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Как аккредитованный завод Clariant Natural Polycarbonate 3D Printer Filament, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
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Clariant Natural Polycarbonate 3D Printer Filament processed on fused filament fabrication equipment replaces CNC-machined polycarbonate stock in early-stage automotive exterior lighting and bracket evaluation when low-quantity parts are required before injection tooling is commissioned. The feedstock is used at 100 wt% unfilled natural polycarbonate; no colour masterbatch, impact modifier, or UV stabilizer is dry-blended at the printer, and regrind derived from failed builds is limited to 15 wt% of total feed because repeated melt processing shifts MVR measured under ISO 1133-1:2022. The relevant flammability criterion for vehicle interior-equivalent parts is ISO 3795:1989 / FMVSS 302, which measures horizontal burn rate; published data for unfilled polycarbonate commonly falls below the 100 mm/min limit but must be verified on the actual printed component because layer orientation and voids alter flame propagation. Processing on a production-scale FFF array requires an all-metal hot end with a cartridge heater capable of maintaining 260–280°C, a borosilicate glass build plate with a PEI adhesion film held at 100–110°C, and an actively heated chamber at 70–80°C; below this chamber temperature, edge lift in lamp bezels with long unsupported spans exceeds 0.5 mm and renders parts unusable for optical fitment trials. Layer height is set to 0.2 mm with a 0.4 mm hardened steel nozzle, and print speed is held near 35 mm/s to maintain interlayer melt fusion. After printing, parts intended for dimensional stability are annealed in an air-circulating oven at 120°C for 1 h per 10 mm of wall thickness, with ramp rates no greater than 0.5°C/min; uncontrolled cooling induces stress cracking adjacent to mounting bosses. Terminal products include headlamp bezel prototypes, mirror housing fitment models, CHMSL carrier evaluations, and HVAC duct mock-ups used for package clearance studies.
In low-voltage enclosure prototyping, natural polycarbonate filament is processed into wall sections of 2.0–3.0 mm nominal thickness to evaluate dielectric insulation and mechanical impact before conversion to flame-retardant injection-moulded grades. Addition ratio remains 100 wt% unfilled PC; no halogenated flame-retardant masterbatch, no antimony synergist, and no mineral filler is added, which is the primary regulatory boundary. Under IEC 60695-11-10, unfilled natural PC typically achieves UL 94 V-2 at 1.5 mm and does not attain V-0 at the same thickness without a dedicated FR package; therefore the material is used for form, fit, and dielectric evaluation, not for final enclosures requiring V-0 ranking. Dielectric strength tested per IEC 60243-1:2013 is commonly reported in the range 20–30 kV/mm for unfilled PC sheet, but FFF layer boundaries introduce local voids that can reduce printed-part breakdown strength by a measurable margin; comparative testing on printed specimens is required before engineering sign-off. The downstream process uses a 0.6 mm brass or hardened nozzle to produce thicker walls, a 0.3 mm layer height, and print speeds of 30–40 mm/s; the chamber is held at 80–90°C to minimise interlaminar porosity. Post-print reaming of cable gland openings and tapping of screw bosses is performed after annealing at 120°C for 2 h, because as-built hole undersize in polycarbonate FFF is commonly observed at 0.2–0.4% of nominal diameter and thread-forming screws can cause radial cracking if used as-built. The material should not be exposed to strong alkaline cleaning agents, ketones, or aromatic hydrocarbons due to environmental stress cracking. Terminal products include terminal guard prototypes, sensor housing evaluation units, busbar cover mock-ups, and low-voltage enclosure covers for IEC 61439-1 layout verification.
Cytotoxicity screening under ISO 10993-5:2009 for short-term contacting device components is performed on printed coupons after the as-built surface has been mechanically polished or coated, because FFF layer troughs retain biological residues and interfere with extraction testing. The raw material is processed at 100 wt% unfilled polycarbonate without plasticiser or colourant; no biocidal additive is incorporated, and no solvent-based smooth coating is assumed to penetrate the melt. The downstream process for medical-device prototyping uses a 0.4 mm hardened steel nozzle, a 0.15 mm layer height, and a heated chamber at 75–85°C to reduce interlayer voids; the build plate is a PEI-laminated glass substrate held at 105°C. Before biological evaluation, parts are annealed at 120°C for 2 h and then cleaned with deionised water and isopropanol to remove residual extrusion lubricants. Steam autoclave sterilisation at 121°C for 30 min is feasible only after annealing, but repeated autoclave cycles cause cumulative hydrolysis and dimensional drift in amorphous PC; published data for this specific configuration is limited, so cycle life must be validated per device protocol. Terminal products include surgical guide prototypes, instrument tray organisation fixtures, diagnostic device enclosure mock-ups, and anatomical models for pre-surgical planning; none are to be used as implanted final devices because ISO 10993-10:2021 sensitisation and irritation data on as-built FFF PC is limited and surface porosity cannot guarantee sterility.
Assembly jigs printed from unfilled natural PC filament are used to mimic the stiffness and thermal endurance of injection-moulded polycarbonate production components before high-volume tooling is cut. The feed formulation is 100 wt% virgin PC; no glass fibre or talc is added, which would alter the coefficient of thermal expansion away from the target material data. Dimensional tolerance for jig features is assessed under ISO 2768-1:1989 after the printed blanks have been annealed and reamed; as-built FFF holes are undersized by 0.2–0.4% and slot edges exhibit a surface waviness of 0.05–0.15 mm depending on layer height. Tensile data generated on printed coupons per ISO 527-2:2012 show marked anisotropy; the Z-axis strength of unfilled PC FFF specimens commonly falls to 40–50% of XY-axis values, which controls allowable load direction in drill jigs and assembly fixtures. The downstream process on a production FFF platform involves a 0.4 mm nozzle, 0.2 mm layer height, 35 mm/s print speed, and a chamber maintained at 80°C; build plate temperatures below 100°C increase first-layer delamination. After printing, fixtures are placed between two flat aluminium plates and annealed in an air-circulating oven at 120°C for 1 h per 10 mm of maximum cross-section, followed by slow cooling at 0.3°C/min to prevent thermal stress concentration. Inserts for threaded locations are installed with a heat-staking press at 260°C tip temperature, not with solvent-based adhesives, because common ketones induce environmental stress cracking in PC. Terminal products include drill jigs, routing templates, assembly fixture base plates, and check gauges used on machining and inspection lines.
Thermoforming plug assists and vacuum tool prototypes are produced by FFF from natural PC filament when lead time constraints override the dimensional stability of cast aluminium or acetal tooling. The formulation ratio is 100 wt% unfilled PC; no mould-release agent is compounded into the polymer, and external silicone-free release is applied only as a surface film that contributes less than 1 wt% of the finished tool mass. Because the tool may be used in pre-production packaging trials, the relevant food-contact reference is EU Regulation (EC) No 10/2011 and US FDA 21 CFR 177.1580; however, direct food-contact equivalence must not be assumed, because FFF porosity and layer seams can harbour contaminants and the tool surface requires a food-grade epoxy seal prior to contact simulation. The downstream process uses a 0.4 mm nozzle with a 0.25 mm layer height, a 70°C heated chamber, and a bed temperature of 100°C; tool bodies are printed with dense 100% infill to provide compressive strength during vacuum pressure differentials. After printing, vacuum holes are drilled and counter-sunk from the back face, and the outer surface is sealed with a low-viscosity epoxy to fill layer striations. Terminal products include vacuum forming tools for thin-gauge PET trays, blister pack cavity tools, plug assists for polycarbonate sheet forming, and lay-up templates for short-run packaging prototypes.
For aerospace cabin interior mock-ups and ground-test layout units, natural PC filament is used only for non-structural geometry evaluation, because unfilled PC does not possess the flame-retardant package required for production cabin interiors. Feedstock remains 100 wt% unfilled PC; no fluoropolymer or phosphorus-based FR concentrate is added, and post-print intumescent coatings are not considered part of the polymer formulation. The relevant airworthiness flammability reference is FAR 25.853(a) Appendix F Part I vertical burn; published data for this specific configuration is limited, and printed-part results vary with infill density, so each geometry requires verification. Processing for large duct sections uses a 0.6 mm nozzle, 0.3 mm layer height, and an actively heated chamber at 85–100°C; sections exceeding 300 mm in the longest axis are split and bonded to control warpage. Mechanical fastening with aluminium brackets is preferred over solvent bonding because aromatic solvent cements cause stress cracking at layer interfaces. Terminal products include cabin air distribution duct mock-ups, avionics cooling duct prototypes, seat mechanism cover fit-check units, and antenna radome test articles fabricated solely for aerodynamic and packaging evaluation, not for flight.
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Clariant Natural Polycarbonate 3D Printer Filament is an unfilled, natural-grade thermoplastic feedstock based on bisphenol-A polycarbonate supplied for fused filament fabrication. The material is distributed in 1.75 mm and 2.85 mm diameter formats, with typical spool net weights of 0.75 kg or 1 kg where regional packaging permits. Unlike pigmented or compounded polycarbonate grades, the natural variant contains no visible colorant and exhibits translucency after processing; optical transmission is lower than cast polymethyl methacrylate because printed layer interfaces, flow lines, and microvoids scatter light. Dimensional acceptance is commonly referenced to ISO 286-1 limit designations or supplier-specific laser-gauge records, with roundness deviation monitored to ±0.05 mm for 1.75 mm feedstock. The material is intended for functional prototypes, fixtures, jigs, and short-run tooling where higher temperature resistance and impact strength are required relative to acrylonitrile-butadiene-styrene and poly(ethylene terephthalate) glycol. Published data for this specific configuration is limited when no distributor-controlled datasheet accompanies the lot; the following sections therefore use reference data for unfilled polycarbonate filament and identify where end-user verification is required.
Moisture uptake is the controlling pre-processing variable for polycarbonate. Unfilled bisphenol-A polycarbonate filament exposed to 23 °C and 50 % RH typically equilibrates to 0.15–0.20 wt% water; at 60 % RH the value can exceed 0.25 wt%. Extrusion stability with a 1.75 mm filament requires a residual moisture content below 0.02 wt%. Above 0.03 wt%, hydrolytic chain scission during the 260–300 °C melt residence produces surface splay, reduced interlayer tensile strength, and visible voids in the weld bead. Drying is performed in a forced-convection oven or desiccant dryer at 80 °C for 6–12 h, or in a vacuum oven at 80 °C and pressure below 50 mbar for 4–8 h. Desiccant dryers should deliver a dew point no higher than -40 °C. Spools removed from sealed packaging at ambient humidity above 60 % are pre-dried before printing. A dry box or heated filament cabinet maintained at 60–70 °C with a desiccant bed is advised for long builds exceeding 8 h. Batch-to-batch variance in moisture content has been observed when storage conditions differ across distributor warehouses; a previously opened spool exposed to ambient air for more than 24 h must be re-dried. Failure to dry is not corrected by raising nozzle temperature, because hydrolysis accelerates with temperature and the melt becomes lower-viscosity and gas-laden.
Polycarbonate solidifies with a coefficient of linear thermal expansion near 65–70 × 10⁻⁶ K⁻¹ below the glass transition. The resulting shrinkage during deposition creates a warping moment at the build-plate interface. The heated bed is set to 90–110 °C for unfilled polycarbonate; below 85 °C, edge lift often begins before the tenth layer in parts with footprints larger than 80 mm. A fully enclosed build chamber stabilized at 60–80 °C reduces the vertical thermal gradient and is required for dimensionally stable sections above 100 mm in the longest axis. Printing without a chamber is possible only for small parts under 50 mm when bed adhesion is optimized. The first layer is deposited at 5–10 °C above the regular bed setpoint, with a first-layer height of 0.20–0.30 mm and a speed reduction to 15–25 mm/s. Adhesion systems commonly use polyetherimide or polycarbonate sheet at 100–115 °C, or adhesive formulations that develop peel strength above 0.2 N/mm at operating temperature. Nozzle temperature for unfilled natural polycarbonate is set between 260 °C and 300 °C, with printed bead tensile strength falling below acceptable limits below 260 °C. The processing window is narrow: a ±5 °C variation around the optimum can shift surface gloss and weld-line strength. Hardened steel or tool-steel nozzles with orifice diameters of 0.4–0.6 mm are recommended; brass nozzles are acceptable at low throughput but show faster wear when filled or reclaimed polycarbonate feedstocks are substituted. Print speeds are typically 30–60 mm/s, with volumetric throughput kept below 8 mm³/s to avoid melt fracture and pressure fluctuation on direct-drive extruders. Retraction distance should be limited to 1–2 mm on direct-drive and 4–6 mm on Bowden systems, with retraction speed below 30 mm/s; excessive retraction pulls humid air into the hot zone and generates nozzle drool or carbonization.
Because melt flow and dimensional tolerance jointly fix the maximum stable deposition rate, unfilled natural polycarbonate filament for fused deposition is characterized by a melt volume-flow rate in the extrusion-grade range rather than injection-molding grades. The value measured at 300 °C under 1.2 kg load according to ISO 1133-1:2022 is commonly 5–12 cm³/10 min. Lower melt flow improves interlayer melt strength but reduces maximum stable volumetric throughput; higher melt flow improves fluent deposition but increases susceptibility to stringing and shorter continuous-use thermal stability. Diameter control is maintained by multi-axis laser gauging during filament production. For reliable feed, a 1.75 mm filament should exhibit ovality no greater than 0.03 mm, while a 2.85 mm filament should remain within ±0.05 mm along the spool. Table 1 lists typical reference data for unfilled polycarbonate filament; these values are not substitutes for lot-specific certificates of analysis.
| Property | Typical range | Test standard |
|---|---|---|
| Density | 1.18–1.20 g/cm³ | ISO 1183-1:2019 |
| Tensile modulus | 2,200–2,600 MPa | ISO 527-2:2012 |
| Tensile stress at yield | 55–65 MPa | ISO 527-2:2012 |
| Tensile elongation at break | 50–120 % | ISO 527-2:2012 |
| Flexural modulus | 2,300–2,500 MPa | ISO 178:2019 |
| Izod notched impact strength, 23 °C | 15–30 kJ/m² | ISO 180:2019 |
| Heat deflection temperature, 1.8 MPa | 110–125 °C | ISO 75-2:2013 |
| Vicat softening temperature, 50 N | 140–150 °C | ISO 306:2022 |
| Glass transition temperature | 140–150 °C | ISO 11357-2:2020 |
Polycarbonate is selected over acrylonitrile-butadiene-styrene when parts must resist creep at service temperatures above 85 °C. ABS typically exhibits heat deflection around 85–100 °C at 1.8 MPa under ISO 75-2, while unfilled polycarbonate remains serviceable to 110–125 °C. Polycarbonate also demonstrates higher notched impact toughness than PETG and ABS, with Izod notched values of 15–30 kJ/m² compared with typical ABS values of 10–25 kJ/m² and PETG values of 5–15 kJ/m²; however, the upper end is dependent on moisture state and fusion quality. Relative to PETG, natural polycarbonate provides higher modulus and much higher heat deflection temperature, but PETG prints at lower bed temperatures and has lower susceptibility to warp. Relative to carbon-fiber-filled polycarbonate, the natural unfilled grade is electrically non-conductive, lower in stiffness, more translucent, and non-abrasive to brass nozzles. Carbon-fiber-filled polycarbonate may reach tensile modulus values above 6,000 MPa, but it sacrifices impact toughness and translucency. The unfilled natural grade is therefore used for translucent light diffusers, prototype electrical enclosures, inspection fixtures, and hot-air ducting where the part must survive brief excursions to 120 °C. It is not the first choice for high-abrasion locating fixtures or for high-cycle injection mold tooling; glass- or carbon-filled polycarbonate or tooling resins are selected there. The processing burden includes drying, enclosure temperatures above 60 °C, and bed temperatures not less than 90 °C, which restrict use on printers without heated chambers or high-temperature beds.
Before lot introduction to production, regulatory screening of the natural unfilled polycarbonate filament is usually assessed against the heavy-metal and restricted-substance requirements of RoHS 2011/65/EU Annex II and the candidate-list obligations of REACH. Because the material is unfilled and uncolored, certain additive-related screening burdens are lower than for pigmented or flame-retarded grades. However, compliance is not self-certified; each production lot must be verified through supplier documentation. Table 2 lists the main screening areas and the relevant test or document type.
| Compliance area | Applicable reference | Verification requirement |
|---|---|---|
| Restricted heavy metals and brominated flame retardants | RoHS 2011/65/EU Annex II | Supplier declaration or XRF screening per lot |
| Substances of very high concern | REACH Article 33 candidate list | Written confirmation of 0.1 wt% threshold |
| Flame resistance | UL 94 HB or V-2 at 1.5 mm | Material-specific UL yellow card if required |
| Food-contact status | FDA 21 CFR 177.1580 or EU 10/2011 | Not presumed; end-use migration testing required |
| Biocompatibility | ISO 10993-1:2018 | Not presumed; part-level evaluation required |
On production floors, the filament is used for vacuum forming fixtures, robotic end-of-arm tooling, and inspection gauges where dimensional stability under overhead lighting and brief contact with warm parts is required. A fixture printed at 0.2 mm layer height with 100 % rectilinear infill and annealed at 120 °C for 4 h can withstand contact with workpieces at 100 °C without gross deformation, provided the load is compressive. If the fixture sees clamping forces, the bolted joint should include metallic bushings; direct thread engagement in unfilled polycarbonate at ambient temperature can initiate radial cracking at fastening torques above 1.5 N·m in M5 bosses printed without heat-set inserts. The annealing cycle must use constrained support or a flat platen because printed polycarbonate parts can distort above the glass transition. Annealing also reduces residual stress and improves chemical resistance but may increase opacity slightly in natural translucent sections. Production-scale behavior has shown variable part shrinkage across build chambers when the chamber fan cycles unevenly; parts located near the door may lose interlayer bonding due to a 10–20 °C local air temperature drop. Therefore, thermocouple-logged chamber mapping is recommended before batch production.
Solvent incompatibility remains a strict boundary. The material should not be exposed to ketones such as acetone and methyl ethyl ketone, chlorinated hydrocarbons such as methylene chloride, or aromatic hydrocarbons such as toluene and xylene, because stress cracking or dissolution occurs. Alcohols may be used for mild surface cleaning but should be evaporated before thermal processing. The filament should not be combined with amine-based additives or flame-retardant masterbatch without compatibility testing, because certain amine species accelerate chain scission at processing temperatures. For outdoor use, UV stabilization must be confirmed separately; natural unfilled polycarbonate without UV protection develops yellowing and loss of surface gloss after extended exposure under ISO 4892-2 weathering cycles. End-use parts in continuous contact with water above 70 °C may undergo hydrolytic degradation unless annealed and stress-relieved. Published data for this specific configuration is limited for long-term creep in printed, void-containing geometries, so load-bearing parts require application-specific validation under ISO 899-1:2024 or similar.