Optik ve Levha Sınıfı Polikarbonat (PC) Granülleri Doğrudan Fabrika Toptan Satış
Polycarbonate (PC) homopolymer granules for optical and sheet conversion are amorphous thermoplastics synthesized from bisphenol A either by interfacial phosgenation or by melt transesterification with diphenyl carbonate. The glass transition temperature is near 147 °C, and the refractive index measured on a transparent plaque is 1.585 under ASTM D542-14. Optical & Sheet Grade Polycarbonate (PC) Granules Direct Factory Wholesale specifications are structured around melt flow rate measured at 300 °C under 1.2 kg load in accordance with ISO 1133-1:2022, residual moisture below 0.02% by weight under ISO 15512:2019, and luminous transmittance and haze measured on 3 mm plaques per ASTM D1003-21. Sheet extrusion grades typically occupy an MFR range of 3–10 g/10 min to preserve melt strength, while optical injection grades are supplied from 15–30 g/10 min for thin-wall replication. Factory-originated lots must be dedusted, melt-filtered, and packaged directly from dedicated silo lines to prevent cross-contamination with flame-retardant or glass-filled compounds. Direct wholesale granule supply is therefore controlled through viscosity drift, moisture limits, optical cleanliness, and batch-level documentation rather than resin identity alone.
What Processing Parameters Keep Optical-Grade PC Granules Below the Hydrolysis Threshold?
Hydrolysis and thermal oxidative chain scission are the dominant defect sources in optical-grade PC. Residual moisture above 0.02% by weight depolymerizes PC during plastication, releasing carbon dioxide and producing splay, silver streaks, and sub-visible haze. Desiccant dryers with a dew point below -40 °C are required; pellet core temperature should reach at least 120 °C for 4 hours. When ambient relative humidity exceeds 60%, feed hoppers must operate with closed-loop dried air and reduced throat exposure. Barrel zone profiles from 260 °C in the feed zone to 300 °C at the nozzle are standard for optical grades; melt temperature above 320 °C accelerates yellowing, while residence time at melt temperature should remain below 8 minutes. Shear heating in small sprues and thin runners can produce local melt temperatures above 340 °C if injection speed exceeds 150 mm/s. Hardened tool steel, generous runner diameters, and cold slug wells reduce shear-induced degradation. Mold temperature between 80 °C and 120 °C minimizes flow-induced birefringence and frozen-in stress; below 80 °C thick sections exhibit elevated haze, while above 120 °C cycle time increases and ejection can become unreliable.
Injection Molding Melt Temperature, Mold Temperature, and Hold Pressure Interdependence
For optical components such as LED collimator lenses, light pipes, and diffusing covers, gates are positioned so knit lines do not intersect the primary optical path. Holding pressure from 60 MPa to 100 MPa is typical for thin-wall parts; insufficient hold pressure creates sink marks and birefringent stress concentration, while excessive hold pressure increases residual stress and dimensional variability. MFR selection dictates fill response: 15 g/10 min for 2–3 mm thick lenses, 25–30 g/10 min for 0.8–1.5 mm light guides. Cavity pressure transducers and gate freeze time are used to establish hold time limits rather than relying on MFR alone. Hot runner systems must avoid stagnant melt zones; degraded PC in dead spots appears as yellowing and black specks. Vent depths between 0.02 mm and 0.03 mm are required to prevent diesel-effect burns on polished surfaces. Optical cavities are typically finished to SPI A-1 or A-2 surface, with mold temperature uniformity maintained within ±5 °C across the cavity. Published data for optical-grade PC in multi-cavity hot-runner systems with localized shear rates above 1000 s⁻¹ is limited, so production trials are required to validate yellowing and haze.
| Property | Test standard | Optical grade | Sheet grade |
|---|---|---|---|
| Melt flow rate at 300 °C/1.2 kg | ISO 1133-1:2022 | 15–30 g/10 min | 3–10 g/10 min |
| Moisture content | ISO 15512:2019 | < 0.02% | < 0.02% |
| Total luminous transmittance, 3 mm | ASTM D1003-21 | 88–91% | 85–90% |
| Haze, 3 mm | ASTM D1003-21 | < 1.0% | < 2.0% |
| Yellow index | ASTM E313-20 | < 1.5 | < 3.0 |
| Tensile stress at yield | ISO 527-2:2012 | 60–65 MPa | 58–63 MPa |
| Flexural modulus | ISO 178:2019 | 2350–2400 MPa | 2300–2400 MPa |
| Notched Izod at 23 °C | ASTM D256-23 | 600–850 J/m | 550–750 J/m |
| Vicat softening temperature, B50 | ISO 306:2013 | 144–148 °C | 144–147 °C |
Polished Roll Stack Temperatures Stabilize Sheet Haze and Warpage
On single-screw extruders with 30:1 to 36:1 L/D, sheet-grade PC granules are processed with barrier screws and gear-pump assisted feed to the die. Melt temperature at the die is maintained at 260–300 °C; lower melt temperature improves melt strength but raises die pressure, while higher melt temperature reduces optical haze but increases risk of edge degradation. Die lip adjusters and internal deckling control transverse thickness. Polished roll stack temperatures from 120 °C to 150 °C are used to prevent rapid quenching that causes internal stress and warpage. The middle roll is commonly 10–15 °C hotter than the first roll to control surface replication. A stable bank at the first nip, typically ±5 mm diameter fluctuation, is required to prevent entrapped air, surface haze, and edge bead defects. Thickness tolerance of ±2.5% with beta gauge feedback control is standard for direct factory sheet extrusion lines. Grade selection for thermoforming requires MFR at 3–8 g/10 min; higher MFR reduces melt strength and narrows the thermoforming window, causing excessive sag. For sheet thickness above 6 mm, residual moisture below 0.02% prevents microbubbles at the core. Outdoor glazing sheet uses a coextruded UV-stabilized cap layer; weathering validation is performed under ISO 4892-2:2013 with a yellow-index shift requirement of ΔYI < 3 after 1000 h xenon-arc exposure. Thermoformed parts require post-forming tensile testing per ASTM D638-14 and impact evaluation on formed sidewall sections.
Color and additive constraints in optical-grade PC are severe. Mold release agents such as pentaerythritol tetrastearate are limited to 0.2% because higher loadings scatter light and raise haze. Phosphite antioxidant packages must be selected for low volatility to avoid plate-out on polished mold surfaces. Optical grades often contain a blue toner to offset yellowing; batch-to-batch color is controlled by CIELAB ΔE* < 0.3 under D65/10° geometry. Light transmission in thick sections is affected by backscatter; for 5 mm thickness, optical-grade PC should maintain transmittance above 86%. For sheet, colorants and diffusers are compounded only after the base resin has passed optical acceptance. Additive concentrates based on incompatible carriers can form lens-like gels in film and sheet, so wax-free carriers are specified.
Optical & Sheet Grade Polycarbonate (PC) Granules Direct Factory Wholesale contracts differ from distributor supply because factory lots retain reactor-level traceability through extrusion pelletizing, air classification, and packaging. Granules are typically packed in 25 kg foil-lined multi-wall paper sacks or 500–1000 kg FIBCs with internal polyethylene liners. Each certificate of analysis lists MFR under ISO 1133-1:2022, moisture under ISO 15512:2019, CIELAB color coordinates measured with D65/10° geometry, and the relevant optical values under ASTM D1003-21. Direct factory silo transfers should pass through 20–40 µm melt screens for optical grades, dedusting cyclones to remove fines, and stainless-steel clean-line flow paths to avoid black specks. A lot with punctured barrier foil, loose sack seals, or granule clusters indicating moisture ingress must be rejected. Factory-loaded bulk containers are preferred for sheet plants consuming more than 20 t/month, provided feed lines are closed-loop and hopper residence time is short.
When Regrind Content Exceeds 20% in Sheet Production
Because reground PC from trimmed sheet and thermoforming skeletons carries heat history and particulate burden, addition above 10% in optical sheet is generally excluded. For non-optical sheet, regrind ratios from 10–30% are common. Each regrind heat history raises MFR by 3–10% and reduces notched Izod by 5–15% depending on moisture control, melt residence time, and grinder fines. Grinders should have 8–12 mm screens and magnetic separation; dust fraction should remain below 0.5% by weight. Closed-loop regrind from hot-runner sprues and unpainted clear parts is acceptable for some optical applications only after melt filtration and silo blending with virgin granule. Sheet factories that exceed 30% regrind must compensate with lower MFR virgin material or risk thermoforming sag and thickness variation. Vinyl contamination above 0.1% can generate hydrochloric acid during processing, causing black specks and corrosion. Alkaline cleaners and ketone-based mold releases are incompatible with polycarbonate and should not enter regrind streams because environmental stress cracking can develop after forming.
Controlling Moisture Uptake in Non-Barrier Factory Wholesale Shipments
Without barrier packaging, polycarbonate granules equilibrate with ambient humidity; equilibrium moisture uptake at 23 °C and 50% RH is approximately 0.15% by weight. Non-barrier packaging is technically acceptable only when destination dryers are sized to remove the additional moisture and when ambient relative humidity during transit remains below 55%. Pellets exposed to humid air require drying at 120 °C for at least 6 hours, with verification by ISO 15512:2019 before processing. If bulk railcars or trucks are used, they must be pressure-dried and sampled at multiple depths because moisture stratification occurs. Lots with visible condensation inside the liner or pellet surface tackiness are grounds for rejection. Sheet producers using outdoor silos in coastal environments should specify barrier packaging even with short transit times because salt aerosols and moisture ingress can produce surface haze and plate-out on polished rolls.
| Compliance requirement | Standard or regulatory reference | Factory lot acceptance criterion |
|---|---|---|
| Food-contact resin declaration | FDA 21 CFR §177.1580 | Resin type complies when used as specified |
| EU plastics food-contact migration | Regulation (EU) No 10/2011 | Overall migration ≤ 10 mg/dm² |
| Restriction of hazardous substances | RoHS 2011/65/EU Annex II | Pb ≤ 0.1%, Hg ≤ 0.1%, Cd ≤ 0.01% by weight |
| Registration, evaluation, authorisation | REACH 1907/2006 | Substance registered for EU market |
| Flame resistance for sheet glazing | UL 94 | V-0 at 3.0 mm for flame-retardant grades |
| Optical release test | ASTM D1003-21 | Haze < 1.0%, transmittance 88–91% for optical grade |
| Melt flow rate lot acceptance | ISO 1133-1:2022 | Within ± 10% of nominal certificate value |
| Weathering validation for stabilized sheet | ISO 4892-2:2013 | ΔYI < 3 after 1000 h xenon-arc |
Polycarbonate has inherent limitations in chemical resistance. Aromatic hydrocarbons, ketones, esters, and amines can cause environmental stress cracking under applied strain; continuous exposure above 60 °C to alkaline solutions may produce surface haze and loss of light transmission. Solvent-based mold releases or cleaning agents containing methyl ethyl ketone, acetone, or toluene should not be used on optical tools. Continuous service temperature under mechanical load is generally limited to 115–120 °C; short-term exposure above 130 °C is possible only at low stress. Unmodified PC is not inherently UV-stable for outdoor glazing; UV-stabilized cap layers or coextruded sheet are required under ISO 4892-2:2013. Grades with improved flow should not be selected for thick sheet because lower molecular weight reduces stress-crack resistance.