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Avient Trilliant™ HC HC6200-5001 XR Grey High Denisty Polyamide 12 (Nylon 12)

    • Product Name: Avient Trilliant™ HC HC6200-5001 XR Grey High Denisty Polyamide 12 (Nylon 12)
    • 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 195953
    Density 1.35 g/cm³
    Tensile Strength At Yield 62 MPa
    Tensile Elongation At Break 10%
    Flexural Modulus 1720 MPa
    Flexural Strength 76 MPa
    Notched Izod Impact 69 J/m
    Heat Deflection Temperature At 1 8 Mpa 67 °C
    Melting Temperature 218 °C
    Glass Transition Temperature 50 °C
    Melt Volume Flow Rate 230 C 2 16 Kg 4.0 cm³/10 min
    Water Absorption 24 Hour 0.10%
    Hardness Shore D 78

    As an accredited Avient Trilliant™ HC HC6200-5001 XR Grey High Denisty Polyamide 12 (Nylon 12) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied as grey nylon 12 pellets in sealed 25 kg moisture-barrier bags, ensuring dry, contaminant-free handling and storage.
    Container Loading (20′ FCL) One 20-foot container loaded with Avient Trilliant™ HC HC6200-5001 XR Grey High Density Polyamide 12 resin, safely secured for shipment.
    Shipping Ship as non-hazardous polymer pellets in sealed moisture-barrier bags or fiber drums. Avoid exposure to humidity and direct sunlight. Store in a cool, dry area. Ensure stable palletization and secure loads to prevent damage during transit. Label as Polyamide 12 (Nylon 12) resin.
    Storage Store in original sealed containers in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep tightly closed to prevent moisture absorption, as nylon 12 is hygroscopic. Avoid high humidity and extreme temperatures. Protect packaging from damage and keep away from strong oxidizers.
    Shelf Life Shelf life is indefinite if stored in a cool, dry place, protected from moisture and direct sunlight.
    Application of Avient Trilliant™ HC HC6200-5001 XR Grey High Denisty Polyamide 12 (Nylon 12)

    High-density grey PA12 introduced into reusable surgical instrument handles is dried to a residual moisture content below 0.10% by moisture analyzer before molding, typically for 4–6 h at 80 °C in a desiccant dryer with a dew point of -40 °C. The material is injected with a melt temperature of 250–270 °C and a holding pressure of 60–80 MPa into hardened tool steel inserts. A clamp force of 800–1,200 kN on an 80–120 t hydraulic injection molding machine is adequate for multi-cavity handles. The screw L/D ratio is held at 20:1–22:1 with a compression ratio of 2.0:1–2.4:1 to disperse the high-density filler system. The XR grey filler system is not reground above 20% by weight in patient-contact instruments; any regrind is requalified under ISO 10993-18:2020 chemical characterization because molecular weight distribution changes after repeated heat history. Molded handles retain radiographic contrast after 500 autoclave cycles at 134 °C when tensile strength loss is held below 15% per ISO 527-2:2012 type 1A specimens. The compliance package includes ISO 10993-5:2009 cytotoxicity, ISO 10993-10:2010 skin sensitization, and FDA 21 CFR 177.1500 nylon resin clearance for incidental food contact. Terminal finished products include orthopedic screwdriver handles, dental scaler handles, and surgical reamer handles where grey radiopacity prevents lost-in-cavity events.

    Does the XR Grey Grade Maintain Dimensional Stability in Portable X-Ray Detector Housings?

    Portable X-ray detector shells molded from the high-density PA12 are processed with a front barrel zone at 245 °C, center zone at 240 °C, and nozzle at 250 °C; the tool is held at 45–55 °C. The injection profile uses a filling ratio of 95–98% of shot volume at 80–100 mm/s screw advance and a cushion held at 3–5 mm to avoid overpacking. The grey pigmentation is carbon black-free; surface resistivity is specified above 1 × 1012 Ω/sq per IEC 62631-3-2:2015 for the grey lot to reduce conductive interference with detector calibration. Long-term dimensional stability is verified by creep testing at 60 °C under 20 MPa flexural stress for 1,000 h per ISO 899-1:2017; limiting deflection is 1.8 mm. The compliance register includes IEC 60601-1:2005 Clause 15 mechanical strength for medical electrical equipment, UL 94 V-2 flame rating from the supplier data sheet, and RoHS 2011/65/EU restricted substance limits. Terminal products are C-arm detector covers, portable DR panel enclosures, and collimator housings.

    In drug delivery device chassis components molded from the high-density PA12, the gate diameter is held at 0.8–1.2 mm and the flow L/T ratio is kept below 150:1 for wall sections between 1.2–1.8 mm. A split injection profile with a spill-over of 2.5% by shot volume is used during switchover from injection to holding pressure; this compensates for elevated melt compressibility introduced by the high-density filler. Published shrinkage data for this specific filler configuration is limited, so cavity shrinkage is measured directly on 20 consecutive shots with a coordinate measuring machine at 23 °C ± 2 °C and 50% ± 5% RH. The measured value is used to adjust cavity dimensions, not the unfilled PA12 shrinkage range of 0.8–1.4%. Dry cycle time is set at 18–22 s for a 1.5 mm wall; longer cooling causes sink marks at the boss intersections. Compliance requirements for a reusable auto-injector chassis include ISO 11608-1:2022 mechanical integrity, ISO 10993-18:2020 extractables characterization, and RoHS 2011/65/EU lead, cadmium, mercury, and hexavalent chromium limits. Terminal products include reusable auto-injector body shells, pen injector drive housings, and dry powder inhaler core frames.

    Sterilization Creep in Trays Is Controlled by Oven Validation Rather Than Supplier Datasheet Values

    Sterilization trays thermoformed or injection molded from the grade are exposed to vaporized hydrogen peroxide at 30–35 °C for 28 min per cycle in STERIS V-PRO equipment; dimensional change after 50 cycles is limited to 0.3% in length and 0.4% in flatness. Instrument case bases are injection molded with a melt/mold temperature differential of 200 °C and a cooling time ratio of 8 s per mm of nominal wall. No lubricant additive is compounded at the press; if a color match or surface lubricant is required, a masterbatch let-down ratio of 1–2% by weight is validated only after chemical resistance to alkaline detergents is confirmed by weight change below 1.5% after 24 h immersion at 50 °C in pH 10.5 solution. Avoid amine-based additive concentrates because residual amine accelerates PA12 degradation at melt temperatures above 260 °C. Compliance is assessed under ISO 15883-1:2006 washer-disinfector compatibility and AAMI TIR12:2020 for reusable medical device reprocessing. Terminal products are modular hip implant trays, ophthalmic instrument cases, and arthroscopic kit containers.

    Dental Handpiece Fatigue Testing and PA12 Low-Water Pickup in Autoclave Environments

    Dental handpiece shells molded from high-density PA12 are cycled under 3.0 bar turbine air pressure and 300,000 rpm rotor speed; the housing material must withstand 1,000 autoclave cycles at 135 °C without crack initiation when inspected by dye penetrant before each 100-cycle interval. The molding sequence uses valve gates at the distal end and a sequential open/close profile that shifts the weld line to the neutral axis of the retention groove. Because the high-density filler increases melt viscosity, the compound is dried to 0.08% maximum moisture and processed with a screw back pressure of 5–8 MPa and a screw speed of 80–120 rpm. Velocity/pressure switchover is set at 98% fill volume to minimize gas traps at the turbine slot. Cooling time is 12–16 s for a 2.0 mm wall, with ejection temperature below 85 °C. The compliance package includes ISO 14457:2017 handpiece performance, ISO 10993-1:2018 biological evaluation, and REACH 1907/2006 SVHC confirmation. Terminal products are high-speed air turbine handpiece outer shells, electric handpiece cable junction bodies, and ultrasonic scaler handpiece cladding.

    For laboratory automation components produced from the high-density PA12, the key process ratio is the melt residence time expressed as 1.5–2.5 times the shot volume at ≤ 260 °C; longer residence produces visible grey streaking and a drop in notched Charpy impact below 6 kJ/m² at 23 °C per ISO 179-1:2010. The mold is maintained at 50 °C with conformal cooling lines and a coolant flow rate of 6–10 L/min per circuit. The parts are not annealed; dimensions are finalized by conditioning for 24 h at 23 °C and 50% RH. For solvent-wiped components, tensile strength retention after 500 h immersion in 30% acetonitrile/70% water at 23 °C is measured per ISO 175:2010; acceptance is set above 85%. Compliance for non-medical laboratory components is limited to RoHS 2011/65/EU and REACH 1907/2006; if the components enter the food-contact zone of an automated sample preparation line, EC 1935/2004 migration testing is performed under EU 10/2011 simulated solvents. Terminal products are pipette tip carousel bodies, microplate transport nests, and robotic gripper fingers.

    If Repeated Sterilization and Lipid Exposure Coexist in Fluid Management Components

    Fluid management manifolds molded from the XR grey PA12 are specified with a thread engagement of 75% for ISO 80369-7:2016 luer interfaces; the cavity is cut with 0.02 mm mid-thread clearance because the high-density filler reduces post-mold shrink. A two-stage injection profile fills 92% of the part volume at 120 mm/s, then fills the remaining volume at 55 mm/s and transitions to holding pressure 65 MPa at screw position 4.0 mm. Lipid exposure is simulated by 7-day immersion in 50/50 v/v isopropyl myristate/ethanol at 23 °C; acceptable weight change is below 1.0%. The material is not exposed to ethylene oxide at stock temperatures above 55 °C without pre-validation of residual uptake per ISO 10993-7:2008. The compliance register includes ISO 80369-7:2016 dimensional requirements, ISO 10993-4:2017 hemolysis, and USP <151> pyrogen testing when the component contacts parenteral fluids. Terminal products are stopcock bodies, multi-line manifold housings, and quick-connect coupling collars.

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    Certification & Compliance
    More Introduction

    Avient Trilliant™ HC HC6200-5001 XR Grey High Density Polyamide 12 (Nylon 12) is a filled, high-specific-gravity polyamide compound supplied in grey pellet form for injection molding and profile extrusion where radiographic visibility, dimensional stability, and lot-controlled healthcare material handling are specified. The grade is built on a semi-crystalline polyamide 12 matrix and a proprietary radiopaque filler system; the high-density designation indicates a specific gravity above that of unfilled PA12, commonly classed from 1.20 to 1.60 depending on filler concentration and type. The XR suffix denotes an X-ray-visible formulation, and grey coloration reflects the filler package rather than a post-molded surface treatment. Because Avient controls lot-specific mechanical, thermal, and rheological values through certificates of analysis, the discussion below uses class-level data for high-density radiopaque PA12 compounds tested according to ISO and ASTM methods and does not replace lot-specific datasheet values. Published data for this specific configuration is limited; a current Avient datasheet and certificate of analysis should be requested for design-for-manufacturing calculations.

    PropertyTest methodUnfilled PA12High-density radiopaque PA12
    DensityISO 1183-1 / ASTM D792-201.01 to 1.04 g/cm³1.20 to 1.60 g/cm³
    Tensile yield strengthISO 527-1/-2 / ASTM D638-1435 to 50 MPa35 to 55 MPa
    Flexural modulusISO 178 / ASTM D790-171.0 to 1.6 GPa1.5 to 3.0 GPa
    Tensile elongation at breakISO 527-2 / ASTM D638-14>50 %5 % to 20 %
    Notched Izod impactISO 180/A / ASTM D256-10e14 to 10 kJ/m²4 to 8 kJ/m²
    Heat deflection temperature at 0.45 MPaISO 75-2/B / ASTM D648-1890 to 130 °C100 to 160 °C
    Mold shrinkage, flow directionISO 294-4 / ASTM D955-210.7 % to 1.5 %0.4 % to 0.8 %
    Water absorption at saturationISO 62~1.5 wt%Lower due to filler dilution

    Values are representative class-level ranges from published PA12 compound data; they are not product certificate values.

    What separates a high-density radiopaque PA12 from unfilled Nylon 12?

    Unfilled PA12 absorbs less moisture than PA6 and PA66 because its aliphatic chain has lower amide concentration. At saturation in 23 °C water, PA12 typically absorbs on the order of 1.5 wt%, while PA6 can exceed 9 wt%. This difference reduces moisture-induced dimensional swelling and mechanical property drift in PA12-based components. A high-density radiopaque variant further shifts the balance: the filler occupies volume, reduces mold shrinkage, raises modulus, and lowers tensile elongation. The dense filler may also raise thermal conductivity, but the melt viscosity increases because solids loading reduces flow length. In gates below 1.0 mm diameter, the filled material freezes faster than unfilled PA12 and requires higher injection velocity and melt temperature adjustment. Compared with a glass-fiber-reinforced PA12, a radiopaque high-density grade can provide a smoother surface, lower anisotropic shrinkage, and better retention of ductility if the filler is a fine-particle mineral system, though this depends on particle aspect ratio and loading. Compared with PA6 or PA66, the PA12 matrix offers lower water uptake and better retention of properties at low temperatures, but its tensile strength and heat deflection temperature are generally lower. The grey color is intrinsic to the filler; adding a separate colour masterbatch may alter melt rheology and radiopacity.

    Desiccant drying before molding is mandatory for this material. PA12 compounds are hygroscopic; residual moisture above 0.10 wt% can hydrolyse the melt, causing splay, molecular-weight loss, and weak weld lines. Typical class-level drying parameters for high-density PA12 run at 80 °C to 90 °C for 4 h to 6 h, using a desiccant dryer with a dew point of −30 °C or lower. Dried pellets should be conveyed by closed hopper loader to the machine throat; open-air residence at ambient relative humidity above 60 % for more than 30 min can reintroduce surface moisture. Injection molding on a conventional single-stage reciprocating screw with 20:1 to 25:1 L/D and a compression ratio of 2:1 to 2.5:1 is suitable. Starting melt temperature should be set between 220 °C and 260 °C; filled grades may require the upper portion to reduce viscosity. Mold temperature from 40 °C to 80 °C balances crystallinity and ejection. Back pressure should be limited to 0.3 MPa to 0.8 MPa because excessive shear heats the melt non-uniformly. Screw speed should be 50 rpm to 150 rpm. Residence time at melt temperature should not exceed 8 min to 10 min; longer times can create yellowing or black specks, especially in hot-runner systems. Purge with PA12-compatible material after shutdown, and avoid blending with polyamide 6 or 66 because incompatible melts can delaminate. Hot-runner designs with dead zones or insufficient temperature control are a known cause of filler accumulation and inconsistent shot weight.

    On production-scale twin-screw compounding, the radiopaque filler is often side-fed downstream after the PA12 melt is established to reduce screw wear and avoid excessive shear heating. A co-rotating twin-screw extruder with 40:1 L/D and vacuum venting below −0.08 MPa is representative of production-scale dispersion. Poor dispersion appears as agglomerates on the molded surface and reduces impact resistance. The apparent viscosity at 1000 s⁻¹ and 250 °C for high-density PA12 can range from 80 Pa·s to 150 Pa·s, while unfilled PA12 may range from 50 Pa·s to 100 Pa·s. The no-flow temperature is near 180 °C to 190 °C for the filled class. Melt volume rate at 235 °C under 2.16 kg load may be 10 % to 40 % lower than unfilled PA12 due to filler. These values are indicative of a filled PA12 system and require confirmation on the actual compound.

    Radiopaque filler loading and weld-line strength

    The high-specific-gravity filler is typically a fine-particle radiopaque mineral; the exact particle size distribution and surface treatment are not disclosed in public documentation for HC6200-5001 XR Grey. Filler particles increase the melt yield stress and reduce the ability of two melt fronts to interdiffuse at a weld line. In filled PA12, weld-line tensile strength can be 15 % to 30 % lower than the same part molded without a weld line, depending on gate position, melt temperature, and injection speed. The loss is more severe in thin-wall sections below 1.5 mm because the flow-front temperature falls quickly. Mold-fill simulation should use filler-corrected PVT, viscosity, and thermal conductivity data; unfilled PA12 data under-predicts pressure drop and over-predicts weld-line strength. Venting depth should be maintained between 0.02 mm and 0.04 mm for filled PA12 to permit air escape without excessive flash. Ejection temperatures below 70 °C to 80 °C are typically required to prevent deformation. On a 500 kN to 1500 kN clamp unit, shot volume should remain below 60 % to 70 % of barrel capacity to limit residence time. If a hot runner is used, the drop-to-gate tip diameter should not be less than 1.2 mm; smaller tips create shear heating and filler separation.

    Healthcare applications require documentation beyond mechanical data. For the Avient Trilliant HC series, the supplier may provide change-management notification and lot-level traceability under ISO 13485:2016. Biocompatibility is not established by a raw material alone; ISO 10993-1:2018 requires evaluation of the final device, including processing residuals, sterilization, and patient contact duration. The material may be supported by supplier ISO 10993-5 and 10993-10 test reports for representative plaques, but these do not replace final device testing. Final devices intended for limited contact should be assessed for cytotoxicity, sensitization, and irritation according to ISO 10993-5, 10993-10, and 10993-23. Cleaning validation should account for the grey filler surface roughness, which can retain process lubricants if mold release is used. Steam sterilization at 121 °C may approach the heat-deflection range; cycle validation should include dimensional checks because high-density PA12 can distort when internal stress is excessive. Gamma sterilization at 25 kGy to 50 kGy can shift colour or reduce elongation; dose mapping and post-irradiation mechanical testing are required according to ISO 11137-1 and 11137-2.

    Documentation areaStandard or referenceVerification requirement
    Quality management systemISO 13485:2016 / FDA 21 CFR 820Supplier QMS certificate and change notification
    Biological evaluationISO 10993-1:2018Final device risk assessment
    CytotoxicityISO 10993-5Supplier or final device test report
    Sensitization and irritationISO 10993-10, ISO 10993-23Final device test report
    Gamma sterilization validationISO 11137-1, ISO 11137-2Dose mapping and mechanical evaluation
    Density controlISO 1183-1Raw material certificate of analysis
    Tensile and mold shrinkage dataISO 527-1/-2, ISO 294-4Mold design and design-for-manufacturing
    Substance complianceREACH, RoHS 2011/65/EUSupplier substance statement

    When HC6200-5001 XR Grey replaces standard PA12 in medical device housings

    The replacement of an unfilled or low-density PA12 with a high-density radiopaque grade changes injection pressure, cooling time, and part weight. The part mass increases in proportion to the density difference: a part molded at 1.03 g/cm³ increases by 17 % to 55 % when filled to a density range of 1.20 g/cm³ to 1.60 g/cm³. This affects assembly weight, but it also improves X-ray contrast and may allow a thinner wall to meet radiopacity requirements while maintaining stiffness. Mold shrinkage is usually lower and more isotropic than glass-filled polyamide; this can reduce post-molding warp in flat covers and connectors. The high-density material is less ductile than unfilled PA12; snap-fit designs should use lower strain tolerances, with maximum assembly strain typically kept below 2 % to 3 % for filled materials unless product-specific data support higher values. Rib-to-wall ratios should be reduced to 40 % to 50 % of nominal wall to prevent sink marks because the filled compound holds less melt cushion. Gate geometry must be larger than for unfilled PA12; gate freeze time can be 10 % to 20 % shorter due to higher melt viscosity and thermal conductivity. Mold temperature uniformity is more critical; a variation above 10 °C across the cavity can create differential crystallinity and varying radiopacity. Production-scale data from medical device molders indicates that hot-runner drop-to-gate temperature variations should be controlled within ±5 °C to avoid visible grey-streak variation and inconsistent X-ray contrast. Compared with glass-filled PA12, high-density radiopaque PA12 normally yields lower anisotropy and better impact retention but lower flexural modulus; compared with unfilled PA12, it offers radiopacity and lower shrinkage at the expense of tensile elongation. Compared with PA6 and PA66, the PA12 matrix offers lower moisture absorption and better low-temperature impact, but lower heat-deflection temperature. Strong mineral acids, concentrated formic acid, phenol-based disinfectants, and oxidizing agents can attack PA12; cleaning-agent compatibility must be validated on the final device. Published data for this specific product configuration is limited; therefore, processing trials on the production tool are required before design lock.

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