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2026-08-04
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Lithium-ion batteries – electrolytes – solid & semi-solid

CONTEMPORARY AMPEREX TECHNOLOGY CO LTD (CATL) [CN] / CN 122338186 A

SOLID-STATE BATTERY CELLS, ELECTROLYTE SHEETS AND THEIR PREPARATION METHODS, BATTERY DEVICES AND ELECTRICAL DEVICES

The electrolyte sheet is divided into a solid electrolyte base layer and a thin electron blocking layer facing the negative electrode. The blocking layer conducts Li+ but not electrons, preventing lithium ions from being reduced to metal within the electrolyte and nucleating dendrites there.

The blocking layer comprises CsxMy[Moa(CN)b(NO)c]·nH2O, in which M is a divalent metal (here Fe), the cyanide- and nitrosyl-coordinated molybdenum anion forms the host framework, and n is the lattice water content. Cs1.1Fe0.95[Mo(CN)5(NO)]·4H2O was precipitated from aqueous Cs[Mo(CN)5(NO)], CsCl and FeCl2·4H2O at 80°C. The powder was dispersed in n-hexane and electrodeposited (0.5 mA cm-2, 25°C, 4 h) onto a 60 μm base layer of Li6PS5Cl and styrene-butadiene rubber (SBR) (98 : 2), forming a 10 μm blocking layer.

The blocking layer exhibits an electronic conductivity of 1 × 10-10 S/cm, an ionic conductivity of 7.45 × 10-3 S/cm at 45°C, and an elastic modulus of 49.8 GPa against 20 GPa for the base layer. Cells with Li1.2Ni0.13Co0.13Mn0.54O2/InCl3 (1 : 1) positive electrodes and silicon-carbon negative electrodes exhibit a first-cycle coulombic efficiency of 94.2% and a 200-cycle capacity retention of 87.4% (0.33 C, 2.0–4.8 V, 15 MPa), compared to 79.5% and 73.8% for cells whose electrolyte sheet is the Li6PS5Cl–SBR layer alone. Dendrite penetration after 200 cycles occurred in 4% of cells, versus 40% without the blocking layer.

Takeaway: Separating the electrolyte sheet into a bulk conduction layer and a thin electronically insulating interlayer addresses dendrite nucleation at its cause, electron availability inside the electrolyte, rather than relying on mechanical resistance to dendrite growth alone. The cyanonitrosyl molybdate provides the required electronic insulation together with a higher elastic modulus than the sulfide base layer.

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

LG CHEMICAL LTD [KR] / WO 2026135266 A1

SILICON-CARBON COMPOSITE, METHOD FOR PREPARING SAME, AND NEGATIVE ELECTRODE AND LITHIUM SECONDARY BATTERY EACH COMPRISING SAME

Zinc acetate and benzimidazole were stirred in a methanol / toluene / ammonium hydroxide medium for 3 h to form ZIF-11, a zeolitic imidazolate framework (ZIF) belonging to the metal-organic framework (MOF) family. The framework was washed with methanol and carbonized under argon at 950°C for 2 h to form a carbon body.

The carbon body was mixed with KOH at a mass ratio of 1 : 3 and heat-treated at 800°C for 2 h to form the carbon porous body, which exhibits a BET specific surface area of 1,450 m2/g, a mean pore diameter of ≈1.67 nm, and a total pore volume of 0.62 cm3/g. The particles exhibit a uniform polyhedral habit with diameters of 3–7 μm (SEM).

Monosilane (SiH4) was introduced at 50 sccm at 425°C for 2 h to deposit silicon within the pores of the carbon porous body. The resulting silicon-carbon composite exhibits a BET specific surface area of 1.9 m2/g, indicating that the pore volume is largely filled. The silicon content of the composite is not reported.

In half-cells against lithium metal, the composite exhibits a discharge capacity of 1,610 mAh/g, an initial efficiency of 89.7%, and a capacity retention of 89.7% (0.5 C; cycle number not reported), as compared to 950 mAh/g / 88.1% / 88.1% at a carbon body : KOH ratio of 1 : 1 (carbon porous body: 720 m2/g), 1,838 mAh/g / 80.5% / 80.5% at 1 : 5 (2,310 m2/g; composite: 243 m2/g), and 550 mAh/g / 64.4% / 20.1% without the KOH heat-treatment step (390 m2/g).

Figure: SEM image of the carbon porous body at 10,000× magnification, showing the polyhedral crystal habit inherited from the ZIF-11 framework and the uniform 3–7 μm particle size obtained without a classification step.

LG CHEMICAL LTD [KR] / Patent Image
Takeaway: Carbonizing a ZIF-11 framework yields a porous carbon whose polyhedral habit and narrow size distribution are inherited from the parent MOF crystal, which the patent frames as removing the pulverization and classification steps required for activated-carbon scaffolds. The KOH ratio then sets the pore volume available for silane infiltration – too low a ratio leaves too few deposition sites, whereas too high a ratio creates pore space that the deposited silicon cannot fill, leaving residual surface area that is presumed to accelerate electrolyte decomposition.

Lithium-ion batteries – positive electrode

LG ENERGY SOLUTION LTD [KR] / WO 2026142292 A1

METAL SALT FOR POSITIVE ELECTRODE ACTIVE MATERIAL PRECURSOR, MANUFACTURING METHOD THEREFOR, POSITIVE ELECTRODE ACTIVE MATERIAL PRECURSOR, POSITIVE ELECTRODE ACTIVE MATERIAL, POSITIVE ELECTRODE, AND LITHIUM SECONDARY BATTERY

NiSO4, MnSO4, and CoSO4 (molar ratio Ni : Mn : Co = 15 : 75 : 10) were dissolved in deionized water (40°C) to 35 mass%, and the solution was cooled to 20°C within 1 s to precipitate a solid. Filtration gave the metal salt (Ni0.15Mn0.75Co0.1)SO4, present as non-spherical secondary particles in which Ni, Mn, and Co are homogeneously distributed as a single phase (XRD). Vacuum drying (110°C) and heat treatment (800°C, 10 h, air) converted it to the oxide precursor (Ni0.15Mn0.75Co0.1)O2, without the chelating agent, base addition, or pH control of co-precipitation.

The precursor was mixed with Li2CO3 (Li : (Ni+Co+Mn) = 1.55 : 1) and heat-treated (650°C, 5 h, air) to give 0.5Li2MnO3·0.5LiNi0.3Mn0.5Co0.2O2. In half-cells (0.1 C, 4.65–2.5 V vs. Li+/Li, 45°C), the material exhibits an initial discharge capacity of 300.3 mAh/g, as compared to 295.1 mAh/g for material from a co-precipitated precursor of the same metal ratio (ammonia chelating agent, NaOH, pH 11.0, 24 h).

Takeaway: Rapid quenching of a hot aqueous transition-metal sulfate solution exploits the temperature-dependent solubility difference to precipitate a single-phase, non-spherical Ni-Mn-Co salt directly. The derived Li-rich material slightly exceeds the initial capacity of a co-precipitated equivalent, while faster, lower-cost precursor synthesis is the patent's stated goal.

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

HYUNDAI MOTOR CO LTD [KR] / KIA CORP [KR] / UIF UNIV INDUSTRY FOUNDATION YONSEI UNIV [KR] / US 20260188715 A1

COMPOSITION FOR MEMBRANE-ELECTRODE ASSEMBLY WITH IMPROVED OXYGEN PERMEABILITY AND PROTON CONDUCTIVITY AND MEMBRANE-ELECTRODE ASSEMBLY INCLUDING SAME

A membrane-electrode assembly (MEA) composition for proton exchange membrane fuel cells (PEMFC) combines a perfluorosulfonic acid (PFSA) ionomer with a polymer of intrinsic microporosity (PIM) carrying a proton conductive end group. Claims specify 60–99 mass% ionomer with 1–40 mass% PIM, a PIM ion exchange capacity (IEC) of ≥0.4 mmol/g and a number average molecular weight (Mn) of 10,000–30,000 g/mol.

PIM-1 and 3-azidopropane sulfonate (1 : 3 mass ratio) were reacted with NH4Cl in N-methyl-2-pyrrolidone (NMP) at 120°C for 24 h and acidified (10 mass% aqueous HCl, 60°C, 1 h), giving an end-sulfonated PIM with Mn 20,800 g/mol and IEC 0.7 mmol/g. It was blended with Nafion at a 1 : 5 PIM : Nafion mass ratio and cast to a 26 µm membrane.

Oxygen permeability reaches 5.81 barrer versus 2.28 barrer for Nafion alone and 4.41 barrer for a variant with benzenesulfonic acid grafted onto PIM-1 rather than substituted at the chain end. In-plane proton conductivity (80°C, 50% relative humidity) is 23.8 mS/cm, above 15.1 mS/cm for the grafted variant and 12.3 mS/cm for unfunctionalized PIM-1, but below 33.3 mS/cm for Nafion alone. Haze falls to 38.74% from the grafted variant's 68.1%, indicating better PIM dispersion. No fuel cell polarization data is disclosed.

Takeaway: This work demonstrates that terminating a polymer of intrinsic microporosity with alkyl sulfonate groups, rather than grafting benzenesulfonic acid onto its backbone, raises oxygen permeability by about 30% and proton conductivity by more than half relative to the grafted analogue, while lowering haze as an indicator of improved miscibility with the PFSA ionomer. Proton conductivity of the blend nonetheless remains below that of the unmodified Nafion membrane, making the composition a permeability-conductivity trade-off rather than a uniform improvement.

Other Categories (Excel lists are included for paid users)

  • Lithium metal batteries (excluding Li-S, Li-Air): Excel list
  • Lithium-air batteries: 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

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