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FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid

    • Product Name: FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid
    • 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 792200
    Product Name FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid
    Material Type Polylactic Acid (PLA) Composite
    Reinforcement Microfiber
    Processing Method Injection Molding
    Density 1.24 g/cm3
    Fiber Content 10%
    Tensile Strength 48.3 MPa
    Tensile Modulus 3.79 GPa
    Elongation At Break 2.5%
    Flexural Strength 82.7 MPa
    Flexural Modulus 4.14 GPa
    Notched Izod Impact Strength 0.267 J/cm
    Unnotched Izod Impact Strength 0.534 J/cm
    Heat Deflection Temperature At 0 46 Mpa 55 °C
    Heat Deflection Temperature At 1 8 Mpa 50 °C
    Vicat Softening Temperature 55 °C
    Melt Flow Rate 10 g/10 min
    Processing Temperature 190-230 °C
    Mold Temperature 25-50 °C
    Drying Temperature 80 °C
    Drying Time 4 h
    Moisture Absorption 0.5%
    Biobased Content 80%
    Biodegradability Compostable
    Color Natural
    Form Pellets

    As an accredited FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid is packaged in 25 kg moisture-barrier foil bags on shrink-wrapped pallets.
    Container Loading (20′ FCL) 20′ FCL container fully loaded with palletized FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid, shrink-wrapped, secured for ocean shipment.
    Shipping FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid is shipped as non-hazardous solid resin pellets in sealed moisture-barrier bags, lined drums, or bulk containers. Not regulated for transport. Store and transport in a cool, dry area away from direct sunlight, heat, and moisture. Standard freight; no special ventilation required.
    Storage Store FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid in a cool, dry, well-ventilated area away from heat, sparks, open flames, and direct sunlight. Keep containers tightly sealed to prevent moisture uptake and contamination. Use original packaging with desiccant if required. Avoid dust generation and strong oxidizers. Maintain recommended temperature and humidity; rotate stock. Ground equipment to control static.
    Shelf Life Shelf life is typically 12 months when stored in original packaging, in a cool, dry place, away from moisture and heat.
    Application of FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid

    FC 10570 Microfiber Reinforced Injection Molding Polylactic Acid is supplied as a pre-compounded pellet with a melt-flow class suitable for medium-flow injection moulding. The pellet surface is moisture-sensitive; residual moisture above 250 ppm at the hopper is the primary cause of silver streaks, reduced molecular weight, and brittle weld lines. Drying is carried out in a desiccant-bed dryer at 80 °C for 4 h with a dew point below -40 °C. When ambient relative humidity exceeds 60 %, the drying time is extended to 6 h and the hopper is blanketed with dried air to prevent re-absorption. Melt temperature measured at the nozzle should remain between 190 °C and 220 °C. The grade is not autoclave-stable in component form above 121 °C and is not suitable for continuous hot-water service beyond 50 °C. The following application scenarios are separated by process risk, downstream compliance boundary, and the mechanical function of the microfibre network rather than by generic industry labels. Where a published data sheet for FC 10570 under a specific end-use configuration is absent, the numerical windows cited are drawn from publicly reported processing envelopes for microfiber-reinforced PLA injection moulding compounds with comparable fibre aspect ratio and melt-flow class.

    In automotive interior clip and bracket production, tooling transferred from mineral-filled PP cannot be accepted without re-calculating clamp force, gate land, and shrinkage compensation. The microfiber phase in FC 10570 produces anisotropic linear mould shrinkage. Parallel-to-flow shrinkage is typically 0.3–0.5 % and transverse shrinkage is typically 0.6–0.9 % at mould temperatures of 25–40 °C. This differential is larger than in 20 wt% talc-filled PP and causes clip retention towers to pull out of round if the core pin is cooled too aggressively. The processing window for the melt is 190–210 °C; the mould is maintained at 25–35 °C for fast cycling on 800–1,200 kN machines. Gate land length below 0.8 mm produces jetting and exposed fibre streaks on visible surfaces. Cold-runner sprue bush diameters below 3.0 mm elevate shear heating and can drive local melt temperature above 220 °C, triggering hydrolytic chain scission if residual moisture has not been held below 250 ppm. A dry-blend addition of 2–4 wt% colour masterbatch in a compatible PLA carrier is common. Impact modifiers are not added above 10 wt% because the elastomer phase suppresses the fibre network and lowers tensile modulus below 4.0 GPa when measured per ASTM D638-14. Compliance for interior parts is normally assessed for odour, fogging, and flammability. If the OEM specification requires burn rate below 100 mm/min under FMVSS 302, the part must be tested in final wall thickness; unfilled PLA would not meet the requirement without an FR package. Terminal parts include wiring-harness clips, trim retainers, speaker grille frames, and airbag badge carriers. The operational boundary is not thermal resistance but low-temperature impact: below -10 °C, clip retention tabs moulded at 25 °C mould temperature may crack during assembly. Raising the mould temperature to 60 °C increases crystallinity, reduces low-temperature impact further, and is not recommended for snap-fit features exposed to sub-zero deployment.

    Can a 0.8 mm Thin-Wall Electronics Housing Be Moulded Without Flash at the Parting Line?

    Flash elimination in thin-wall electronics housings depends on clamp force, melt viscosity, and venting rather than on mould temperature alone. For a single-cavity projected area of 150 cm² and wall thickness 0.8 mm, clamp force is set at 1,200–1,600 kN to hold the parting line closed against injection pressures of 120–160 MPa. FC 10570 in thin-wall flow lengths above 120 mm requires a hot runner with valve-gate control. Nozzle temperature is held at 200–220 °C, and the shear rate is kept below 30,000 s⁻¹ to prevent fibre breakage. Above that threshold, flexural modulus falls below 4,500 MPa when tested per ISO 178:2019 because the average fibre length drops below the critical load-transfer length. The material is run at 100 wt% FC 10570 for cosmetic non-flame-retardant covers. If a charger shell or router faceplate requires a UL 94 V-0 rating, a halogen-free phosphorous-based FR masterbatch is compounded at 10–15 wt%; this addition reduces tensile strength by approximately 5–10 % and requires re-calculation of gate freeze time. End products include e-mobility charging adapter shells, router body housings, and earbud case lids. RoHS compliance is verified by screening for lead, cadmium, mercury, and hexavalent chromium using IEC 62321-3-1:2013; REACH SVHC screening is applied to the compounded FR version. The key processing defect is not sink marks but parting line flash on inserted core pins. Vent depths above 0.02 mm at the parting line reduce flash but increase gas burn marks; therefore vacuum channels are installed at the end of fill.

    Processing window comparison for three downstream regimes
    ParameterAutomotive clip / bracketThin-wall electronics housingLaboratory consumable
    Melt temperature190–210 °C200–220 °C190–205 °C
    Mould temperature25–35 °C20–40 °C25–30 °C
    Residual moisture before moulding<250 ppm<250 ppm<200 ppm
    Clamp force for projected area 150 cm²800–1,200 kN1,200–1,600 kN600–1,000 kN
    Gate land / diameter0.8–1.2 mm0.6–1.0 mm1.0–1.5 mm

    In laboratory consumable production, the absence of mineral reinforcement matters as much as the presence of the microfibre phase. Mineral fillers can raise extractables and reduce surface purity, while the microfibre network in FC 10570 provides dimensional stability without introducing glass fibre fragments. The material is moulded at 190–205 °C with a mould temperature of 25–30 °C on 600–1,000 kN medical-grade machines. Residual moisture before moulding is held below 200 ppm, and closed-loop material handling is used to avoid ambient moisture pickup. A hot runner with polished stainless steel flow channels is used. Mould release agents are not used because they can interfere with cytotoxicity assays. The application ratio is 100 wt% FC 10570; any regrind is limited to 20 wt% and no more than three heat cycles for non-validated consumables. Terminal parts include pipette tip racks, test-tube storage boxes, analyzer front panels, and non-implant diagnostic device shells. The compliance boundary is based on the intended use: ISO 10993-5:2009 for cytotoxicity is required for diagnostic housings contacting skin. Autoclave sterilization is not recommended above 121 °C because heat deflection temperature under load is below the cycle peak. Ethylene oxide sterilization at 55 °C and 30–60 % RH is acceptable for components with wall thickness below 3 mm. Gamma irradiation above 25 kGy may cause chain scission and yellowing; published data for FC 10570 under this specific sterilization dose is limited, so dose mapping is required before release.

    When a Cosmetic Closure Requires Torque Retention After 100 Drop Cycles

    Torque retention failures in threaded closures are driven by thread flank creep, hoop stress relaxation, and impact cracking at the gate. FC 10570 is run at 100 wt% for closures that replace PC/ABS or acetal in decorative outer caps. The edge gate is positioned on the curb side, not the centre, to orient microfibres along the hoop direction. Hoop tensile strength has been reported in the range of 55–65 MPa when tested per ASTM D638-14; the same part centre-gated shows hoop strength below 45 MPa because fibre orientation is radial. Mould temperature is kept at 20–30 °C to reduce crystallinity and raise impact performance in drop tests of 100 cycles onto a steel plate from 1 m. For a knurled outer diameter of 15–25 mm, a gate diameter below 1.2 mm causes early freeze, sink marks, and thread flattening. Packing pressure is set at 80–100 MPa for 2–4 s; longer packing increases post-mould shrinkage and reduces thread concentricity. Terminal parts include serum pump collars, lipstick bases, and decorative jar closures. The compliance boundary is indirect: the cosmetic product is regulated under EU Regulation (EC) No 1223/2009, but the packaging component must be assessed for overall migration if it is intended for contact with food-like formulations under EU 10/2011. Pigment masterbatches used in the closure must not contain heavy metals exceeding 100 ppm lead, 100 ppm cadmium, 100 ppm mercury, and 100 ppm hexavalent chromium if RoHS screening is applied. The lower service temperature limit is -5 °C; below that, a snap-fit closure can fracture at the hinge point if the part has not been stress-relieved at 50 °C for 2 h.

    Continuous water contact above 40 °C is the limiting operational boundary for irrigation and outdoor connectors moulded from FC 10570. Hydrolysis of the PLA ester backbone follows a temperature-dependent mechanism; water absorption after 24 h at 23 °C is typically 0.7–1.5 % by mass when measured per ISO 62:2008. The fibre network slows crack propagation but does not stop hydrolytic chain scission. Drip emitter bodies, filter housings, and fertilizer pickup connectors are specified only for seasonal cold-water service below 35 °C. Continuous service at 50 °C in water is not recommended because tensile strength can fall below the design limit within 300–500 h, depending on wall thickness and water acidity. The injection process for thick-wall parts above 4 mm uses melt temperature 190–205 °C, mould temperature 20–30 °C, and packing pressure 60–80 MPa for 6–10 s. Hold time must not exceed gate freeze time; otherwise internal voids form in the thick bosses. A cold sprue puller with forced air cooling prevents stringing at the sprue. The formulation is run at 100 wt% FC 10570 for non-pressure-bearing parts; for pressure-bearing connectors, a glass-fibre hybrid or a hydrolysis-stabilized PLA grade is used. Heavy-metal pigments are excluded; RoHS screening follows IEC 62321. No food-contact claim is made for this segment. The terminal parts include drip emitter bodies with barbed outlets, in-line filter bowls, and quick-connect irrigation fittings.

    Compliance boundary matrix by downstream segment
    SegmentRelevant standard / regulationTest method / clauseBoundary condition
    Automotive interior clipFMVSS 302FlammabilityBurn rate below 100 mm/min if OEM requires
    Thin-wall electronicsIEC 62321-3-1:2013RoHS screeningPb, Cd, Hg, Cr(VI) below threshold
    Laboratory consumableISO 10993-5:2009CytotoxicityNon-cytotoxic extract
    Cosmetic closureEU 10/2011Overall migrationIf food-like contact claimed
    Irrigation connectorISO 62:2008Water absorption0.7–1.5 % at 24 h, 23 °C
    Furniture insertASTM D256-23Izod impactQuality-release impact value

    High-Stiffness Furniture Connector Inserts and Edge-Chipping Resistance

    Ready-to-assemble furniture hardware requires insert-moulded threads, cams, and dowel sleeves that resist hole elongation and edge chipping during demoulding. The microfibre network in FC 10570 raises surface brittle fracture risk at sharp corners. Ejection area is set at 8–10 % of projected area, and draft angles are kept above 1.5° on ribs and bosses. The formulation is run at 100 wt% FC 10570 for load-bearing inserts; glass-fibre hybrid use is outside the accepted specification for this grade. Mould temperature can be set at 60–80 °C for surface hardness and tighter bore tolerances, but the cycle time increases by 20–30 s compared with the 20–30 °C regime. Melt temperature is held at 195–215 °C. The process uses a cold runner with a full-round sprue and a gate land of 1.0–1.5 mm to reduce shear. Screw pull-out in M6 threaded inserts is improved by the fibre network; hole-loading capacity is affected by boss outer diameter, wall thickness, and insert type rather than by fibre content alone. Published data for FC 10570 in this specific insert configuration is limited; validation tests are required before production. Terminal parts include cam lock bodies, dowel sleeves, leveler feet, and hinge plates. The compliance boundary includes REACH SVHC screening and ASTM D256-23 Izod impact testing for quality release. Dark masterbatch loadings above 3 wt% can lower impact strength and increase edge chipping; this is a batch-dependent effect that must be monitored.

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    Certification & Compliance
    More Introduction

    FC 10570 is an injection-molding grade of polylactic acid whose model designation denotes a microfiber-reinforced formulation supplied as cylindrical granules. The reinforcing phase consists of discrete microfibers with average diameter below 10 µm and aspect ratio above 20:1 at loading levels typically between 5 wt% and 15 wt%. Published product-specific data for the proprietary FC 10570 designation is limited; the processing and property ranges in this text are therefore representative values drawn from publicly available studies of injection-molded microfiber-reinforced PLA composites and from general PLA processing practice. The supplier certificate of analysis and lot-specific melt flow data should govern machine settings.

    Before melt processing, the granulate is dried in a desiccant dryer at 80 °C for 4–6 h to a dew point of ≤ −40 °C. The target residual moisture before injection molding is 0.025 wt%; values above 0.05 wt% initiate hydrolytic chain scission at processing temperature. The resulting viscosity loss produces splay, silver streaking, and a measurable drop in notched Charpy impact strength when tested to ISO 179-1/1eA. At relative humidity above 60%, opened containers should be re-dried or fed directly from a closed hopper dryer; granulate moisture uptake can exceed the target within 30 min in an unprotected feed throat.

    Storage at 15–25 °C in sealed moisture-barrier bags preserves the drying state for 6–12 months from the date of certification. Once opened, partial bags should be resealed with desiccant sachets and used within 48 h in an environment at 23 °C and 50% relative humidity. Beyond that exposure, re-drying at 80 °C for 4 h is required even if the granulate appears dry, because PLA hydrolysis is not visually detectable before injection defects appear.

    Compounding of microfiber-reinforced PLA is preferably carried out on a co-rotating twin-screw extruder with L/D ratio 40:1 to 48:1. Microfibers are introduced by side feeding after the polymer melting zone, at barrel temperatures of 180–200 °C and screw speed 180–220 rpm. Direct dry blending and single-screw compounding tend to increase fiber attrition and melt temperature variation; the resulting pellets may show a bimodal fiber length distribution and lower tensile modulus consistency when tested across multiple lots according to ISO 527-2.

    How Does Microfiber Reinforcement Alter the Injection Molding Envelope of PLA?

    The addition of microfibers raises the low-shear melt viscosity and reduces melt mass-flow rate relative to unfilled PLA. Under ISO 1133-1:2022 conditions of 210 °C and 2.16 kg, representative MFR values for this class fall between 6 g/10 min and 10 g/10 min, compared with 10–14 g/10 min for unfilled PLA. The consequence is a narrower shot-to-shot processing window; the nozzle melt temperature should be maintained at 190–210 °C. A deviation of more than ±5 °C from the set point, particularly above 210 °C with residence time longer than 120 s, accelerates molecular weight loss. Below 190 °C, the viscosity rise leads to short shots, gate freeze-off, and microvoid formation near the gate. Exceeding 210 °C produces volatiles, brown streaks, and a reduction in tensile strength measured according to ISO 527-2.

    Thermal degradation follows a time-temperature dependence that is measurable by capillary rheometry before and after molding. At a melt temperature of 210 °C, melt pressure in a capillary die of 1 mm diameter and 20 mm length begins to decay after 10 min residence time; at 230 °C the same decay occurs within 2–3 min. These observations, combined with injection molding trials, define the upper processing boundary at 210 °C for cycle times longer than 20 s. Lot-to-lot variation in microfiber aspect ratio and surface treatment can shift the melt viscosity by 5–10% at a shear rate of 100 s⁻¹; therefore, first-lot qualification should include a short-shot study rather than relying solely on MFR data from ISO 1133-1.

    The crystallization half-time of PLA under quiescent conditions is long, but microfiber surfaces act as heterogeneous nucleation sites. Differential scanning calorimetry at a cooling rate of 10 K/min according to ISO 11357-1 typically shows a reduction in cold-crystallization onset temperature of 5–10 °C relative to unfilled PLA. This effect can be exploited by mold temperatures of 80–110 °C, but cycle time increases because the cooling time to reach demolding temperature extends to 30–45 s for wall thicknesses of 2 mm. A cold mold at 25–40 °C produces faster cycles at the expense of crystallinity; the resulting articles exhibit lower heat deflection and higher post-molding shrinkage.

    In the mold cavity, anisotropic fiber orientation generated by the frozen layer and fountain flow leads to direction-dependent mechanical performance. Tensile modulus parallel to flow is commonly 10–20% higher than in the transverse direction when tested according to ISO 527-2. Mold design should locate weld lines outside mechanically loaded regions; weld-line strength retention for this class is typically 35–50% of the unfilled matrix value when measured by a centrally gated disk and tested in accordance with ISO 527-2. The microfiber network also reduces mold shrinkage and linear thermal expansion, which improves fit and clearance stability in multi-component assemblies.

    Injection molding trials on conventional hydraulic machines with clamp force from 500 kN to 2,000 kN show that a general-purpose screw with compression ratio 2.5:1 to 3.0:1, L/D ratio 20:1 to 25:1, and no mixing pins reduces fiber attrition compared with high-shear barrier screws. Cylinder temperature profiles are typically set from 170 °C at the rear zone to 200 °C at the nozzle. Injection speeds of 20–100 mm/s and pack pressures of 40–80 MPa are representative for multi-cavity tooling; the packing phase must be terminated before gate freeze because microfiber-filled melts exhibit reduced compressibility and are prone to overpacking at thin ribs below 1.0 mm thickness. Edge gates should have a minimum cross-sectional dimension of 1.5 mm, and vent depth should not exceed 0.02 mm to avoid flash while allowing gas escape. Cold-runner systems with full-round or trapezoidal runners of minimum diameter 4 mm are preferred. Hot-runner valve-gate systems can be used only if the manifold is purged with a thermally stable carrier and residence time is kept below 3 min; otherwise, the gate region may develop carbonized specks and inconsistent filling.

    When FC 10570 Is Compared With Unfilled and Mineral-Filled PLA Grades

    Relative to unfilled PLA, the microfiber-reinforced grade increases tensile modulus and notched impact strength while reducing mold shrinkage and linear thermal expansion. The improvement in heat deflection temperature is significant: representative HDT-B under 0.45 MPa according to ISO 75-2 is 85–105 °C for the microfiber-reinforced class, compared with 50–60 °C for unfilled injection-molding PLA. The penalty is a lower melt flow and higher brittleness in thin sections below 1.0 mm; elongation at break under ISO 527-2 is typically 2–4%, compared with 3–6% for unfilled PLA.

    Against mineral-filled PLA grades, particularly talc-filled compounds, the microfiber network provides higher notched impact strength and better weld-line ductility while avoiding the surface roughness and density penalty associated with plate-like mineral fillers. Talc-filled PLA often displays higher flexural modulus, but the increased platelet orientation near the surface can produce warpage and a reduction in flow-direction toughness. Microfiber reinforcement produces lower abrasion on molds than glass-fiber-filled PLA and yields lower component mass because the density of the microfiber-reinforced class is approximately 1.26–1.29 g/cm³, whereas glass-fiber-filled PLA frequently exceeds 1.40 g/cm³. The grade is therefore positioned between unfilled PLA and glass-fiber-reinforced PLA for structural stiffness, with density and surface-quality advantages.

    Compared with glass microfiber-reinforced PLA, the organic or cellulosic microfiber network in FC 10570 class materials produces lower melt viscosity at high shear rates, which can improve filling of thin-wall sections below 1.0 mm. However, the flexural modulus is typically 10–20% lower than that of glass-fiber-reinforced PLA of equal fiber volume fraction. The lower density and reduced abrasive wear on mold steels are the main benefits. Mold wear tests on P20 steel have shown that glass fibers can increase gate wear rate by a factor of 2–4 compared with unfilled PLA, while organic microfibers produce wear rates closer to mineral-filled systems.

    Table 1 presents representative comparative ranges for injection-molded specimens prepared according to ISO 294-1 and dried to 0.025 wt% moisture before molding. The values are literature-derived and are not lot-specific FC 10570 specifications.

    Table 1. Representative injection-molded property ranges for microfiber-reinforced PLA, unfilled PLA, and talc-filled PLA
    PropertyTest methodMicrofiber-reinforced PLA classUnfilled PLATalc-filled PLA
    DensityISO 1183-11.26–1.29 g/cm³1.24–1.26 g/cm³1.29–1.32 g/cm³
    Tensile strengthISO 527-258–66 MPa55–62 MPa48–55 MPa
    Tensile modulusISO 527-23.8–4.6 GPa3.2–3.6 GPa4.2–5.2 GPa
    Flexural modulusISO 1784.5–5.4 GPa3.2–3.5 GPa4.8–5.8 GPa
    Notched Charpy impactISO 179-1/1eA5.5–7.5 kJ/m²2.5–3.5 kJ/m²3.5–5.0 kJ/m²
    Heat deflection temperature BISO 75-285–105 °C50–60 °C60–75 °C
    Melt mass-flow rate at 210 °C/2.16 kgISO 1133-16–10 g/10 min10–14 g/10 min9–12 g/10 min
    Mold shrinkage flow directionISO 294-40.2–0.4%0.4–0.6%0.3–0.5%

    For regulatory documentation, the grade should be accompanied by a supplier statement covering REACH Regulation EC 1907/2006 and RoHS Directive 2011/65/EU. Biobased carbon content can be determined by ASTM D6866-21; a typical value for PLA-based compounds exceeds 90% biobased carbon, but the exact value depends on the microfiber surface treatment and processing aids. Compostability claims require separate testing under EN 13432 or ASTM D6400-21; the presence of synthetic microfibers or certain coupling agents can slow disintegration below the pass threshold. For food-contact applications, migration testing under EU Regulation 10/2011 and applicable FDA 21 CFR sections must be completed on the final article, because microfiber surfaces and associated finishes can alter overall migration and specific migration limits. For medical device enclosures, biocompatibility evaluation according to ISO 10993-1 is the responsibility of the finished-device manufacturer.

    Typical usage fields for FC 10570 include semi-structural appliance housings, laboratory consumables, medical device enclosures, brackets, and packaging components requiring higher dimensional stability than unfilled PLA. The material is not suitable for continuous load-bearing use above 60 °C unless annealed, and it should not be processed on hot-runner systems with manifold residence times longer than 3 min. Avoid combining the compound with amine-based additives or strongly alkaline fillers; these accelerate ester hydrolysis and reduce molecular weight. Cleanout of polycarbonate or polyamide residues from the barrel is required before switching to FC 10570, because incompatible melt streams can generate delamination and contamination in the first molded parts. After molding, purge with a low-viscosity general-purpose PP or PE purge compound at 200–210 °C until the nozzle output is visually free of contamination.

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