| HS Code | 241656 |
| Product Name | Methylene Methanedisulfonate |
| Synonyms | Methylene Dimethanesulfonate; MDMS; Methanesulfonic acid methylene ester |
| Cas Number | 869-01-2 |
| Molecular Formula | C3H8O6S2 |
| Molecular Weight | 204.22 g/mol |
| Appearance | White to off-white crystalline powder |
| Melting Point | 50-55 °C |
| Boiling Point | 343.0 ± 25.0 °C (predicted) at 760 mmHg |
| Density | 1.48 ± 0.1 g/cm3 (predicted) |
| Solubility | Soluble in DMSO, DMF, acetone, methanol; sparingly soluble in water |
| Storage Condition | Store at 2-8 °C, tightly sealed, protected from moisture |
| Purity | ≥98% (typical) |
As an accredited Methylene Methanedisulfonate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in a sealed amber glass vial, 5 g quantity, with desiccant, for laboratory use. |
| Container Loading (20′ FCL) | Load 20′ FCL with Methylene Methanedisulfonate in sealed drums on secured pallets; protect from moisture, heat, and direct sunlight. |
| Shipping | Shipping description: UN 2811, Toxic solid, organic, n.o.s. (Methylene methanedisulfonate), hazard class 6.1, packing group II. Ship in securely sealed, labeled UN-approved packaging, protected from moisture and incompatible oxidizers. Avoid dust generation and contact. Verify the classification against the current SDS and applicable regulations before transport. |
| Storage | Store Methylene Methanedisulfonate in a tightly sealed container, protected from moisture and light. Keep in a cool, dry, well-ventilated area away from heat, ignition sources, and incompatible materials such as strong bases or oxidizers. Maintain the container at stable temperature, avoid unnecessary handling, and ensure workspace is properly labeled and accessible only to trained personnel. |
| Shelf Life | Store tightly sealed, dry, and cool. Under these conditions, typical shelf life is up to two years. |
Methylene methanedisulfonate (CAS 99591-74-9; C2H4O6S2; molecular weight 188.18 g/mol) is metered into high-nickel NCM811 and NCA traction-cell electrolytes at 0.8–1.5 wt% of finished electrolyte mass. The base electrolyte in one production configuration is 1.0 M LiPF6 dissolved in ethylene carbonate, ethyl methyl carbonate, and dimethyl carbonate at a 1:1:1 volume ratio; the additive is introduced after lithium salt dissolution and before final 0.2 µm PTFE cartridge filtration. The finished cell must pass IEC 62660-2:2018 cycle-life and storage test designations, UN 38.3 transport tests T1–T5, and GB/T 31485-2015 safety test methods. Downstream cell production uses vacuum injection equipment inside a dry room with a dew point no higher than -40 °C, followed by formation cycling at 0.05C–0.2C and 25–45 °C; during the first charge the sulfonate ester reduces on the graphite anode and forms a sulfur-containing SEI that depresses transition-metal migration from delithiated high-nickel cathode surfaces. Terminal product types include prismatic aluminum cells of 100–300 Ah, blade cells for cell-to-pack architectures, and 46xx cylindrical cells for battery-electric vehicle packs.
The process window is constrained by an impedance threshold. At addition levels above 2.5 wt%, the anode SEI becomes sufficiently resistive to measurably reduce low-temperature pulse power at -20 °C, while below 0.3 wt% the additive no longer supplies complete coverage of graphite edge planes. Large-format prismatic cells also exhibit local additive depletion in the core region when electrolyte wetting is non-uniform; vacuum-pressure cycling between -0.095 MPa and 0.6 MPa is therefore specified during filling to reduce the gradient. On production lines that pre-dissolve the additive into a carbonate co-solvent before lithium salt addition, a measurable exotherm has been observed in the blending vessel when jacket temperature is not held below 25 °C; sequencing is reversed so the salt dissolves first and the additive is metered as a final step at 15–20 °C. Finished electrolyte after methylene methanedisulfonate addition is sampled for moisture below 20 ppm and free acid below 50 ppm before release to the cell line. Electrolyte blending skids with Hastelloy C-22 wetted parts and nitrogen-purged dosing lances are specified to control moisture and trace metal pickup.
| Standard | Scope | Test method designation |
|---|---|---|
| IEC 62660-2:2018 | EV propulsion cells | Cycle life, storage ageing |
| UN 38.3 | Transport | T1–T5 |
| GB/T 31485-2015 | China EV cells | Safety and abuse |
| REACH (EC) No 1907/2006 | EU chemical registration | Registration duties |
In lithium iron phosphate stationary storage cells, methylene methanedisulfonate is added at 0.5–1.0 wt% to a 1.0 M LiPF6 electrolyte based on ethylene carbonate and diethyl carbonate; the lower portion of this range is used when 280 Ah prismatic cells must retain at least 80% residual capacity after 6,000 cycles. Industry compliance for the finished storage battery includes IEC 62619:2022 industrial battery safety testing, UL 1973 stationary battery certification, and GB/T 36276-2023 power storage test methods. The downstream production process involves automatic dosing into vacuum-filled prismatic cells within a nitrogen-swept filling station, formation at 0.1C to 3.65 V at 25–35 °C, and capacity grading after a 72–96 h ageing step at 45 °C. Terminal products are rack-mount energy storage cabinets, containerized grid-side systems, and commercial and industrial peak-shaving units.
Because LFP operates at a lower nominal voltage than high-nickel NCM, the additive loading is biased toward calendar-life suppression of iron dissolution and electrolyte oxidation rather than high-voltage cathode stabilization. The main incompatibility is with amine-based electrolyte impurities, which can react with the sulfonate ester before formation; incoming solvents are therefore controlled for amine nitrogen content and water by Karl Fischer titration before the additive is introduced.
When 4.45 V pouch cells are cycled without a sulfur-containing anode film former, gas generation at the graphite electrode increases and the cell is rejected during hot-bar sealing thickness inspection. Methylene methanedisulfonate is therefore dissolved into the electrolyte at 1.0–2.0 wt% to suppress oxidative decomposition at the 4.40–4.45 V charge cutoff without creating an excessively thick anode SEI. Compliance for the assembled battery includes IEC 62133-2:2017, IEEE 1725-2021 for mobile phone cells, and UN 38.3 transport requirements. The production line uses high-shear mixing of the electrolyte concentrate, vacuum filling into aluminum-laminated pouches, hot pressing at 80 °C, formation at 0.2C to 4.45 V, degassing, and re-sealing before final grading. Terminal products include 3.80–3.85 V nominal pouch cells for smartphones, tablets, laptops, and wearable devices.
High-rate NCM523/622 cylindrical cell lines that specify 10C pulse discharge require methylene methanedisulfonate loadings below 1.0 wt% because higher additions increase SEI resistance and reduce pulse power. The acceptable range is 0.5–1.0 wt% in a low-viscosity electrolyte based on 1.0 M LiPF6 in ethylene carbonate and ethyl methyl carbonate. Compliance is assessed under IEC 62133-2:2017 and UL 2054; UN 38.3 applies to the assembled pack. Production uses high-speed cylindrical winding, vacuum filling, and a two-step formation protocol at 0.1C and 0.5C to 4.20 V, followed by 72 h ageing at 45 °C. Terminal product types are 18650 and 21700 cells for cordless power tools, e-bikes, and portable power packs.
Centralized electrolyte formulation routes pre-disperse methylene methanedisulfonate as a dry solid into a nitrogen-protected pre-blend of ethylene carbonate and dimethyl carbonate at 5–10 wt% concentrate, then meter the concentrate into the final electrolyte at 0.5–2.0 wt% total additive concentration. Operations are governed by ISO 9001:2015 quality management and REACH Regulation (EC) No 1907/2006 registration duties; finished electrolyte is tested for water content by Karl Fischer titration using ASTM E203-24 and for density by ASTM D4052-22. Production equipment comprises jacketed stainless-steel blending vessels, magnetically coupled sealless pumps, and 0.2 µm cartridge filtration under argon or nitrogen. Terminal products are battery-grade electrolyte formulations shipped in 200 L stainless-steel drums to cell manufacturers for NCM, NCA, and LFP lines.
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Methylene methanedisulfonate (CAS 99591-74-9; C₃H₆O₆S₂; molecular weight 202.18 g mol−1) is a white crystalline heterocyclic sulfonate supplied for lithium-ion battery electrolyte formulation. Battery-grade material is controlled for an HPLC assay of not less than 99.5%, moisture below 100 ppm by Karl Fischer coulometry, and free-acid content below 50 ppm expressed as H₂SO₄. The product is packaged in fluorinated high-density polyethylene containers under nitrogen; typical lot sizes range from 1 kg to 25 kg. In carbonate-based electrolytes, the compound is dissolved at 0.5 wt% to 2.0 wt% based on total electrolyte mass. Unlike bulk solvents, it functions as a sacrificial film-forming additive that decomposes before carbonate reduction on graphite anodes.
The heterocyclic sulfonate structure contains two sulfonate groups on a shared methylene framework. Differential scanning calorimetry shows a sharp melting endotherm between 117 °C and 121 °C at 10 °C min−1; thermogravimetric analysis under nitrogen records a decomposition onset above 220 °C at the same heating rate. These thermal boundaries are relevant to dry-room handling because the powder remains free-flowing below 40 °C, but vacuum drying above 60 °C can promote ring-opening if residual free acid is present. Solubility is not a bulk property: in EC:DEC (1:1 w/w) at 25 °C, dissolution at 2 wt% is complete within 30 min under low-shear stirring, whereas the same loading in pure EMC may require heating to 40 °C to prevent visible turbidity above 1 NTU.
Battery-grade acceptance criteria are set by electrolyte manufacturers to control moisture, acid, and ionic impurities that accelerate LiPF₆ hydrolysis. The following release-test template is representative of incoming inspection for MMDS.
| Parameter | Specification | Reference method |
|---|---|---|
| Appearance | White crystalline powder | Visual inspection |
| Assay | ≥ 99.5% | HPLC-UV, area normalization at 210 nm |
| Moisture | ≤ 100 ppm | Karl Fischer coulometry, ASTM E203-16 |
| Free acid | ≤ 50 ppm as H₂SO₄ | Anhydrous methanol titration, GB/T 9736 |
| Chloride | ≤ 10 ppm | Ion chromatography, ASTM D4327 |
| Sulfate | ≤ 20 ppm | Ion chromatography, ASTM D4327 |
| Melting range | 117–121 °C | Differential scanning calorimetry, ASTM E794 |
| Loss on drying | ≤ 0.10% | 60 °C vacuum, 4 h |
Release testing uses HPLC-UV on a C18 column with a phosphate buffer/acetonitrile mobile phase. Free-acid titration is performed in anhydrous methanol with 0.01 N sodium methoxide to a potentiometric endpoint. Chloride and sulfate are determined by ion chromatography with suppressed conductivity detection. Chloride above 10 ppm is controlled because it accelerates aluminum current-collector corrosion in LiPF₆ electrolytes.
On the first charge of a graphite anode, MMDS undergoes ring-opening reduction at a potential between 1.3 V and 1.5 V vs Li/Li⁺. The reduction products include lithium sulfite, lithium sulfate, and alkyl sulfonate oligomers that crosslink into a compact interphase. This interphase blocks solvent co-intercalation and reduces the first-cycle irreversible capacity loss associated with carbonate decomposition. In electrochemical impedance spectra collected from 1 MHz to 10 mHz, the post-formation charge-transfer resistance of a 1 wt% MMDS electrolyte is typically 10–20 Ω cm² lower than that of an additive-free baseline. The effect is interfacial rather than bulk: conductivity at 25 °C for 1 wt% MMDS in 1 M LiPF₆ EC:EMC (3:7 v/v) remains within 8–10 mS cm−1, essentially identical to the additive-free electrolyte.
X-ray photoelectron spectroscopy of the anode surface after formation shows S 2p binding energies at 167–169 eV, assignable to sulfonate/sulfate species, while O 1s spectra show Li₂CO₃ and lithium alkylcarbonate components. Sputter depth profiling indicates the sulfur-containing layer is concentrated within the inner 5–10 nm of the SEI. This distribution is significant because the inner SEI layer governs lithium-ion transport and anode passivation.
Vinylene carbonate (VC) polymerizes on graphite and creates a polymer-rich SEI with high coulombic efficiency but increased gas generation at elevated temperature. 1,3-Propanesultone (PS) creates a sulfonate-rich SEI similar to MMDS but is shipped as a toxic solid under UN 2811. MMDS differs in that its two sulfonate groups per molecule allow higher crosslink density without the first-cycle capacity loss associated with PS. The following table summarizes formulation and process distinctions.
| Additive | Typical use level | SEI feature | Process limitation |
|---|---|---|---|
| Methylene methanedisulfonate | 0.5–2.0 wt% | Sulfonate-rich, compact | Low solubility in pure linear carbonates below 0 °C |
| Vinylene carbonate | 1–3 wt% | Poly(VC), carbonate oligomers | Higher gas at 60 °C |
| 1,3-Propanesultone | 1–2 wt% | Sulfonate, Li₂SO₃/ROSO₂Li | Toxic solid, UN 2811 |
| Ethylene sulfate | 0.5–1 wt% | Sulfite/sulfate-rich | Moisture-sensitive, rapid ring-opening |
The selection of MMDS over PS is often driven by high-nickel cathode stability. Transition-metal dissolution from LiNi₀.₈Co₀.₁Mn₀.₁O₂ at 60 °C is suppressed when the SEI contains sulfonate species; ICP-OES analysis of the anode after 200 h storage shows lower nickel and manganese deposition than VC-only controls. Published data for this specific configuration is limited, but the trend is consistent with acid-scavenging by sulfonate decomposition products.
On a 2000 L glass-lined electrolyte mixing vessel operating under dry air with a dew point of −40 °C, the addition sequence is controlled to avoid contact between MMDS and free HF. LiPF₆ is dissolved first and the batch is cooled to 20–25 °C before MMDS is charged through a nitrogen-purged lance. The batch is stirred for 45 min at 60 rpm; high-shear dispersion above 300 rpm is avoided because it can generate localized heating and promote ring-opening. If the batch moisture exceeds 100 ppm after mixing, the batch is rejected because water reacts with LiPF₆ to produce HF, which degrades MMDS to methanedisulfonic acid and raises the free-acid value above 50 ppm. A 0.2 µm PTFE membrane filter is installed before filling; a pressure drop above 0.5 bar indicates undissolved additive or hydrolysis solids and triggers a filter integrity check.
In high-speed cylindrical cell filling, filterability and viscosity are critical. The viscosity of a 1 wt% MMDS electrolyte at 25 °C is typically 4–6 cP, only 0.1–0.3 cP above baseline. If free acid rises above 50 ppm due to moisture ingress, the electrolyte can become slightly hazy because methanedisulfonic acid promotes salt precipitation. In such cases, turbidity exceeds 1 NTU and the batch is diverted to a holding tank for retesting before use in cell assembly.
When MMDS is used at 1 wt% in place of PS in a 10 Ah graphite/NCM811 pouch cell, the formation protocol is modified to include a 0.05C constant-current step for the first 2 h, followed by 0.1C to 3.65 V and a constant-voltage hold at 3.65 V for 30 min. The lower initial rate prevents lithium plating on graphite edges while the sulfonate SEI forms. Post-formation impedance measured at 1 kHz is frequently 15–25 Ω cm², compared with 30–45 Ω cm² for PS-only cells. After 500 cycles at 45 °C per IEC 62660-1, capacity retention differences between the two additives narrow because both are consumed by SEI repair; the MMDS cell may show less gas generation, but published data for this specific configuration is limited.
In 60 °C storage tests lasting 500 h, pouch cells with MMDS show lower anode impedance growth than PS-containing cells, provided the cell moisture content before filling is below 100 ppm. If moisture control is poor, MMDS hydrolyzes to methanedisulfonic acid, which attacks the cathode interface and increases interfacial impedance by more than 20 Ω cm² within 100 h. The compound must not be combined with primary or secondary amines, alkali metal alkoxides, or strong aqueous bases because nucleophilic ring-opening generates methanedisulfonate salts and increases electrolyte viscosity beyond the 10 cP limit typical of high-speed injection filling.
Regulatory classification under CLP Regulation (EC) No 1272/2008 includes skin irritation category 2 and eye irritation category 2; the substance is not subject to transport classification as dangerous goods under UN 3077 unless present in a mixture. Storage in sealed fluorinated containers under argon at −5 °C to 10 °C is recommended. Exposure to ambient air above 60% RH for more than 30 min requires pre-drying at 45 °C under vacuum for 4 h before use. Under RoHS Directive 2011/65/EU, the substance contains no restricted heavy metals, but downstream documentation under IEC 62321-1:2013 may be requested for sulfur-containing electrolyte additives.