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3.0 V High-voltage Electrolyte for EDLC

    • Product Name: 3.0 V High-voltage Electrolyte for EDLC
    • 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 393142
    Product Name 3.0 V High-voltage Electrolyte for EDLC
    Voltage Rating 3.0 V
    Electrolyte Type Organic electrolyte
    Solute Quaternary ammonium salt
    Solvent Organic carbonate mixture
    Conductivity 10-20 mS/cm
    Water Content ≤ 20 ppm
    Purity ≥ 99.9%
    Flash Point ≥ 60 °C
    Density 1.0-1.3 g/cm³
    Operating Temperature Range -40 °C to +70 °C
    Capacitance Retention ≥ 90% after 1000 hours
    Lifespan ≥ 5000 hours at rated voltage
    Storage Temperature Range -10 °C to +40 °C
    Packaging Sealed aluminum container

    As an accredited 3.0 V High-voltage Electrolyte for EDLC factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 1 L sealed aluminum bottles under argon, ensuring purity and safety for high-voltage EDLC electrolyte applications.
    Container Loading (20′ FCL) Load 3.0V EDLC electrolyte in 20′ FCL: use approved drums, secure bracing, mark flammable, observe segregation and ventilation.
    Shipping This electrolyte is shipped in sealed, leak-proof containers with moisture-resistant packaging. Transport follows hazardous material regulations, with proper labeling and documentation. Keep away from heat, sparks, and direct sunlight during transit. Handle with care to prevent damage, leakage, or contamination.
    Storage Store the 3.0 V high-voltage EDLC electrolyte in a tightly sealed, original container to prevent moisture absorption and contamination. Keep in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Avoid contact with oxidizing agents, acids, and bases. Ensure proper labeling and use spill-containment measures.
    Shelf Life Shelf life: typically 12 months when stored sealed, cool, and dry. Avoid moisture and contamination; proper storage ensures stability.
    Application of 3.0 V High-voltage Electrolyte for EDLC

    In 12 V start-stop and 48 V belt-driven starter-generator architectures, 3.0 V high-voltage EDLC cells are assembled into six-cell or eighteen-cell series strings to create modules rated at 18 V or 54 V. A representative high-rate electrolyte is 1.0 mol/L tetraethylammonium tetrafluoroborate (TEABF4) in acetonitrile, with water content controlled below 20 ppm and free acid below 30 ppm. Bulk conductivity measured in a four-electrode conductivity cell at 25 °C is reported in the range 55–60 mS/cm; this is approximately three times the conductivity of a 1.0 M TEABF4/propylene carbonate analogue. The acetonitrile solvent imposes the main processing boundary: closed-cup flash point is 2 °C per ASTM D3828 and boiling point is 81 °C at 101.3 kPa. Cell assembly therefore occurs in a dry room with dew point ≤ −50 °C, electrolyte is introduced by vacuum dosing, and the aluminium can is hermetically sealed by laser welding. Formation consists of a constant-voltage hold at 3.0 V for 4–12 h; leakage current measured at 25 °C after 72 h is accepted only below 0.5 mA for a 3000 F cylindrical cell. Cell-to-cell sorting before module build requires capacitance spread within ±2% and DC internal resistance spread within ±5% to limit string imbalance. Qualification follows IEC 62391-2:2019 endurance testing at rated voltage and upper category temperature; for acetonitrile cells the upper category temperature is commonly limited to 65 °C, while 85 °C operation requires propylene carbonate or blended nitrile formulations. Mechanical and environmental validation is performed under ISO 16750-3:2012 vibration profiles for sprung and unsprung mass in road vehicles. The terminal product is a sealed 48 V or 12 V high-power module used for engine cranking, start-stop coasting-phase support, and transient recuperation buffering; the 48 V eighteen-cell module is integrated into belt-driven starter-generator rails where peak charge and discharge currents exceed sustained alternator capability.

    What Limits Calendar Life in 3.0 V EDLC Modules Used for Data Centre Ride-Through?

    Data centre ride-through configurations place the capacitor bank on a 48 V DC-bus or integrate it into a UPS bridge module to cover generator start and controlled server shutdown cycles lasting 10–30 s. The electrolyte selection is driven by calendar life and fire-safety constraints rather than peak conductivity. Acetonitrile provides 55–60 mS/cm at 25 °C but carries a 2 °C closed-cup flash point; 1.0 M TEABF4 in propylene carbonate provides 16–18 mS/cm with a 132 °C closed-cup flash point per ASTM D3828. Data centre modules often use the propylene carbonate system or an acetonitrile/PC blend only where high discharge rate is not required, because the lower vapour pressure reduces containment requirements during a thermal event. Module qualification is performed under UL 810A for electrochemical capacitor safety and IEC 62040-3 for UPS functional performance, with thermal imaging at full charge to verify that surface temperature rise remains below 45 °C in a 25 °C ambient. Cell balancing is fixed at 2.85 V per cell float, leaving a 0.15 V derating margin below the 3.0 V ceiling to reduce oxidation of residual water and solvent at the positive electrode surface. Production sorting for an eighteen-cell string requires capacitance spread within ±1.5% and ESR spread within ±4%; passive resistive balancing current is sized between 1 mA and 5 mA per 100 F of cell capacitance. The rack-mount enclosure is assigned IP20 according to IEC 60529, with forced airflow across busbar terminations; dry-room fill is executed at dew point ≤ −40 °C, followed by ageing at 60 °C for 48 h before final leakage acceptance. Terminal product is a 48 V rack-mount module with integrated balancing board, status relay output, and a target service interval of 10 years at 25 °C; published data for 20-year calendar life at elevated data centre inlet temperatures is limited.

    Because hub-mounted pitch electronics are exposed to ambient temperature without block heating, the 3.0 V EDLC bank must deliver full pitch motor voltage after a cold soak at −40 °C. The selected electrolyte is 1.0 mol/L spiro-(1,1')-bipyrrolidinium tetrafluoroborate (SBPBF4) in acetonitrile, which gives a wider anodic stability window than TEABF4 under repeated charge acceptance; low-temperature solubility of SBPBF4 is lower than TEABF4, so cold-soak validation is mandatory before field release. The eighteen-cell module is floated at 2.85 V per cell, with an alarm threshold at 2.95 V per cell and active balancing during standby to prevent voltage divergence caused by leakage current differences. Module assembly uses matched cells sorted for capacitance within ±1.5% and ESR within ±4%, welded busbars, and a conformal-coated balance board to resist salt mist; the complete bank is tested under IEC 60068-2-52 cyclic salt mist and vibration derived from IEC 61400-1 design load cases. Electrolyte filling and sealing are performed in a dry room at dew point ≤ −50 °C; the cell undergoes vacuum fill, constant-voltage formation at 3.0 V, and final leakage screening before module integration. Qualification also follows IEC 62391-2:2019 for endurance at rated voltage and low-temperature capacitance/ESR testing; acceptance at −40 °C requires capacitance retention from 25 °C to be no less than −20% and ESR increase no greater than the 25 °C value according to the module specification. The terminal product is a 54 V pitch backup bank, sized to deliver 10–20 kJ per blade during emergency feathering for a typical 2 MW turbine; exact energy sizing is dependent on pitch motor inrush and gear ratio rather than turbine power alone.

    If Propylene Carbonate Replaces Acetonitrile in Smart Meter Pulse Duty

    Smart metering uses the EDLC not for high-rate discharge but as a long-life backup for real-time clock data retention, metrology memory hold-up, and final transmission after mains interruption. When propylene carbonate replaces acetonitrile, the electrolyte flash point rises from 2 °C to 132 °C per ASTM D3828 and vapour pressure drops, which is compatible with sealed plastic meter housings exposed to 70 °C in direct sunlight. The formulation is 1.0 mol/L TEABF4 in propylene carbonate with water content below 20 ppm and a stabilizer package below 1.0 wt%; bulk conductivity is 16–18 mS/cm at 25 °C. This conductivity is substantially lower than acetonitrile, but pulse current in a 10 F cell rarely exceeds 50 mA, so the voltage drop during transmission is acceptable within the meter's power-management window. Leakage current acceptance is more stringent than automotive: after 72 h at 3.0 V and 60 °C, leakage is checked against manufacturer-specific upper limits; published data for this specific configuration is limited. Compliance is based on IEC 62053-21 for static meter accuracy under supply variation, UL 810A for capacitor safety, and RoHS 2011/65/EU substance restrictions including lead and cadmium in external contacts and internal materials. Cell assembly is performed in a dry room at dew point ≤ −40 °C; electrolyte is dosed at 1.2–1.5 mL per 10 F cell into a stainless steel can, and the cap is crimped with an EPDM or butyl rubber gasket to prevent solvent permeation over the meter's service interval. The terminal product is an integrated RTC backup cell or small module in an electricity or gas meter, with a service life target of 10–15 years at 60 °C and intermittent 70 °C exposure; high-temperature storage tests are typically run at 85 °C for 1000 h as an accelerated proxy for oxidative stability.

    Low-Current Intermittent Charge Acceptance in 3.0 V EDLC Energy-Harvesting Nodes

    Because the energy-harvesting source is itself high-impedance, indoor photovoltaic and thermoelectric nodes charge the EDLC at currents between 10 μA and 1 mA, which changes the dominant ageing factor from ohmic heating to voltage-driven electrolyte oxidation and dielectric leakage. A 3.0 V cell is normally oversized for the required pulse energy and then restricted by the energy management circuit to a working window between 1.8 V and 2.8 V; the 0.2 V headroom to rated voltage is a calendar-life derating measure. The formulation for such nodes is 1.0 M SBPBF4 in propylene carbonate or a PC/ethylene carbonate blend, with water below 20 ppm and chloride below 1 ppm to reduce corrosion of stainless steel current collectors. Bulk conductivity is lower than acetonitrile, typically in the range 12–18 mS/cm depending on ethylene carbonate content, but the charge source impedance is itself high and the node transmits for only 50–200 ms per cycle. Compliance is limited to IEC 62391-2:2019 cell-level endurance and damp heat testing according to IEC 60068-2-30; the final device must also meet RoHS 2011/65/EU and any radio certification requirements specific to the installed transceiver. Process steps for the small coin or cylindrical cell include dry-room assembly at dew point ≤ −40 °C, vacuum fill with 0.3–0.6 mL of electrolyte, crimp sealing with an EPDM gasket, and constant-voltage formation at 3.0 V until leakage stabilizes. The terminal product is a 1.0 F to 10 F energy storage cell integrated into a LoRaWAN sensor node or wireless HVAC transmitter; no series balancing is required because the cell operates as a single-cell string.

    Automated Guided Vehicle Opportunity Charging Requires Sub-30-Second High-Rate Recharge

    During opportunity charging at an automated guided vehicle station, the 48 V EDLC module is recharged in 20–30 s and then discharged during vehicle acceleration and lift actuation. The electrolyte is 1.0 mol/L TEABF4 in acetonitrile with water below 20 ppm and free acid below 30 ppm; bulk conductivity at 25 °C is 55–60 mS/cm, which supports charge acceptance currents up to 100 A per module without excessive resistive heating. Cell balancing is mandatory because fast cycling amplifies voltage divergence; the balance board clamps each cell at 2.85 V during charging and disconnects the DC-bus if any cell exceeds 3.0 V. Module assembly uses eighteen matched cells in series, with capacitance spread within ±1.5% and ESR spread within ±4%, laser-welded aluminium busbars, and a forced-air-cooled enclosure that keeps busbar surface temperature below 85 °C during repeated charge pulses. Compliance is governed by EN 1175-1:1998+A1:2010 for battery-powered industrial truck electrical safety, and the control circuit is installed according to IEC 60204-1; the capacitor cells themselves remain under UL 810A component safety evaluation. Electrolyte filling and sealing are performed in a dry room at dew point ≤ −50 °C; after vacuum fill and formation at 3.0 V, the module is subjected to a 1000-cycle rapid charge/discharge test at 25 °C and elevated temperature screening before shipment. Terminal product is a 48 V, 3000 F-class module for pallet shuttle or small automated guided vehicle systems; cycle life under opportunity charging is specified by the manufacturer as not less than 500,000 cycles, but published independent data for this exact load profile is limited.

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    Certification & Compliance
    More Introduction

    Product designation EL-HV30 is a 3.0 V high-voltage electrolyte for electric double-layer capacitors (EDLCs). The formulation is based on 1.0 mol/L quaternary ammonium tetrafluoroborate in a cyclic carbonate/nitrile solvent system, with an additive package for aluminum current collector passivation and water scavenging. The electrolyte is intended as a replacement for 2.7 V acetonitrile/tetraethylammonium tetrafluoroborate in cells where rated voltage must be increased to 3.0 V without changing the activated carbon electrode chemistry. The energy density improvement available from the voltage increase is 23.5%, calculated from the ratio (3.0/2.7)² − 1, but this gain is accompanied by a reduction in room-temperature conductivity from 55–60 mS/cm to 13.5 ± 1.5 mS/cm.

    Charge storage in EDLCs occurs through potential-dependent ion electrosorption at the activated carbon/electrolyte interface. The electrolyte does not participate as a redox-active species in normal operation; the rated cell voltage is instead limited by oxidative electrolyte decomposition on the positive electrode and reductive decomposition on the negative electrode. In acetonitrile-based 2.7 V systems, the anodic current at 3.0 V rises steeply when moisture, temperature, or carbon surface oxides are present. The EL-HV30 solvent blend shifts the oxidative decomposition onset on glassy carbon beyond 3.3 V versus Ag/AgCl at a scan rate of 1 mV/s, using a three-electrode cell and a 0.05 mA/cm² current density threshold. The corresponding cathodic limit remains below 0 V, allowing stable cycling between 0 V and 3.0 V in symmetric activated carbon cells.

    Representative incoming inspection data for the product are given in Table 1. The specification is not a single-point value but a band that must be applied at receiving because water and free acid are the dominant variables that shift leakage current and gas generation in filled cells.

    Incoming inspection specification for EL-HV30
    PropertySpecificationTest method / equipment
    AppearanceClear, colorless to pale-yellow liquidVisual inspection under dry nitrogen at 25 °C
    Conductivity at 25 °C13.5 ± 1.5 mS/cmConductivity cell with platinized platinum electrode, calibrated with 0.01 mol/L KCl at 25.00 ± 0.05 °C
    Density at 20 °C1.21 ± 0.02 g/cm³ASTM D4052-22
    Dynamic viscosity at 25 °C5.0 ± 0.5 mPa·sASTM D7042-21
    Water content20 mg/kgASTM E1064-16, coulometric Karl Fischer
    Free acid as HF50 mg/kgAcid-base titration with 0.01 mol/L KOH in methanol
    Oxidative decomposition onset3.3 V vs Ag/AgCl at 0.05 mA/cm²Linear sweep voltammetry, glassy carbon working electrode, 1 mV/s
    Salt concentration1.0 ± 0.05 mol/LIon chromatography after dilution

    The specification band is applied at incoming inspection because water and free acid are the main variables that shift leakage current and gas generation in filled cells. On automated vacuum-filling lines, the fill weight tolerance is held at ±0.5% because the 5.0 mPa·s viscosity reduces time-pressure dispense repeatability below 20 °C. Filling is performed after cell bodies have been dried under 5 Pa absolute pressure at 85 °C to 120 °C for 12 h to 24 h, depending on electrode thickness and separator water loading. Karl Fischer titration is performed with a coulometric titrator, and free acid is determined by titration with 0.01 mol/L KOH in methanol under nitrogen. Conductivity and density are measured simultaneously on a Stabinger viscometer and density meter at 20 °C and 25 °C. Batch samples are drawn from each 200 L stainless steel mixing vessel after 4 h recirculation through a 0.2 μm PTFE filter to ensure homogeneity.

    Why Does 3.0 V Operation Narrow the Choice to Carbonate-Rich Solvent Systems?

    The difference between EL-HV30 and a conventional 2.7 V acetonitrile/tetraethylammonium tetrafluoroborate electrolyte is primarily solvent stability. Acetonitrile has a low closed-cup flash point of 2 °C and a vapor pressure of 73 mmHg at 25 °C; the corresponding carbonate-rich solvent has a closed-cup flash point of 132 °C and vapor pressure of 0.03 mmHg at 25 °C. These values are for the base solvents, and the finished electrolyte flash point is expected to be above 100 °C. Acetonitrile also exhibits an anodic stability limit that is insufficient for long-life float at 3.0 V on high-surface-area carbon, particularly in the presence of adsorbed water. The high-voltage solvent blend has a dielectric constant of approximately 64.9 at 25 °C, compared with 37.5 for acetonitrile, which maintains ion dissociation but raises viscosity.

    Bulk property comparison at 25 °C for standard 2.7 V acetonitrile/tetraethylammonium tetrafluoroborate and EL-HV30
    Parameter2.7 V acetonitrile/TEABF₄EL-HV30 3.0 V
    Rated cell voltage2.7 V3.0 V
    Conductivity at 25 °C55–60 mS/cm13.5 ± 1.5 mS/cm
    Dynamic viscosity at 25 °C0.6 mPa·s5.0 ± 0.5 mPa·s
    Density at 20 °C0.82 g/cm³1.21 ± 0.02 g/cm³
    Closed-cup flash point of base solvent2 °C132 °C
    Vapor pressure of base solvent at 25 °C73 mmHg0.03 mmHg
    Dielectric constant of base solvent at 25 °C37.564.9

    The practical consequence of the conductivity gap is that direct substitution into a high-rate 3000 F jelly-roll cell increases bulk electrolyte resistance by a factor of 4.0 to 4.4 when electrode geometry is unchanged. Cell ESR increase is not identical to the bulk conductivity ratio because separator tortuosity and electrode pore resistance contribute separately, but the direction is monotonic. Applications requiring high power in the 1–10 s discharge window should reduce electrode thickness, increase separator porosity, or use a cell design with lower current collector resistance. The higher closed-cup flash point and lower vapor pressure reduce the fire-load contribution in modules tested under IEC 62391-2 short-circuit and overvoltage conditions, but the carbonate-rich solvent raises low-temperature ESR: at -40 °C, conductivity falls to approximately 2.0 mS/cm, and cell ESR is typically higher by a factor of 8 to 12 relative to 25 °C. Published data for this specific configuration is limited; the stated range is based on conductivity-temperature behavior of carbonate-based electrolytes with similar salt loading.

    The voltage window specification is not a simple bulk decomposition number. In symmetric activated carbon cells, the negative electrode can maintain a potential close to 0.0 V to 0.5 V versus Ag/AgCl, while the positive electrode approaches 2.5 V to 3.0 V depending on mass balance and electrode capacitance ratio. If the positive electrode mass is too low, its potential may exceed 3.3 V at 3.0 V cell voltage and oxidative degradation will occur even though the cell is within rating. Electrode mass balancing must therefore remain within the same tolerance as specified for 2.7 V cells or be corrected for the higher voltage window.

    Aluminum Current Collector Passivation and Water Scavenging Limits

    Water is the dominant operational boundary for EL-HV30. The tetrafluoroborate anion hydrolyzes in the presence of free water, releasing fluoride species that etch aluminum current collectors and increase interfacial impedance. For this reason the incoming water limit is 20 mg/kg, and production dry rooms should maintain dew point below -50 °C during electrolyte transfer. Cells filled with electrolyte that has been exposed to ambient humidity above 30% RH for more than 15 min show elevated leakage current during the first 72 h at 3.0 V. The additive package includes a water scavenger that binds residual water, but the scavenger capacity is finite; therefore, vacuum drying of electrodes and separators must be completed before fill.

    On production lines using etched aluminum current collectors, pitting corrosion at 3.0 V is controlled by an anodic passivation additive. The passivation effect is measured electrochemically by holding a two-electrode cell at 3.0 V and 70 °C for 1000 h according to the endurance screening procedures in IEC 62391-2; acceptance limits for capacitance loss and ESR increase are set by the cell manufacturer. Electrolyte batches that exceed 50 mg/kg free acid have produced visible pitting on 20 μm aluminum foil after 500 h at 70 °C, and are rejected at incoming inspection.

    For cell assembly, EL-HV30 is dispensed under a nitrogen atmosphere through a 0.2 μm PTFE filter. The recommended storage condition is 5 °C to 30 °C in the original sealed container, with a shelf life of 6 months when unopened. Containers that have been opened must be backfilled with dry nitrogen and used within 72 h if stored in a dry room at dew point below -50 °C. Do not mix with water above the specified limit, strong oxidizers, or strong acids. The solvent blend is not intended for direct contact with cell components that dissolve in carbonate solvents or that contain free amine species; separator wetting with the higher-viscosity solvent must be verified by contact-angle or wicking test before production release.

    Typical EDLC applications for EL-HV30 are 12 V start-stop modules, backup power for industrial controllers and wind turbine pitch actuators, and energy harvesting systems where float voltage is 3.0 V per cell and charge-discharge currents are limited to 1 A to 10 A for 100–3000 F cells. The electrolyte is not intended for pseudocapacitive or battery electrode chemistries that require electrolyte oxidation-reduction activity. Each cell design must be requalified under IEC 62391-2 endurance and ISO 16750-2 vehicle electrical environment tests before production release.

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