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Electrolyte for MnO2/Li Primary Battery

    • Product Name: Electrolyte for MnO2/Li Primary Battery
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 847691
    Chemical Composition Lithium perchlorate (LiClO4) in propylene carbonate (PC)
    Solute LiClO4
    Solvent Propylene carbonate
    Concentration 1.0 mol/L
    Water Content ≤20 ppm
    Conductivity 5-7 mS/cm at 25°C
    Density 1.1 g/cm³ at 25°C
    Viscosity 2.5 cP at 25°C
    Flash Point 132°C
    Operating Temperature Range -20°C to +60°C
    Shelf Life 12 months under inert atmosphere
    Moisture Sensitivity Hygroscopic; store sealed in dry, inert environment

    As an accredited Electrolyte for MnO2/Li Primary Battery factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in a 1 L sealed HDPE bottle with tamper-evident cap, labeled clearly for MnO2/Li primary battery electrolyte use.
    Container Loading (20′ FCL) 20′ FCL container loading of hazardous electrolyte for MnO2/Li primary batteries, securely packed in drums, with proper segregation and bracing.
    Shipping Ships as a hazardous material (Class 3 flammable liquid). Pack in leak-proof, corrosion-resistant containers, sealed under inert atmosphere. Avoid moisture, heat, and ignition sources. Provide proper labels, MSDS, and documentation. Transport by ground or cargo vessel per IATA/IMDG; forbidden on passenger aircraft.
    Storage Store the electrolyte in tightly sealed, corrosion-resistant containers under a dry, inert atmosphere. Keep in a cool, well-ventilated area away from direct sunlight, moisture, heat, and ignition sources. Avoid contact with acids, strong oxidizers, or reactive metals. Label clearly, inspect regularly, and follow manufacturer’s safety data sheet for disposal and spill procedures.
    Shelf Life Typically 2–5 years when stored sealed, dry, and at room temperature, away from moisture, heat, and direct sunlight.
    Application of Electrolyte for MnO2/Li Primary Battery

    In spiral-wound Li/MnO₂ cells manufactured for 3 V high-pulse security equipment, electrolyte selection is constrained by two competing requirements: sufficient low-temperature conductivity for immediate pulse delivery and a moisture threshold that prevents lithium surface corrosion during multi-year storage. The electrolyte consists of lithium perchlorate at 0.8–1.0 mol dm⁻³ in a propylene carbonate/1,2-dimethoxyethane solvent blend with a volumetric PC:DME ratio between 40:60 and 60:40; DME-rich grades shift the conductivity low-temperature knee toward −40 °C, while PC-rich grades reduce volatility at the cost of higher viscosity. Electrolyte fill in CR123A-class cells is dosed at 0.30–0.45 mL per Ah, corresponding to 0.45–0.65 mL per nominal 1.55 Ah cell, with the lower fill reserved for tightly wound electrode groups where electrolyte wicking reaches the innermost separator layer within 20 min at −70 kPa vacuum; published cell-specific retention data are limited, and the lower fill limit should be validated by wicking tests. During production, the cathode is formed from heat-treated electrolytic manganese dioxide blended with 6–10 wt% conductive carbon and 3–5 wt% PTFE binder on an expanded stainless steel or aluminum grid; the electrode group is wound around a 2.0–2.5 mm mandrel and inserted into a nickel-plated deep-drawn steel can. Electrolyte is injected in a dry room with dew point not exceeding −40 °C, followed by vacuum standing, closure with a polypropylene gasket, crimping, and a controlled pre-discharge step that consumes 2–5% of rated capacity to stabilize the lithium surface. Free amine contamination is excluded from the production area because amine compounds accelerate lithium surface pitting during high-temperature storage. Finished cell types in this group include CR123A, CR2, and 2/3A cylindrical cells, subsequently assembled into electronic locks, infrared illuminators, laser rangefinders, and security alarm panels. Compliance is evaluated under UL 1642, IEC 60086-4:2019, UN ST/SG/AC.10/11/Rev.7, Part III, subsection 38.3 tests T1–T8, and the RoHS Directive 2011/65/EU for restricted substances in cell components.

    Why Does the Bobbin-Wound Metering Cell Use a PC-Rich Electrolyte While Spiral-Wound Cells Do Not?

    Bobbin-wound Li/MnO₂ cells for utility automatic meter reading, industrial data loggers, and remote telemetry require discharge currents below 50 mA and shelf service exceeding 10 years; the long storage requirement shifts the electrolyte toward a propylene carbonate-rich blend with a volumetric PC:DME ratio between 70:30 and 80:20, using lithium perchlorate at 0.5–0.8 mol dm⁻³ to reduce 1,2-dimethoxyethane evaporation through crimp seals while retaining a liquid range that supports operation at −30 °C. Electrolyte addition in bobbin cells is commonly 0.55–0.75 mL per Ah because the bobbin electrode geometry has a longer radial diffusion path than spiral-wound electrodes; a CR17450 cell with 2.4 Ah nominal capacity receives 1.3–1.8 mL, depending on separator thickness and void volume. During manufacturing, the lithium anode is pressed onto the inner wall of a nickel-plated steel can, a microporous polypropylene separator is inserted, and the pre-pressed cathode bobbin—composed of heat-treated electrolytic MnO₂, carbon black, and a 4–6 wt% PTFE binder—is placed concentrically without breaking the cathode edge. The cell is filled under vacuum with a dosing tolerance of ±0.05 mL, aged at 45 °C for 24–48 h to equilibrate electrolyte distribution, and pre-discharged by 3–5% before final crimp closure. Operational boundary: cells filled with PC-rich electrolyte should not be stored above 85 °C; accelerated aging under such conditions has shown separator pore collapse and lithium surface roughening. Terminal products include CR17450, CR26500, and CR34615 cylindrical primary cells embedded in gas meters, heat meters, water meters, and remote telemetry units. Compliance follows IEC 60086-4:2019, UL 1642, and UN 38.3 Rev.7; metering components are additionally assessed under IEC 62052-11 when the cell is mounted on the same PCB.

    Where board-mounted backup requires discharge currents below 10 µA and annual self-discharge below 2%, coin-type Li/MnO₂ cells use a lower-moisture electrolyte than cylindrical cells because the shrink-seal interface of a coin can is less tolerant of creeping electrolyte. The electrolyte is a 0.6–1.0 mol dm⁻³ lithium perchlorate solution in PC/DME with a volumetric ratio near 50:50, filtered to reduce sodium and calcium to ≤5 mg kg⁻¹ each; the addition ratio for a CR2032 cell is 70–110 µL, equivalent to 0.28–0.44 mL per Ah at a rated capacity of 220–240 mAh. In production, the cathode pellet is pressed at 10–15 MPa onto a stainless steel expanded-metal grid after blending heat-treated electrolytic MnO₂ with 5–8 wt% acetylene black and 2–4 wt% polytetrafluoroethylene; a lithium disc is pressed into the stainless steel anode cap, a 25 µm polypropylene separator is placed over the cathode, and electrolyte is delivered by a positive-displacement ceramic pump before the polypropylene gasket is crimped to seal the cell. Ambient humidity above 60% RH during crimping increases white salt creep around the gasket and must be controlled by dry-room sequencing. Finished coin cell types include CR2016, CR2025, CR2032, and CR2450, used in real-time-clock modules, automotive remote keyless entry fobs, CMOS battery backup, glucose meters, and electronic shelf labels. Safety and transport compliance is assessed under IEC 60086-4:2019, UL 1642, and UN ST/SG/AC.10/11/Rev.7, Part III, subsection 38.3; coin-cell ingestion safety requirements are applied as specified in IEC 60086-4:2019.

    Thin-Foil Pouch Li/MnO₂ Cells for Single-Use Cold-Chain Data Loggers

    Thin-foil pouch Li/MnO₂ cells for single-use cold-chain data loggers and disposable RFID tracking tags require an electrolyte that remains conductive after 48 h of exposure to −30 °C while avoiding crystallization at the lithium/separator interface. The electrolyte is formulated with a DME-rich PC/DME volumetric ratio of 30:70 to 40:60, using lithium perchlorate at 0.5–0.8 mol dm⁻³; the addition ratio is 0.35–0.50 mL per Ah for cells below 150 mAh capacity, and 0.20–0.30 mL per Ah for cells above 500 mAh. The downstream process begins with slot-die coating of the MnO₂ cathode onto an aluminum foil substrate, followed by lamination against a lithium foil anode and a 16–25 µm polypropylene or polyethylene separator; the electrolyte is filled under partial vacuum, and the pouch is sealed by impulse heat-staking at 180–200 °C with seal width not less than 2 mm. DME-rich formulations are unsuitable for crimp-sealed cells stored above 60 °C because 1,2-dimethoxyethane vapor pressure unseats polypropylene gaskets; pouch cells avoid this failure by eliminating the crimp boundary. Terminal products include 3 V pouch primary cells with capacities from 30 mAh to 1 Ah, integrated into cold-chain temperature loggers, disposable medical diagnostic cartridges, smart labels, and event-activated RFID tracking modules. Compliance includes UN 38.3 Rev.7 transport tests, IEC 60086-4:2019, UL 1642, and restricted-substance screening under REACH Regulation (EC) No 1907/2006 Annex XVII for imported electrolyte components.

    Cell configurationPC:DME volumetric ratioElectrolyte salt concentrationElectrolyte fill ratioPrimary safety standards
    Spiral-wound high-rate CR123A / CR240:6060:40LiClO₄ 0.8–1.0 mol dm⁻³0.30–0.45 mL Ah⁻¹IEC 60086-4:2019; UL 1642; UN 38.3 Rev.7
    Bobbin metering CR17450 / CR26500 / CR3461570:3080:20LiClO₄ 0.5–0.8 mol dm⁻³0.55–0.75 mL Ah⁻¹IEC 60086-4:2019; UL 1642; UN 38.3 Rev.7
    Coin backup CR2016–CR245050:50 nominalLiClO₄ 0.6–1.0 mol dm⁻³70–110 µL per CR2032; 0.28–0.44 mL Ah⁻¹IEC 60086-4:2019; UL 1642; UN 38.3 Rev.7
    Thin-pouch cold-chain 30 mAh1 Ah30:7040:60LiClO₄ 0.5–0.8 mol dm⁻³0.35–0.50 mL Ah⁻¹ below 150 mAh; 0.20–0.30 mL Ah⁻¹ above 500 mAhIEC 60086-4:2019; UL 1642; UN 38.3 Rev.7; REACH Annex XVII

    If the Crimp Seal Is Exposed to High Humidity, Water Ingress Rather Than Electrolyte Conductivity Limits Shelf Life

    If a crimp-sealed cylindrical Li/MnO₂ cell is deployed in outdoor GPS buoys and emergency locator transmitters, water ingress through the polypropylene gasket becomes the dominant failure mode long before electrolyte dry-out. The electrolyte for this application is formulated with a PC/DME ratio of 55:45 to 65:35, lithium perchlorate concentration 0.8–1.0 mol dm⁻³, and a water specification of ≤20 mg kg⁻¹ at the point of fill; electrolyte fill is maintained at 0.45–0.55 mL per Ah because cells are intermittently pulse-loaded with 1.0–2.5 A current peaks for RF transmission. Downstream, the steel can is nickel-plated and the polypropylene gasket is coated with a high-viscosity hydrocarbon sealant before crimping; the cell is filled under vacuum and then subjected to a leak test using helium mass spectrometry with a reject limit of 1×10⁻⁶ mbar·L s⁻¹. The sealant is cured below 50 °C to avoid premature electrolyte vaporization. Terminal products include CR123A and 2/3A cells embedded in avalanche transceivers, EPIRB emergency beacons, GPS tracking collars, and wildlife telemetry tags. Standards include IEC 60086-4:2019, UL 1642, UN 38.3 Rev.7, and IEC 60529 IP67 enclosure-level sealing when the cell is potted inside the device.

    To maintain a discharge plateau above 2.0 V under 30 kΩ loads for 14 days, continuous glucose monitor backup units require a tightly controlled PC/DME ratio of 50:50 and a lithium perchlorate concentration of 0.8 mol dm⁻³; the electrolyte is injected into CR2032-class cells at 60–90 µL, lower than conventional RTC coin cells, to reduce the risk of creep across the polypropylene gasket during flexing of the wearable module. The downstream production process uses a lithium disc pressed into the stainless steel anode cap, a 25 µm polypropylene separator, and a cathode pellet pressed at 12 MPa from heat-treated electrolytic MnO₂ with 6 wt% acetylene black and 3 wt% PTFE binder; after electrolyte dosing, the cell is closed by double-crimp and aged for 72 h at 60 °C to screen for internal shorting and leakage. The electrolyte is not formulated for continuous currents above 1 mA; sustained higher loads produce voltage drop and reduce service life. Terminal products are disposable wearable glucose sensors and transmitter modules requiring a primary 3 V supply over a 14-day wear interval. Compliance for the cell is assessed under IEC 60086-4:2019, UL 1642, and UN 38.3 Rev.7; device-level risk management follows ISO 14971:2019 when the cell is integrated into a wearable sensor.

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    Certification & Compliance
    More Introduction

    Model ELM-1M-PC/DME-50 is a nonaqueous electrolyte supplied for lithium manganese dioxide primary cells assembled and tested to IEC 60086-4:2019. The electrolyte consists of anhydrous lithium perchlorate dissolved in a volumetric propylene carbonate/1,2-dimethoxyethane blend, with a salt concentration controlled between 0.98 mol dm⁻³ and 1.02 mol dm⁻³ and a solvent ratio of 50:50 ± 2 vol%. The finished liquid is filtered through a 0.2 µm PTFE membrane, filled under inert gas, and released with water content not exceeding 50 mg kg⁻¹. The product is intended for crimp-sealed coin cells, spirally wound cylindrical cells, and hermetically sealed prismatic cells where the cathode is heat-treated manganese dioxide and the anode is metallic lithium. It is not intended for rechargeable lithium-ion systems, and it is not a direct substitute for electrolytes used in lithium thionyl chloride or lithium carbon monofluoride cells.

    What moisture limit governs lithium anode passivation and impedance growth in nonaqueous primary cells?

    In Li/MnO₂ primary cells, the electrolyte participates in formation of the anode solid electrolyte interphase rather than functioning solely as an ion-transport medium. When the solution contacts metallic lithium, propylene carbonate and perchlorate anions are reduced to a composite film containing lithium carbonate, lithium alkoxides, lithium chloride, and small amounts of lithium hydroxide if water is present. The film limits further solvent reduction and controls the resting open-circuit voltage of the cell. Water ingress above 50 mg kg⁻¹ alters the film from a compact, chloride-bearing passivation layer to a thicker, less uniform deposit with a higher proportion of lithium hydroxide and carbonate. This change is observed on production cells as an increase in closed-circuit voltage depression during pulse discharge and a rise in internal impedance after high-temperature storage.

    The release specification therefore relies on coulometric Karl Fischer titration according to ISO 760, not on conductivity alone. Samples are drawn through PTFE septum lines and titrated in a dry compartment; titrator background drift is held below 5 µg min⁻¹. The water limit of 50 mg kg⁻¹ is applied because cell-level impedance data are strongly sensitive to small amounts of protic contamination, and drying of electrolyte after packaging is not permitted in the production flow.

    PropertyRelease specificationMethod / equipment
    LiClO₄ concentration0.98–1.02 mol dm⁻³Potentiometric titration in acetonitrile
    PC/DME volume ratio50:50 ± 2 vol%Gas chromatography with flame ionisation detection
    Water content50 mg kg⁻¹ISO 760 coulometric Karl Fischer
    Chloride content10 mg kg⁻¹Ion chromatography
    Free acidity as HF30 mg kg⁻¹Nonaqueous acid-base titration
    Conductivity at 25 °C10.5–12.5 mS cm⁻¹Two-electrode impedance spectroscopy at 1 kHz
    Kinematic viscosity at 25 °C2.8–3.6 mm² s⁻¹ASTM D7042
    Density at 20 °C1.11–1.14 g cm⁻³ASTM D4052

    Elemental impurities for iron, sodium, potassium, calcium, and chromium are each limited to less than 5 mg kg⁻¹ by inductively coupled plasma optical emission spectrometry. The chloride specification is tighter than the water specification because free chloride accelerates localised lithium corrosion and can attack aluminium cathode grid material when the cell potential remains above 3.0 V.

    At a production-scale crimp-sealed CR2032 line, electrolyte filling is executed in a dry-air enclosure with a dew point below −45 °C and oxygen below 100 ppm. Positive-displacement ceramic microvalves with 316L stainless steel or PTFE wetted parts are specified; 1,2-dimethoxyethane swells silicone and many perfluoroelastomer seals, so elastomer grades are screened by immersion in electrolyte at 60 °C for 72 h according to ASTM D471. Fill mass is matched to the heat-treated MnO₂ cathode pore volume and separator voidage, not to a fixed volume. On 20 mm diameter coin cells, the qualified fill mass is 0.18–0.28 g, with final confirmation by low-rate pulse discharge and post-fill impedance. In spirally wound cylindrical cells, vacuum filling through the mandrel void is used to avoid gas pockets, and the first low-rate discharge check is run within 24 h of filling to identify pockets of poor wetting.

    Battery assembly lots have shown two recurrent failure modes associated with electrolyte handling. The first is water ingress through crimp-seal compression after filling, which produces intermittent high-impedance cells and is traced by Karl Fischer analysis of electrolyte sampled from unsealed cells. The second is solvent evaporation from open reservoirs in automated dosing systems, which shifts the PC/DME ratio and increases viscosity. Continuous closed-loop delivery from stainless steel pressure vessels with 0.2 µm filter cartridges is used to control both failure modes.

    Electrolyte viscosity variation has been monitored across 14 production lots; kinematic viscosity at 25 °C remained within 2.9–3.4 mm² s⁻¹ measured by ASTM D7042, corresponding to a fill-weight variation below ±3 % on fixed-time ceramic micropump dosing. This variation is acceptable for coin-cell lines but must be revalidated for large-format prismatic cells with multi-point filling manifolds.

    Prior to electrolyte filling, heat-treated manganese dioxide cathodes are dried under vacuum at 350–400 °C for 2–4 h and transferred to the dry room without exposure to ambient air. Cathode water content above 500 mg kg⁻¹ is a known source of batch-to-batch impedance variation, independent of electrolyte water. If the dried cathode is exposed to room ambient for more than 15 min, water uptake can reverse the drying step and produce high-impedance cells in subsequent electrical ageing.

    The product is assigned a storage life of 12 months at 5–25 °C in unopened stainless steel or glass containers under argon. Opened containers are not returned to long-term storage; the headspace is blanketed with argon and the water content is re-verified after any exposure exceeding 30 min at ambient humidity. The product is a flammable liquid because of its DME content. Closed-cup flash point testing by ASTM D3278 places the 50 vol% DME grade below 25 °C, and handling areas must comply with local flammable-liquid ventilation requirements. Perchlorate salts require separation from strong acids, reducing agents, and organic peroxides.

    Stability boundaries shift when DME content exceeds 50 vol%

    The product family includes 30 vol%, 50 vol%, and 70 vol% DME variants. Raising DME content from 50 vol% to 70 vol% reduces electrolyte viscosity and improves wetting of microporous polyolefin separators at low temperature, but it also increases solvent vapour pressure and reduces the closed-cup flash point. The 70 vol% variant is therefore limited to cells with high-integrity closure systems and is not supplied as a drop-in replacement for polypropylene crimp-seal applications without seal qualification under ASTM D471 and cell-level thermal cycling per IEC 60086-4:2019.

    When DME content exceeds 50 vol%, the lithium surface film becomes more oligoether-like and less carbonate-rich. This lowers interfacial resistance at −20 °C, which is useful for low-temperature pulse discharge, but it also reduces the passivating character of the film during sustained high-temperature storage. The 70 vol% DME grade is not specified for continuous exposure above 60 °C unless the cell manufacturer has completed anode passivation qualification. Voltage recovery after pulse discharge in the 50 vol% grade is typically faster than in the 70 vol% grade after identical 60 °C ageing, because the carbonate-rich film has lower interfacial leakage.

    Low-temperature conductivity, vapour pressure, and seal compatibility data

    Comparison of 1.0 mol dm⁻³ LiClO₄ in 50 vol% PC/DME with equivalent LiCF₃SO₃ and LiTFSI formulations indicates that conductivity at 25 °C for the LiClO₄ system is 10.5–12.5 mS cm⁻¹, whereas LiCF₃SO₃ in the same solvent blend is typically 4.5–5.5 mS cm⁻¹ at identical molality. The difference is attributed to stronger ion pairing of the triflate anion and a larger hydrodynamic radius. LiTFSI-based electrolytes can achieve 11.0–13.0 mS cm⁻¹ at 25 °C and show lower sensitivity to water, but their reduction products on metallic lithium do not provide the same chloride-bearing compact surface film. In MnO₂/Li primary cells, this film is functionally relevant for voltage stability and long-term self-discharge; product qualification therefore includes anode film formation tests in reference cells, not merely salt performance comparisons.

    The vapour pressure of the 50 vol% DME grade at 60 °C is controlled by the DME content and limits the upper processing temperature in open reservoirs. Closed-loop filling systems are sized to maintain a vapour space concentration below 50 % of the lower flammability limit. Seal compatibility data show that the 50 vol% DME grade has acceptable dimensional change in polypropylene and PPS gaskets after 72 h at 60 °C, while the 70 vol% DME grade can exceed 10 % volume swell in some low-crystallinity polyolefins.

    Standard or regulationScopePosition of this electrolyte
    IEC 60086-4:2019Safety of lithium primary batteriesReference cell builds are used for abnormal charge, forced discharge, and thermal cycling; the electrolyte is qualified as part of the cell system
    ISO 760Water determination by Karl FischerRelease water content ≤ 50 mg kg⁻¹
    ASTM D7042Dynamic viscosity and densityRelease viscosity 2.8–3.6 mm² s⁻¹ at 25 °C
    ASTM D4052Density by digital density meterRelease density 1.11–1.14 g cm⁻³ at 20 °C
    ASTM D471Rubber property effect of liquidsSeal compatibility screening for crimp-seal and mandrel closure elastomers
    EC No 1907/2006 (REACH)Chemical registration and restrictionComponents are REACH-registered within applicable tonnage bands; no candidate-list substance at reportable concentration

    When LiClO₄–PC/DME replaces LiCF₃SO₃ in high-temperature storage applications

    Substitution of an existing LiCF₃SO₃-based electrolyte with this LiClO₄ product is a change to anode passivation chemistry rather than a simple conductivity increase. The chloride-bearing reduction film stabilises the lithium anode during high-temperature storage, but it also increases the penalty for residual moisture in the dry room. Production lines previously qualified with triflate electrolytes are required to re-verify dew-point control, Karl Fischer sampling, and crimp-seal leak rate. Abuse testing under IEC 60086-4:2019 is repeated because the higher conductivity of LiClO₄ raises the available short-circuit current; the consequential cell surface temperature rise remains within the standard pass/fail limits when the separator thickness and anode-to-cathode capacity ratio are unchanged. The product is not interchangeable with LiTFSI or LiCF₃SO₃ electrolytes in formulations where low moisture uptake is the primary selection criterion.

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