| HS Code | 479837 |
| Electrolyte Type | High-voltage lithium-ion battery electrolyte |
| Lithium Salt | LiPF6 |
| Lithium Salt Concentration | 1.2 M |
| Solvent System | EC:EMC:DMC (3:5:2 by volume) |
| High Voltage Additive | FEC and PS |
| Voltage Window | 2.8-4.45 V |
| Ionic Conductivity | 8.5 mS/cm at 25°C |
| Water Content | ≤10 ppm |
| Free Acid Hf | ≤50 ppm |
| Density | 1.22 g/cm³ at 25°C |
As an accredited Electrolyte for High-voltage LCO/SiOx@C Battery factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in argon-filled, moisture-proof aluminum pouches, 1 kg per container, for safe high-voltage battery electrolyte storage. |
| Container Loading (20′ FCL) | 20′ FCL: High-voltage LCO/SiOx@C battery electrolyte, packed in sealed drums, secured, labeled, and handled per hazardous goods regulations. |
| Shipping | Shipped as hazardous material in sealed, moisture-proof containers under inert gas to preserve stability. Must avoid exposure to air, heat, and ignition sources. Labeled with flammable and corrosive warnings. Transport via ground or air compliant with IATA/IMDG regulations, with temperature control and upright positioning to prevent leakage or degradation. |
| Storage | Store in tightly sealed containers under dry, inert atmosphere (e.g., argon or nitrogen) to prevent moisture uptake and decomposition. Keep in a cool, well-ventilated, fire-safe area, away from heat, sparks, and open flames. Avoid exposure to extreme temperatures and direct sunlight. Use appropriate PPE and follow lithium-ion electrolyte handling protocols. |
| Shelf Life | Store sealed in a cool, dry place away from moisture and air; shelf life is typically 12 months. |
In high-voltage lithium cobalt oxide/silicon oxide-carbon composite pouch cells for high-energy-density smartphones, the electrolyte is formulated with fluorinated ethylene carbonate content between 8 wt% and 12 wt% and 1,3-propane sultone or prop-1-ene-1,3-sultone at 0.5 wt% to 2.0 wt%. The base solvent system is typically 1.0 M to 1.2 M LiPF6 in ethylene carbonate and ethyl methyl carbonate, with ethylene carbonate held below 25 vol% to avoid low-temperature precipitation. Filling is performed on a vacuum injection machine at a chamber vacuum below −0.095 MPa and a sealing temperature range of 175 °C to 185 °C. Formation uses a 0.05C constant-current step to 4.45 V and a constant-voltage taper to 0.02C at 45 °C under 0.3 MPa to 0.5 MPa clamping pressure. The electrolyte must remain anodically stable at 4.50 V vs Li/Li+ while forming a fluorinated silicon oxide layer on SiOx@C particles from fluoroethylene carbonate and lithium difluoro(oxalato)borate, limiting first-cycle irreversible loss to below 8%. Terminal cells in this class are assembled into 5,000 mAh to 6,000 mAh pouch cells with thickness below 4.8 mm for foldable handsets and high-capacity tablets. Safety and performance are verified against IEC 61960-3:2017 capacity labeling, GB 31241-2022 battery safety, and UN 38.3.4.6 impact test. Operational boundaries include electrolyte preparation in a dry room with dew point below −40 °C and avoidance of amine-based additives, which accelerate LiPF6 hydrolysis and produce HF above 20 ppm. Fluorinated additives used in this segment must comply with EU REACH Regulation EC 1907/2006 Annex XVII restrictions where applicable.
Batch-to-batch variance in high-voltage pouch lines is commonly observed at the wetting stage when the electrolyte contact angle on the SiOx@C anode exceeds 25° after 8 h of vacuum-assisted wetting, producing non-uniform SEI coverage. Degassing after formation is conducted at −0.098 MPa for 6 s to 10 s, and residual moisture in the sealed pouch is monitored by Karl Fischer titration at ≤20 ppm. On high-speed assembly lines using hot-pressing at 70 °C for 120 s, electrolyte loss through vapor entrainment must be kept below 0.5 wt% to avoid capacity imbalance. The lithium bis(oxalato)borate content is sometimes limited to 0.5 wt% to 1.0 wt% because higher loadings increase the cell impedance at −10 °C by more than 15% relative to baseline, as measured by the IEC 61960-3:2017 low-temperature discharge test.
Because SiOx@C anodes with more than 12 wt% silicon oxide generate a thicker and more porous SEI during the first lithiation, the electrolyte in UAV packs is usually formulated with 10 wt% to 15 wt% fluoroethylene carbonate and 1.0 wt% to 2.0 wt% prop-1-ene-1,3-sultone to suppress CO2 and CO evolution at the SiOx particle boundaries. Field data from multi-rotor UAV pack qualification show that storage at 4.45 V and 45 °C for 90 days produces acceptable swelling only when residual water in the electrolyte is maintained below 20 ppm and when the additive package includes 2.0 wt% to 4.0 wt% adiponitrile. Formation is implemented on a 256-channel cabinet with individual channel voltage accuracy of ±0.5 mV and chamber temperature uniformity of ±0.5 °C, using a 0.05C CC-CV procedure to 4.45 V with a 0.02C cutoff. Calendar life testing follows IEC 62660-1:2019 storage test conditions, and airworthiness evaluation uses UN 38.3.4.1 altitude simulation at 11.6 kPa for at least 6 h. Operational boundaries are specific: the electrolyte should not be exposed to ambient dew point above −30 °C during pack assembly, and the formulation is incompatible with carbonate solvents containing more than 50 ppm free acid, which accelerates SiOx dissolution and raises the 100% state-of-charge open-circuit voltage decay to more than 2 mV/day. Where public data for this specific LCO/SiOx@C configuration is limited, the storage acceptance thresholds are derived from internal pack qualification rather than public standards. Terminal products include fixed-wing survey drones and multi-rotor inspection platforms where the pack energy density must exceed 250 Wh/kg at cell level.
High-temperature abuse testing of action camera and body-worn camera cells places a separate constraint on the electrolyte: the cell is expected to survive 130 °C hot-box exposure without venting, while the electrolyte must support 2C continuous discharge at 60 °C without excessive gas generation. For this segment, the formulation often replaces part of the dimethyl carbonate with 2.0 wt% to 5.0 wt% sulfolane and adds 1.0 wt% lithium difluoro(oxalato)borate, because the difluoro(oxalato)borate anion forms a thinner and more thermally stable cathode electrolyte interphase on high-voltage LCO. The SiOx@C anode side is stabilized with 8.0 wt% fluoroethylene carbonate and 0.5 wt% 1,3-propane sultone. During manufacture, cells are filled in a dry room with dew point below −50 °C, sealed at 180 °C, and then subjected to a 45 °C formation protocol at 0.05C to 4.45 V followed by 60 °C aging for 7 days. Gas pockets are removed by vacuum degassing at −0.098 MPa for 8 s. Safety evaluation is performed according to UL 1642 crush and thermal ramp tests, IEC 62133-2:2017 forced internal short-circuit test, and UN 38.3.4.2 thermal test. A process limitation appears when the sulfolane content exceeds 5.0 wt%: the ionic conductivity at −20 °C falls below 2.0 mS/cm, measured by electrochemical impedance spectroscopy with a 10 mV perturbation from 100 kHz to 0.1 Hz. Published formation-gas composition data for this exact high-voltage LCO/SiOx@C action camera configuration is limited; therefore the acceptable gas pocket volume is established per cell manufacturer's internal specification rather than a public standard. Terminal products in this segment include Wi-Fi-enabled action cameras, helmet-mounted law-enforcement cameras, and external chest-mounted recording units requiring a 3,000 mAh to 4,000 mAh pouch cell with a 4.45 V maximum charge voltage.
Electrolyte purity requirements for patient-worn ambulatory monitors are defined by the need to hold self-discharge below 1.0 mV/day at 4.40 V after formation, and to keep HF concentration below 50 ppm after 500 h at 45 °C. The incoming electrolyte is controlled to a water content below 20 ppm, acidity below 50 ppm as HF, chloride below 2 ppm, and sulfate below 5 ppm, with LiPF6 purity above 99.99%. The solvent system is typically 1.0 M LiPF6 in ethylene carbonate, ethyl methyl carbonate, and dimethyl carbonate, with 2.0 wt% fluoroethylene carbonate, 1.0 wt% 1,3-propane sultone, and 0.5 wt% lithium difluoro(oxalato)borate. Manufacturing is performed in a dry room with dew point below −50 °C, and the electrolyte is dispensed through 0.2 µm PTFE filters to remove particulates above 200 nm. Pouch cells for medical packs are formed at 0.05C to 4.45 V at 40 °C, followed by 14 days of 25 °C aging with open-circuit voltage screening; cells with a voltage drop greater than 2 mV/day are rejected as high-self-discharge units. Regulatory evaluation follows ISO 13485:2016 for quality management, IEC 60601-1:2005+AMD1:2012 for medical electrical equipment safety, and IEC 62133-2:2017 for rechargeable cell safety. The electrolyte is not suitable for implantable applications requiring hermetic titanium enclosures and solid-state separators. Terminal products include wearable insulin pumps, continuous glucose monitors, ambulatory cardiac monitors, and portable oxygen concentrators with 2,500 mAh to 3,500 mAh pouch cells operating at a maximum charge voltage of 4.45 V.
Industrial handheld terminals that operate in uncontrolled thermal environments expose the electrolyte to intermittent excursions above 40 °C while the LCO cathode is held at 4.50 V vs Li/Li+. At this potential, ethylene carbonate oxidation generates CO2, water, and surface-bound polycarbonate oligomers; the water then hydrolyzes LiPF6 to HF, which attacks the SiOx network in the SiOx@C anode. Field observations from ruggedized handheld scanner packs show that after 300 cycles at 45 °C, separator pore resistance measured by electrochemical impedance spectroscopy increases from 5 mΩ to 18 mΩ when the additive package lacks a high-voltage stabilizer. An electrolyte formulation for this segment uses 1.1 M LiPF6 in ethylene carbonate/ethyl methyl carbonate with 3.0 wt% adiponitrile, 1.0 wt% prop-1-ene-1,3-sultone, and 8.0 wt% fluoroethylene carbonate, while the charge voltage is clamped to 4.45 V to keep the anodic current below 0.05 mA/cm² at 45 °C. Cells are validated under IEC 60068-2-14 thermal cycling from −20 °C to 70 °C with a 30 min dwell time, and under MIL-STD-810H for low-pressure storage at 4,500 m equivalent altitude. The dominant manufacturing bottleneck is wetting on the SiOx@C anode: if the electrolyte contact angle exceeds 30° after 6 h of vacuum wetting at −0.09 MPa, the first-cycle coulombic efficiency drops by 2% to 3% and the pack fails the 80% capacity retention requirement after 500 cycles. Terminal products include warehouse scanners, portable thermal printers, and field data terminals using 3,000 mAh to 5,000 mAh pouch cells.
Field teardowns of 4.0 Ah cordless power tool packs show lithium deposition concentrated at the outermost 5 mm of the SiOx@C anode, where current density rises due to tab offset and electrode misalignment, when the electrolyte is a 1.0 M LiPF6 in ethylene carbonate/ethyl methyl carbonate formulation with 8.0 wt% fluoroethylene carbonate. Reformulation with 0.5 M lithium bis(fluorosulfonyl)imide addition and 2.0 wt% vinyl ethylene carbonate reduces the electrolyte viscosity at 25 °C to below 3.0 mPa·s and improves the −20 °C discharge capacity retention to over 70% of rated capacity, as measured by IEC 61960-3:2017 low-temperature discharge. Cell assembly requires laser-welded aluminum tabs with 0.2 mm thickness and a negative electrode calendering density below 1.5 g/cm³ to maintain electrolyte penetration; the formation protocol uses 0.1C CC-CV to 4.40 V with a 0.05C cutoff at 25 °C. The electrolyte is incompatible with high concentrations of adiponitrile above 4.0 wt% in this application because the protective cathode film raises direct-current internal resistance above 40 mΩ and triggers the power tool’s undervoltage lockout during high-torque stall events. Safety validation is performed in accordance with IEC 62133-2:2017 and UL 2054 for battery packs, while the terminal cordless tools comply with IEC 62841-1 for hand-held motor-operated electric tools. Terminal products include 20 V cordless impact drivers and 18 V reciprocating saw packs using 2.5 Ah to 5.0 Ah high-voltage LCO/SiOx@C pouch cells.
Competitive Electrolyte for High-voltage LCO/SiOx@C Battery prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
HVE-LS is a non-aqueous lithium-ion electrolyte supplied for high-voltage lithium cobalt oxide cathodes paired with silicon suboxide-carbon composite anodes. The solvent matrix is a ternary carbonate system of ethylene carbonate, dimethyl carbonate, and ethyl methyl carbonate, modified with fluoroethylene carbonate and a phosphorus-oxygen-containing film former. The lithium salt is lithium hexafluorophosphate at a nominal concentration of 1.0 mol/L. The product is intended for cells with an upper charge cut-off between 4.45 V and 4.50 V and anode areal capacities above 3.0 mAh/cm². Incoming release limits specify moisture below 20 mg/kg, hydrogen fluoride acidity below 50 mg/kg, density of 1.24–1.30 g/cm³ at 25 °C, and ionic conductivity of 8.0–10.5 mS/cm at 25 °C. The electrolyte is filled only in dry rooms with a dew point at or below -40 °C and stored in sealed stainless steel or fluoropolymer-lined containers under nitrogen at 2–8 °C.
The product is supplied in 200 L stainless steel drums and 20 L fluorinated high-density polyethylene jerry cans. Typical cell formats are 18650 and 21700 cylindrical cells, and pouch cells up to 10 Ah, in which the SiOx@C anode has been calendered to 28%–35% porosity. On high-speed filling lines, lot viscosity variation should be limited to ±0.1 cP to avoid dose pump cavitation and variable electrode wetting. After vacuum filling, the lower contact angle of this solvent system on polyolefin separators is verified by electrochemical impedance spectroscopy at 1 kHz, and the wetting endpoint is recorded when the high-frequency resistance changes by less than 5% over 10 min.
The transition from 4.20 V to 4.45 V against Li/Li+ places the delithiated lithium cobalt oxide surface in a regime where lattice oxygen contributes to charge compensation. This increases the reactivity of surface oxygen toward carbonate solvents, generating lithium carbonate, ether-type species, and polycarbonates. If the cathode-electrolyte interphase is not stabilized, oxidative decomposition products deposit on the cathode, raise the charge-transfer impedance, and accelerate capacity loss. HVE-LS uses a fluorine-containing cosolvent and a phosphorus-oxygen film former to build a denser cathode interphase during the first formation cycle. The release condition for anodic stability is an oxidation current below 0.02 mA/cm² on aluminum foil at 4.6 V, measured by linear sweep voltammetry at 1 mV/s.
The silicon suboxide-carbon anode introduces a mechanical degradation mode that is not present in pure graphite cells. During lithiation, SiOx particles expand by more than 100% by volume, and the carbon coating must maintain electronic contact across the particle surface. Cracking of the primary particles exposes unreacted silicon to the electrolyte, and the reduction reaction consumes active lithium. In a conventional carbonate electrolyte without fluoroethylene carbonate, the solid electrolyte interphase is solvent-rich and insufficiently elastic; repeated volume changes rupture the film and expose fresh surface area. HVE-LS contains fluoroethylene carbonate, which defluorinates on the anode to lithium fluoride and vinylene carbonate-type polymer fragments. The resulting interphase on SiOx@C contains a higher proportion of lithium fluoride, which reduces solvent permeability and improves adhesion to the carbon layer.
The additive balance between cathode and anode is not independent. Excessive fluoroethylene carbonate or vinylene carbonate raises the full-cell impedance at 2 C and increases gas evolution during formation. Insufficient film former leaves the high-voltage LCO surface unprotected and permits transition metal dissolution. HVE-LS is compounded so that first-cycle Coulombic efficiency is maintained above 85% in SiOx@C cells, provided the anode is matched to the cathode capacity and the formation current is not above 0.05 C. The product also includes a nitrogen-containing adsorption additive that suppresses aluminum current collector pitting. This is particularly relevant when cathode foils are below 12 µm in thickness and local current density at the tab edge is high.
The oxidation kinetics are temperature-sensitive. Accelerated storage of full cells at 60 °C for 7 days is used to screen candidate electrolyte formulations because the high-temperature condition amplifies transition metal dissolution and electrolyte hydrolysis. The HVE-LS additive package is formulated to keep the post-storage resistance increase below 30% in 4.45 V LCO/SiOx@C cells. At 25 °C, the same impedance growth typically occurs over a much longer interval, but the exact lifetime depends on cell design and cycling depth. The operational boundary for HVE-LS is 4.55 V. Above this cut-off, carbonate solvent decomposition and cathode surface reconstruction accelerate rapidly, and the electrolyte cannot guarantee the specified capacity retention. Published data for this specific configuration above 4.55 V is limited; qualification is therefore required for any design that exceeds this threshold.
All release tests are performed on the liquid electrolyte before shipment. Table 1 lists the specification limits and the corresponding test procedures. The reported values are release limits, not cell-level predictions.
| Parameter | Release limit | Test procedure | Typical instrument |
|---|---|---|---|
| Water content | <20 mg/kg | ASTM E203 | Karl Fischer coulometer |
| Hydrogen fluoride acidity | <50 mg/kg | Potentiometric titration with 0.01 M sodium hydroxide | Auto-titrator |
| Density at 25 °C | 1.24–1.30 g/cm³ | ISO 1675 / ASTM D4052 | Digital density meter |
| Ionic conductivity at 25 °C | 8.0–10.5 mS/cm | Electrochemical impedance spectroscopy at 1 kHz | Conductivity cell |
| Kinematic viscosity at 25 °C | 3.5–4.5 cP | ASTM D445 | Automated viscometer |
| Anodic stability at 4.6 V vs Li/Li+ | <0.02 mA/cm² | Linear sweep voltammetry, 1 mV/s | Three-electrode cell with aluminum working electrode |
| Particulate content >10 µm | <100 particles/mL | Optical particle counting after filtration | Liquid particle counter |
Batch release records include solvent ratio by gas chromatography-mass spectrometry, with fluoroethylene carbonate content controlled to ±0.5 wt%. Viscosity is controlled to ±0.1 cP and ionic conductivity to ±0.3 mS/cm across compounding lots. These limits are monitored on 200 L stainless steel mixing systems with 0.22 µm polytetrafluoroethylene cartridge filtration before filling. Closed-loop sampling is performed through a syringe port under nitrogen; no open-container transfer is permitted at relative humidity above 5%. The first 2–3 L through a new filter cartridge is discarded or returned to the purifier because filter wetting can release low levels of adsorbed water and oligomers.
Commercial filling sequences for HVE-LS use a two-step vacuum filling profile. The dry cell is evacuated to below -90 kPa gauge, the electrolyte is injected at 0.4–0.7 MPa, and the cell rests under dry nitrogen until the high-frequency resistance at 1 kHz stabilizes. Formation charging starts at 0.05 C constant current to 4.45 V, then holds at constant voltage until the current decays to 0.02 C. The first-cycle gas is removed by vacuum degassing before final sealing; residual gas is principally ethylene and carbon dioxide from solvent reduction and solid electrolyte interphase formation. Cells that skip the degassing step can exceed 0.6 MPa internal pressure, leading to separator intrusion or pouch delamination. This is more severe in pouch cells with aluminum-polymer laminate packaging because the package does not provide the same mechanical constraint as a cylindrical can.
Formation gas composition can be measured by gas chromatography with a thermal conductivity detector; the major components are ethylene, carbon dioxide, and trace hydrogen. In cells with excessive moisture, hydrogen fluoride and phosphorus pentafluoride may appear, and the gas stream becomes corrosive to degassing manifolds. During electrolyte handling, the product is incompatible with water, alcohols, and strong amines. Salt hydrolysis in the presence of moisture produces hydrogen fluoride and phosphorus oxyfluoride. Open exposure at ambient humidity can raise acidity above 100 mg/kg within 24 h. Transfer lines should be passivated with a small volume of electrolyte before production filling, and wetted parts should be stainless steel or fully fluorinated elastomers. Nitrile rubber seals are not recommended because prolonged contact can swell the elastomer and introduce contamination. If ambient relative humidity exceeds 60%, pre-drying of all filling equipment is required and open handling time should not exceed 15 min.
Regulatory testing should be performed on the finished cell rather than on the liquid electrolyte alone because formation changes the electrolyte composition. Table 2 lists the applicable standards for common qualification programs.
| Standard or regulation | Scope | Typical test article condition |
|---|---|---|
| IEC 62660-2 | Cycle life and performance for traction cells | Pouch or cylindrical cell at 45 °C, SOC 100% |
| IEC 62133-2 | Safety for portable sealed secondary cells | Cell with production-intent housing |
| UN 38.3 | Transport safety of lithium metal and lithium-ion cells | Cell and battery pack as shipped |
| REACH regulation 1907/2006 Annex XVII | Restricted substances in solvents and additives | Liquid electrolyte sample |
| RoHS 2011/65/EU Annex II | Lead, cadmium, mercury, hexavalent chromium, PBB, PBDE | Finished cell components |
For transport of the liquid electrolyte, the shipper must verify classification as a corrosive flammable liquid and assign the appropriate packing group. HVE-LS solvent vapor is flammable and the liquid is corrosive; containers must be grounded, bonded, and kept below the flash point during transfer. The flash point is specified by closed-cup testing according to ASTM D56; because the value is below 60 °C, the liquid is classified as a flammable liquid. The product does not contain intentionally added lead, cadmium, mercury, or hexavalent chromium above the thresholds of RoHS 2011/65/EU Annex II.
Compared with standard 1 M LiPF6 in ethylene carbonate-dimethyl carbonate-ethyl methyl carbonate designed for graphite/LCO cells up to 4.2 V, HVE-LS differs in three respects. First, the fluoroethylene carbonate content is higher to support SiOx@C cycling, whereas conventional low-voltage LCO electrolytes may rely primarily on vinylene carbonate. Second, the phosphorus-oxygen additive is selected for high-voltage LCO surface passivation and aluminum current collector protection, not for overcharge gas suppression. Third, the solvent ratio is adjusted to maintain high-frequency conductivity while retaining the flash point classification for a corrosive flammable liquid. HVE-LS should not be treated as a drop-in replacement for low-voltage LCO cells; the additive package can increase first-cycle irreversible capacity on pure graphite if the anode is not pre-lithiated or if the formation current is too high.
The product also differs from electrolytes intended for lithium-rich manganese-based cathodes or for solid-state cells. Lithium-rich systems require stabilization of lattice oxygen beyond 4.6 V, which is outside the intended window for HVE-LS. Lithium titanate anodes and lithium iron phosphate cathodes do not require the same high-voltage additive package and may show increased interfacial impedance without benefit. HVE-LS is intended only for liquid-electrolyte cells with a high-voltage LCO cathode and a SiOx@C anode operating between 4.45 V and 4.50 V. For any cell design with upper voltage above 4.55 V, qualification must include storage at 60 °C for 30 days and post-storage impedance growth below 30% before production release.