dynamics at the interface is key for the design of better performing composites. In practical electrochemical devices, close contact between the inorganic and polymer phases is necessary, as fast transfer of the charge carriers across the boundary between the two materials is required to achieve good battery performance.
Distinctions need to be made between electron conduction and ion conduction mechanisms due to the different nature of the charge carries, i.e. electrons/holes or ions, respectively. In the early models proposed by Mott for electron conducting polymers, delocalized and doped π-orbital systems in the macromolecule facilitate the transport of the electrons/holes along the polymer backbone.60 Occasionally, electrons can transfer (tunnel) from one polymer chain to the next, giving rise to a percolating network for electronic conduction.60 Long-range transport however can be hindered by the presence of amorphous domains in the polymer.61 Therefore, recent efforts focused on understanding and controlling the microstructure of these materials or developing new polymers where semi-crystallinity is not required for fast electronic transport.62
In contrast, the predominant mechanism of ion transport in typical salt-in-polymer electrolytes such as PEO functions through ion solvation by the polymer in a predominantly amorphous matrix.63,64 In this type of electrolytes, ions are transported from site to site following the energy landscape created by the local α-relaxation of the polymer backbone (Fig. 5).65–68 This process is generally referred to as segmental motion and its magnitude, and the conductivity of the electrolyte, depend on the molecular weight of the polymer.69,70 Research efforts to lower the timescale of the backbone relaxation or completely decouple ion dynamics from it have been met with moderate success to increase ionic conductivity.63,71 Furthermore, the low transference number of PEO-based electrolytes and the associated concentration polarization during cycling limit the maximum current density in practical devices.72
Fig. 5 (a) Schematic of the transport mechanisms and energy landscape for PEO-based polymer electrolyte (adapted from ref. 60 with permission from The Royal Society of Chemistry). (b) Schematic representation of pristine (top) and degraded (bottom) interfaces between SPE and ISE forming a solid-polymer electrolyte interphase (SPEI), adapted from ref. 78. (c) Schematic of the transport mechanisms and energy landscape for LPSCl argyrodite ISE (adapted with permission from ref. 75, Copyright 2018 American Chemical Society). |
In recent years, the field of single-ion conducting polymer electrolytes with a transference number close to unity has received particular interest. These polymers, often referred to as ionomers, are characterized by electrically charged moieties immobilized by covalent bonds to the polymer backbone.63,73,74 The high molecular weight of the macromolecule reduces the mobility of the ions connected to it. Therefore, long range transport in this system is dominated by the mobile, non-covalently bound ion, allowing for transference number close to unity.63,73 While this avoids concentration polarization in the electrolyte when currents are applied to the electrochemical devices, long rage transport is still limited by the segmental motion of the solvating host polymer, so that temperatures above 40 °C are still necessary to reach practical conductivity.
In ISEs, the high concentration of ionic defects together with their high diffusivity allows for fast ion transport. As a prerequisite for an electrolyte, ion mobility needs to be decoupled from the electronic charge carrier concentration and mobility. In lithium conducting ISEs, the main mechanism for transport involves ion hopping from site to site in the crystal framework (Fig. 5).75 To give rise to long-range transport, ion hops need to take place not only locally within the anion crystal cages (intracage jumps) but also from cage to cage (intercage jumps).75 While ion diffusivity is largely determined by the energy landscape, the high concentration of ionic charge carriers is mostly a feature of the material's stoichiometry. For example, in the highly conducting LPSCl the concentration of Li+ is about 37 mol dm−3. In comparison, typical concentrations of salt in liquid and polymer (PEO with EO:Li = 10:1) electrolytes are 1 mol dm−3 and 2.5 mol dm−3, respectively.
The ion transport mechanism further complicates at the interface between polymer and inorganic electrolyte. For ion transfer between the two electrolytes, desolvation/solvation of the ion from/by the polymeric matrix and its transfer between the two electrolyte phases take place. Given the higher mass of ions compared to electrons, charge transfer can happen only through available coordination/defect sites in the polymer and inorganic phases with ion-tunneling not playing a significant role in the dynamics of the interface.76 However, the charge-transfer can still be modelled as an activated process between the energy landscapes of the mobile ions in the two phases.77 The resulting equations describing the transport kinetics are similar to Butler–Volmer kinetics at an electrode–electrolyte-interface.77,78 In this scenario, space-charge layers likely do not play a significant role as the concentration of ‘unbalanced’ localized charge is expected to be negligible in an ISE.78,79
However, lithium transfer can be significantly hindered by the formation of an insulating decomposition layer between the two electrolytes (see Fig. 5). In this scenario, ionic transport between the two electrolytes can be slowed down by the lower ionic conductivity of the interphase layer of decomposition products.78,80 The formation of such interphases was also observed in several studies of the ISE interface with liquid electrolytes, and the so-called solid–liquid electrolyte interphase contributes significantly to the total impedance of the cell.77,81–83
At the electrodes of an electrochemical device, metallic or semiconducting inorganic active materials are in contact with the electrolyte. The mechanism governing the charge transfer depends greatly on the chemical environment of the participating ions (and electrons). At a metal electrode in contact with an electrolyte, electrons tunneling from the metal into the electrolyte are the main charge transfer mechanism.84 However, most alkali metals form a solid electrolyte interphase (SEI) that prevents/slows down further reduction of the electrolyte.84,85 In this case, charge transfer occurs directly at the interface between the metal and the ISE in the SEI.
Intercalation-type CAMs are of particular relevance for battery applications. At the interface of the active materials and the electrolyte, a coupled ion-electron transfer takes place through a concerted process involving a redox reaction and the charge-balancing uptake or release of a mobile ion species.76 This interfacial process is generally limited by the contact area between electrolyte and active material. To achieve good contact between ISE and the active material, high pressures and/or high temperatures are usually required. In contrast, the malleability of SPEs allows for uniform coating of the active materials, homogenizing ion flux at the surface of the active material. However, electrolyte decomposition and interphase formation can slow ion and electron transfer at the interface.86
With the setup shown in Fig. 6a, the Li+ transfer resistance between PEO-LiTFSI and LPSCl was only 0.3 Ω cm2 at 80 °C.80 Measurement of the interface resistance was possible by introducing reference electrodes in the polymer layers, thereby excluding the contribution from the electrodes to the EIS spectra. Without employing reference electrodes, many authors were able to determine the interfacial resistance between PEO-type SPE and LLZO to be in the range between 100 Ω cm2 to 10 kΩ cm2 at 80 °C, which is strongly dependent on the salt concentration of the SPE and annealing treatment of the ISE.89–91 For LATP, the interfacial resistance determined by Chen et al. with PEO-based electrolyte was reported to be 30 Ω cm2 at 80 °C.92
Fig. 6 Cell types and electrochemical techniques employed for the characterization of the transport dynamics at the interface between SPE and ISE. (a) Schematic of a cell setup employing reference electrodes (top) on which EIS was used to determine the interface resistance between PEO-LiTFSI SPE and LPSCl (bottom). Key properties such as bulk resistance (RB) and grain-boundary resistance (RGB), the solid-polymer electrolyte interphase resistance (RSPEI), the charge transfer resistance (RCT) and Warburg diffusion (W) are highlighted in the Nyquist plot. Adapted with permission from ref. 80, copyright 2019 American Chemical Society. (b) Schematic of a micro-device developed for the determination of the conduction properties along the interface between SPE and ISE (top) and exemplary Nyquist plot of the EIS data recorded with such interdigitated electrodes (bottom). Reproduced from ref. 93 with permission from The Royal Society of Chemistry. |
Another setup to study ion transport along the interface between inorganic materials and polymer electrolytes of sub-micron thickness is shown in Fig. 6b.93 With this setup, Dong et al. were able to determine the effects that a SiO2 substrate has on the ionic conductivity of a few nanometers thick layer of PEO-based electrolyte. They concluded that grafting of the polymer to the inorganic material reduced its segmental motion and its ionic conductivity. At the same time, they could show that transport along the interface is influenced strongly by the salt concentration and PEO end-chain functionality.
Another technique to study the movement of ions in their chemical environments is nuclear magnetic resonance spectroscopy (NMR). Zagórski et al. successfully measured the diffusion of lithium from PEO into the garnet LLZO solid electrolyte.94 With this method, they also showed that the timescale of the charge transfer across the interface is around 0.1 s, which is in good agreement with EIS results.90 To probe the relaxation dynamics of the polymer and the effect of an inorganic filler on such dynamics, a composite electrolyte was analyzed with quasi-elastic neutron scattering (QENS) by Chen et al.95 They showed that segmental motion of the polymer chain is progressively reduced when PEO is mixed with LiTFSI and when the PEO-LiTFSI is further mixed with NASICON-type Ohara glass. Interestingly, they noticed that the polymer relaxation did not change when only Ohara glass was added to the polymer, suggesting an interplay between the lithium salt and the surface of the ISE in slowing down polymer segmental dynamics.
In addition to spectroscopic methods, atomic force microscopy (AFM) was used by Dixit et al. to measure the local mechanical properties of a PEO and LLZO composite electrolyte.96 They were able to correlate battery performance to the properties of the extrinsic surface (i.e. the surface of the whole CE). The degree of ISE dispersion and size under the surface and the polymer molecular weight are significant metrics predicting the delivered capacity and capacity retention in assembled batteries.96
In polymer-rich CEs, transport can proceed with mechanism 1, 3 and 4 and the preferred pathway greatly depends on the SPE and ISE employed. In bicontinuous CEs, as well as in inorganic-rich CEs, the existence of a 3D interconnected bicontinuous percolation network of the two phases allows that all four mechanisms can contribute to the total conductivity. If the lithium transfer between ISE grains is rapid, the polymer mostly serves as binder and does not contribute significantly to ionic conductivity.
CEs made of fibrous ISEs in a SPE matrix are of particular interest, in which the aspect ratio of the ISE component can increase the mean free path for ion transport in the more conductive ISE. Both in randomly oriented architectures and in aligned microstructures, the number of ion-transfer steps between the two phases is reduced compared to polymer-rich CEs with spherical ISE particles. Careful consideration of the main transport dynamics can improve the conductivity of the composites and it is crucial to consider the interface resistance when designing the CE structure.
In layered cell design (Fig. 6a), all the current applied between two electrodes needs to pass through both the ISE and the SPE layers and across the interfaces. This arrangement has been shown to be particularly effective in decreasing the concentration polarization resistance in SPEs due to the accumulation of anions at the electrodes, thanks to the almost unity transference number of the ISE.103
Now, the properties of several examples of oxide-based CEs are presented. An overview of the obtained overall conductivity for different compositions of particle- or fiber-in-polymer composite electrolytes is given in Fig. 8, where only polymers are considered that are themselves ionic conductors (i.e. salt-in-polymer electrolytes, single-ion conductors). Multiple reports of polymer-rich CEs can be found in literature for LLZO, with overall conductivities often reported in the range of 0.1 mS cm−1 or below at room temperature in the case of PEO-based composites.104,105 Also, ISE-rich composites were prepared, however in this case, the conductivity did not exceed the conductivity of the pure PEO-based electrolyte.94 The ineffectiveness of LLZO, even91 at high volume fractions suggest that a percolating network cannot be formed by simple ISE particle contact. Furthermore, the high interfacial resistance reported between PEO and LLZO means that transport across the two phases is unlikely even when the particles are tightly packed and separated by a thin layer of SPE. The low ionic conductivity of these composites at room temperature reflects the sluggish transport in the polymer phase, with the ISE mainly acting as plasticizer.100 To overcome these limitations, both aligned and random distribution of LLZO fibers were investigated by several research groups.106–109 The reported conductivity values match well with each other, with a 3D network of nanofibers reaching a conductivity of 0.025 mS cm−1 at 30 °C.
Composites of SPE and NASICON-type ISE have also been extensively studied. Examples for each architecture described in the previous section are reported in Fig. 8. Polymer-rich composites showed limited conductivity improvements, with conductivities in the range of 0.1 mS cm−1.110–112 ISE-rich CEs with PEO-based electrolyte showed moderate improvements over the bare SPE, with conductivities at room temperature in the order of 0.1 mS cm−1, as demonstrated by Jung et al.113 Recently, increasing attention to the ISE architecture in the polymer has lead scientists to the preparation of hybrid electrolytes where the microstructure of the ISE is controlled. A range of LAGP-based microarchitectures was studied and developed by Zekoll et al., with the best performing one showing a conductivity of 0.14 mS cm−1.53 One interesting approach is the one employed by Zhai et al. where ice-templated ISE powders allowed the preparation of a porous, interconnected network of ISE that could be infiltrated by a SPE.114 To achieve a percolation network in a 3D structure of LATP, Palmer et al. used a spray-coating technique.115
Compared to the phosphate and oxide classes of ISEs, thiophosphate-based ISEs are characterized by a much higher chemical reactivity towards solvent and polymers used in CE preparation. In the case of polyether based molecules, the reactivity was associated to interactions between the oxygen of the ether group and the oxophilic phosphorus in the thiophosphate.116 Conveniently, a possible mitigation pathway involves the addition of lithium salts, as the lithium ions are complexed by the ether groups, thus reducing the nucleophilic properties of the ether oxygen.116 Still, the formation of an interphase complicates the description of the conduction mechanism in the CE, as mobile species such as polysulfides are formed and can contribute to the total ionic conductivity.
This was experimentally shown in a study on CEs based on PEO-LiTFSI as SPE and LGPS as ISE by Hu et al.117 Varying the EO:Li salt concentration between 6:1 and 18:1, the authors showed a maximum lithium ionic conductivity for the 9:1 ratio.117 A similar positive influence on the conductivity was observed for 78Li2S–22P2S5 based CEs when adding a lithium salt. In their work, Zhang et al. showed that replacing PEO with PEO8:LiTFSI resulted in an increase in ionic conductivity from 0.2 mS cm−1 to 0.5 mS cm−1 at room temperature.118
Regarding the CE composition and its influence on ion transport, ISE-rich CEs generally have a much higher conductivity compared to polymer-rich CEs. Generally, the ionic conductivity of the polymer-rich CE is independent from the ISE used and in the order of 0.1 mS cm−1, suggesting that transport through the PE matrix is still predominant.119–124 However, conductivities in the order of 1 mS cm−1 were reported for ISE-rich composites, implying fast transport in the percolating thiophosphate ISE. At the same time, the low fractions of SPE electrolyte included in recent works used the polymer matrix simply as a binder for the ISE particles, rather than contributing significantly to ion transport.
One of the major challenges in combining ISEs and SPEs is the transfer resistance between the two materials. While at elevated temperatures (>60 °C) it can be reduced to few Ω cm2 for ISEs in contact with PEO-LiTFSI, the ambient temperature values are often in the order of kΩ cm2. Such a high resistance practically isolates the embedded ISE particles from participating in the total ionic conductivity of particles-based CEs. In most polymer-rich composites presented in the literature, the small improvement of the ionic conductivity can be ascribed to the formation of a plasticized polymer zone in proximity to the ISE particles.125 Such plasticization dynamics are dependent on the thermal history of the CE below the melting point of the SPE.126 However, the thermal history of CEs is often underreported, leaving the exact causality unclear.
The chemical reactivity between ISEs and SPEs also plays an important role in the dynamics taking place at the contact between the two materials. In particular, chemical interaction and or reaction between the components can significantly influence ion transport. This was also shown to be detrimental for ISEs in contact with liquid electrolytes, and similar reactivity was observed for thiophosphates in contact with SPEs. While minimizing side-reactions between the components of the electrolyte is necessary for long term stability, the slow kinetics at the interface is still the strongest limitation for CE applicability in devices working at ambient temperature.
Overall, a trend towards architecture-engineered ISEs can be observed for both phosphate- and oxide-based CEs, focusing on the transport of ions in the ISE. This can be achieved by employing ISE fibers in the CE or by structuring the ISE to allow for polymer (and active materials) infiltration into an ISE-based porous structure. At the same time, a porous framework can increase the interface area available for charge transfer from the SPE to the ISE compared to traditional layered concepts, overcoming the limitation of the charge transfer between the two electrolytes. However, high-temperature processing seems to be unavoidable for these ISEs and the scalability of these concepts is likely limited to low volume applications. On the other hand, thiophosphate-based CEs show promising results when combined with SPEs. The main open challenge is reducing their chemical reactivity towards polymers and (polar) solvents. The trend in terms of composition goes towards maximizing the ISE content in the CE, with the SPE serving mostly as binder.
Chemical, electrostatic, dispersive and/or mechanical interactions between binder and the CAM surface are responsible for good binding ability.136 Mechanically, the binder needs to be strong, yet allow for accommodation of volume change without fracture during cycling. Tuning the type and strength of the interactions by varying the binder chemistry and functionality is required to obtain the optimum binding properties for each cell chemistry. According to Nguyen and Kuss, the “ideal electrode matrix should be able to (1) form strong interactions with active materials to maintain adhesion over cycling; (2) offer strong adhesion towards current collectors to prevent electrode delamination; (3) provide a continuous conductive network within the electrode; (4) exhibit sufficiently high failure strain to accommodate volume changes during charge/discharge cycling without breaking; (5) be electrochemically and chemically stable in the harsh battery environment and with high voltage cathodes (6) be applicable with the slurry casting method to be compatible with current electrode fabrication facilities; (7) be accessible at low cost to commercialize at wide scale”.132
For LiSSBs, binders are integrated with battery components as ISE-binder composite in the ISE separator and in the composite cathode (CAM, binder, ISE, carbon additive). Fig. 9 sketches the role of binders in the ISE separator (Fig. 9a) and composite cathode (Fig. 9b) and highlights the respective interfaces. Binder polymers may, but usually do not contain lithium salts, as ion conduction is not their primary role. Instead, they maintain the percolation network between the ISE, CAM, carbon additives and current collector to ensure efficient ion and electron transport through the inorganic cell components. Bielefeld et al. correlated binder content and ion percolation in a SSB cathode composite of NMC and LPS with PVDF and acrylonitrile butadiene rubber (NBR) binders.12 The authors point out that the presence of non-conducting binders blocks ion percolation pathways and reduces the total effective ionic conductivity of the ISE. Therefore, it is important that either low binder content or ion conducting binder is used for SSBs. Also, binder distribution in the composite is very important.
There are three important differences to be considered when using binders in cells with solid instead of liquid electrolyte: (1) solid electrolyte cannot flow around or infiltrate the binder or cracks; (2) the prepared ISE separator layer needs to be made as thin as possible (replacing liquid electrolyte infiltrated separators used in lithium-ion batteries); and (3) anode, ISE separator and composite cathode need to be consolidated in one cell with low internal resistance. In addition to improving cohesion of composite cathodes, the binder also influences the ionic and electronic percolation networks. These points pose a significant challenge for cell preparation. Commonly, slurry-based film casting is used to make ISE films with binder and appropriate solvents, but dry processing methods have also been developed. In the case of SSBs, the most used binders for intercalation-type cathodes are PEO, NBR, polyvinylpyrrolidone, PTFE and PVDF, and the most used for ISE–binder separators are NBR, polyacrylonitrile butadiene (HNBR), PTFE, polystyrene-block-polybutadiene-block-polystyrene (SBS) (Fig. 9c).137
Herein, the choice of solvent is crucial.137,138 For example, polar solvents with high dielectric constants such as acetonitrile or dimethyl carbonate interact with Li7P3S11, resulting in the formation of PS43− and P2S64− units and in a reduced conductivity.140 A similar decomposition is obtained when ethyl acetate is used with 78Li2S–22P2S5 and PEO. As a result, the ionic conductivity was reduced by almost 75% compared with the pure ISE.118 Degradation of LPS and LGPS with ethers, for example triethylene glycol dimethyl ether, was also demonstrated, but could be prevented by addition of LiTFSI, which coordinates to the ether oxygen, thus reducing its reactivity towards nucleophilic attack on the ISE.116
No significant degradation was observed with the less polar solvents toluene and xylene. This was demonstrated for CEs comprised of 75Li2S–25P2S5 and NBR or polybutadiene processed with either xylene or toluene, which showed only minor change in conductivity compared to the pure ISE.137 Very recently, a blend of the less polar dibromomethane solvent and the more polar hexyl butyrate solvents was shown to work synergistically to dissolve NBR and LiTFSI, while preserving the argyrodite-type ISE, forming a SSB with the Li+-conducting NBR-LiTFSI binder.141
In addition to solvents, the functionality of the polymer also influences the properties of the ISE–binder composite. Riphaus et al. compared the results of several binders poly(styrene-co-butadiene) (SBR), polyisobutene (PIB), polymethyl methacrylate (PMMA), HNBR, polyethylene vinyl acetate (PEVA) with Li10SnP2S12 (LSPS) ISE.142 The LSPS–HNBR composite showed the highest conductivity (3.2 mS cm−1) and PEVA the lowest one (1.5 mS cm−1). This is in line with previous reports, stating that incorporation of a binder leads to a reduced effective ionic conductivity compared to the pure ISE (here: LSPS with 3.6 mS cm−1).
Fig. 10 summarizes the ionic conductivity of selected thiophosphate-ISE-binder combinations prepared with different solvents by film casting. The influence of binder content on ionic conductivity is discussed. We highlight only thiophosphate-based ISE-binder composites as oxide-based ISE-binder composites have too low effective conductivity due to the high transfer resistance from particle to particle without sintering at high temperature. Due to the superior ionic conductivity and malleability of sulfide ISEs at ambient temperature, ion transport from particle to particle can be ensured more easily. Where available, the conductivity is also compared dependent on the binder content.
For all the ISE-binder composites, a common trend is observed. As evident in Fig. 10, the presence of binders generally decreases the overall ionic conductivity as compared with the pure ISE. For the compositions with the highest ISE content, the respective ionic conductivities are similar for all types of binders. However, with increasing binder content, the drop in ionic conductivity of composites is different for polar and non-polar binders. In the case of LPSCl-PEO, almost an order of magnitude lower conductivity is observed, if we compare LPSCl-PEO with 98 wt% and with 90 wt% LPSCl.143 A similar sharp drop in conductivity is observed for 78Li2S–22P2S5–PEO composites, when increasing PEO content from 3 wt% to 20 wt%.118
For non-polar binders, when we compare LPSCl-PVDF with 90 wt% and with 80 wt% LPSCl, the drop in conductivity is not as significant.133 In the case of two different non-polar binders with same ISE, (75Li2S–25P2S5–NBR versus 75Li2S–25P2S5–BR and Li3PS4–NBR versus Li3PS4–PVC) conductivity is similar, even though composites are made in two different non polar solvents (xylene and toluene).137,144 However, if we compare the same binders with different ISEs (NBR-LPSCl, NBR-75Li2S-25P2S5 and NBR-Li3PS4 (ref. 137)), ionic conductivity is determined by the ISEs.15,137,144 For the same ISEs, polar binders show slightly lower conductivity than non-polar binders (e.g. 78Li2S–22P2S5 – 95% PVDF versus 78Li2S–22P2S5 – 95% PEO).118 Polar binders accelerate the localized ISE-binder agglomeration due to the strong electrophilic interaction between electron rich functional groups of binders (O, N, F) with aliovalent atoms such as P or transition metals.139 The favored binders with thiophosphate ISEs are those containing nonpolar groups, such as poly(acrylonitrile-co-butadiene) (NBR), polystyrene-block-polybutadiene (SBS) or poly(styrene-ethylene-butylene-styrene) (SEBS).140 In addition to composition, compactness and density of the ISE films are also important. In case of 75Li2S–25P2S5 in styrene-butadiene-styrene copolymer (SBS), the application of 410 MPa instead of 330 MPa to compress the CE sheet resulted in a doubling of the conductivity.144
Fig. 11 (a) Surface interaction of click binders (C10) with NMC cathode and SEM image of cathode composite layer. Solubility of binders (BR, NBR, C4, C10, C40, PAN, PVDF) with different solvents (heptane, isopropyl ether, p-xylene, DCM, THF, NMP) of varying polarity. Reproduced with permission from ref. 145, copyright @ 2018 American Chemical Society. (b) Schematic diagram illustrating microstructures of NMC-Li6PS5Cl-NBR without and with addition of LiG3 to NBR binder. The diagram depicts transition from non-conducting to conducting composite by addition of LiG3 to NBR binder. The Li+ ionic pathways are indicated by blue arrows. (c) The charge–discharge voltage profiles for NMC711 at first cycle without and with LiG3 (1.6 to 2.5 wt%) addition to composite cathode. Reproduced with permission from ref. 15, copyright JohnWiley and Sons and CCC, 2019. |
The molar ratio between the 3-MPA to butadiene of SBS was varied as 4:100, 10:100 and 40:100. The corresponding SBS-COOH click binders are denoted as C4, C10, and C40, respectively. The finely tuned polarity of C10 is compatible to LPSCl ISE and p-xylene solvent. Fig. 11a presents the solubility of binders (BR, NBR, C4, C10, C40, PAN, PVDF) in several solvents of varying polarity and the ISE compatibility. The ISE is stable in polarity up to p-xylene (blue region). The C10 is soluble in p-xylene, where ISE is stable. More polar binders (C40, PAN, PVDF) are only soluble in more polar NMP, where ISE is not stable. Following the favorable solubility and ISE compatibility, the C10 binder is used in a SSB with NMC and LPSCl.
The C10 click binder offers the H-bond between the surface of NMC cathode and the carboxylic acid groups of the binder (Fig. 11a).145 With increasing content of carboxylic acid groups, adhesion to the CAM increases, even in the presence of ISE. The favorable adhesion and stable interface between ISE-binder-CAM is beneficial to address volume changes and contact loss of cathode particles during cycling. As a result, the C10 exhibits superior capacity retention (78.8% capacity retention) as compared to conventional NBR binder (57.8% capacity retention).
To enhance ion transport, Oh et al. prepared a binder based on solvated ionic liquid incorporated in NBR polymer, applicable for an SSB with LPSCl (Fig. 11b).15 This offers additional functionality in SSB cathodes, such as ionic conductivity, buffering volume changes and stabilization of the cathode–electrolyte interface. The solvated ionic liquid (Li(G3)4) employs a saturated salt solution of glyme-based solvent (triglyme: G3).15 A sheet-type slurry-fabricated cathode composite, NMC–LPSCl–NBR–LiG3, where NBR–LiG3 is used as ion conducting gel-type binder (0.17 mS cm−1) is prepared.15 The presence of LiG3 with NBR results in the increase in ionic conductivity of the composite cathode. The solvated ionic liquid is stable in LPSCl and exhibits negligible volatility. Such improvement in conductivity is reflected in the improvement of rate capability and capacity retention in the SSB with LPSCl. With the presence of LiG3 in NBR–LiG3 (1.6 or 2.5 wt% LiG3) in NMC–NBR composite, the first cycle discharge capacity at 0.025C was increased from 131 mA h g−1 (0 wt% LiG3) to 172 mA h g−1 (1.6 wt%) or 164 mA h g−1 (2.5 wt%), respectively. The LiG3-NBR binder plays a multifunctional role to improve ion conduction and maintain stable contact between ISE and NMC particles.15
Fig. 12 Photographs of (a) cathode composite (active material, ISE, binder, super C65 carbon additive) prepared by dry mixing, (b) cathode composite slurry with xylene solvent and (c) sheet type NMC electrode film as prepared by wet slurry process. Reproduced with permission from ref. 16. Copyright © 2017 Elsevier B.V. license @ CCC, Elsevier. |
For example, Sakuda et al. prepared a sheet-type SSB with 75Li2S-25P2S5, graphite composite anode and NMC composite cathode.146 This preparation is similar to that of lithium-ion battery electrodes. For the cathode slurries, acetylene black (AB) as additive and a styrene-butadiene-based binders (SEBS or SBS), are added and mixed with ISE, C and NMC. The cathode slurries are made with a suitable choice of solvents, based on the binder selection: heptane for SEBS and anisole for SBS. For the SE and anode sheets, SBS is used as binder and anisole as solvent to make the slurries. The electrode slurries are coated on current collectors (copper foil for the anode and aluminum foil for the cathode), followed by drying. All the sheets were stacked and pressed at 330 MPa to construct a full sheet-type SSB.146
Lee et al. prepared a new class of polymer binder-ISE-CAM composite by slurry-based method by mixing LPSCl electrolyte and binders in butyl butyrate solvent.147 The structure of the binder was based on polytert-butyl acrylate (TBA) and poly(tert-butyl acrylate)-b-poly(1,4-butadiene) (TBA-b-BR) and their deprotected forms (exposing t-butyl protected acid groups). Both the ISE-TBA and ISE-TBA-b-BR composites show similar conductivity with LPSCl as ISE (about 1 mS cm−1) (Fig. 10).147 The cathode composites with NMC with deprotected binders are operated in a full cell. Due to the presence of more carboxylic acid groups, binders improve adhesion between CAM and ISE particles, preventing further contact loss during battery operation.
Due to the incompatibility of sulfide-based electrolytes with the majority of polar solvents, a versatile alternative preparation route is required. The alternative route should be scalable and applicable to many cell chemistries, operable under continuous conditions, and solvent-free to avoid ISE decomposition in organic polar solvent.16 For both the cathode and ISE separator sheets, the dry approach is superior as compared to conventional wet chemical method. According to Nam et al., a sheet-type electrode fabricated using a wet-slurry process showed poorer rate capability and capacity due to the poor ionic contact in cathode components when compared to that of dry mixing process.16 However, the non-scalable dry method is as yet not perfect since the added binder partially blocks ion conduction pathways.
In this regard, Hippauf et al. introduced a scalable dry film approach to prepare cathode sheets for successfully operable practical cell size (9 cm2).148 This method employs dry premixing of NMC, LPSCl, carbon additive and fibrous PTFE, followed by applying shear force to prepare films. The dry film approach can effectively reduce the surface blocking of active materials with fibrous binders. In comparison to the slurry method, the dry film approach results in superior rate performance, even with lowest binder content. Lee et al. adopted the dry film approach to prepare a sheet-type NMC and LPSCl composite cathode and prototype SSB with exceptional performance (0.6 A h and > 900 W h l−1).
Regarding point (3) to maintain the electron conducting network in the electrode also holds true for SSBs, but this requirement needs to be extended by the prerequisite to also ensure the ion conducting network across the entire cell including the ISE separator. Dual conducting binders with ionic and electronic conductivity may help with maintaining both percolation pathways in the composite cathode. Interestingly, Lee et al. use a non-aqueous acrylate-type binder and anhydrous xylene and anhydrous isobutyl isobutyrate solvents for the preparation of the ISE separator.17 In order to minimize loss of ionic conductivity due to the binder, use of ion conducting binders, in particular single-ion-conductors, may prove fruitful.
Point (4), the accommodation of volume change during cycling is especially relevant for SSBs as any cracking would immediately and irrevocably reduce cell performance. Using binder alternatives like self-healing polymers, hyper branched or crosslinked polymers, polymer gels or solvated ionic liquids are possibilities to mitigate this problem. As for point (5), electrochemical and chemical stability in the harsh battery environment is equally relevant. Degradation of the ISE, CAM and binder must be avoided. This requires careful investigation of the electrochemical stability of especially the ISE and binder in a strongly oxidizing environment. In particular, further theoretical investigations into the stability of these components will be very helpful, especially if accompanied by matching experiments.
Regarding point (6), slurry casting capability looks to be complemented by recent progress with the dry film process for the preparation of SSBs. It is imperative that the cathode components including CAM, carbon additive, binder, ISE and solvents are carefully matched regarding the (electro)chemical stability of all components. The slurry casting process is at least equally challenging for SSBs as for lithium-ion batteries, if not more so, as most ISEs are exceptionally air and moisture sensitive, as well as instable with many solvents and common battery materials. And point (7), cost and scaling is difficult to estimate at present, as production processes have not yet been finalized and the potential for cost reduction during scaling of SSB construction is still unclear.
Transferring innovations and concepts from LIB research has the potential to accelerate SSB development. Recently, Niu et al. reported a polyelectrolyte binder, synthesized by the polymerization of bis(2-hydroxyethyldisulfide) (HEDS), hexamethylene diisocyanate (HMDI) and poly(tetramethylene ether glycol) (PTMEG).149 It contains hard and soft phases, which offer excellent mechanical strength and flexibility to accommodate volume expansion in sulfur-based cathodes with liquid electrolytes.149 Mechanical flexibility and a wide electrochemical window are also beneficial for high voltage cathodes to prevent cell performance loss during SSB operation. In reference to binders for batteries with liquid electrolyte, the functional binders with self-healing property,149 hyper branched/crosslinked polymers,150 or solvated ionic liquids151 may also create new opportunities in SSBs. The full scope of the versatile properties of polymers regarding solubility, cross-linking, gel formation, and a range of mechanical properties (soft, hard, elastic, or swellable) and interactions (hydrophobic to hydrophilic) will be beneficial to SSB research. Particular focus needs to be placed on the development of (electro)chemically stable sheet type cathodes and thin ISE sheets for which the selection and development of binder will be crucial.
The coating on CAM should primarily serve three functions: exhibit wide electrochemical window to offer protection for the ISE against high voltage cathodes, decrease the charge transfer resistance and maintain contact with the ISE. Especially during cycling, crack formation and contact loss is observed due to the volume changes of the CAM. Therefore, rheological properties of the polymers can play an important role to compensate contact loss and maintain the ion percolation network.
Different types of dry and wet coating procedures153,154 have been reported to prepare coatings on CAMs: solvent casting,153 electrostatic spray deposition,155in situ crosslinking of polymer with CAM,156 chemical vapor deposition for conformal coating of polymers on cathodes.157 Examples of polymers utilized as coating in the SSB cathode are shown in Fig. 13. The classes of polymers utilized are polymers with polar functional groups,23 poly(ionic liquid),23 poly(electrolytes) (e.g. lithion),158 electron conducting polymers (e.g. poly(3,4-ethylenedioxythiophene). PEDOT)159 and dual polymers combining conducting polymer and insulating polymers (e.g. polyaniline/PEO,84 PEDOT/PEG159), most of which have been tested in cells with polymer or liquid electrolytes. Therefore, we build our discussion on the extensive knowledge base already available on batteries with solid polymer and liquid electrolytes as this gives important insight into the CAM polymer interactions and may provide a directive on how polymer coatings can also benefit SSBs with ISEs.13,14,160
Fig. 14 General representation of energy level diagram denoting HOMO and LUMO energy level and electrochemical window of polymers. The oxidation and reduction potentials as referenced to the SHE potential and the electrochemical window of pristine polymers and PEO-LiTFSI complex (as theoretically calculated in ref. 156). The electrochemical potential of cathode: μc, electrochemical potential of anode: μa. The structure of the polymers and the values of electrochemical stability are presented as reported in ref. 23. |
Marchiori et al. calculated the oxidation and reduction potentials (ESW = Eox − Ered) of several polymers with different polarity and structure: polyacrylonitrile (PAN), polyethylene imine (PEI), poly(vinyl alcohol) (PVA), polyethylene oxide (PEO), polycaprolactone (PCL), polyethylene carbonate (PEC), poly(trimethylene carbonate) (PTMC) (Fig. 14).23 The redox potentials are obtained through calculation of Gibb's free energy of the redox reaction and by using the Nernst equation. The corresponding redox pair is N/Red (Ox/N) where, N, Red and Ox are neutral, reduced and oxidized state of polymers, respectively.
The reduction (Ered) and oxidation (Eox) potentials of pristine polymers referenced to standard hydrogen electrode (SHE) potential are shown in Fig. 14. Of the selected polymers, PAN exhibits the highest oxidation potential (4.46 V versus SHE), and reduction potential (−3.65 V versus SHE) close to the Li+/Li potential. The PEI showed lower reduction potential than lithium with narrow ESW of about 6.32 V, restricting their application as interlayer. PTMC has a very large ESW (8.46 V), which means that negligible oxidation of PTMC is expected when used as coating for high voltage cathodes. However, Marchiori et al. also point out that the reactivity observed in experiments may be significantly different than the thermodynamic calculations suggest.23 For example, it is known that PAN reacts with lithium metal even though the reduction potential of PAN (−3.65 versus SHE) is quite close to the electrochemical potential of the lithium metal anode.161
Additionally, the presence of LiTFSI salt in PEO-LiTFSI decreases the electrochemical stability window (Fig. 14) as compared to pristine PEO.162 The higher diffusivity of the anion towards positive electrodes prompts additional oxidation of the salt anion. Such effects of salt decomposition result in capacity fade of LiFePO4 (LFP)-PEO-LiTFSI cathodes.162 Nie et al. also showed that LiCoO2 (LCO) serves as catalytic sites for PEO-LiTFSI decomposition in the cathode with SPE as separator.163
Still, the most used polymer coating is PEO-LiTFSI, as employed with LCO, LFP and NMC cathodes.84,160,164,165 The ESW of PEO-LiTFSI (3.8 V versus Li+/Li with carbon electrode) limits their application for high voltage cathodes.166 With LCO and LiNi0.5Mn1.5O4 (LNMO) cathodes, PEO-LiTFSI electrolyte exhibits a noisy voltage profile, which is interpreted as possible decomposition of PEO-LiTFSI in contact with a high voltage cathode. However, Homann et al. recently presented evidence that PEO-LiTFSI exhibits an oxidation potential of 4.6 V versus Li+/Li under galvanostatic cycling and potentio-dynamic conditions with LCO and NMC CAMs.167 Thus, the oxidation of PEO-LiTFSI was not found to be the cause for the noisy galvanostatic voltage profile of high voltage cathodes, potentially reopening the discussion on the electrochemical stability of PEO. Still, the possibility of polymer decomposition at high voltage cathodes with high surface area under repetitive cycling cannot be ruled out.
Irrespective of this, a conformal polymer coating has already been applied as protection layer on CAM and carbon additives in a SSB. It reduces the decomposition at the interfaces with the ISE. Deng et al. employed molecular layer deposition (MLD) to form an efficient conformal coating of 5 nm to 10 nm thickness with conducting polymer PEDOT on NMC and carbon nanotubes, and prepared a composite cathode with LGPS (Fig. 15a).157 The PEDOT served as protective layer on NMC to prevent LGPS degradation at NMC. The first charge–discharge voltage profile of composite cathode containing LGPS, PEDOT@NMC-811 and PEDOT@CNT in comparison to bare NMC and CNT is shown in Fig. 15b. At the first discharge, the polymer coated cathode (5 nm thickness) exhibited almost 2 times increment in capacity as compared to bare NMC at 0.05C rate (Fig. 15b). The performance enhancement is more distinct at higher C rate. The 5 nm PEDOT coated cathode delivers a capacity of over 100 mA h g−1 at 1C, which is 10 times higher than that of the bare cathode with LGPS. The capacity retention of 51% in PEDOT modified cathode composite is higher than that of the uncoated analogue (13.6%). The LGPS was electrochemically stable with PEDOT@CNT inside composite cathode as depicted from cyclic voltammograms (Fig. 15c).
Fig. 15 (a) Schematic illustration of the designed solid-state battery (Li/LGPS/PEDOT@NMC-CNT) with PEDOT interlayer on CAM. The composite cathode is denoted as PEDOT@(NMC-CNT)-LGPS. The conformal polymer coating onto cathode surface (PEDOT@Ni0.8Mn0.1Co0.1O2) (NMC-811) and onto CNT additive (PEDOT@CNT) is presented. (b) Charge–discharge profile of PEDOT@(NMC-CNT) (with a coating thickness 2 nm to 10 nm) along with bare cathode active material at the first cycle at 0.05C rate. (c) Cyclic voltammograms of In/LGPS/(LGPS-CNT) cell with and without PEDOT coating on CNT, recorded at 0.1 mV s−1 at the first cycle. Reproduced with permission from ref. 157. CCC, copyright @ 2020, American Chemical Society. |
The strategy of polymer coating on CAM has so far been more used in liquid and polymer electrolytes, where high voltage CAMs degrade liquid or polymer electrolytes. The effect of polymer coating on electrochemical stabilization of the cathode electrolyte interface is prominent with high voltage cathodes. For example, the anionic polyelectrolyte lithion (lithiated nafion) coating on NMC prevents degradation of ether-based electrolytes at the cathode interface.158 As a second example, polyethyl-α-cyanoacrylate coating on LCO exhibits better capacity retention with PEO-based electrolyte due to enhanced interface stability.168 The –CN group improves salt dissolution, ion conduction, and prevents transition metal ion dissolution from the cathode.168 In the same context, polymers with higher stability are desirable candidates for which some examples are reported for use as CAM coatings in batteries with liquid electrolyte. The dual core shell coating with an inner core coating with lithium polyacrylate (LiPAA) and an outer shell coating with cross-linked polymer based on silane-coupling agent (KH550) and poly(acrylic acid) (PAA), or single ion conducting block-co-poly(ionic liquid) coating are prominent examples.169,170Table 1 summarizes the cell cycling data of several composite cathodes with a wide range of polymer coatings, employed with liquid, polymer and inorganic solid electrolyte.
CAMreference | Polymer coating | Electrolyte | Capacity | Capacity retention |
---|---|---|---|---|
a PEDOT: poly(3,4-ethylenedioxythiophene). LGPS: Li10GeP2S12 : NMC: nickel manganese cobalt oxide. Diglyme: bis(2-methoxyethyl) ether. LiNO3: lithium nitrate. HFiP: tris(hexafluoro-iso-propyl)phosphate. Lithion: lithiated Nafion. PEG: polyethylene glycol. EC: ethylene carbonate, DMC: dimethyl carbonate, EMC: ethyl methyl carbonate. PECA: polyethyl α-cyanoacrylate. LiDFOB: lithium difluoro(oxalato)borate. LiPAA: lithiated polyacrylic acid. KH550: 3-aminopropyltriethoxy silane. LiPF6: lithium hexafluorophosphate. PANI: polyaniline. The specific capacity of all the cathode active materials are reported with lithium metal as anode material except for ref. 157. In ref. 157, Li-In is used as anode material for LGPS solid electrolyte and PEDOT coated composite cathode. | ||||
LiNi0.8Co0.1Mn0.1O2 (ref. 157) | PEDOT | LGPS | 100 mA h g−1 at 20th cycle at 1C | 51% after 23 cycles at 0.1C |
NMC158 | Lithion | Diglyme–LiNO3–HFiP | 1.6 mA h cm−2 at 1st cycle at 0.1C | 80% after 200 cycles at 0.2C |
LiNi0.6Co0.2Mn0.2O2 (ref. 159) | PEDOT-co-PEG | LiPF6 in EC:DMC (1:1) | 184.3 mA h g−1 at 1st cycle at 0.1C | 94% after 100 cycles at 0.5C |
LiCoO2 (ref. 168) | PECA | PEO-LiDFOB | 172.8 mA h g−1 at 1st cycle at 0.1C | 39% after 75 cycles at 0.1C |
LiNi0.8Co0.15Al0.05O2 (ref. 169) | LiPAA/KH550 | LiPF6 in DC:EMC:DMC (1:1:1) | 201.3 mA h g−1 at 1st cycle at 1C | 82.5% after 100 cycles at 1C |
LiNi0.8Co0.1Mn0.1O2 (ref. 171) | PANI-PEG | LiPF6 in EMC:DMC:EC (1:1:1) | 201.6 mA h g−1 at 1st cycle at 0.2C | 93.4% after 100 cycles, 0.2C |
Alternatively, ion-conducting polymer interlayers that have suitable rheological properties may serve as a soft adaptive buffer to decrease the interface resistance between CAM particles, mitigate crack formation and improve ion transfer between CAM and ISE. For example, coating with ionogel electrolytes,172 self-healing polymers,173,174 or by in situ polymerization,156 may prove to be very beneficial. Even though these have already been developed for batteries with liquid and polymer electrolyte, their application in SSBs with ISEs has yet to be tested. However, a potential caveat to the use of these more complex polymer chemistries is the reactivity of many ISEs with polar compounds, which we have discussed in the binder section. More research is required for a better understanding of the complex interplay of materials including polymers in the composite cathode.
Evidently, chemical compatibility of all materials in the composite cathode needs to be ensured, which will not be simple to achieve considering the reactivity of the compounds involved. Nonetheless, progress has been made on increasing the electrochemical stability of polymers. However, the plethora of chemical, rheological and mechanical properties of polymers offers a large area for innovation. In particular, research on charge transport and mechanical properties at the polymer/ISE, polymer/CAM and polymer/carbon additive interfaces is required. The key aspects include improving electrochemical stability, understanding the mechanics of the interfaces, and optimizing the electronic and ionic transport in the composite cathode. This challenge offers scientists the opportunity to pursue a truly interdisciplinary approach, develop new hybrid materials and create multifunctional cell designs.
Several preparation methods have been used to create polymer coatings on lithium metal foil. For example, solution based coating techniques such as spin coating,175,176 solution casting177 and tape casting178,179 are applied to achieve thin coatings without expensive equipment. The choice of process parameters and materials affects the uniformity and thickness of the coating layers,180 which generally range from submicron to a few micrometers.181 In addition to the usual procedure to introduce a coating on lithium metal, as is required for use with liquid electrolytes, polymer interlayer deposition on ISE was also reported to enable straightforward coating by dipping the ISE into the polymer solution177,182 and to prevent the reaction of acetonitrile in contact with lithium metal.177 In addition, molecular layer deposition (MLD) allows to prepare uniform coatings with a thickness of a few nanometers and provide the possibility to combine inorganic and organic precursors at low growth temperatures.183,184 However, the MLD process suffers from moisture sensitivity of the coatings, a limited number of available organic precursors with sufficient vapor pressure and the permeability of MLD coatings, resulting in a precursor gas absorption and subsequent layer growth.185
For the analysis of the chemical composition and microstructure of the interface between lithium metal and liquid electrolytes, XPS and SIMS measurements were used186 and more recently also cryo-TEM.187 The formation of a SEI passivation layer is almost inevitable when using lithium metal as anode material. The absence of a stable SEI would lead to a continuous reaction of lithium metal with almost all liquid and solid electrolytes.33,188 Furthermore, short-circuits caused by dendrite growth during cell cycling can be prevented by an ideal SEI.189,190 However, the potentially infinite relative volume change during lithium stripping and plating still challenges the mechanical stability of the thin native SEI layer.191 Thus, the performance of a protective layer largely depends on its capability to accommodate the stress resulting from the lithium anode volume change. Elastic polymers can address the existing interfacial challenges and facilitate the formation of a low resistive and stable SEI.192,193
Initially, protective polymer coatings were introduced to protect lithium in liquid electrolytes. Due to its lithium affinity, ether-based polymers appeared to be suitable coating materials. Gao et al. coated a lithium anode with the cyclic ether containing poly((N-2,2-dimethyl-1,3-dioxolane-4-methyl)-5-norbornene-exe-2,3-dicarbox-imide) and cells with a NMC cathode with liquid electrolyte provided a capacity of 1.2 mA h cm−2 with high capacity retention of 90% after 400 cycles.194Fig. 16a exemplarily depicts the structure of the polymer coating, a schematic illustration of the optimized SEI and protected lithium in combination with liquid electrolyte. As a second example, Dong et al. deposited a flexible, 5.1 μm thick polymer film composed of 18-crown-6 and PVDF via spin coating on lithium metal and achieved an enhanced cycling stability in Li–Cu half-cells with liquid electrolyte.175 The assumption that the Li+ affinity of oxygen atoms of 18-crown-6 improves the homogeneity and kinetics of the Li+ transport is confirmed by a reduced resistance compared to a pure PVDF layer. XPS measurements of the coated lithium anode revealed the presence of LiF and the authors attributed it to a stabilization of the SEI and prevention of dendrite growth.195–197 Other polymers including aluminium alkoxide (alucone),183 poly(diallyldimethylammonium chloride) (PDADMA),196 poly(dimethylsiloxane) (PDMS),198 poly(vinylidene fluoride-co-hexafluoropropylene) (PVDF-HFP),199 or cross-linked polymeric ionic liquid178 have also been used as protective coatings in lithium metal batteries with liquid electrolyte.
Fig. 16 (a) Schematic illustration of the formed protective surface layer and the voltage profile of a symmetric Li metal cell. Adapted with permission from ref. 194 CCC, copyright @ 2017, American Chemical Society. (b) Schematic representation of the contribution of composite electrolyte decomposition products on SEI formation and corresponding X-ray photoelectron spectroscopy measurement of decomposition products observed in the S 2p signal. Adapted with permission from ref. 200 CCC, copyright @ 2020, American Chemical Society. |
The most extensively investigated polymer coatings on lithium are PEO-based SPEs.201 Since the Li+ ion transport in PEO is facilitated by segmental motion and relaxation of the polymer backbone in the amorphous regions, a higher amorphous fraction will be advantageous for ion conduction, but the mechanical stability decreases. Early studies reported that lithium metal in contact with PEO-based electrolytes can suffer from a gradually increasing interfacial impedance.192,202 In addition, a study on the interface between lithium metal and pure PEO without lithium salt revealed that the dissolution of lithium into PEO is associated with good adhesion of lithium and PEO.203 Additionally, the authors reported an increased conductivity in Li/PEO/Li cells by a factor of 16 after annealing at 120 °C for 7 days and suggested that a lithium cation and a free electron is dissolved in PEO.
Fig. 16b depicts the XPS analysis of decomposition products at the interface of lithium with LPSCl and PEO-LiTFSI CE by Simon et al.200 The authors found that the LPSCl particles increased the lithium ionic conductivity from 0.84 mS cm−1 (PEO-LiTFSI) to 3.6 mS cm−1 (40 wt% LPSCL in PEO-LiTFSI – CE 40) at 80 °C. The formed decomposition products, predominantly LiF and Li2S, were incorporated in the SEI, resulting in a reduced interface resistance from 5.8 Ω cm2 (PEO-LiTFSI) to 3.3 Ω cm2 (CE 40) and a reduced growth rate of SEI resistance from 1.2 Ω cm2 h−0.5 (PEO-LiTFSI) to 0.57 Ω cm2 h−0.5 (CE 40) at 80 °C. In a second example, a cross-linked poly(ethylene glycol) methyl ether acrylate SPE layer was used to protect LATP ISE, which would be reduced in direct contact with lithium metal.103 A PEO-LiTFSI interlayer has also been used to improve the cycling stability of Li/PEO-LiTFSI/LPS/NMC with β-Li3PS4, which is known to chemically decompose in direct contact with lithium.193 Additionally, Tang et al. reported the use of 15 vol% of a liquid carbonate based electrolyte to protect the chemically instable LATP ISE and the interfacial resistance was decreased from 1400 Ω (pristine LATP) to 90 Ω.204
The incorporation of fillers can improve the chemical stability and mechanical strength of the SPEs.201,205 Additionally, a ceramic filler (e.g. Al2O3, TiO2) increases the low-temperature ionic conductivity of PEO-based SPEs by hampering recrystallization via Lewis acid–base interactions.206,207 Chen et al. deployed 50 wt% LATP ISE filler in a cross-linked PEO-based polymer gel electrolyte plasticized with tetraethylene glycol dimethyl ether (TEGDME).208 It was found that the cycling performance at room temperature was increased significantly with the introduction of the LATP filler, resulting in decreased overpotentials (0.04 V compared to 0.13 V without filler), reduced interfacial impedance (360 Ω cm2 compared to 750 Ω cm2 without filler) and doubled Li+ transference number. Huo et al. showed that the incorporation of 20 vol% of LLZTO filler in a PEO matrix results in a CE with an ionic conductivity of 0.16 mS cm−1 at 30 °C.209 Recently, Xu et al. reported a CE of PEO-LiClO4 containing nanosized SiO2 with an ionic conductivity of 0.11 mS cm−1 at 30 °C and a high capacity retention of 70% after 100 cycles at 0.3C and 90 °C.210
Despite its comparatively low ionic conductivity of 10−6 S cm−1, which restricts its application to thin film batteries, glassy lithium phosphorous oxynitride (LiPON) offers stable and fast cycling with lithium metal anodes. Therefore, it is used as solid electrolyte in commercial thin film batteries. LiPON exhibits a wide voltage window (0–5.5 V) in contact with lithium metal and Li/LiPON/LiCoO2 cells achieve more than 50% of the maximum capacity at a high discharge rate of 5 mA cm−2. For a lithium free Cu/LiPON/LiCoO2 cell the capacity decreased only by 20% over 1000 cycles at a discharge current of 1 mA cm−2.211 It was also reported that LiPON is capable to be cycled at remarkable current densities up to 10 mA cm−2.212 These results have inspired the development of LiPON-like polymers with decent ionic conductivities (around 10−5 S cm−1) synthesized from molecular precursors like hexachlorophosphazene (Cl2PN)3.213 Additionally, Abels et al. synthesized soluble polyphosphazenes ((H2PO2N)n) with a chemical composition similar to glassy LiPON by a two-step one pot synthesis.214 Such LiPON-inspired polymers may facilitate a stable SEI formation on lithium by decomposing into Li2O, Li3P and Li3N, which are decomposition products of glassy LiPON.215
Fig. 17 Schematic illustration of the benefit of polymer interlayers between lithium anode and solid electrolyte. (a) A polymer interlayer is employed to fill the voids at the lithium metal LLZTO interface and thereby improve the interfacial contact. Adapted from ref. 177, Copyright © 2019 Elsevier B.V. license @ CCC, Elsevier. (b) Inhomogeneous ion flux will result in dendrite growth (left), whereas a polymer coating, such as PEO, PVDF-HFP or PVDF, on the lithium anode can facilitate a homogeneous ion flux (right). |
Huo et al. reported the use of an electron-blocking interfacial shield comprising a PAA interlayer between lithium anode and LLZO (Fig. 18a), which decreased the interfacial resistance from 1104 Ω cm2 without PAA interlayer to 55 Ω cm2 with PAA interlayer.219 Symmetric Li/PAA/LLZTO/PAA/Li cells showed stable cycling for 400 h at a current density of 0.5 mA cm−2 whereas a Li/LZZTO/Li cell could not be cycled (Fig. 18b).
Fig. 18 Schematic illustration of the electron-blocking interlayer shield between lithium anode and LLZTO ISE and the electrochemical performance of a Li symmetrical cell. (a) A PAA interlayer is employed to hamper the dendrite growth at the lithium metal LLZTO interface. (b) Voltage profile of lithium symmetric cells with and without PAA interlayer at a current density of 0.5 mA cm−2. Adapted from ref. 219. |
Since the mechanical properties of thermoplastic polymers depend on temperature and pressure, an applied pressure at elevated temperatures should improve the interfacial contact. Gupta et al. investigated the influence of applied pressure and temperature on the interface stability between lithium metal and SPE (PEO-LiTFSI).220 They found that the conductivity increased with temperature from 10−4 S cm−1 at 60 °C to 10−3 S cm−1 at 100 °C and that the interfacial impedance decreased exponentially with increasing stack pressure up to an asymptote at 400 kPa at 60 °C and 200 kPa at 80 °C. However, the critical current density (CCD) for initiation of dendritic growth (0.5 mA cm−2) was invariant with temperature. This is contradictory to the trend of an increased CCD with increasing temperature that was observed for LLZO in Li/LLZO/Li symmetrical cells.221 An improved wetting and interfacial contact between lithium metal and LLZO with elevated temperature is suggested to account for a decreased interfacial charge-transfer resistance and accordingly a more uniform current density.222 In contrast, PEO-LiTFSI may not follow this trend since it exhibits a too low shear modulus to hamper the dendrite growth at elevated temperature.220 Regarding the hampering of dendrite growth, theoretical models for LiSSBs with the lithium polymer interface proposed a suppression of lithium dendrites can be obtained by a polymer electrolyte with a sufficiently high shear modulus (Gelectrolyte > 2 × Glithium),223–225 which leads to a required shear modulus of 6 GPa that is challenging to achieve for PEO above the glass transition temperature.167
A comprehensive overview of the interface of lithium metal to ISEs by Krauskopf et al. showed that the mechanisms of lithium growth through ISEs cannot be explained exclusively by this criterion.44 Additionally, Porz et al. reported a study of the lithium ISE interface.226 They concluded that interfacial defects favor dendrite propagation in high modulus, brittle inorganic solid electrolytes. Therefore, uniform Li+ flux is required for dendrite-free plating of lithium. SPE interlayers between the lithium metal anode and the ISE are considered a promising approach to prevent electrolyte decomposition and dendrite growth, as illustrated in Fig. 17b. Zhou et al. reported a stable and dendrite free cycling of LATP enclosed between two cross-linked poly(ethylene glycol) methyl ether acrylate SPE layers in a Li/SPE/LATP/SPE/LiFePO4 cell.103 The conductivity of the SPE was around 0.1 mS cm−1 at 65 °C and cycling of the cell obtained a CE of 99.9% at 0.2C with a slightly increased cell polarization (0.22 V) compared to a Li/SPE/LiFePO4 cell (0.15 V). The polymer layer provided a uniform Li+ flux by an efficient wetting of the lithium anode and the anion blocking ceramic reduced the anion depletion at the Li/PEO interface, which contributed to dendrite suppression and an enhanced Coulomb efficiency by preventing ISE degradation.103
With liquid electrolytes, Sahalie et al. employed a composite coating containing Al2O3 particles in a polyacrylonitrile (PAN) matrix on a copper current collector.229 The composite layer showed a more homogeneous lithium ion flux, which was explained by the beneficial effect of aluminum- and fluoride-based decomposition compounds of the LiPF6 salt in the SEI, and exhibited a sufficient strength to prevent dendrite formation. Cycling experiments with a NMC cathode and liquid electrolyte at 0.2 mA cm−2 achieved an initial discharge capacity of 160 mA h g−1 and a capacity retention of 30% after 82 cycles. As a second example with liquid electrolyte, solvent processed polyelectrolyte (poly(N,N-dially-N,N-dimethylammonium bis-(trifluoromethylsulfonylimide)) (PDADMA)) was coated on copper and employed as host for lithium deposition in a Li/Cu cell with liquid electrolyte.230 The PDADMA coating provided dendrite-free cycling at a current density of 1 mA cm−2 and high Coulomb efficiency for 80 cycles.
Lee et al. recently reported the successful operation of a ‘lithium free’ SSB by electroplating lithium metal at the interface of a stainless-steel current collector (SUS) and a Ag–C nanocomposite in a SUS/Ag–C/LPSCl/NMC cell.17 The lithiophilic silver nanoparticles and carbon black formed a composite with PVDF that facilitated dendrite free and uniform lithium plating. The authors demonstrated more than 1000 cycles of the SUS/Ag-C/LPSCl/NMC cell at 60 °C while achieving a remarkably high energy density (900 W h l−1) and Coulomb efficiency (99.8%). Notably, this cell concept relies on the use of a PVDF–Ag–C nanocomposite coated on the current collector, which allows the reversible plating and stripping of lithium. As a second example, the use of a garnet PEO-LiTFSI composite layer both on the copper current collector and the cathode was recently reported by Zegeye et al.231 The garnet-PEO CE exhibited an electrochemical window of 4.75 V, an ambient temperature conductivity of 0.48 mS cm−1 and cycling with a NMC cathode delivered a CE of 98.8% and a capacity retention of 41.2% after 65 cycles at 0.2 mA cm−2 at 55 °C. Table 2 summarizes the cell cycling data of polymer coated anodes using liquid, polymer and inorganic solid electrolyte.
AnodeReference | Polymer coating | Electrolyte | CAM | Capacity | Capacity retention |
---|---|---|---|---|---|
a Polycyclic polymer: poly((N-2,2-dimethyl-1,3-dioxolane-4-methyl)-5-norboronene-exo-2,3-dicarboximide). PVDF: polyvinylidene fluoride. 18-crown-6: 1,4,7,10,13,16-hexaoxacyclooctadecane. CPMEA: cross-linked poly(ethylen glycol) methyl ether acrylate LiTFSI: lithium bis(trifluoromethanesulfonyl)imide. PEO: polyethylene oxide. PAA: polyacrylic acid. PAN: polyacrylonitrile. Al2O3: aluminium oxide. LiNO3: lithium nitrate. KaNO3: potassium nitrate. Li3PO4: lithium phosphate. LiFePO4: lithium iron phosphate. EC: ethylene carbonate. DMC: dimethyl carbonate. EMC: ethyl methyl carbonate. FEC: fluoroethylene carbonate. DOL: dioxolane. LiPF6: Lithium hexafluorophosphate. VGCF: vapor grown carbon fibers. CNT: carbon nanotube. | |||||
Lithium194 | Polycyclic polymer | LiPF6 in EC:EMC:FEC (3:7:1) | LiNi0.5Co0.2Mn0.3O2 | 1.0 mA h cm−2 at 1st cycle at 0.3 mA cm−2 | 90% after 400 cycles at 0.3 mA cm−2 |
Lithium175 | 18-crown-6, PVDF | LiTFSI inDOL:DME (1:1), LiNO3 | S | 530 mA h g−1 at 1st cycle at 0.2C | 78% after 200 cycles at 0.2C |
Lithium103 | CPMEA | Li1.3Al0.3Ti1.7(PO4)3 | LiFePO4 | 120 mA h g−1 at 1st cycle at 0.6C | 85% after 640 cycles at 0.6C |
Lithium193 | LiTFSI-PEO | β-Li3PS4 | LiNi0.6Mn0.2Co0.2O2, VGCF | 140 mA h g−1 at 1st cycle at 0.05C | 90% after 50 cycles at 0.05C |
Lithium216 | PEO | Li7La2.75Ca0.25Zr1.75Nb0.25O12, LiTFSI in DOL:DME (1:1) | S (7.5 mg cm−2), CactNT | 645 mA h g−1 at 1st cycle at 0.2 mA cm−2 | 75% after 32 cycles at 0.2 mA cm−2 |
Lithium177 | LiTFSI-PEO | Li6.4La3Zr1.4Ta0.6O12 | LiFePO4 | 149 mA h g−1 at 1st cycle at 0.2C | 90% after 200 cycles at 0.2C |
Lithium219 | PAA | Li6.4La3Zr1.4Ta0.6O12 | LiFePO4 | 120 mA h g−1 at 1st cycle at 0.5C | 83% after 200 cycles at 0.5C |
Anode free229 | PAN–Al2O3 | LiPF6 in EC:DEC (1:1), KNO3 | LiNi0.3Mn0.3Co0.3O2 | 160 mA h g−1 at 1st cycle at 0.2 mA cm−2 | 30% after 82 cycles at 0.2 mA cm−2 |
Anode free17 | Ag–C–PVDF | Li6PS5Cl | LiNi0.9Co0.05Mn0.05O2 | 146 mA h g−1 at 1st cycle at 0.5C | 89% after 1000 cycles at 0.5C |
Anode free231 | LiTFSI-PEO-Li6.75La3Zr1.75Ta0.25O12 | LiTFSI-PEO-Li6.75La3Zr1.75Ta0.25O12 | LiNi0.3Co0.3Mn0.3O2 | 2.20 mA h cm−2 at 1st cycle at 0.2 mA cm−2 | 41.2% after 65 cycles at 0.2 mA cm−2 |
Composite electrolytes exhibit enhanced mechanical properties that are required for sufficient suppression of dendrite growth and obtain the possibility of an improved room temperature ionic conductivity compared to SPEs. Nevertheless, the incorporation of filler particles in the polymer matrix can result in a trade-off in properties since the modification of the polymer structure can have an opposing effect on ionic conductivity and mechanical strength. Recently, Lee et al. demonstrated a ‘lithium free’ cell with a remarkably high overall performance and a Coulomb efficiency of 99.8% that used a PVDF–Ag–C nanocomposite as coating on the current collector.17 The trend to ‘lithium free’ cell concepts has become dynamic in recent years and the efforts to a fundamental understanding will certainly provide new challenges for polymer interlayers. Particularly, the effect of a polymer coating on the nucleation of lithium needs to be intensively studied and a better understanding will help to achieve the required homogenous and stable lithium plating. While most of the reported literature focuses on SPEs based on PEO, other polymers are still underrepresented. Obviously, polymers combine convenient solution or melt processing with the possibility to tune the mechanical properties. Structures can range from an elastic to a rigid cross-linked network. In addition to the properties of the polymer layer, the decomposition products also affect the stability of the lithium polymer interface.
Over time, it seems to become increasingly evident that no single solid electrolyte combines all required properties in one material and that it takes the right combination and handling of all types of materials to create a SSB with competitive energy density, rate capability and cycling stability. However, our review also shows that the number of investigations is not evenly distributed among the SSB components. In particular, there seems to be a striking lack of investigations on the use of polymers as coatings in the composite cathode. This may be because of the long-standing teaching that particularly PEO-based solid polymer electrolytes are not stable at high potential versus Li+/Li, but recent studies appear to open up new avenues of research regarding the development and application of new and more stable polymers.
Much may already be learnt also from lithium-ion battery research, particularly regarding the use of binders for cell preparation and efforts to make the ‘lithium-free’ anode a scalable reality using polymer coatings. For SSB preparation, reactivity between polymer, cathode active material, carbon additive, inorganic solid electrolyte and solvent plays a crucial role, incentivizing research on dry processing methods, avoiding the use of polar solvents in particular. Another important topic is the electrochemical stability of polymers at cathode and anode interfaces. Only those with wider electrochemical stability window are expected to be suitable as SSB interlayer, as chemical reaction and surface degradation between battery materials usually slows ion transport. However, it is important to keep an open mind about this, as interphases of degradation products sometimes turn out to be suitable protective layers that form in situ. Therefore, the degradation products that are formed at the interfaces also need to be studied carefully, to finely correlate chemical functionality, mechanical properties and SSB performance.
Footnote |
† Current address: Robert Bosch GmbH, Tübingerstr. 123, 72762, Reutlingen, Germany. |
This journal is © The Royal Society of Chemistry 2021 |