Vikas
Sharma
*,
Kushal
Singh
and
Krishnamurthy
Narayanan
*
Battery Division HPCL Green R & D Centre Bengaluru, KIADB Industrial Area, Tarabanahalli, Devanagonthi, Bengaluru, Karnataka-562114, India. E-mail: vikas.sharma@hpcl.in; knarayanan@hpcl.in
First published on 17th May 2024
Large-scale energy storage technologies are becoming increasingly necessary for the effective use of clean and sustainable energy sources. Solid-state lithium batteries (SSLBs) based on non- or less flammable solid-state electrolytes are gaining popularity owing to their greater safety than regular Li-ion batteries. Additionally, when built using a bipolar architecture, SSLBs can offer significant advantages in terms of battery parameters, i.e., power and energy densities together with the cost. Since the introduction of “rocking chair” batteries in the 1990s, the energy density of lithium-ion batteries has steadily increased. In order to achieve a higher energy density, an anode-free arrangement has been proposed and extensively researched in recent years. This review article briefly discusses the key elements and technologies for bipolar SSLBs, including composite electrodes, bipolar plates, and Li+-conducting SEs. This paper highlights the present problems and difficulties in this developing sector while providing an outline of the recent advancements in anode-free solid-state batteries. Although there are various challenges that need to be addressed, anode-free solid-state batteries can be developed faster using the knowledge gained from solid-state lithium metal batteries and liquid electrolytes. This will indeed assist the existing battery technology to move one step forward towards the development of novel, inexpensive, eco-friendly and high-performance bi-polar anode-less solid-state batteries.
To date, liquid electrolytes are the most widely used electrolyte materials, but they still suffer from safety problems such as liquid leakage, explosiveness, weak thermal stability, and ignitability.21,22 However, solid electrolytes exhibit superior properties to liquid electrolytes, such as low flammability, high thermal stability, no volatilization and leakage, no risk of explosions and fire, which are more favourable for developing solid-state Li ion batteries with high stability and safety.23–25 Additionally, the battery cell design can be simplified with solid electrolytes since they do not require any additional containment or separator components and deliver better mechanical performance.26–32
Solid-state lithium batteries are predicted to lead the next generation of vehicle power batteries. (Fig. 1).21 Solid-state electrolytes consist of polymer-based electrolytes, and sulfide- and oxide-based inorganic electrolytes, and each type of electrolyte exhibits respective advantages and disadvantages.33–35 One of the major concerns for the practical applications of LIBs using non-aqueous liquid electrolytes is battery safety, which is independent of the competitive ionic conductivity (10 mS cm−1).22 The flammability and thermal instability of organic solvents used in these electrolytes cause serious safety issues, particularly when batteries are overcharged, internally shorted, or exposed to elevated temperatures. In LIBs equipped with graphite anodes above 80 °C, the solid electrolyte interphase (SEI) is unstable and starts dissolving at 120 °C. As a result, lithium in graphite anodes will start reacting with electrolytes and at 135 °C the polyethylene separator will start to melt. With the polyethylene (PE) separator, the temperature beyond 135 °C does not work and cells become shorted. Moreover, the increase in cell temperature leads to the decomposition of cathode materials. If oxygen is evolved from the cathode, the battery will readily catch fire due to the availability of all hygroscopic materials in the vicinity, causing cell explosion. Several ways have been investigated for replacing/changing the electrolyte, which can increase cell safety and stability. Because of their high thermal and chemical stabilities, solid-state electrolytes (SSEs) are considered most promising.23–25,36 Furthermore, SEs have a wider electrochemical potential window (∼8 V against Li/Li+) than that of liquid organic electrolytes (∼4.2 V vs. Li/Li+), allowing them to mix with high-voltage cathodes and provide high specific energy to batteries.36 SEs also make battery construction easier by eliminating the requirement of separators to avoid the physical contact between the cathode and the anode. Solid-state LIBs, however, are currently under development, owing to the scarcity of solid electrolytes with high lithium ion conductivity and low interfacial compatibility between the electrodes and the electrolyte.23,24,26–32 Li-ion conducting SEs can be generally classified into three categories, namely, (1) inorganic electrolytes, (2) organic electrolytes, and (3) composites. For any feasible design of solid-state LIBs, the material to be employed as an electrolyte should have a conductivity of at least 1 mS cm−1, and a conductivity beyond that will be appreciable.
Fig. 1 Energy density growth trend of lithium batteries in the future (Advanced Energy Materials, 8(11), 1702657) (reproduced with permission from ref. 21). |
A solid-state battery with lithium is depicted in Fig. 2. The Li ions migrate during the charging and discharging processes, respectively, as indicated by the curved arrows. The external circuit's load is driven by the electrons produced via chemical redox reactions. The set of cathode and anode materials and their corresponding suitable electrolytes are also mentioned in Fig. 2, marked with matching colors (in the web version).
Fig. 2 Schematic of a representative lithium-based solid-state battery, showing the direction of ion movement and some of the possible anode, electrolyte, and cathode combinations (reproduced with permission from ref. 37). |
The use of SSE advancements in complete cell structures is required to demonstrate their applicability and validate the claimed advantages. Understanding the constraints of materials, processing power, and most significantly, cell form factor, is necessary for the integration of such structures. There are various approaches to integrate SSEs into whole-cell topologies. The primary potential cell design topologies for all SSE families are shown in Fig. 3.
Fig. 3 Illustration of main cell architectures utilized in solid-state battery research to date: (a) all-solid-state configuration using a solid-state cathode interfaced with a solid electrolyte and a high-energy density solid anode; (b) a hybrid approach using a liquid or polymer-based cathode interfaced with a solid electrolyte and a high–energy density anode; and (c) anode-free design in which the cell is constructed with only a cathode and a separator while the metal anode is formed upon first charge. (Reproduced with permission from ref. 38). |
A hybrid design naturally develops in some SSE systems as a potential fix for rate capability and high-temperature processing compatibility problems. Some SSEs provide this potential path for integration, as schematically displayed in Fig. 3. Due to their brittleness, oxides are difficult to mechanically adhere and provide stable interfaces with cathode components; however, a hybrid system is made viable by using another ionic conductor in the liquid or polymer phase, such as a gel.
The anode in the majority of research investigations is employed as a means for extending life by using extra Li metal.39 The existing literature lacks the discussion on the fact that extensive use of Li–metal reduces the volumetric energy density of the batteries. Additionally, excessive Li metal consumption raises safety concerns, which include potential fire and explosions. This inspired the researchers to think in a novel dimension to use less Li–metal anodes.
During charging and discharging of an anode-free battery, Li–metal plates and strips are located on the exposed current collector (CC). Since the negative-to-positive areal capacity ratio (N/P) of the anode-free battery is almost zero, it is considered as a special type of Li–metal battery. The anode-free design minimizes the volume in the anode side and produces a higher energy density (Fig. 4b) than that of the conventional Li–metal battery (Fig. 4a). However, the dendritic Li plating and low coulombic efficiency of the anode-free batteries result in poor cycling stability.40
Fig. 4 (a) Li–metal battery and (b) anode-free battery. (Reproduced with permission from ref. 41). |
Fig. 5 compares the alternative cell designs in terms of notional GED (gravimetric energy density) and VED (volumetric energy density), assuming that similar active materials are used in liquid electrolyte– and SSE-based cells. This assumption necessitates the liquid and solid electrolyte systems having equal electrochemical stability windows. Reducing the electrochemical stability window reduces the active material utilization based on its usual intercalation profile. As a result, both specific capacity and cell voltage fall, resulting in lower GED and VED. As a result, the ranking of GED and VED of various cell ideas in Fig. 5 is only relevant if sufficiently stable electrolytes are used, highlighting the critical importance of the electrochemical stability window in the development of SSB and anode-less solid-state batteries (ALSSBs), as discussed further below.42
Fig. 5 Schematics of cell configurations, stack weight and volume distribution, and estimated energy density for conventional Li-ion batteries and solid-state batteries with intercalation-type electrodes, Li–metal anode, and anode-free configuration. (Reproduced with permission from ref. 42). |
Low coulombic efficiency (CE) and lithium dendrite formation were identified as the primary issues faced by anode-free batteries in this review and explored in the first section. The anode-free battery has hurdles due to interfacial concerns such as heterogeneous Li plating, interfacial parasitic reactivity, and dead lithium. The modification of the surface chemistry is, therefore, a promising strategy for improving the electrochemical performance of anode-less batteries, which has received widespread attention and is also included in this review. Compared to liquid electrolytes, all-solid-state batteries without anodes are challenged by the more complex interface problems described in the previous section. In this context, it becomes necessary to explore the foundations of bipolar battery construction, which will be discussed in a later section.
Fig. 6 Schematic of the main types and the direction of improvement of solid-state electrolytes. (Reproduced with permission from ref. 43). |
Fig. 7 Summary of common electrolyte system types and examples. (Reproduced with permission from ref. 43). |
Types of SSE | Ionic conductivity | Interfacial compatibility | Electrochemical stability | Mechanical strength | Price |
---|---|---|---|---|---|
LE | Excellent | High | Medium | Low | Cheap |
CE | High | Low | Medium | Excellent | Cheap |
PBE | Low | Excellent | High | Medium | Expensive |
HSE | High | High | High | High | Expensive |
Among all the electrolytes illustrated in Fig. 7, it has become clear with the advancement of knowledge that the hybrid solid-state electrolytes display good electrochemical performance, but they are expensive than the conventional ceramic electrolytes. Most importantly, hybrid SSEs are considered safer than the liquid electrolytes because of their superior thermal and electrochemical stabilities. A few other astonishing properties including high ionic conductivity, high stability, and low interfacial resistance make them even more interesting. Hybrid SSEs rationally combining the properties of two or more SSEs are promising candidates for establishing a suitable solid-state lithium battery.44–47 The most common hybrid electrolyte consists of a soft polymer electrolyte and a rigid inorganic SSE. The presence of the rigid part provides high ionic conductivity at room temperature and the soft part solves the issues pertaining to wettability at the interface with electrodes.45,48 Another category of hybrid electrolytes comprises multilayer-structured hybrid electrolytes, in which a ceramic SSE layer provides Li+ ion conductivity and a constituent separator with a soft polymer electrolyte outer layer is enclosed to tune the interface against electrodes.49–51 Sometimes, the soft polymer electrolyte is replaced with a trace amount of liquid electrolytes, which are spread on the SSE surface to improve the ionic conduction between the rigid oxide SSEs and the respective electrodes. This kind of configuration is referred to as liquid–oxide hybrid electrolyte.49
Fig. 8 Schematic of the novel cathode-supported SSLIB in comparison with a conventional rigid SSLIB and a typical liquid LIB. (Reproduced with permission from ref. 43). |
Based on their settings and electrode/electrolyte materials, various types of solid-state electrolytes have been used. As a result, solid-state electrolytes can be generally divided into two categories: bulk and thin-film electrolytes. It is primarily the thickness of the electrolyte that makes the difference. Bulk solid-state electrolytes typically have a thickness of several hundred micrometers to several microns, whereas thin-film solid-state electrolytes have a thickness of several hundred nanometers to several microns. Bulk solid-state electrolytes are typically manufactured using methods including mechanical milling, sintering and compaction, annealing, and heat treatment. However, thin-film solid-state electrolytes are made by various methods such as solution casting, atomic Layer deposition, pulsed laser deposition, spark plasma sintering, and CVD. A novel concept of a cathode-supported solid-state electrolyte was established with a facile tape casting technique.54 The as-prepared cathode-supported solid electrolyte membrane significantly improves the interfacial contact between the cathode and the solid electrolyte by enhancing the wettability of solid electrolytes onto the cathode and reinforcing interfacial adhesion. SSLBs directly fabricated with the as-prepared cathode-supported solid electrolyte membrane and a metal lithium anode deliver superior battery performances over the conventional SSLBs.54,55 The cost of these batteries is still higher, which also does not support the ongoing higher price tag of electric vehicles across the globe. Moreover, the process to make a solid-state battery is complex. Materials for this technology are scarce and very expensive. Above that, there is no standardized material used in the manufacturing process, and moreover, no standardized process for fabrication.56 This makes it extremely difficult for their mass production. Various auto companies such as GM, Toyota, and Mercedes have heavily invested in solid-state battery technology, in hopes of increasing range and charging capabilities.57
Fig. 9 Cross-section of a thin-film solid-state battery showing different components. The substrate acts as a support on which the thin film is usually deposited. (Reproduced with permission form ref. 37). |
Materials with strong Li storing capabilities are frequently preferred for anodes. Al, Sn, and Si alloys are ideal options because they have reversible electrochemical interactions with lithium and have good specific capacity, e.g., 4200 mA h g−1 for a LiSi alloy. Among several types of high-energy-density electrochemical systems such as advanced LIBs, metal–air batteries, and fuel cells currently under development, SSLBs would be the most promising technology for large-scale storage and generation systems represent facility where security issues are of vital importance. In addition, the non-polar architecture of SSLBs exhibit significant performance and battery cost-effectiveness compared to traditional LIBs. There are a series of issues associated with thin-film batteries pertaining to the electrolyte, interface and cathode. The two key issues are solid electrolytes with high ionic conductivity and solid interfaces. For the preparation of thin-film battery electrodes, sophisticated and costly techniques are required, such as magnetron sputtering (MS), pulsed laser deposition (PLD), atomic layer deposition (ALD) and vacuum evaporation.58,59 The fabrication and utilization of thin-film batteries is the current hot research topic due to its good power density, which can be significantly increased by the design of 3-D structures. Compared to the bulk-type solid-state batteries, thin-film batteries exhibit higher charge/discharge rates due to the improved contact between the thin-film electrodes and SSEs. Some of the most promising applications of thin-film batteries include: (1) wearable devices, (2) internet-of-things devices, (3) medical implants, (4) military and aerospace applications, (5) energy-harvesting devices, and (6) smart cards.60,61 Thin film battery chemistry is important to understand the role of thickness in energy storage. This can be helpful in developing bipolar electrodes with lesser thickness and mass loading to achieve high performance.
In the electrolyte arena, a recent advancement has been made in the direction of developing and utilizing bipolar electrodes. Toyota created a bipolar solid-state cell stack prototype and demonstrated that four layers of single unit cells could be stacked to achieve a maximum voltage of 16.26 V.9 Gambe et al.32 also constructed a bipolar stack based on a quasi-solid-state electrolyte and experimentally showed a stack voltage of up to 12 V. Ito et al.40 built a parallel solid-state cell stack with a capacity of 1 A h by stacking three double-coated unit cells. In parallel stacking, instead of series stacking in bipolar plates (BP), the electrical current flows in-plane along the current collectors (CC) to the external tabs. In the case of series stacking, the electrical current flows from one unit cell to the near-adjacent unit cell through the BP.
Fig. 10 Schematic diagrams of (a) the monopolar design of current LIBs with liquid electrolytes and (b) bipolar design of SSLBs equipped with SEs. The Li+ and electron pathways during discharge are also indicated. (Reproduced with permission from ref. 63). |
For the construction of SSLBs, it requires an electrically conductive BP (Current collector), which works as both an electrical interconnection and partition between the adjacent cells.30,34,36,43,44 To avoid internal short-circuiting, the BP should be electrically insulated around its edges.42–44 Hence, for the successful operation of batteries; (a) BP must be chemically and electrochemically stable under the prescribed operating conditions (Fig. 12), (b) it should be electronically conductive for current flow between the cells without significant ohmic losses, (c) it should be capable of maintaining good adhesion to the electrodes with high mechanical stability against possible expansion and contraction during charge–discharge cycling42–44 and (d) it should show overcharge tolerance because in the presence of performance variation in the constituent cells, relatively poor performing cells can have higher states of charge at a given time than the other cells.40,41
Bipolar electrodes offer various advantages such as simplifying battery components, boosting power/energy density, and lowering manufacturing cost. The bipolar electrodes find applications in various emerging fields such as wearable technologies, combination with solid-state electrolytes, and recyclable batteries. Moreover, bipolar electrodes have been successfully applied in lead–acid batteries and also nickel metal hydride batteries, expanding their working and application regimes.66,67 However, there are a few shortcomings associated with bipolar electrodes regarding the issues of sealing and serious substrate corrosion that leads to battery failure after few cycles, which need to be considered as factors or scope for improvements in their composition and structure.66
Fig. 11 shows the fabricating process of a pouch-type solid-state bipolar battery that is interfacially wetted with an ionogel. The bipolar anode was initially made by coating the LMO composite cathode and the LTO composite anode on both sides of the same aluminum thwart current collector.53–55 An ionogel antecedent arrangement was at that point splashed onto the surfaces of the LMO composite cathode, LLZO–LTO/LMO bipolar anode, and LLZO–LTO bilayers, individually. Along these lines, the impregnated anodes were kept at room temperature for 2 h in situ gelation. Later, the ionogel presented an LMO composite cathode and an LLZO–LTO/LMO bipolar terminal, and LLZO–LTO double layers were stacked and sealed into a pouch cell.
Fig. 11 Schematic illustration of the fabrication process of the pouch-type LMO/LLZO–LTO bipolar solid-state battery interfacially wetted with the ionogel. (Reproduced with permission from ref. 68). |
Fig. 12a shows the stainless-steel triple stack with an area-oversized current collector. The Simple bipolar setup leads to failure even prior to cell assembly during open-circuit voltage (OCV), as demonstrated in Fig. 12b. Initially, the three-cell connection indicates an OCV of approximately 7.8 V (single cell OCV of 2.3 to 2.7 V) under OCV conditions. However, after approximately 0.6 h, the OCV decreases rapidly by 2.6 V (red arrow in Fig. 12a, which corresponds to a single-cell voltage). However, the OCV is failure-free at 20 °C. At 60 °C, the molten LiTFSi/PEO can form a short circuit between two neighboring cells, as shown in Fig. 12b. Consequently, the two short-circuited cells act as one cell and result in a voltage decay. In addition, the bipolar stack achieves failure-free charge–discharge cycling performance (as shown in the paper45). This similar performance indicates that the design is sufficient.
Fig. 12 Connection of molten LiTFSI/PEO can explain the short circuit via the detrimental Li ion connection between the cells. OCV is given as a function of time at 20 and 60 °C. Already after ≈0.6 h at 60 °C, the OCV decreases by 2.6 V (this values corresponds to the OCV of a single cell), which points to an ionic shortcut between two cells, while the OCV remains constant at 20 °C. (a) Triple stack with an area-oversized current collector (stainless steel). (b) Setup revealing failure-free galvanostatic charge/discharge performing similar to the single cell. (Reproduced with permission from ref. 69). |
Fig. 13 (a) Schematic diagram of the assembling and preparation processes of SSLBs with PEGDA-based SE, and surface/cross-sectional SEM images for the integrated LiFePO4–SE electrode. (b) First charge–discharge profiles for a two-cell bipolar SSLB and cycling performance of monopolar cells at 60 °C. (c) Structural representation and photographs of a multi-layered, bipolar-type SSLB constructed with a hybrid SE (Li0.29La0.57TiO3–PEO) and battery components. Cross-sectional SEM image and corresponding EDS results of LiNi0.6Co0.2Mn0.2O2 PE on the Al/Cu cladded Bipolar Plate. (d) Charge–discharge curves and cycling performance of bipolar-type SSLBs based on a hybrid SE measured at 60 °C. (Reproduced with permission from ref. 63). |
Even though sulfide-based SSEs suffer from various chemical basic insecurities against dampness, they are much considered due to their advantage over oxide-based SEs. Sulfide-based SEs appear tall in the case of Li+ conductivity, and even in a few cases, it appears that the conductivity matches the fluid electrolyte. A straightforward cold squeezing handle can actuate contact between inflexible cathode materials and SSEs, leading to the arrangement of the thickly stuffed interface. In free-standing, sulfide-based SSE sheets strengthened with a non-woven polymer framework, a lean Li3PS4 SSE sheet (thickness ∼70 μm) was arranged by coating of the SSE slurry onto the nickel thwart. After coating, the ensuing cold squeezing can be done onto a polyparaphenylene terephthalamide (PPTA) substrate, which serves as a mechanically compliant platform (Fig. 14).
Fig. 14 (a) Coin-type bipolar SSLB constructed by stacking the unit cells with SUS BPs. (b) Galvanostatic charge–discharge profiles for one-, two- and three-cell stacked bipolar SSLBs with quasi-SE, and cycle performances of a two-cell stacked bipolar SSLB at different C-rates. Adapted from ref. 37 (CC BY). (c) Schematic illustration of the preparation of hybrid SEs comprising LLZO, Py14TFSI, and LiTFSI. (d) Photographs of the hybrid SE after a thermal shrinkage test (120 °C), and the electrochemical performance of a two-cell bipolar battery with an LLZO–IL-based electrolyte measured at 25 °C. (Reproduced with permission from ref. 72). |
Bipolar electrodes work perfectly with the solid-state electrolyte and their unique combination promises low cost and high energy and power densities for solid-state batteries. Due to the sealing process–free attribute, it leads to a simple and compact battery configuration, thus offering a lower manufacturing cost. The noninflammable characteristic of solid-state electrolytes further enhances thermal abuse resistance.66
Fig. 15 Fabrication and characterization of the printed bipolar ASSLSBs. (a) Schematic representation depicting the fabrication procedure of the printed bipolar ASSLSBs, along with the SEM image (in-series configuration) and photographs (in-plane configurations). (b) Charge/discharge profiles of the printed bipolar ASSLSBs during the 1st cycle (at a charge/discharge current density of 0.1C/0.1C) as a function of cell number. (Reproduced with permission from ref. 73). |
Authors have manufactured a UNIST letter on a bipolar (two cells associated in series) ASSLSB on the curvilinear surface of a toy airplane through a UV curing-assisted stepwise printing handle (inset of Fig. 16a). Typical charge/discharge profiles at charge/discharge currents of 0.1C/0.1C are shown in Fig. 16a. The bipolar ASSLSB fueled a light-emitting diode (driven) light and worked a propeller introduced on the toy airplane (Fig. 16b), which illustrates its potential application as an unused sort of solid coordinate control source. In this work, the printed bipolar ASSLSB (two cells associated in series) was mechanically collapsed beneath different mishappening modes (Fig. 16c). The printed bipolar ASSLSB fueled a LED-driven light beneath seriously collapsed states. Interestingly, no obvious alteration in the release capacity was observed amid the collapsing tests.73,74 The safety test for the printed bipolar plate–based pouch cell powering LEDs is shown in Fig. 16d.
Fig. 16 Application of the printed bipolar ASSLSBs. (a) Charge/discharge profiles (at a charge/discharge current density of 0.1C/0.1C) of the “UNIST” letter-shaped bipolar (2 cells connected in series) ASSLSB directly fabricated on the curvilinear surface of a toy aircraft. (b) Photographs showing the operation (LED lamp and propeller of the toy craft) of the printed bipolar ASSLSB. (c) Discharge capacity retention of the printed bipolar ASSLSB in various folding modes. (d) Safety test of the printed bipolar ASSLSB (3 cells connected in series). It stably powered a LED lamp even after being vertically cut in half and exposed to flame. (Reproduced with permission from ref. 73). |
The development of bipolar batteries faces some technical challenges such as the internal short-circuits, corrosion sensitivity of the bipolar plates, and unreliable cell stacking.75 In order to realize bipolar batteries, a series of effective strategies are proposed: (i) developing SEs with a high Li+ conductivity and wide electrochemical windows and (ii) a stable conformal interface between SEs and active electrodes can be built. Bipolar battery construction demands electrically conductive bipolar plates as current collectors, which may be suitably provided with edge electrical insulation to prevent internal short-circuiting.66
The anode-free batteries, particularly Li metal–based, have advantages in terms of the highest retrievable gravimetric/volumetric energy densities, facile process of the anode coating and reduced maintenance and production costs of cells.76,77 However, there are issues pertaining to the interfacial contact resistance, curtailed ion pathway and dead lithium formation, which can lead to unsatisfactory cation utilization upon repetitive cycling, and thus, affect the performance badly. Some key strategies and prospective improvement suggestions are listed below for achieving high-performance anode-less batteries:61
(1) An improved SEI layer in terms of mechanical strength and flexibility is responsible for efficient ion influxes. The commercial electrolyte does not meet the requirements; therefore, the formulations with novel salts, solvents, and additives were continuously tried. However, most approaches are concentrated around “Edisonian”-type optimization.78 Additionally, high costs of the novel electrolytes hamper their widespread applications. Hence, the appropriate choice should rely on the low-cost and readily available species for industrial formulations.79
(2) The lattice mismatch of copper with the Li foil could lead to the formation of dead lithium. Even substrate modification cannot yield the close-to-unit CE for the plating process. For this, a Li supplementary strategy involving the introduction of a pre-lithiation agent from the cathode or Li-rich substrate would provide extra cyclable cations and enhance the reversibility.76,80
(3) With regard to characterization, there are possibilities of catastrophic damage to the structure of electrodes due to sensitive Li deposits or other metastable phases contained in anode-free Li ion batteries. Thus, it is hard to detect these signals with the conventional characterization methods. Thus, it is expected to develop the characterization method that could be implemented under the coupled multi-physical fields.76,81
(4) For practical applications, the anode-free batteries suffer from insufficient Li-ion utilization and limited cycle life. As a result, the construction of the anode-less LMB models with balanced energy density and cycle endurance would be the practical choice.41,42,76
Artificial SEI | Coulombic efficiency (%) | Cycling stability | Current density | Ref. |
---|---|---|---|---|
Al2O3 | 98 | 250 cycles | 3 mA cm2 | 86 |
SiOx | 99.3 | 200 cycles | 2 mA cm2 | 87 |
Graphene oxide | 98 | 50 cycles | 0.5 mA cm2 | 88 |
PEO | 98.6 | 200 cycles | 0.2C | 89 |
garnet@PVDF | 97.6 | 30 cycles | 0.2 mA cm2 | 90 |
Ag@polydopamine and graphene oxide | 98.6 | 60 cycles | 0.5 mA cm2 | 91 |
Al2O3@PAN | 97 | 82 cycles | 0.2 mA cm2 | 92 |
Fig. 17 Summary of the strategies toward bipolar cell configuration, including electrode materials, substrate materials, electrolyte materials; reproduced with permission from ref. 93. |
SE type | SE constituent | No. of cell [V] | Bipolar SSB | Ref. |
---|---|---|---|---|
Polymer | PEGDA–PEGDMA–LiTFSI | 2/5.6–7.6 | ∼136 mA h g−1 (0.5C-rate) | 94 |
Polymer | PEGDA–LiTFSI | 2/5.5–7.5 | ∼138 mA h g−1 (0.05C-rate) | 95 |
Polymer | PEO–LiTFSI + PVDF + Al2O3 | 3/9.12 | NA | 55 |
Sulfide | Li3PS4 | 2/2.0–6.4 | ∼83 mA h g−1 (14 mA g−1) | 96 |
Oxide | LAGP | 2/5.6–7.5 | ∼145 mA h g−1 (0.1C-rate) | 70 |
Hybrid | Lithiated Nafion + sulfolane–diglyme | 2/3.2–5.6 | 940 mA h g−1 (167.5 mA g−1) | 97 |
Hybrid | PSiP–DEME–TFSI + LiTFSI | 2/3.0–6.0 | 0.288 mA h cm−2 (2.3 mA h) (0.036 mA cm−2) | 98 |
Hybrid | LiTFSA–TEGDME + Al2O3 | 2/5.0–8.0 | ∼100 mA h g−1 (0.2C-rate) | 99 |
Hybrid | LLTO + PEO–LiClO4 | 3/9.2–12.0 | 125 mA h g−1 (∼4 mA h) (30 mA g−1) | 71 |
Hybrid | LLZO + PAN + LiPF6–PC–DEC | 5/7.5–13.5 | ∼1.3 mA h cm−2 (102 mA h) (0.2C-rate) | 100 |
Fig. 18 displays the potential design approaches for achieving high-performance and long-term stability in ALSSBs. In particular, synergistic approaches that combine the benefits of host structures, lithium-based coatings, protection layers, pressure, and specific formation pathways appear to be interesting. However, several key challenges should be taken into account in order to introduce and establish ALSSBs on the market. With this review, the authors have tried to provide a picture of the development undergoing in the area of bipolar anode-less batteries and their related configurational and functioning aspects. Extensive research is still needed to explore the underlying mechanisms for achieving market-ready ALSSBs through multi-scale analysis, insightful performance development, and rational manufacturing.
Fig. 18 Promising design strategies for realizing high-performance and long-term stable anode-free solid-state batteries. (Reproduced with permission from ref. 42). |
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