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| HS Code | 597034 |
| Material | Polycarbonate (PC) |
| Chemical Formula | C16H14O3 |
| Density | 1.20 g/cm³ |
| Glass Transition Temperature | 147 °C |
| Continuous Service Temperature | 120 °C |
| Heat Deflection Temperature At 1 8 Mpa | 130 °C |
| Tensile Strength | 60–70 MPa |
| Tensile Modulus | 2.3–2.4 GPa |
| Flexural Strength | 90 MPa |
| Flexural Modulus | 2.3 GPa |
| Impact Strength Izod Notched | 600–800 J/m |
| Rockwell Hardness | M70 |
| Thermal Conductivity | 0.21 W/(m·K) |
| Coefficient Of Thermal Expansion | 65 × 10^-6 /K |
| Volume Resistivity | 10^15 Ω·cm |
| Dielectric Strength | 15–17 kV/mm |
| Refractive Index | 1.585 |
| Light Transmittance | 88–90% |
| Water Absorption 24h At 23 C | 0.15–0.20% |
| Uv Resistance | Poor without UV stabilization or coating |
| Oxygen Index | 25–27% |
As an accredited Polycarbonate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polycarbonate pellets supplied in 25 kg sealed polyethylene-lined bags, palletized and shrink-wrapped for secure transport. |
| Container Loading (20′ FCL) | 20′ FCL: load polycarbonate pellets in sealed bags, stack evenly, secure with dunnage, keep dry and contaminant-free. |
| Shipping | Polycarbonate is shipped as a non-hazardous plastic resin, typically in pellet or granule form. It is packed in moisture-resistant bags, fiber drums, or bulk containers to prevent contamination. Avoid excessive heat and humidity during transit. Standard dry cargo transport is suitable, with no special hazard labeling required for most shipments. |
| Storage | Store polycarbonate in a cool, dry, well-ventilated area away from direct sunlight, UV radiation, and high heat sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid proximity to strong oxidizing agents, acids, and bases. Maintain stable temperatures and low humidity to preserve material integrity and prevent degradation. |
| Shelf Life | Polycarbonate's shelf life is typically 5-10 years when stored in a cool, dry, dark environment, away from UV and moisture. |
Automotive forward lighting lenses and light guides are produced from polycarbonate grades selected for luminous transmittance above 89 % and haze below 1 % when measured on 3.2 mm moulded plaques according to ASTM D1003. The material specification references SAE J576 for plastic optical components and UNECE R112 together with FMVSS 108 at the full-lamp homologation level. Formulation additives are held within narrow ranges: 0.20–0.50 wt% UV absorber, 0.05–0.15 wt% phosphite stabiliser, and 0.10–0.30 wt% internal mould release. Higher mould release loadings above 0.30 wt% are avoided because subsequent polysiloxane hardcoat layers exhibit adhesion loss. Processing uses desiccant-bed drying at 120 °C for 4 h to a dew point below −40 °C, achieving residual moisture below 0.02 wt% before melt plastication in a screw with L/D 20:1–24:1 and compression ratio around 2.5:1. Molten polymer is maintained at 290–310 °C at the nozzle, with mould temperature clamped at 90–110 °C; heater-band overshoot above 320 °C accelerates molecular weight reduction and increases yellow-index shift. Lenses are filled via fan gates at the part edge or valve gates on the optical centre for circular light guides. After demoulding, parts receive a primer adhesion layer and a silicone hardcoat deposited by flow-coating or dip-coating at 3–8 µm dry thickness, then cured 30 min at 120 °C. Finished component types include outer headlamp lenses, daytime-running-light guides, turn-indicator covers, and internal bezels. On production lines, moisture-driven splay is the dominant failure mode when hopper loading is delayed or regrind exceeding 20 wt% is introduced without proportional drying time. Uncoated polycarbonate lenses are not specified for exterior front surfaces because UV exposure and road abrasion degrade haze beyond regulatory limits within the first twelve months.
In switchgear housing and connector insulator applications, flame-retardant polycarbonate compounds are specified to meet UL 94 V-0 at 1.5 mm and IEC 60695-2-11 glow-wire ignition at 850 °C for 30 s. The comparative tracking index is evaluated under IEC 60112; unfilled polycarbonate typically exceeds 600 V CTI, while glass-filled and phosphorus-retarded modifications may fall to 250–450 V depending on additive package. Formulation ratios for connector bodies and mini-circuit-breaker enclosures commonly use 8–12 wt% resorcinol bis(diphenyl phosphate) or bisphenol A bis(diphenyl phosphate), combined with 0.1–0.4 wt% PTFE anti-drip agent and 0–15 wt% glass fibre where dimensional stability under terminal insertion force is required. The compound is pre-dried at 100–110 °C for 4 h to below 0.05 wt% moisture if the carrier is PC/ABS, or 120 °C where the carrier is neat polycarbonate. Moulding is conducted with melt temperature 250–280 °C for PC/ABS grades and 280–300 °C for polycarbonate grades, with mould temperature 60–90 °C. Holding pressure is set to maintain 95–98 % pack and compensate for shrinkage of 0.5–0.7 %. In insert-moulded terminal blocks and relay bases, brass inserts are preheated to 80–100 °C to reduce differential shrinkage cracking at the insert interface. Hot-tip and valve-gate systems reduce gate-stringing when regrind addition is kept below 25 wt%. Finished component types include MCB housings, terminal rail bases, EV charging connector carriers, relay sockets, and inverter covers. Production bottlenecks arise from thin ribs adjacent to thick screw bosses, where differential cooling produces sink marks and internal stress sufficient to fail glow-wire testing at the boss-to-rib transition; tooling cores are therefore cooled with bubblers and the melt is held at the lower end of the temperature window to limit thermal degradation of the phosphorus flame retardant.
| Application scenario | Standard designation | Test condition | Acceptance criterion |
|---|---|---|---|
| Automotive forward lighting | SAE J576 / ASTM D1003 | Luminous transmittance and haze on 3.2 mm moulded plaque | Transmittance ≥ 89 %, haze ≤ 1 % |
| Switchgear and connector enclosures | UL 94 / IEC 60695-2-11 | Vertical burn at 1.5 mm; glow wire at 850 °C for 30 s | V-0; no ignition or flame ≤ 2 s |
| Medical device fluid contact | ISO 10993-1:2018 / USP Class VI | Biocompatibility and chemical characterisation | No cytotoxicity, no Class VI reactivity |
| Multi-wall roof glazing | EN 16153 / EN 13501-1 | Mechanical load and fire classification | B-s1,d0 classification |
| Thin-wall electronics | UL 94 / IEC 62321 | Vertical burn at 0.75 mm; restricted substances screening | V-0; RoHS compliance |
During repeated autoclave and gamma sterilisation cycles, polycarbonate components for Class II and Class III medical devices require molecular weight retention above 80 % after exposure to 25–40 kGy gamma irradiation, as measured by gel permeation chromatography. Materials are qualified under ISO 10993-1:2018 with chemical characterisation per ISO 10993-18, cytotoxicity per ISO 10993-5, and irritation and sensitisation per ISO 10993-10; biocompatibility is additionally documented in a USP Class VI test certificate. For fluid-contact housings and connectors, the resin meets FDA 21 CFR 177.1580 for polycarbonate food-contact applications where the design is not intended for long-term drug storage. Formulation is deliberately lean: internal mould release is limited to 0.05–0.10 wt%, migratory plasticisers are excluded, and gamma-stable grades may contain hindered amine stabiliser at 0.10–0.30 wt%. Moulding is performed in cleanroom conditions corresponding to ISO 14644-1 Class 8 or better, with desiccant drying at 120 °C for 4 h to below 0.02 wt% moisture. Melt temperature is maintained at 280–300 °C and mould temperature at 70–95 °C; regrind use is typically excluded from validated production records because lot traceability and extractables profiles must remain unchanged. Sterilisation compatibility includes steam autoclaving at 121 °C for 20 min, ethylene oxide exposure, and gamma radiation up to 40 kGy; repeated autoclave cycles above 50 are known to reduce notched Izod impact progressively through hydrolytic chain scission. Finished component types include luer lock connectors, IV stopcocks, surgical instrument handles, haemodialysis housing shells, blood oxygenator exterior shells, and high-pressure syringe barrels. A defined operational boundary is contact with lipid-based lubricants and certain cleaning agents, which can induce environmental stress cracking in stressed snap-fit regions; silicone or EPDM sealing elements are preferred over PVC because plasticiser migration creates surface microcrazes.
Before multi-wall sheet exits the polishing stack, a coextruded UV cap layer of 50–100 µm thickness on the weather-exposed side contains 2–6 wt% UV absorber, while the core layer carries no significant UV package. The sheet is certified under EN 16153 for multi-skin roof cladding, with light transmittance measured according to EN 410 and fire classification typically B-s1,d0 per EN 13501-1. Coextrusion uses a main single-screw extruder with L/D 30:1 and a satellite coextruder feeding the cap layer at 10–15 % of total sheet thickness. Melt temperature at the flat die is held at 270–295 °C, and the three-roll polishing stack runs at 70–100 °C to control surface gloss and residual stress. Multi-wall geometries from 4 mm to 25 mm are formed by vacuum calibration after the die, and the web is cut to length before natural cooling on a run-out conveyor; forced-air quenching is avoided because it locks in orientation stress that promotes warpage after installation. Finished product types include twin-wall and triple-wall greenhouse sheets, skylight panels, covered walkway roofing, and noise-barrier glazing. On installation lines, the cap layer must face the sun; reversed panels exhibit early yellowing and loss of impact strength within 24–36 months. PVC plastisol gaskets and sealing profiles are incompatible due to plasticiser migration causing craze formation at bearing points; only EPDM, silicone, or polyurethane elastomer sealing materials are specified.
Because FR PC/ABS must fill wall sections below 1.0 mm while maintaining UL 94 V-0 at 0.75 mm, the formulation modifies both rheology and thermal stability. The blend is typically 60–70 wt% polycarbonate and 30–40 wt% ABS, with 8–12 wt% bisphenol A bis(diphenyl phosphate), 0.2–0.4 wt% PTFE anti-drip, 1–2 wt% carbon black or colour masterbatch, and optional core-shell impact modifier at 2–5 wt%. Melt volume-flow rate is measured under ISO 1133-1:2022 at 300 °C/1.2 kg; FR thin-wall grades typically fall between 18–30 cm³/10 min. Drying uses desiccant-bed systems at 100–110 °C for 4 h to below 0.05 wt% moisture because ABS contributes residual moisture at the same dew point as PC/ABS. Injection moulding is performed with high-speed filling at 200–300 mm/s, melt temperature 280–310 °C, mould temperature 80–110 °C, and holding pressure 80–120 MPa. Thin-wall tools use hot-runner systems with valve gates and venting channels of 0.02–0.04 mm depth to evacuate phosphorus volatiles. Finished component types include notebook top covers, tablet rear shells, smartphone internal frames, charger bodies, and router housings. Process conflicts arise from the narrow window between flow-enhancing high melt temperature and decomposition of the phosphorus flame retardant above 310 °C, which deposits on mould surfaces and increases ejection force; bimetallic screws and free-flow nozzle designs without dead spots are required. Glass fibre is usually omitted in thin-wall electronics because it raises anisotropic warpage and reduces notched Izod below 20 kJ/m² in gate areas.
Transparent polycarbonate face shields and helmet visors derive impact resistance from the base resin, but their optical surface requires a polysiloxane hardcoat to achieve abrasion resistance under ANSI Z87.1 and EN 166. The sheet or injection-moulded lens is specified with UV absorber at 0.3–0.5 wt%, heat stabiliser at 0.05–0.10 wt%, and internal mould release at 0.10–0.20 wt%. Sheet for thermoforming is dried at 120 °C for 4 h and extruded at melt temperature 270–290 °C, then thermoformed at 180–200 °C using vacuum or pressure forming into female tools. Injection-moulded helmet shells are processed at 280–300 °C melt temperature and 80–100 °C mould temperature, with clamp force sized at 6–8 kN/cm² of projected area. Hardcoat is applied by flow-coating or dip-coating to 3–5 µm dry thickness and cured at 120–130 °C for 30–45 min. Abrasion resistance is verified by ASTM D1044 Taber haze increase below 5 % after 100 cycles using CS-10F wheels. Finished product types include riot helmet visors, fire-helmet face screens, machine guard windows, and safety spectacle lenses. The operational boundary is contact with alkaline cleaning chemicals and strong solvents, which attack uncoated edges and stress-concentrated clip zones; hardcoated polycarbonate cannot be machined after coating without exposing bare resin.
In high-voltage battery module insulators and cell holder frames, glass-filled flame-retardant polycarbonate must simultaneously resist ignition and maintain dielectric strength after thermal cycling. Qualification requires UL 94 V-0 at 1.5 mm; pack-level component standards include ISO 6469-1, IEC 62660-3, and GB 38031-2020 for vibration, mechanical shock, and fire resistance. Comparative tracking index is evaluated under IEC 60112; unfilled polycarbonate may exceed 600 V, but glass-filled flame-retardant grades commonly fall to 250–400 V, so creepage distances are increased where glass content exceeds 15 wt%. Formulation uses 10–20 wt% glass fibre, 8–15 wt% phosphorus flame retardant, 0.2–0.5 wt% heat stabiliser, and 0.2–0.3 wt% anti-drip agent. The compound is pre-dried at 120 °C for 4 h to below 0.02 wt% moisture. Injection moulding is conducted at melt temperature 270–300 °C and mould temperature 80–110 °C, with sequential valve gating to manage glass-fibre orientation. Finished component types include battery module end plates, cell holder frames, busbar insulators, and high-voltage connector supports. Glass-fibre orientation causes anisotropic shrinkage of 0.2–0.5 % along flow and 0.5–0.8 % transverse to flow; tooling compensation requires a mould temperature gradient not exceeding 10 °C. Published data for CTI above 400 V at 20 wt% glass loading combined with high phosphorus flame retardant is limited, so busbar spacing is validated by moulded-plaque CTI testing rather than supplier datasheet extrapolation.
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On injection molding lines, melt temperature is normally maintained between 280 °C and 320 °C, with mold temperature controlled from 70 °C to 100 °C. These conditions preserve sufficient melt flow length for thin-wall electrical housings while limiting thermal degradation. In a reciprocating screw with an L/D ratio of 20:1 to 24:1 and compression ratio of 2.0:1 to 2.5:1, the melt MVR of 9–12 cm³/10 min permits filling at moderate injection speeds. Shear heating is measurable but predictable; residence time at 300 °C longer than 8–10 minutes typically shifts melt color and reduces melt viscosity through chain scission. Shot size should remain between 30% and 70% of barrel capacity because small shots increase residence time and large shots degrade melt homogeneity. Clamp force requirements follow standard projected-area calculations, commonly 25–50 kN per cm² of projected part area for technical parts, though local geometry and gate design alter the practical pressure requirement.
For a 10 cm³/10 min MVR grade at 300 °C, capillary rheometry data typically show apparent viscosity in the range of 300–500 Pa·s at 1000 s⁻¹ and 1200–1800 Pa·s at 100 s⁻¹. This shear-thinning behavior permits filling thin walls but demands adequate gate size to reduce shear heating. Drying discipline is a critical process boundary. At 120 °C pellet bed temperature, residual moisture decreases below 0.02 wt% within 4 h in a properly designed desiccant dryer; after drying, pellets must be conveyed dry and processed within a hopper protected by nitrogen or dehumidified air. Batch-to-batch variability in optical appearance and impact strength is frequently traced to insufficient dew-point control, not to differences in melt flow rate.
Mold shrinkage for unreinforced PC under ISO 294-4:2018 is typically 0.5–0.7% in flow and 0.5–0.7% transverse, giving low post-mold warpage relative to semicrystalline materials. Ejection draft angles from 0.5° to 1° are normally used on textured cores because PC replicates mold surfaces and can generate demolding drag. Vent depth should not exceed 0.02–0.03 mm for conventional molding to avoid flash while allowing gas displacement.
Bisphenol-A polycarbonate (BPA-PC) is an amorphous thermoplastic produced commercially through interfacial polycondensation of bisphenol A with phosgene or through melt transesterification with diphenyl carbonate. The polymer exhibits a glass transition temperature near 147 °C as measured by differential scanning calorimetry under ISO 11357-2:2020, no melting point, and a solid-state density of 1.20 g/cm³ according to ISO 1183-1:2019. Conventional unreinforced grades such as Makrolon® 2805, Lexan™ 943A, and Panlite® L-1250Y are characterized by melt volume-flow rates in the range of 9–12 cm³/10 min at 300 °C and 1.2 kg load per ISO 1133-1:2022. The repeating carbonate linkage and aromatic rings provide a combination of transparency, dimensional stability, and impact-energy absorption. Tensile stress at yield for a general-purpose transparent extrusion/molding grade is typically 63–65 MPa under ISO 527-1:2019 and ISO 527-2:2012, while flexural modulus is commonly 2350–2400 MPa under ISO 178:2019. Transparent grades transmit 88–91% of visible light at 3.0 mm thickness according to ASTM D1003-21, with haze below 1.0% in polished plaques.
The same aromatic structure that yields high modulus and thermal capability also imposes a narrow melt-processing window. Polycarbonate hydrolyzes when residual moisture exceeds 0.02 wt% in the melt, producing splay, molecular-weight loss, and reduced notched impact strength. Processing therefore requires a closed-loop desiccant dryer supplying air at a dew point no higher than -40 °C. Pellets are typically dried at 120 °C for 2–4 h, with drying time extended to 4–6 h when ambient relative humidity exceeds 60%. The use of hopper-heated dryers or ambient air is considered incompatible with high-gloss optical parts because such air can exceed the moisture specification and create surface defects on injection molded lenses and automotive glazing.
At a wall thickness of 3.0 mm, a general-purpose transparent polycarbonate exhibits a notched Izod impact value between 600 J/m and 850 J/m under ASTM D256; notched Izod values are thickness-dependent and the material becomes notch-sensitive under multiaxial loading. HDT/A at 1.8 MPa is typically 124–132 °C per ISO 75-2:2013, while Vicat softening temperature B50 is 144–150 °C per ISO 306:2022. The material's refractive index of 1.584–1.586 under ISO 489 is higher than that of acrylic, which affects optical design of lenses and light guides. Stress optical coefficient of bisphenol-A PC is approximately 70 × 10-12 Pa⁻¹; this means residual gate stresses produce observable birefringence in polarized light. In optical lens applications, low-birefringence grades and optimized gate design are used. Published data for specific injection-compression configurations is limited.
| Property | Test method | Polycarbonate | PMMA | PETG | ABS |
|---|---|---|---|---|---|
| Density (g/cm³) | ISO 1183-1:2019 | 1.20 | 1.19 | 1.27 | 1.04–1.07 |
| Visible light transmittance (%) | ASTM D1003-21 | 88–91 | 92–93 | 88–90 | Opaque/translucent |
| Tensile stress at yield/break (MPa) | ISO 527-2:2012 | 60–70 (yield) | 70–75 (break) | 50 (yield) | 40–50 (yield) |
| Flexural modulus (MPa) | ISO 178:2019 | 2350–2400 | 3300 | 2100 | 2100–2400 |
| Notched Izod at 23°C (J/m) | ASTM D256 | 600–850 | 12–20 | 80–100 | 200–400 |
| HDT/A at 1.8 MPa (°C) | ISO 75-2:2013 | 124–132 | 95–105 | 63–70 | 95–105 |
Polycarbonate homopolymer can be formulated to meet UL 94 V-0 at 1.5 mm or 3.0 mm in flame-retardant grades such as Lexan™ 945 and Makrolon® FR6027; unreinforced general-purpose transparent grades typically carry UL 94 HB or V-2 at equivalent thicknesses. Under UL 94 V-0, no single flame application may burn for more than 10 s, and the sum of burn times for five specimens may not exceed 50 s; V-2 permits flaming drips, while V-0 does not. Dielectric strength of dried, unfilled PC is commonly 25–35 kV/mm per IEC 60243-1:2013, and volume resistivity at 23 °C is generally 1014–1015 Ω·m per IEC 62631-3-1. Compliance for food-contact applications is typically declared under FDA 21 CFR 177.1580 for authorized polycarbonate resins, while European food-contact grades are assessed under Commission Regulation (EU) 10/2011 and amendments. REACH compliance is documented against Regulation (EC) 1907/2006, and RoHS conformity is verified against Directive 2011/65/EU Annex II restricted substance limits.
| Requirement | Standard/regulation | Typical PC condition |
|---|---|---|
| Flame rating | UL 94 | V-0 at 1.5 mm or 3.0 mm in FR grades |
| Food contact resin | FDA 21 CFR 177.1580 | Authorized BPA-PC resin subject to end-use limits |
| EU food contact | EU 10/2011 | Compliance declared per migration limits and simulant testing |
| RoHS restricted substances | 2011/65/EU Annex II | Max Cd 0.01 wt%, Pb 0.1 wt%, Hg 0.1 wt%, CrVI 0.1 wt%, PBB/PBDE 0.1 wt% |
| REACH SVHC | 1907/2006 | Grade-specific declaration; no PC resin monograph restriction |
Electrical and flame-retardant properties depend on moisture content and part thickness. Conditioning of specimens at 50% RH and 23 °C before dielectric testing is required to obtain reproducible results. In hot-pluggable electrical connectors and battery charger housings, the practical upper continuous-use temperature is bounded by UL relative thermal index values assigned to specific formulations rather than by glass transition alone. Commercial polycarbonate is also supplied in blend form, such as PC/ABS and PC/PBT, where impact, chemical resistance, and melt flow are rebalanced. PC/ABS reduces melt viscosity and notch sensitivity at the expense of upper service temperature; PC/PBT improves solvent resistance but reduces optical clarity. These blends are not direct substitutes for transparent polycarbonate.
In production finishing operations, contact with aromatic hydrocarbons, ketones, esters, chlorinated solvents, plasticizer-loaded vinyl, or alkaline cleaners above pH 10 can induce environmental stress cracking in molded polycarbonate, especially when internal molded-in stresses exceed 1–2 MPa at the surface. Solvent-based adhesive systems should be qualified by exposure testing under ASTM D543 using the actual part geometry and stress state. Alcohol-based cleaners at concentrations up to 70% isopropanol are commonly used for short surface wiping, but prolonged immersion or heated vapor exposure is not recommended for loaded parts. Annealing at 120–130 °C for 1–2 h after machining or solvent contact reduces the residual stress that accelerates crazing, but it cannot restore polymer chain length after hydrolytic degradation.
For thick-walled trial parts machined from extruded polycarbonate plate, cutting tools with high positive rake angles and low feed rates are required because localized heating above the glass transition can create surface smears and internal stress. Coolant-free machining is possible for shallow cuts below 0.5 mm, but flooded coolant or compressed air is preferred for deeper profiling to prevent edge microcracks. Thermoformed PC sheet must be pre-dried to below 0.05 wt% moisture, and sheet surface temperature is typically 170–190 °C for forming; below this range the sheet cracks, while above 200 °C surface degradation and bubble formation occur. Post-forming annealing at 120 °C for 1 h reduces stress whitening around clamps.
Polycarbonate is selected over PMMA when impact and edge-fastener loads control the design because notched Izod values are on the order of 30–60 times higher than those of PMMA under ASTM D256. This shift is accompanied by lower scratch resistance: PMMA surfaces typically exhibit pencil hardness in the 3H–4H range under ASTM D3363, while polycarbonate is 2B–HB, requiring hard-coating after molding for glazing applications. Compared with soda-lime glass at equal thickness, polycarbonate provides roughly half the mass per unit area but with greater thermal expansion; the coefficient of linear thermal expansion of unreinforced PC is approximately 65–70 × 10-6 m/(m·K) per ISO 11359-2, which requires larger mounting clearances and flexible sealants in outdoor enclosures. In lighting and optical components, the higher refractive index of 1.586 enables thinner lenses for a given focal length, but birefringence near gates and weld lines can degrade polarization-sensitive optics.
Relative to PETG, polycarbonate offers roughly 1.8–2.1 times higher HDT/A at 1.8 MPa and higher flexural modulus, but PETG is generally more resistant to certain cosmetic and aromatic solvents and may process at lower melt temperatures. Data on long-term optical haze retention in PC under high-illuminance LED exposure is grade-dependent and is not uniformly published across all resin suppliers. When direct replacement of acrylic or glass is evaluated, the design review must account for polycarbonate's lower surface hardness, higher thermal expansion, notch sensitivity under sustained load, and need for moisture-stable drying before melt processing.