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| HS Code | 752804 |
| Chemical Formula | C4H6O3 |
| Molar Mass | 102.09 g/mol |
| Appearance | Colorless liquid |
| Density | 1.204 g/cm3 at 20 °C |
| Melting Point | -48.7 °C |
| Boiling Point | 242 °C |
| Flash Point | 132 °C (closed cup) |
| Refractive Index | 1.421 |
| Viscosity | 2.53 mPa·s at 25 °C |
| Solubility In Water | Soluble |
As an accredited Propylene Carbonate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Propylene Carbonate is packaged in 200 kg polyethylene drums, tightly sealed, labeled with safety information for safe handling and transport. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Pack propylene carbonate in sealed drums/pallets, secure against shifting, label hazard, ensure ventilation and compatibility. |
| Shipping | Propylene carbonate is typically shipped as a non-hazardous, stable liquid, not regulated as dangerous goods under ADR/IMO. Transport in clean, dry drums, IBCs, or ISO tanks. Avoid oxidizers and moisture contamination. Label containers with technical name and CAS 108-32-7. Provide SDS and ensure compatibility with mild steel or stainless steel equipment. |
| Storage | Store in a cool, dry, well-ventilated area away from heat, open flames, and direct sunlight. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid contact with strong oxidizing agents, acids, and bases. Use corrosion-resistant materials and label clearly. Ensure spill containment and appropriate personal protective equipment during handling. |
| Shelf Life | Propylene carbonate is stable for 2–5 years when stored sealed, cool, and dry, away from moisture and acids. |
Propylene carbonate functions as a high-permittivity cyclic carbonate co-solvent in non-aqueous lithium-ion electrolytes. The dielectric constant of 64.9 at 25 °C supports complete dissolution of LiPF₆ at 1.0 mol/L. Dynamic viscosity of the pure solvent is 2.53 mPa·s at 25 °C, and the normal boiling point is 242 °C. The closed-cup flash point is 132 °C. These properties allow the solvent to reduce low-boiling linear carbonate content without increasing container pressure during standard charge-discharge cycling. Published battery-grade cyclic carbonate specifications commonly require purity of at least 99.99 wt%, water not exceeding 20 mg/kg by coulometric Karl Fischer titration, acidity not exceeding 50 mg/kg as HF by ion chromatography, and chloride residue not exceeding 1 mg/kg. Protic impurities above these limits consume LiPF₆, generate HF, and accelerate transition-metal dissolution from layered oxide cathode powders.
| Parameter | Control Limit | Analytical Method |
|---|---|---|
| Purity | ≥ 99.99 wt% | Capillary gas chromatography |
| Water | ≤ 20 mg/kg | Karl Fischer coulometric titration |
| Acidity as HF | ≤ 50 mg/kg | Ion chromatography |
| Chloride | ≤ 1 mg/kg | Ion chromatography |
The principal process conflict in lithium-ion anodes is propylene carbonate co-intercalation into crystalline graphite. Unmodified PC-rich electrolytes solvate Li⁺ as [Li(PC)ₙ]⁺. The solvated ion inserts between graphene planes before a stable solid electrolyte interphase is formed, causing exfoliation at 0.7 V to 0.9 V versus Li/Li⁺. This failure mode is suppressed by replacing part of the propylene carbonate with ethylene carbonate or by adding vinylene carbonate at 2 wt% to 5 wt% or fluoroethylene carbonate at 5 wt% to 10 wt%. The alternative is to use propylene carbonate with non-graphitic carbons, lithium titanate, or silicon-dominant anodes, where the co-intercalation mechanism does not govern first-cycle capacity loss. Electrolyte mixing for PC-containing formulations is performed in dry rooms with dew point not higher than -40 °C. Filtration through 0.1 µm stainless steel cartridge units follows the final blending operation. Finished cells are qualified under UN 38.3 and, for stationary energy storage, IEC 62619.
In physical-solvent acid gas removal units, propylene carbonate is circulated as an unheated absorption liquid for carbon dioxide separation from natural gas and synthesis gas. The Fluor Solvent process exploits the high physical solubility of CO₂ in propylene carbonate: approximately 3.2 cm³ CO₂ per cm³ solvent at 25 °C and 0.1 MPa. The absorber is typically operated at 2.0 MPa to 7.0 MPa and a lean-solvent temperature of 20 °C to 30 °C. Rich solvent is regenerated by staged pressure reduction. A high-pressure flash recovers co-absorbed methane for recompression. A medium-pressure flash releases the carbon dioxide product stream. A vacuum flash at 0.02 MPa to 0.05 MPa is used where deep regeneration is required. Unlike amine systems, the propylene carbonate loop does not require reboiler steam for solvent regeneration; pumping and compression energy dominate the variable cost. This operating envelope is limited by propylene carbonate hydrolysis to propylene glycol and carbon dioxide, which accelerates above 80 °C and in the presence of free water. Feed gas water content is therefore controlled to <1 vol% before the absorber, and solvent temperature is kept below 65 °C in continuous service. Natural gas composition testing for such units is routinely referenced to ASTM D1945 for gas chromatography.
Propylene carbonate is converted with methanol to dimethyl carbonate and propylene glycol in a reversible transesterification network. The industrial process is operated with a methanol excess of 3:1 to 5:1 methanol-to-propylene carbonate molar ratio. The dimethyl carbonate/methanol azeotrope boils at 63.5 °C at 0.1 MPa and contains approximately 30 wt% dimethyl carbonate, which forces a reactive distillation sequence. Sodium methoxide or solid-base catalysts are used at 60 °C to 80 °C. Water content in the feed is held below 0.1 wt% because water drives reverse hydrolysis to propylene glycol and carbon dioxide and reduces dimethyl carbonate yield. The product dimethyl carbonate is distilled to 99.9 wt% for polycarbonate-grade use. Propylene glycol co-product is recovered from the bottoms stream. Process equipment uses structured packing in the reactive distillation column to maintain liquid-phase catalyst contact and to avoid excessive reboiler residence time.
High-solids two-component polyurethane topcoats use propylene carbonate as a slow polar solvent. Pure propylene carbonate has a vapor pressure of 0.03 mmHg at 20 °C and a flash point of 132 °C closed cup. These properties place it in low-volatile solvent formulations without the odor and flammability profile of methyl ethyl ketone. The typical addition window is 3 wt% to 7 wt% of total formulation mass. At this level sag resistance and substrate wetting improve. Above 10 wt% the solvent remains in the film after the pot life window and retards through-hardness development. Water content must be controlled below 0.05 wt% in moisture-sensitive isocyanate systems to avoid carbon dioxide bubbles from the isocyanate-water reaction. Viscosity measurements follow ASTM D2196; volatile organic compound testing is performed by ASTM D2369. The solvent is not classified as a hazardous air pollutant under U.S. Clean Air Act definitions and is registered under REACH.
In cold-box and no-bake phenolic urethane foundry binder systems, propylene carbonate is incorporated into the phenolic resin component as a polar viscosity reducer. The binder addition on silica sand is 1.2 wt% to 2.5 wt% based on sand mass. Propylene carbonate content in the Part I phenolic resin typically ranges from 5 wt% to 15 wt%. This reduces Part I viscosity to 200 mPa·s to 400 mPa·s at 25 °C. The mixed sand is blown into core boxes and cured with triethylamine vapor in cold-box operations. Excess propylene carbonate above 20 wt% of Part I delays initial cure and lowers immediate tensile strength development. The solvent is not consumed in the amine cure reaction and remains as a fugitive emission during metal pouring.
Propylene carbonate dissolves tetraethylammonium tetrafluoroborate and spiro quaternary ammonium salts for electric double-layer capacitor electrolytes. The normal salt concentration is 0.8 mol/L to 1.2 mol/L. PC-based electrolytes support a cell voltage of 2.7 V to 3.0 V, higher than aqueous systems. The freezing point of pure propylene carbonate is -48.8 °C, which permits low-temperature operation, but the viscosity increase below -20 °C raises equivalent series resistance. Conductivity at 25 °C for PC-based quaternary ammonium electrolytes is lower than acetonitrile-based alternatives, typically 10 mS/cm to 15 mS/cm. Cells using PC-based electrolytes are qualified under IEC 62391-1 for capacitance and internal resistance measurements. Electrolyte filling is performed in dry-room conditions with water below 20 mg/kg; higher water content accelerates capacitance fading and gas evolution.
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Propylene carbonate (CAS 108-32-7, EC 203-572-1, molecular weight 102.09 g/mol) is a cyclic five-membered carbonate ester synthesized by the carboxylation of propylene oxide with carbon dioxide over alkali-metal halide or quaternary ammonium catalysts at 180–200 °C and 5–8 MPa. Commercial model designations generally separate battery-grade (PC-BG), high-purity pharmaceutical and cosmetic grade (PC-HP), and general industrial grade (PC-IND). The specification split is controlled by water content, acidity, chloride content, and ultraviolet absorption; supplier certificates of analysis commonly reference ISO 760 for Karl Fischer water determination, ASTM D1209-21 for APHA color, and ASTM D4052-22 for density. PC-BG is controlled at water ≤20 mg/kg, acidity ≤50 mg/kg as acetic acid, and chloride ≤1 mg/kg; PC-HP is commonly certified at water ≤100 mg/kg, APHA color ≤10, and UV absorbance ≤0.10 at 270 nm for a 10 mm cell. The liquid is polar, aprotic, and exhibits low corrosion rate on 316L stainless steel at 25 °C, with a density of 1.204 g/cm³ at 20 °C.
Electrolyte formulations containing 10–30 wt% propylene carbonate are used in lithium-ion cells where low-temperature discharge and high-temperature calendar life must be balanced. PC has a dielectric constant of 64.4 at 25 °C and a viscosity of 2.5 mPa·s at 25 °C; this combination supports lithium-salt dissociation while keeping bulk electrolyte resistance low when blended with linear carbonates. Differential scanning calorimetry shows that PC-rich blends resist crystallization because the melting point of pure PC is -48.8 °C, whereas ethylene carbonate solidifies at 36.4 °C. In cylindrical 18650 production cells, PC-containing electrolytes often replace part of the ethylene carbonate to maintain liquid range during cell filling in dry rooms held at dew point ≤ -50 °C. A processing constraint is that neat propylene carbonate can co-intercalate into graphitic anodes and exfoliate the graphitic structure; therefore battery-grade formulations typically add vinylene carbonate at 2–5 wt% to form a stable solid electrolyte interphase. Cycle-life testing under IEC 62660-1:2019 has been used to compare capacity retention limits, though published cell-specific data for PC-heavy formulations is limited.
Comparative physical property data for cyclic and linear carbonate solvents, compiled from supplier technical bulletins and standard test methods, are shown below.
| Property | Propylene carbonate | Ethylene carbonate | Dimethyl carbonate | Diethyl carbonate |
|---|---|---|---|---|
| CAS registry number | 108-32-7 | 96-49-1 | 616-38-6 | 105-58-8 |
| Molecular weight (g/mol) | 102.09 | 88.06 | 90.08 | 118.13 |
| Melting point (°C) | -48.8 | 36.4 | 4.6 | -43.0 |
| Boiling point at 101.3 kPa (°C) | 242 | 248 | 90 | 126 |
| Flash point closed cup (°C, ASTM D93) | 132 | 143 | 17 | 25 |
| Dielectric constant at 25 °C | 64.4 | 89.6 at 40 °C | 3.1 | 2.8 |
| Viscosity at 25 °C (mPa·s) | 2.5 | solid; 1.9 at 40 °C | 0.58 | 0.75 |
For acid gas removal service, propylene carbonate functions as a physical solvent for carbon dioxide and hydrogen sulfide removal; acid gas solubility is pressure-dependent and requires regeneration by pressure letdown rather than steam stripping. Packed absorption columns operated at 3–6 MPa feed pressure and 40–60 °C use PC because water content remains low, minimizing hydration losses. Regeneration flash drums at 0.1–0.3 MPa release absorbed CO₂ without significant solvent vapor loss because PC vapor pressure is 0.03 mmHg at 20 °C. Published data for specific absorption capacity is limited in public technical bulletins; design is typically based on Henry’s law coefficients generated from proprietary pilot-plant trials.
Replacement of N-methyl-2-pyrrolidone in coil-coating primer removal and industrial cleaner formulations has been evaluated where flash point and regulatory restrictions drive reformulation. PC exhibits a closed-cup flash point of 132 °C under ASTM D93, compared with 86 °C for NMP. In solvent-blend reclaim systems, PC is charged into high-shear dispersion units with 316L stainless steel vessels; active dissolution of acrylic and epoxy ester binders is monitored by rheometer viscosity drop at 25 °C and 10 s⁻¹. A processing boundary is the hydrolysis-sensitive cyclic carbonate ring: prolonged contact with aqueous alkaline paint strippers raises free propylene glycol and carbon dioxide evolution, lowering flash point and increasing acid number. Published industrial trials have quantified gel-time extension in two-component urethane cleaners at PC addition levels of 5–15 wt%, but complete replacement of NMP in high-solids epoxy removal is not recommended where solvency parameter matching requires nitrogen-containing fast solvents.
Thermogravimetric analysis of dry PC under nitrogen shows thermal decomposition onset near 240 °C, but the practical continuous-use ceiling in closed heat-transfer loops is lower because trace water and acid accelerate ring-opening. Hydrolysis is acid- and base-catalyzed and produces propylene glycol and carbon dioxide; the reaction rate increases sharply below pH 4 and above pH 9. Stainless steel equipment is specified because carbon steel surfaces can promote decarboxylation under hot alkaline conditions. In solvent regeneration columns operated at 120–150 °C, the water content in the stripping feed is maintained ≤0.1 wt% to keep propylene glycol formation below 0.5 wt% per pass. A continuous overhead sweep with dry nitrogen at 0.2–0.5 L/min per litre of holdup is used on production recovery stills to displace evolved CO₂ and shift equilibrium toward carbonate retention. Comparative stability data for different catalyst residues are limited in public supplier literature; therefore incoming acid number and chloride concentration should be trended against hydrolytic decomposition under plant-specific storage temperatures.
Product models are differentiated by the specification matrix shown below. General solvent service typically accepts higher water and acidity because downstream distillation recovers the carbonate; battery and capacitor applications demand tighter ionic impurity control to reduce corrosion and electrochemical side reactions.
| Parameter | Test method | PC-IND | PC-BG | PC-HP |
|---|---|---|---|---|
| Purity (GC-FID area%) | supplier GC-FID | ≥99.5 | ≥99.9 | ≥99.9 |
| Water (mg/kg) | ISO 760 / ASTM E203 | ≤200 | ≤20 | ≤100 |
| Acidity as acetic acid (mg/kg) | titration | ≤100 | ≤50 | ≤50 |
| Chloride (mg/kg) | ion chromatography | ≤5 | ≤1 | ≤1 |
| APHA color | ASTM D1209-21 | ≤20 | ≤10 | ≤10 |
| Density at 20 °C (g/cm³) | ASTM D4052-22 | 1.198–1.208 | 1.200–1.207 | 1.200–1.207 |
Polyurethane casting and cleaning operations have used PC as a high-flash polar modifier in place of dimethyl sulfoxide in two-zone solvent recovery. The comparative advantages are a higher dielectric constant (64.4 vs 47.2 at 25 °C) and a higher closed-cup flash point (132 °C vs 87 °C). However, PC exhibits stronger solvency for flexible polyurethane residues, which can reduce filtration cycles in solvent reclamation because oligomeric diol fragments remain suspended. On production-scale wiped-film evaporators with heated surface area of 2.5 m², PC-based wash streams are distilled at 150–170 °C under 5–10 kPa absolute pressure; the recovered solvent is monitored by ASTM D4052-22 density analysis and Karl Fischer titration. Amine-based polyurethane catalysts must be excluded from the wet solvent tank because amine adducts accelerate ring-opening hydrolysis and generate volatile propylene oxide decomposition products.
Aluminium electrolytic capacitor electrolyte systems often incorporate propylene carbonate with quaternary ammonium borate or phosphate salts. The solvent’s dielectric constant permits ionic dissociation at operating temperatures from -40 °C to 105 °C, while its vapour pressure of 0.03 mmHg at 20 °C reduces solvent loss through capacitor seals. Conductivity data for 1 M tetraethylammonium tetrafluoroborate in PC are reported in the range 12–14 mS/cm at 25 °C, measured by impedance spectroscopy in sealed conductivity cells. A limitation is that PC’s viscosity of 2.5 mPa·s at 25 °C rises to approximately 20 mPa·s at -30 °C, which lowers high-rate pulse response in automotive cold-start applications. Suppliers specify chloride ≤1 mg/kg and sulfate ≤5 mg/kg for capacitor-grade material to minimize corrosion of etched aluminium foil.
In cosmetic solvent and nail polish remover formulations, PC-HP is selected primarily for low skin irritation relative to acetone, but formulation viscosity and evaporation rate must be managed because PC evaporates slowly; its evaporation rate relative to butyl acetate is reported at 0.01 under ASTM D3539-11 comparative conditions. The compound is listed under the International Nomenclature of Cosmetic Ingredients as propylene carbonate; no Annex II prohibition is assigned under EU Regulation (EC) No 1223/2009. In nail lacquer remover pastes, PC is combined with fumed silica thickeners at 3–5 wt% to produce a non-flowing gel; this reduces the drying effect associated with acetone but requires longer contact time on the nail plate. Antimicrobial preservation tests under ISO 11930:2019 are recommended where PC is used with water-containing micellar systems because the carbonate ring can slowly hydrolyze and alter pH. Bulk storage requires closed-top stainless steel or high-density polyethylene vessels blanketed with dry nitrogen; aluminium and unlined carbon steel are avoided for liquid service because trace acid generated by hydrolysis can initiate corrosion.
Regulatory status across major markets includes REACH registration and TSCA listing obligations. Under Regulation (EC) No 1272/2008 (CLP), industrial propylene carbonate is commonly classified as Eye Irritant 2, H319, while the flash point above 60 °C excludes classification as a flammable liquid category 1 or 2. Ready biodegradability is reported under OECD 301F conditions, with carbon dioxide release and dissolved organic carbon removal monitored over 28 days. The operational boundary remains moisture intrusion: transfer lines and day tanks should be closed-loop with dry nitrogen padding, and aqueous alkaline or strongly acidic additives should be segregated to limit ring-opening hydrolysis and subsequent generation of propylene glycol and carbon dioxide.