Showing posts with label Lithium metal battery. Show all posts
Showing posts with label Lithium metal battery. Show all posts

An Overview of the Four Steps in the Formation of Lithium Batteries

The formation process is an indispensable step in the manufacturing of lithium-ion batteries, as it directly affects the battery’s performance, safety, and lifespan.

One of the key roles during the formation process is the formation of a stable solid electrolyte interphase (SEI) film on the surface of the anode.

The SEI film protects the anode material from further erosion by the electrolyte, preventing the dissolution of the anode material in the electrolyte and thus extending the battery’s lifespan.

Tsinghua University’s Kang Feiyu Team Reports in Nature Communications: Homogeneous Polymer-Ion Solvent Electrolyte with Weak Dipole-Dipole Interactions Enables High-Performance Lithium Metal Pouch Cells

Lithium metal batteries have attracted significant attention due to their high energy density. However, their development has been hindered by issues such as uncontrollable dendrite growth of lithium metal anodes, unstable solid electrolyte interphase (SEI), and poor cycling stability. Solid-state electrolytes (SSEs) are attractive due to their inherent safety, with polymer solid-state electrolytes (SPEs) receiving particular attention for their processability, cost-effectiveness, and good contact with electrodes. However, traditional SPEs (such as poly(ethylene oxide) (PEO)-based electrolytes) have low ionic conductivity (typically <10⁻⁵ S cm⁻¹ at room temperature), limiting their application at room temperature.

Recently, Kang Feiyu, Lu Wei, Liu Ming, and He Yanbing’s team from Tsinghua University’s Shenzhen International Graduate School proposed a 1,1,2,2-tetrafluoroethyl-2,2,3,3-tetrafluoropropyl ether (TTE) diluent to significantly modulate dipole-dipole interactions in polymer ionic solvate electrolytes (TPISEs). TTE can encapsulate ionic solvents, reducing dipole-dipole interactions between ionic solvents and the polymer matrix, thereby promoting their uniform distribution and forming a continuous ionic percolation network within the polymer matrix. As a result, the ionic conductivity of TPISEs was enhanced to 1.27×10⁻³ S cm⁻¹ at 25°C. Meanwhile, TTE induces ionic solvents to transform from contact ion pairs to aggregates, which helps form a stable Li/electrolyte interface, with an exchange current density 190 times higher than without TTE. The Li||LiNi₀.₈Co₀.₁Mn₀.₁O₂ (NCM811) full cell exhibits good cycling stability across a temperature range of 30°C to 60°C. The practical pouch cell, using a 50 μm thick lithium metal foil and high areal capacity cathode (3.58 mAh cm⁻²), achieved a high specific energy of 354.4 Wh kg⁻¹ and maintained 78.1% capacity after 450 cycles at 25°C and 54 mA g⁻¹. This study provides a design strategy for polymer electrolytes to overcome the ionic conductivity bottleneck in practical solid-state batteries.

This achievement was published in “Nature Communications” under the title “Homogeneous polymer ionic solvate electrolyte with weak dipole-dipole interaction enabling long cycling pouch lithium metal battery,” with first authors Chen Likun, Gu Tian, and Mi Jinshuo.


【Key Points of the Work】

This study significantly enhances the ionic conductivity and interface stability of polymer-ionic solvate electrolytes (TPISEs) by introducing 1,1,2,2-tetrafluoroethyl-2,2,3,3-tetrafluoropropyl ether (TTE) to modulate dipole-dipole interactions.


Mechanism of Ionic Conductivity Enhancement

Construction of Weak Dipole-Dipole Interactions: TTE can encapsulate ionic solvents, reducing dipole-dipole interactions between ionic solvents and the polymer matrix. This weak interaction promotes uniform distribution of ionic solvents in the polymer matrix, forming a continuous ionic percolation network. Compared with traditional polymer electrolytes, this uniform distribution allows lithium ions (Li⁺) to move more freely in the polymer matrix, significantly improving ionic conductivity. At 25°C, the ionic conductivity of TPISEs reaches 1.27×10⁻³ S cm⁻¹, far exceeding traditional polymer electrolytes (such as PEO-based electrolytes, typically <10⁻⁵ S cm⁻¹ at room temperature).

Optimization of Ionic Transport Pathways: The introduction of TTE transforms ionic solvents from contact ion pairs (CIPs) to aggregates (AGGs), which facilitates rapid lithium ion transport. In traditional polymer electrolytes, lithium ions mainly transport through coordination with polymer chain movement, while strong ion-dipole interactions limit the migration rate of lithium ions. In TPISEs, the TTE-encapsulated ionic solvents reduce interactions with polymer chains, allowing lithium ions to migrate more quickly in the polymer matrix, achieving efficient ion transport.


Interface Stability

Formation of Stable Solid Electrolyte Interface (SEI): TTE induces ionic solvents to transform from CIPs to AGGs, helping form an SEI layer rich in lithium fluoride (LiF). This SEI layer has high mechanical modulus and uniformity, effectively suppressing lithium dendrite growth. Experiments show that the average Derjaguin-Müller-Toporov (DMT) modulus of the SEI layer formed by TPISEs is 9.46 GPa, 8 times that of the SEI layer formed by traditional polymer electrolytes (1.18 GPa). This high-modulus SEI layer not only physically blocks lithium dendrite penetration but also reduces side reactions of the lithium metal anode, significantly improving battery cycling stability and Coulombic efficiency.

Formation of High-Quality Cathode-Electrolyte Interface (CEI): The introduction of TTE also optimizes the chemical composition and structure of the cathode-electrolyte interface (CEI). In TPISEs, preferentially oxidized FSI⁻ anions in the CEI layer produce more LiF, reducing side reactions between the electrolyte and cathode material. This high-quality CEI layer not only effectively prevents electrolyte decomposition but also promotes rapid lithium ion migration in the cathode material, improving battery charging-discharging efficiency and cycling stability.


Battery Performance

Wide Temperature Range Cycling Stability: Due to the high ionic conductivity and stable interface characteristics of TPISEs, Li||NCM811 full cells exhibit good cycling stability across a wide temperature range of 30°C to 60°C. At low temperatures, TPISEs maintain high ionic conductivity to ensure normal battery discharge; at high temperatures, stable SEI and CEI layers effectively suppress electrolyte decomposition and side reactions, extending battery life.

High Specific Energy and Long Cycle Life: Pouch cells using TPISEs perform excellently in practical applications. Using a 50 μm thick lithium metal foil and high areal capacity cathode (3.58 mAh cm⁻²), the battery achieves a high specific energy of 354.4 Wh kg⁻¹ and maintains 78.1% capacity after 450 cycles at 25°C and 54 mA g⁻¹. This high performance is attributed to the significant advantages of TPISEs in ionic transport and interface stability, meeting the practical application requirements of high-energy-density lithium metal batteries.


Figure 1 | Design principle of TPISEs for high-performance, high-safety lithium metal batteries
  • Illustrates the restricted ion transport pathways and ion solvent structure dominated by contact ion pairs (CIPs) in PISEs.
  • Illustrates the rapid ion transport pathways achieved through uniformly distributed ion solvents and the structure of TPISEs dominated by aggregates (AGGs).
  • Illustrates the ion solvent structure dominated by solvent-separated ion pairs (SSIPs) and lithium ion transport pathways in PISEs using traditional solvents.

Figure 2 | Properties and solvation structure of electrolytes based on PISEs
  • HAADF image of PISEs and corresponding elemental distribution map of electron energy loss spectrum.
  • HAADF image of TPISEs and corresponding elemental distribution map of electron energy loss spectrum.
  • Arrhenius plot of PISEs and TPISEs.
  • 2D ¹H¹⁹F heteronuclear correlation spectrum of PISEs.
  • 2D ¹H¹⁹F heteronuclear correlation spectrum of TPISEs.
  • Schematic diagram of TPISEs solvation structure.
  • Lithium ion self-diffusion coefficient and corresponding diffusion mode derived from MD simulation mean square displacement.
  • Raman spectra of PISEs and TPISEs.
  • PDOS curve of HCEs.
  • PDOS curve of PISEs.
  • PDOS curve of TPISEs.

Figure 3 | Lithium reversibility and SEI microstructure
  • Coulombic efficiency of Li||Cu batteries using HCEs, PISEs, and TPISEs at 0.1 mA cm⁻² and 0.2 mAh cm⁻² for lithium deposition/stripping.
  • Modified Aurbach Coulombic efficiency test of Li||Cu batteries using HCEs, PISEs, and TPISEs.
  • Tafel plots of lithium symmetric cells using PISEs and TPISEs.
  • Galvanostatic charge-discharge curves of lithium symmetric cells using HCEs, PISEs, and TPISEs at 0.5 mA cm⁻² and 0.5 mAh cm⁻², with inset showing scanning electron microscopy images of lithium metal anodes after 100 hours of cycling.
  • Galvanostatic charge-discharge curves of lithium symmetric cells using HCEs, PISEs, and TPISEs at 1 mA cm⁻² and 1 mAh cm⁻².
  • Atomic force microscopy images of lithium metal anodes after cycling using PISEs (top) and TPISEs (bottom).
  • Three-dimensional views of LiF and C₂H₆O in the sputtered volume of SEI formed using HCEs, PISEs, and TPISEs as characterized by TOFSIMS.
  • Atomic ratio of F element in SEI formed using HCEs, PISEs, and TPISEs as characterized by XPS.


Figure 4 | Cycle stability of Li||NCM811 full cells and cathode structure characterization
  • Rate performance of Li||NCM811 full cells using PISEs and TPISEs.
  • Long-term cycle stability of Li||NCM811 full cells using PISEs and TPISEs at 25°C (cathode mass loading = 2 mg cm⁻², lithium metal thickness = 450 μm).
  • Long-term cycle stability of Li||NCM811 full cells using PISEs and TPISEs at 30°C (cathode mass loading = 2 mg cm⁻², lithium metal thickness = 450 μm).
  • Long-term cycle stability of Li||NCM811 full cells using PISEs and TPISEs at 60°C (cathode mass loading = 2 mg cm⁻², lithium metal thickness = 450 μm).
  • Insitu XRD characterization of NCM811 cathode using TPISEs during initial charge-discharge cycles.
  • HAADF-STEM image of NCM811 particles after cycling with PISEs.
  • HAADF-STEM image of NCM811 particles after cycling with TPISEs.

Figure 5 | Cycle stability and safety tests of pouch cells
  • Long-term cycle stability of Li||NCM811 pouch cells using PISEs and TPISEs at 25°C (cathode mass loading = 2 mg cm⁻², lithium metal thickness = 50 μm).
  • Charge-discharge curves of Li||NCM811 pouch cells using TPISEs at different cycle numbers.
  • Long-term cycle stability of high-energy Li||NCM811 pouch cells using TPISEs at 25°C (cathode mass loading = 20 mg cm⁻², lithium metal thickness = 50 μm). Inset shows the Li|TPISE|NCM811-based pouch cell for abuse testing.
  • Charge-discharge curves of high-energy Li||NCM811 pouch cells using TPISEs at different cycle numbers.
  • Infrared thermal imaging photos of Li|TPISE|NCM811 pouch cells under abuse conditions.

[Conclusion]

In this work, we designed a homogeneous polymer-ion solvent electrolyte (TPISEs) with weak dipole-dipole interactions, achieving a high ionic conductivity of 1.27×10⁻³ S cm⁻¹ at 25°C. The TTE-induced aggregate-dominated ion-solvent structure helps form stable LiF-rich SEI and CEI, stabilizing both the lithium metal anode and NCM811 cathode interfaces simultaneously. Notably, the exchange current density at the Li/TPISEs interface is 190 times higher than without TTE addition. As a result, solid-state Li|TPISE|NCM811 batteries exhibit excellent cycling stability over a wide temperature range from -30°C to 60°C. Excitingly, practical lithium metal pouch cells using TPISEs achieve 78.1% capacity retention after 450 cycles at a specific energy of 354.4 Wh kg⁻¹.


——End——

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Comprehensive Solution for Negative Electrode Binders for Lithium Batteries

Comprehensive Solution for Negative Electrode Binders for Lithium Batteries                                                                                                                                                                                            

Overview of Lithium-ion Battery Binders

In the production of lithium-ion batteries, binders are often referred to as "auxiliary materials" together with conductive agents, additives, etc., but they are an indispensable key material. Their main function is to adhere active substances and conductive agents to the current collector to ensure electrical contact between powder material particles in the electrode and between the powder material and the current collector. Binders have a low mass ratio in the electrode and do not participate in electrochemical reactions. Their main function is to adhere active substances and conductive agents to the current collector to keep the electrode intact. Binders affect the formation of the solid electrolyte interface (SEI), charge transfer inside the electrode and between the electrode-electrolyte interface, the wetting behavior of the electrode, and the cycle performance and cost of the battery. Therefore, an ideal binder can ensure the stability of the electrode structure with the least possible usage.

An article to understand EIS lithium battery applications, with typical circuit model diagrams

An article to understand EIS lithium battery applications, with typical circuit model diagrams
1. What is electrochemical impedance spectroscopy (EIS)? 🔍
1️⃣Electrochemical impedance spectroscopy (EIS) is a non-destructive parameter determination and effective method for determining battery kinetic behavior. A small-amplitude sinusoidal voltage signal with a frequency of w1 is applied to the battery system, and the system generates a sinusoidal current response with a frequency of w2. The change in the ratio of the excitation voltage to the response current is the impedance spectrum of the electrochemical system.

Analysis of the influence of slurry quality on coating surface fluctuation|‌Lithium battery production process front end (mixing/coating)

Analysis of the influence of slurry quality on coating surface fluctuation|‌Lithium battery production process front end (mixing/coating)

Lithium battery production process - mixing/coating
The production process of lithium batteries varies among different battery manufacturers. Generally speaking, it is divided into three stages: front, middle and back.
1. Front section: pole piece production
(Mixing, coating, tableting, baking, slitting, tableting, tab forming)
(Core link: coating)
2. Middle section: battery cell assembly
(winding or lamination, pre-packaging of cells (into shells), electrolyte injection, sealing)
(Core link: winding)
3. Post-processing (activating the battery cell)
(battery cell formation, capacity division, static placement, testing, and sorting)
(Core links: formation, volume fractionation, and testing)

Exploring the mixing process of lithium-ion batteries---mixer

Exploring the mixing process of lithium-ion batteries---mixer


Understand the principle of lithium-ion battery mixing equipment in one article

Found the culprit! -- Stanford University EES reveals: the fundamental reason for the difference in Coulombic efficiency of high-performance lithium metal battery electrolytes!

Found the culprit! -- Stanford University EES reveals: the fundamental reason for the difference in Coulombic efficiency of high-performance lithium metal battery electrolytes!

                  

Lithium metal batteries are considered ideal energy storage devices due to their high capacity and energy density, but the high activity of lithium limits their commercialization. In recent years, advances in the design of liquid electrolytes have improved the efficiency of lithium metal batteries, but the efficiency improvement has reached a bottleneck, and the reason is still unclear.

Science Bulletin: Carbonate electrolyte releases NO₃⁻ and I⁻ to achieve stable lithium metal batteries!

Science Bulletin: Carbonate electrolyte releases NO₃⁻ and I⁻ to achieve stable lithium metal batteries!

                   

The formation of inactive lithium (Li) in lithium metal batteries (LMBs) mainly originates from the undesirable components of the solid electrolyte interface (SEI) and the growth of lithium dendrites. Lithium nitrite (LiNO₃) as an electrolyte additive has shown great potential to alleviate interfacial instability and lithium dendrite growth by in situ constructing a nitride-rich SEI. However, the limited solubility of LiNO₃ in carbonate electrolytes (~0.01 mg mL⁻¹) restricts its practical application.

The "Breathing Technique" in Lithium Battery Baking: Decoding the Core Technology of Nitrogen Cycle

The "Breathing Technique" in Lithium Battery Baking: Decoding the Core Technology of Nitrogen Cycle


Why is nitrogen circulation introduced in the vacuum baking of lithium batteries? The seemingly safe inert gas actually hides the risk of condensation! Behind the efficiency improvement is the ultimate control of the "breathing rhythm" by precision technology - this article deciphers the game logic of nitrogen filling, dehumidification and risk prevention and control.

Is it necessary to introduce nitrogen circulation during vacuum baking of battery cells? When filling with nitrogen, the pressure inside the cavity will change. Will the moisture condense again and affect the baking effect?

Key auxiliary materials in lithium batteries - conductive agents

 Key auxiliary materials in lithium batteries - conductive agents


Conductive agent is an important auxiliary material for batteries, and conductive carbon black is the most widely used conductive agent. The main function of conductive agent is to improve the conductivity of batteries. Only a small amount of addition can greatly improve the performance of lithium batteries. Conductive agent products include conductive carbon black, carbon nanotubes, graphene, etc., which are important auxiliary materials for batteries.

1
Why do we need to add conductive agent to lithium batteries?

The normal charging and discharging process of lithium batteries requires the participation of lithium ions and electrons. This requires that the electrodes of lithium-ion batteries must be mixed conductors of ions and electrons, and the electrode reaction can only occur at the junction of the electrolyte, conductive agent, and active material. The positive electrode active materials are mostly transition metal oxides or transition metal phosphates, which are semiconductors or insulators with poor conductivity, and conductive agents must be added to improve conductivity.

Nature Energy: Accurate monitoring of lithium battery status!

 

First author: Meng Li
Corresponding author: Boryann Liaw
Corresponding Unit: Idaho National Laboratory, USA
Achievements at a Glance
This study developed a novel non-destructive method to track the remaining amount of active lithium (Li) in lithium-ion batteries, similar to the fuel gauge in a car engine. By converting the theoretical capacity of transition metal oxides into lithium content analysis, the researchers were able to reliably track the lithium content in the electrode and reveal the impact of battery formulation and testing methods on performance. The study found that lithium content tracking was able to reveal stoichiometric changes near the electrode-electrolyte interface compared to capacity analysis.
By tracking four key variables from battery formation to end of life, the researchers used a thermodynamic framework to characterize electrode and battery performance. This precise lithium content utilization differential analysis is expected to enable more accurate battery engineering, evaluation, failure analysis and risk mitigation. This method may be applicable to all stages from battery cell design optimization, manufacturing to battery management, thereby improving battery performance and reliability.

Interfacial friction makes the vertical structure of lithium metal batteries

Interfacial friction makes the vertical structure of lithium metal batteries


summary

A practical high-energy-density lithium metal battery requires a free-standing lithium metal anode with a thickness of less than 20 μm, but it is difficult to achieve large-scale processing of thin layers and free-standing structures due to the low melting point and strong diffusion creep effect of lithium metal. In this study, a free-standing lithium chips with a thickness of 5 to 50 μm was formed on the lithium metal surface by mechanical rolling, which was determined by the in-situ tribochemical reaction between lithium and zinc dialkyl dithiophosphate (ZDDP). A layer of organic/inorganic hybrid interface (about 450 nm) was formed on the lithium metal surface with extremely high hardness (0.84 GPa) and Young's modulus (25.90 GPa), which not only enables scalable processing of lithium chips, but also realizes dendrite-free lithium metal anode by inhibiting dendrite growth. The rolled lithium anode has a long cycle life and high-rate cycling stability ( more than 1700 cycles at 25°C even at current densities of 18.0 mA cm −2  and 1.5 mA cm −2  ). This work provides a scalable tribological design approach for producing practical thin free-standing lithium metal anodes.

In-depth! Detailed explanation of lithium-ion battery formation technology

In-depth! Detailed explanation of lithium-ion battery formation technology

Lithium-ion battery production requires formation to achieve electrode wetting and full activation of electrode materials. During the first charge, as lithium ions are embedded in the negative electrode, the electrolyte components undergo a reduction reaction at the negative electrode to form a stable solid electrolyte interface film (SEI film) to prevent irreversible consumption of electrolyte and lithium ions in subsequent cycles.


Therefore, this technology is of extraordinary significance to battery performance. The effect of formation directly affects the subsequent performance of lithium-ion batteries, including storage performance, cycle life, rate performance and safety. This article focuses on the technical parameters/methods of formation and its impact on battery performance.

Why do electrodes crack during lithium battery coating? How to solve it?

Why do electrodes crack during lithium battery coating? How to solve it?

1. Detailed reasons for the cracking of the pole piece


1. Slurry problem


   The slurry viscosity is not suitable:

     - Viscosity is too high: The slurry has poor fluidity, making it difficult to spread evenly during coating and prone to cracking.

     - Viscosity is too low: The slurry tends to flow, resulting in uneven coating thickness and cracking after drying.


  Uneven slurry dispersion:

     - Active materials, conductive agents and binders are not fully dispersed, resulting in local stress concentration.

     - Agglomerated particles exist in the slurry, forming weak points during coating.

An Overview of the Four Steps in the Formation of Lithium Batteries

The formation process is an indispensable step in the manufacturing of lithium-ion batteries, as it directly affects the battery’s performan...