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2026-08-25
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Triweekly Patent Update – Free Version

Lithium-ion batteries – electrolytes – all-solid & solid-liquid

SK ON CO LTD [KR] / WO 2026151280 A1

COMPOSITION FOR FORMING OXIDE-BASED SOLID ELECTROLYTE SHEET, OXIDE-BASED SOLID ELECTROLYTE SHEET, AND ALL-SOLID-STATE LITHIUM SECONDARY BATTERY

A composition for oxide-based solid electrolyte sheets replaces the inorganic pigment light absorber used in photonic sintering with a solvent-soluble organic dye having a maximum absorption wavelength (λmax) of 600–780 nm, matched to the visible spectrum of the pulsed light source.

Tantalum-doped lithium lanthanum zirconium oxide (LLZTO, D50: ≈200 nm), the organic dye Disperse Red 19max700 nm, 1 mass% relative to the oxide particles), polyvinyl butyral (PVB) binder, and a toluene / isopropyl alcohol solvent were combined at 48 mass% LLZTO, cast onto stainless steel foil, and dried to a green sheet. Light sintering applied 0.4 J/cm2 pulses (300 V, 3,000 μs on-time, 40 Hz) 200 times over 5 s, a cumulative 80 J/cm2, yielding a 27 μm sheet.

The sheet exhibits an ionic conductivity of 6.05 × 10-4 S/cm at 25°C, compared to 1.68 × 10-4 S/cm when Fe2O3 inorganic pigment replaces the dye at equal loading, and 2.50 × 10-6 S/cm and 3.76 × 10-6 S/cm for dyes absorbing maximally at 350 nm and 810 nm. The Fe2O3 sheet also shows the most severe substrate discoloration and, under differential interference contrast (DIC) microscopy, surface cracking, whereas the dye-containing sheet shows none. No cell-level electrochemical data was identified.

Figure: Differential interference contrast micrographs of the solid electrolyte sheet surface after light sintering.
Upper: sheet containing Fe2O3 inorganic pigment
Lower: sheet containing the organic dye

SK ON CO LTD [KR] / Patent Image
SK ON CO LTD [KR] / Patent Image
Takeaway: Dissolving the light absorber into the slurry, rather than dispersing an insoluble pigment, colors the oxide particles themselves and distributes the absorbed light energy evenly through the green sheet. This raises ionic conductivity while reducing the substrate damage and cracking that constrain photonic sintering, and it replaces the multi-hour high-temperature furnace step, with its attendant lithium volatilization, by a short process compatible with continuous coating on foil.

Lithium-ion batteries – negative electrode (excluding Li metal electrodes)

BTR NEW MAT GROUP CO LTD [CN] / CN 122393238 A

NEGATIVE ELECTRODE MATERIALS AND THEIR PREPARATION METHODS, NEGATIVE ELECTRODE SHEETS AND BATTERIES

An anode material comprising a silicon matrix, carbon, and a metal carbide was developed to suppress the formation of crystalline lithium-silicon alloy. The suppression parameter P = (A − B) / A is derived from the first-cycle charge specific capacities of two coin half-cells (0.01 C) discharged to 0.005 V and 0.025 V, respectively, and charged to 1.5 V. Crystalline lithium-silicon alloy begins to form below 0.025 V, so a larger capacity difference indicates stronger suppression, with a target range of 5% ≤ P ≤ 15%.

Nano-silicon particles (average size: 100 nm, supplied as a pre-formed powder of unspecified synthesis route) were mixed with titanium carbide (TiC) at a mass ratio of 8 : 1, high-energy ball milled (ball-to-powder ratio 20 : 1, 8 h), dispersed in ethanol at a solid content of 10 mass%, and spray granulated to form the silicon composite precursor.

In a first chemical vapor deposition (CVD) step, the precursor was fluidized in a vertical fluidized bed under argon, heated at 3°C/min to 700°C, and held for 3 h under propane (2 L/min), depositing a first carbon material inside the granules. A second CVD step in a horizontal rotary furnace at 700°C for 3 h under acetylene (2.5 L/min) formed a dense outer carbon layer.

The resulting material exhibits a P value of 12%, a TiC content of 7.5 mass% with an average carbide size of 20 nm, a carbon content of 32 mass%, a silicon (111) crystallite size of 3.7 nm (XRD, Scherrer equation), a D50 of 5.2 μm, and a BET specific surface area of 3.5 m2/g.

In half-cells, the material exhibits a reversible capacity of 2,397.5 mAh/g and a first-cycle Coulombic efficiency of 91.2%. Blended with graphite to a mixture capacity of 480 mAh/g, the electrode exhibits a capacity retention of 83.5% after 50 cycles (0.25 C) with an electrode thickness expansion of 23.5%, as compared to 60.9% / 38.5% for graphite substituted for TiC at the same mass ratio (P: 3%), and 71.5% / 42.1% for a material containing 0.25 mass% TiC (P: 4.5%).

Figure: XRD pattern of the anode material (y-axis: intensity, a.u.), with broad reflections indexed to silicon (♦) reflecting the nanoscale crystallite size and sharp reflections indexed to TiC (▽) confirming the carbide as a distinct crystalline phase, with no impurity phases detected.

BTR NEW MAT GROUP CO LTD [CN] / Patent Image

Takeaway: Metal carbides dispersed through the silicon-carbon composite exhibit a compressive strength exceeding the stress generated by silicon during lithiation, relieving stress concentration between primary particles and limiting the formation of crystalline lithium-silicon alloy at deep discharge. The charge-capacity difference measured between two discharge cut-off voltages provides a simple electrochemical descriptor of this suppression capability, and holding it within a defined window balances reversible capacity against cycling stability and electrode expansion.

Because crystalline alloy nucleation is itself a principal driver of particle fracture, the carbide could be expected to raise the primary silicon size tolerated before cracking. The tested particles lie below the size range in which fracture becomes likely, however, so no such limit is demonstrated.

That tolerance would matter mainly for silicon supplied as a pre-formed milled powder, where holding the entire distribution – including a ppm-level oversize tail – below the fracture-critical diameter is difficult and costly, whereas silane deposition inherently confines silicon to fine dimensions.

Lithium-ion batteries – positive electrode

SAMSUNG SDI CO LTD [KR] / WO 2026155294 A1

POSITIVE ELECTRODE AND ALL-SOLID-STATE BATTERY COMPRISING SAME

Li2S, LiI, and the boron-group metal halide AlI3 (mass ratio 45.71 : 5.71 : 17.14) were ball-milled (25°C, 450 rpm, 10 h, 20 G milling energy) to form a Li2S-LiI-AlI3 composite, which was then ball-milled with carbon nanofibers (CNF) at 68.56 : 11.44 under identical conditions.

The composite was dry-mixed in a resonant acoustic mixer with argyrodite Li6PS5Cl solid electrolyte (D50: 1.0 μm), PTFE binder, and a poly(ethylene glycol) dimethyl ether/LiTFSI–Li2S additive (mass ratio 80 : 20 : 0.72 : 0.48), coated on carbon-coated aluminum foil, and pressed (200 MPa, 10 min) to an areal capacity of 3 mAh/cm2. The resulting active material layer is 45 μm thick at a porosity of 32%.

In all-solid-state cells with a silver-carbon composite negative electrode layer on stainless steel (45°C, 1.4–2.65 V), the electrode exhibits an initial capacity of 389 mAh/g, 140 cycles to 80% state of health, and a rate capability of 94.4% (third-cycle 0.1 C discharge capacity divided by second-cycle 0.05 C discharge capacity), as compared to 334 mAh/g, 17 cycles, and 86.1% at 68 μm and 42% porosity for the same 80 : 20 electrode without AlI3, to 327 mAh/g, 28 cycles, and 89.3% for an AlI3-containing electrode at 70 : 30 (active material below the range), and to 340 mAh/g, 19 cycles, and 85.2% at 90 : 10 (above the range).

Takeaway: Adding a boron-group metal halide to a Li2S-LiI-carbon nanofiber composite lowers positive electrode porosity, giving a thinner electrode at equal areal capacity. Holding the active material to solid electrolyte ratio inside a narrow window maximizes capacity, rate capability, and cycle life.

The concept targets a cell design that combines two cost and safety levers: a sulfide solid electrolyte that avoids flammable organic solvent, and a Li2S positive electrode that is free of nickel and cobalt and removes the need to handle lithium metal foil during assembly, which the patent identifies as a mass-producibility barrier. Maturity nevertheless remains early. The best cell reaches only 140 cycles to 80% capacity, and testing relies on 45°C operation under applied stack pressure. Near-term entry points are therefore applications that value specific energy and intrinsic safety over long service life, such as drones and other aviation or defense power packs, rather than automotive traction batteries.

Fuel cells (PEMFC / SOFC / PAFC / AEMFC) – electrochemically active materials

TOYOTA MOTOR CO LTD [JP] / US 20260204594 A1

MEMBRANE ELECTRODE ASSEMBLY

A membrane electrode assembly for proton exchange membrane fuel cells (PEMFC) pairs a nitrogen-containing multidentate ligand coordinatable to iron ions with a highly oxygen-permeable ionomer in the cathode catalyst layer.

The ionomer (Polymer A) was prepared by radical copolymerization of perfluoro(2-ethyl-1,3-dioxole) (PED) with a perfluorosulfonyl fluoride vinyl ether (PSVE-A) at room temperature (top Figure). 1,10-Phenanthroline was added at 6 μg/cm2 with iron ions at 1.0 μg/cm2, at a cathode loading of 0.2 mg-Pt/cm2.

At 80°C and 30% relative humidity, Example 1 reaches 0.72 V at 1.0 A/cm2, against 0.61 V for Comparative Example 2, which pairs the same ligand with Aquivion ionomer. After 300 h of high-potential holding at 95°C, Example 1 retains 94% of its initial 0.05 A/cm2 voltage, against 77% for ligand-free Comparative Example 3 (bottom Figure). The patent presumes the cyclic ionomer structure restricts ligand migration into the cathode, suppressing catalyst poisoning.

PED: Perfluoro(2-ethyl-1,3-dioxole), cyclic oxygen-permeable monomer
PSVE-A: Perfluorosulfonyl vinyl ether comonomer carrying the sulfonic acid group (cat. = catalyst, r.t. = room temperature)
Example 1: 1,10-Phenanthroline in anode catalyst layer, Polymer A as cathode ionomer
Example 2: 1,10-Phenanthroline in cathode catalyst layer, Polymer A as cathode ionomer
Comparative Example 1: No nitrogen-containing compound, Aquivion cathode ionomer
Comparative Example 2: 1,10-Phenanthroline in anode catalyst layer, Aquivion cathode ionomer
Comparative Example 3: No nitrogen-containing compound, Polymer A as cathode ionomer
Retention: Cell voltage at 0.05 A/cm2 after the 300 h durability test relative to the initial value

Top Figure: Copolymerization scheme forming Polymer A from PED and PSVE-A
Bottom Figure: Voltage retention after the 300 h high-potential durability test

TOYOTA MOTOR CO LTD [JP] / Patent Image
TOYOTA MOTOR CO LTD [JP] / Patent Image
Takeaway: Nitrogen-containing multidentate ligands improve fuel cell durability but cost power output, because they migrate into the cathode and poison the catalyst. A cyclic perfluorodioxole-based ionomer is proposed to restrict that migration, letting one assembly gain durability without giving up low-humidity power.

Other Categories (Excel lists are included for paid users)

  • Lithium metal batteries (excluding Li-S, Li-Air): Excel list
  • Lithium-ion batteries – electrolytes – liquid: Excel list
  • Lithium-ion batteries – separators: Excel list
  • Lithium-sulfur batteries: Excel list
  • Na-ion batteries: Excel list