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Polycarbonate (PC)

    • Product Name: Polycarbonate (PC)
    • 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
    Material Name Polycarbonate (PC)
    Polymer Family Thermoplastic
    Volume Resistivity Ohm Cm 1e16
    Flammability Ul94 V-2
    Uv Resistance Poor without additives
    Chemical Resistance Good for dilute acids and alcohols; poor for alkalis, ketones, and aromatics
    Processing Methods Injection molding, extrusion, blow molding, thermoforming

    As an accredited Polycarbonate (PC) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Polycarbonate (PC) resin pellets packaged in 25 kg moisture-barrier bags, stacked on pallets for industrial storage and transport.
    Container Loading (20′ FCL) Polycarbonate (PC) is loaded into a 20′ FCL, palletized or bagged, moisture-protected, securely stowed, and weight-compliant for safe sea transport.
    Shipping Polycarbonate (PC) is typically shipped as dry resin pellets in moisture-barrier bags, lined boxes, supersacks, or bulk containers. It is non-hazardous for transport, requiring no special dangerous-goods documentation. Keep containers closed and store in a cool, dry area away from direct sunlight and heat to prevent moisture absorption and degradation.
    Storage Store polycarbonate (PC) in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep original containers tightly closed to prevent moisture ingress and dust contamination. Avoid contact with strong oxidizers, alkalis, and organic solvents. Use grounded equipment to control static. Maintain stable temperatures, typically below 30°C, and follow manufacturer’s recommendations for shelf life and handling.
    Shelf Life Polycarbonate (PC) generally has a shelf life of 2 years under cool, dry, dark conditions, away from UV and moisture.
    Application of Polycarbonate (PC)

    What Limits Track Pitch Replication in Injection-Compression Molded Polycarbonate Optical Substrates?

    In optical disc replication, high-flow polycarbonate with a melt volume-flow rate of 60 cm³/10 min to 80 cm³/10 min at 300°C/1.2 kg (ISO 1133-1:2022) is injection-compression molded against a nickel stamper. The substrate must retain a thickness of 1.1 mm plus a 0.1 mm cover layer for Blu-ray discs while reproducing track pitch values down to 0.32 µm. Processing on a dedicated injection-compression machine with clamp force above 200 t uses barrel set temperatures of 340°C to 400°C, hot-runner tip temperatures above 400°C, and mold-surface temperatures between 120°C and 140°C. Pellets are dried at 120°C for 4 h to a moisture content below 0.02 percent; residual water above this threshold produces splay, carbonized specks, and loss of pit definition. Low-viscosity polycarbonate reduces flow-induced birefringence, but excessive melt temperature above 400°C accelerates thermal degradation, creating black specks that are detectable in optical readout. The process window for preserving optical path length difference below 20 nm/mm is therefore governed by the interaction of melt temperature, injection speed, packing pressure, and stamper temperature. Molded substrates are metallized and bonded with UV-curable resin; warpage caused by asymmetric cooling must remain within flatness limits defined by the relevant ECMA and ISO/IEC optical disc specifications. In recordable formats, dye-coated substrates require low surface roughness and low oligomer exudation. Compliance for the plastic substrate typically references EU RoHS 2011/65/EU Annex II restrictions on lead and cadmium in the disc stack, but principal technical acceptance criteria are defined by disc format specifications rather than general material standards.

    Stamper lift-off, substrate birefringence, and edge warpage are the main production-scale defects observed on high-volume optical disc lines. When clamp force is insufficient for the flow length, uneven stamper contact produces localized replication loss near the outer edge. Mold temperature differences of more than 2°C across the cavity create asymmetrical shrinkage and tilt. Machines without closed-loop injection velocity control exhibit batch-to-batch variation in birefringence above 5 nm/mm. High-flow polycarbonate grades used for Blu-ray replication have lower notched impact than general-purpose polycarbonate, normally below 10 kJ/m² at 23°C under ISO 180/1A, but the disc substrate does not require high energy absorption after molding. Because the substrate is a thin-walled disk, molecular orientation in the flow direction is frozen during rapid cooling; slow cooling above the glass transition temperature with mold temperatures above 140°C allows relaxation but extends cycle time and can cause sticking.

    Headlamp Lens Molding Window and Hard-Coat Adhesion Requirements

    Automotive polycarbonate headlamp outer lenses are molded from UV-stabilized grades with a melt volume-flow rate commonly between 10 cm³/10 min and 18 cm³/10 min at 300°C/1.2 kg. Barrel set temperatures are maintained between 280°C and 320°C, while mold wall temperatures below 90°C create visible flow lines and reduce impact strength in weld-line regions. Large polycarbonate lenses for passenger vehicles require clamp force from 500 t to 1,200 t depending on projected area. Drying before molding follows 120°C for 4 h to below 0.02 percent moisture; moisture above 0.03 percent reduces surface gloss and creates silver streaks. After ejection, lenses are transferred to a cleanroom coating line for primer and silicone-based hard-coat deposition. Adhesion is tested under ISO 2409 cross-cut tape pull after immersion in water at 65°C for 72 h; delamination along the cut edge indicates insufficient substrate cleaning or primer curing. Weatherability of coated lenses is evaluated under SAE J2527 xenon-arc exposure for 4,000 h, with yellow index increase below 2 units and haze below 3 percent. The substrate compound contains benzotriazole ultraviolet absorbers; combinations with free-amine additives are excluded because they can accelerate discoloration under high-temperature processing and contribute to mold deposit. The molded lens must comply with photometric and mechanical requirements of ECE R112 for type approval and FMVSS 108 for the US market, while SAE J576 covers plastic optical components. Typical production failure modes include edge microcracking during ultrasonic welding of the lens to the housing, stress whitening around gate vestiges, and hard-coat cracking over sharp wall-thickness changes.

    In switchgear and electric vehicle charging infrastructure, flame-retardant polycarbonate is specified when transparent covers, indicator windows, or touchscreen lenses must pass UL 94 V-0 at 1.5 mm while retaining clarity. The material is dried to below 0.02 percent moisture at 120°C for 4 h, then molded with barrel profiles from 280°C to 330°C and mold temperatures from 80°C to 110°C. Transparent flame-retardant grades typically rely on organophosphorus or sulfonate-based systems rather than brominated oligomers, because the latter reduce light transmission below 85 percent at 3 mm. The glow-wire test under IEC 60695-2-11 at 850°C is the primary acceptance criterion for unattended appliance enclosures, while comparative tracking index measured under IEC 60112 commonly falls in the 175 V to 250 V range, restricting high-voltage creepage distances unless design clearances are increased. For outdoor charge plugs, UV stabilization and low-temperature impact at -30°C are added; notched impact under ISO 180/A at -30°C is often specified above 8 kJ/m² to prevent brittle fracture during cable pull tests. Molding operators encounter plate-out from flame-retardant packages on polished mold surfaces; vent depths above 0.02 mm must be avoided to prevent flash while allowing volatiles to escape. Amine-based mold release agents and unauthorized regrind above 20 percent compromise hydrolysis resistance and are excluded from production control plans. Terminal parts include circuit-breaker covers, EV charge plug housings, industrial control panel windows, and sensor covers for battery management systems.

    When Polycarbonate Is Specified for Drug-Delivery Housings Under ISO 10993-1

    Medical-grade polycarbonate is injection molded in cleanroom cells for transparent drug-delivery device housings, luer-activated valve bodies, and surgical instrument handles. Biocompatibility evaluation follows ISO 10993-1 with endpoint testing commonly including ISO 10993-5 for cytotoxicity, ISO 10993-10 for sensitization, and ISO 10993-11 for systemic toxicity. Material conformity is also assessed under USP <661.1> for plastic components of packaging systems. Drying at 120°C for 4 h to a moisture content below 0.02 percent is required to prevent hydrolysis in the barrel. Barrel temperatures are set from 280°C to 320°C, and mold temperatures are held between 80°C and 120°C to reduce molded-in stress. Stress is the primary processing variable because polycarbonate develops environmental stress cracking in contact with lipid emulsions, alcohol-based disinfectants, and some surfactants. Molded-in stress above 15 MPa combined with external clamp load on a luer fitting can produce craze networks within hours. Production lines therefore use polarized-light inspection or solvent crack-resistance testing as a go/no-go gate for high-stress components. Ethylene oxide sterilization is compatible with polycarbonate; gamma irradiation at 25 kGy to 50 kGy causes observable yellowing unless radiation-stable grades and color compensation are used. Steam autoclave cycling at 121°C for 15 min is acceptable for limited cycles, but repeated cycling above 100 cycles causes molecular weight loss, haze, and reduction in notched impact under ISO 180/A to below 15 kJ/m². Leachables risk assessment under ISO 10993-17 includes bisphenol A quantification, and the final device must meet toxicological risk assessment requirements of EU MDR 2017/745 Annex I.

    On multiwall sheet extrusion lines equipped with coextrusion blocks and vacuum calibration, polycarbonate with a melt volume-flow rate of 3 cm³/10 min to 10 cm³/10 min at 300°C/1.2 kg is processed through slot dies at melt temperatures of 260°C to 300°C. The coextruded UV cap layer, typically 20 µm to 75 µm thick, must remain continuous across the sheet width; breaks in the cap layer lead to yellowing, embrittlement, and loss of impact within 2 years in southern European exposure. Solid sheet for glazing is evaluated under EN 16240 for light transmission and mechanical performance, while multiwall sheets fall under EN 16153. Fire classification for construction products is determined under EN 13501-1; some flame-retardant polycarbonate sheet grades achieve B-s1,d0, but unreinforced standard grades are lower. Thermally induced movement is significant because polycarbonate has a linear coefficient of thermal expansion of 0.065 mm/m·°C; a 6 m sheet exposed to a 40°C temperature swing requires an expansion gap of approximately 15 mm to prevent buckling. Cold bending of solid sheet is limited to radii above 100 times the sheet thickness to avoid surface craze. Cleaning with alkaline or aromatic solvents is prohibited, as both attack the UV cap layer and the substrate. Puncture impact resistance is demonstrated by falling-mass testing under EN ISO 6603-1, with thickness- and geometry-dependent energy thresholds specified by the profile fabricator. Terminal products include skylights, machine guard glazing, greenhouse roof panels, and bus shelter glazing.

    Visor and Ophthalmic Lens Moulding: Impact Performance Under EN 166 and ANSI Z87.1

    Polycarbonate is the default material for plano safety lenses, face shield visors, and goggle bodies because it absorbs high-speed particle energy without perforation. Injection-molded visors are produced from grades with melt volume-flow rates between 15 cm³/10 min and 25 cm³/10 min at 300°C/1.2 kg. Molds for optical surfaces are polished to below 0.025 µm Ra and are maintained at wall temperatures from 80°C to 110°C to reduce flow-line distortion. Compliance for finished eye protectors is tested under EN 166 and ANSI/ISEA Z87.1; high-mass and high-velocity impact regimens are specified in those standards, and uncoated polycarbonate lenses must remain unperforated after direct projectile strikes. Hard-coat adhesion is evaluated under ISO 2409 after immersion in water at 40°C for 24 h; coated lenses must also pass abrasion resistance testing under EN 168 to maintain optical quality. The optical grade used for visors retains a notched Izod impact strength above 60 kJ/m² at 23°C under ISO 180/A; thin-wall sections below 1 mm still perform under high-speed puncture but become notch-sensitive when scratched. Ketones, aromatic solvents, and strong alkali cleaning agents produce surface haze and stress cracking in this application. Terminal products include face shields, safety goggles, riot helmet visors, and optical comparator covers.

    Polycarbonate in Aircraft Cabin Glazing: Heat Release and Density Constraints

    Aircraft cabin interior panels, instrument display covers, and window reveals are thermoformed from low-heat-release polycarbonate sheet. The material is selected over lower-impact acrylic for parts that must survive cabin pressurization and blunt-impact events without shattering. Fire performance is evaluated under FAR 25.853(a) for vertical burn, with additional heat release testing under FAR 25.853(d) and ASTM E662 for smoke density. Some aircraft programs require OSU heat release below 65 kW/m² peak and 65 kW·min/m² total; specific values depend on the applicable airworthiness bulletin. Extruded sheet is dried at 120°C for 4 h before thermoforming at 170°C to 200°C. Density of polycarbonate, 1.20 g/cm³, is advantageous for weight reduction compared with glass but similar to PMMA. The main processing conflict is thermoforming temperature: above 200°C, dimensional sag becomes severe and heat-release additives may migrate to the surface, creating a visible bloom. Below 170°C, thin-wall sections tear at draw ratios above 2:1. Trimmed edges and mounting holes must be radiused; sharp corners in polycarbonate act as crack initiators under cyclic pressurization. Terminal components include air duct covers, window reveals, and cockpit instrument overlay lenses.

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    Certification & Compliance
    More Introduction

    Bisphenol A polycarbonate (PC) is an amorphous engineering thermoplastic produced by interfacial phosgenation of bisphenol A or by non-phosgene melt transesterification with diphenyl carbonate. The polymer backbone contains carbonate linkages and aromatic rings, giving a glass transition temperature near 147°C (ISO 11357-2) and a specific gravity of 1.20 g/cm³ (ISO 1183-1). Unfilled transparent grades transmit 88–89% of visible light through a 3 mm plaque (ASTM D1003-13) with haze below 1%. Commercial designations include extrusion grades such as SABIC Lexan 9034 and Covestro Makrolon 3103; injection-molding grades such as Lexan 141R, Makrolon 2405, and Trinseo Calibre 301-6; and branched grades for sheet, profile, and foam. Representative published data for Lexan 141R include melt volume-flow rate of 10.5 cm³/10 min at 300°C under 1.2 kg (ISO 1133-1:2022), tensile stress at yield of 60 MPa (ISO 527-2), flexural modulus of 2350 MPa (ISO 178), notched Izod impact strength of 640 J/m (ASTM D256-10), and heat deflection temperature under 1.8 MPa of 127°C (ISO 75-2).

    How Does Residual Moisture Affect Melt-State Hydrolysis and Dimensional Control in PC Injection Molding?

    Residual moisture in polycarbonate is not limited to surface splay. The carbonate linkage undergoes hydrolytic scission when pellets are molten above 280°C in the presence of more than 0.02 wt% water (ISO 15512). This reduces number-average molecular weight, increases melt volume-flow rate, and can lower notched Izod impact strength by 25–40% while producing silver streaks, microvoids, and brittle regions in molded parts. Production-scale injection molding of medium-viscosity grades such as Lexan 141R or Makrolon 2405 therefore uses closed-loop desiccant dryers delivering air at a dew point of −40°C or lower, with resin bed temperature at 120°C and residence time of 4 h for cold pellets. A dry-air return circuit and insulated hopper prevent moisture regain in high-humidity molding rooms; when ambient relative humidity exceeds 60%, dried pellets should not remain in open hoppers for more than 30 min before entering the barrel.

    Barrel temperature profiles for a 40 mm general-purpose screw are commonly set at 260°C feed zone, 285°C compression zone, 300°C metering zone, and 310°C nozzle. Mold temperature is maintained at 80–100°C; lower mold temperatures increase flow-induced orientation and residual stress, reducing impact resistance and environmental stress-crack resistance. Hydraulic injection pressure of 70–110 MPa is typical, with clamp force of 0.8–1.1 t/cm² of projected area. Packing pressure is held at 60–80% of injection pressure for 2–5 s per millimetre of nominal wall thickness. Thermal degradation becomes process-relevant above 330°C or when residence time exceeds 8 min, producing chain scission, yellowing, and free carbonyl species. Post-mold shrinkage is anisotropic and measured as 0.5–0.7% in the flow direction and 0.6–0.8% transverse (ISO 294-4); gate lands are typically dimensioned at 60–100% of wall thickness to maintain packing density without excess shear.

    In sheet extrusion, high-viscosity grades with melt volume-flow rates below 6 cm³/10 min are processed on single-screw extruders with L/D 30–36, barrier screws, and 40 µm screen packs. Polishing roll temperatures from 120°C to 140°C are used to control surface replication and sheet curl. The narrower processing window for high-viscosity sheet grades arises from the conflict between melt strength, required for roll-stack transfer, and excessive shear heating at screw speeds above 60 rpm on larger machines.

    Polycarbonate sheet and molded glazing are specified where impact resistance, transparency, and mass reduction carry engineering priority. For transportation and industrial machine guarding, sheet thicknesses from 2 mm to 12 mm are common. Uncoated PC has relatively poor abrasion resistance, so polysiloxane hardcoat or UV-curable acrylic topcoat systems are applied by flow coating or dip coating and thermally cured near 130°C. Hardcoated PC sheet is often specified to maintain haze below 5% after 500 Taber cycles (ASTM D1044). High-speed puncture behavior is characterized by instrumented impact per ISO 6603-2; the notched Izod value alone does not predict penetration resistance in thick sections. For rail and mass-transit interiors, unfilled PC sheet generally requires fire-retardant cap layers or compounded FR grades to meet EN 45545-2 requirements for smoke density and heat release on vertical surfaces.

    Steam sterilization at 121°C or 134°C creates a specific limitation for PC medical components. Repeated autoclave cycles hydrolyze the polymer and reduce elongation at break, leading to embrittlement in snap-fit and luer-style connectors. Published data for specific device configurations is limited; however, ethylene oxide sterilization is widely used for PC because it preserves molecular weight. Gamma irradiation above 25 kGy tends to produce visible yellowing in unpigmented PC, although strength retention may remain acceptable. Electronic packaging and medical housings are typically qualified under ISO 10993-1 biological evaluation and USP Class VI material protocols. Food-contact use is subject to 21 CFR 177.1580 and Commission Regulation (EU) 10/2011, with specific migration limits for bisphenol A. In hospital environments, repeated wiping with isopropanol or quaternary ammonium disinfectants can accelerate environmental stress cracking in stressed PC parts, especially at concentrations above 70%.

    When Halogen-Free Flame-Retardant Additives Reduce Ductility at Low Temperature

    UL 94 V-0 compliance at 1.5 mm can be achieved with halogen-free phosphate, phosphazene, or sulfonate salt systems, but the additives modify low-temperature ductility. Unfilled unfilled PC grades frequently carry UL 94 V-2 at 1.5 mm; V-0 grades require additive loading that may reduce notched Izod impact from 640 J/m to values in the 150–450 J/m range at 23°C, depending on additive chemistry and wall thickness. At −20°C, some FR grades show a ductile-to-brittle transition above the unfilled resin, requiring additional wall thickness or design changes in outdoor electrical enclosures. Comparative tracking index under IEC 60112 is reported in the 175 V to 600 V range, depending on filler and FR chemistry, and creepage distances are assigned under IEC 60664-1.

    Compounding of halogen-free FR PC is conducted on co-rotating twin-screw extruders with L/D of 40 or greater. Barrel set points from 270°C to 300°C and screw speeds from 400 rpm to 600 rpm are used because higher shear intensifies resin degradation and plate-out. Liquid phosphates may be injected downstream of the melting zone, while phosphazene powders are fed through a side feeder to minimize thermal history. Bimetallic barrels and hardened screw elements are specified when abrasive FR fillers are included. The process conflict is that flame retardancy increases with phosphorus content, while melt strength and impact retention decrease; UL 94 V-0 at 1.5 mm therefore does not imply equivalent mechanical performance to unfilled PC. For outdoor use, UL 746C UV and water exposure must be evaluated separately because some FR additives accelerate surface erosion in wet-service environments.

    Comparative Property Matrix: PC, PMMA, ABS, and PETG

    The selection between PC and other transparent amorphous thermoplastics is driven by impact, heat, chemical exposure, and scratch requirements. Polycarbonate differs from PMMA in its much higher notched Izod impact strength, but PMMA offers higher visible-light transmission and better inherent scratch resistance. ABS is lower in heat deflection temperature and is often opaque, while PETG provides better chemical resistance to hospital-grade disinfectants but lower heat resistance.

    Representative transparent unfilled grades; values are published single-point data or typical ranges and vary by grade and conditioning.
    PropertyPolycarbonate (PC)PMMAABSPETG
    Density (ISO 1183-1) g/cm³1.201.191.04–1.071.27
    Light transmission (ASTM D1003-13) %88–899285–88 clear88–90
    Tensile yield (ISO 527-2) MPa60–6670–7440–5048–52
    HDT/A 1.8 MPa (ISO 75-2) °C125–12795–10090–10063–70
    Notched Izod (ASTM D256-10) J/m600–80012–20200–40090–200

    Inorganic glass is replaced by PC when weight savings and impact safety are required, but the elastic modulus of glass near 70 GPa is far higher than the 2.3–2.4 GPa flexural modulus of unfilled PC. Glass also resists scratching and solvent exposure without coating. PMMA is preferred for outdoor lenses where weathering and surface hardness are primary, but its brittle failure excludes it from high-impact machine guards. ABS provides economical housings with good surface aesthetics but does not match PC in transparency or heat resistance. PETG is selected for reusable medical containers and packaging exposed to alcohol-based disinfectants when lower HDT is acceptable; PC is excluded from some disinfectant-heavy environments because aromatic hydrocarbons, ketones, and esters can produce stress cracking under load. Polycarbonate also reacts unfavorably with amines and strong aqueous bases, whereas PETG and ABS show different resistance profiles.

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