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BigRep PRO HT BioPolymer Filament

    • Название продукта: BigRep PRO HT BioPolymer Filament
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
    • Запрос цены: admin@ascent-chem.com
    • Производитель: Ascent Petrochem Holdings Co., Limited
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    Спецификации
    Код ТН ВЭД 776067

    Как аккредитованный завод BigRep PRO HT BioPolymer Filament, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

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    Применение биополимерной нити BigRep PRO HT

    BigRep PRO HT BioPolymer Filament is a 2.85 mm diameter high-temperature bio-polyamide-type feedstock processed on large-format FFF systems with build envelopes up to 1005 mm per axis. Its recommended extrusion window is 250–270 °C, with a print bed setpoint of 100–120 °C and a heated chamber maintained at 40–80 °C. The datasheet positions the heat deflection temperature under ISO 75-2:2013 Method B at 0.45 MPa in the 112–118 °C region, which supports tool surfaces exposed intermittently below 100 °C but excludes continuous exposure to steam autoclave conditions above 110 °C. Pre-drying at 80 °C in a dry-air oven to a residual moisture content ≤0.1% by weight is required before large-format deposition; failure to dry produces gas blisters and interlayer tensile strength loss. REACH and RoHS Recast 2011/65/EU declarations are maintained by the manufacturer; the material is not a direct food-contact resin under FDA 21 CFR 177 or EU 10/2011 unless a separately validated barrier coating is applied. The following application scenarios document where the material is used in actual downstream manufacturing workflows, with compliance references, feedstock proportion, process parameters, and terminal article classes.

    Downstream scenarioPrimary compliance referenceTest method or process anchorDocumented boundary condition
    Thermoforming toolingISO 75-2:2013 Method B; ISO 527-2:20120.45 MPa HDT 112–118 °C; 45% gyroid infillTool bulk temperature held below 85 °C; barrier coating required for indirect food contact
    Composite layup toolingASTM D638-14; AS9100D first-article inspectionOut-of-autoclave cure below 95 °C; vacuum bag 0.8 barNot validated for autoclave cycles above 110 °C
    Robotic end-of-arm toolingISO 9409-1:2004; ISO 179-1:2010Charpy notched specimens conditioned at 23 °CAssembled gripper mass limited to 12 kg at 3 g robot acceleration
    Low-volume automotive interior trimFMVSS 302; ISO 105-B06Cabin soak profile 85 °C; horizontal burn rate target ≤100 mm/minExcluded from demist ducting with discharge air above 110 °C
    Food processing equipment change partsFDA 21 CFR 174.5; EN 1672-2:2020Washdown below 60 °C; cleaning solution pH 2–11Direct food contact requires validated barrier coating
    Medical device manufacturing fixturesISO 13485:2016; ISO 14937:2009Vaporized hydrogen peroxide at 50 °C; degassing at 100 °C for 2 hSteam autoclave at 121 °C is outside the documented material envelope

    Where Thermoforming Tools Are Printed Instead of Cast

    In packaging and automotive trim operations, the replacement of machined aluminium or cast polyurethane plug assists with printed PRO HT tools is constrained by surface porosity, vacuum manifold leakage, and the tool face temperature reached during sheet contact. The compliance anchor for this scenario is ISO 75-2:2013 Method B at 0.45 MPa, which places the printed material in the 112–118 °C window; however, the tool bulk is held below 85 °C by circulating water channels to avoid creep under clamping pressure. Indirect food-contact tooling for PP and PETG blister lines is not covered by EU 10/2011 unless a barrier coating compliant with FDA 21 CFR 175.300 is applied to the forming face. Material charge ratio is 100% virgin PRO HT by mass, with 6 perimeter walls and a 45% gyroid infill in the vacuum plenum; the working face is extruded as a solid 4 mm skin, and no regrind or carrier resin is introduced. Downstream production proceeds on a large-format FFF system with a 0.8 mm nozzle at 255–265 °C, build chamber at 55–65 °C, and layer height 0.25 mm; after printing, vacuum grooves are machined to 8 mm diameter and sealed with two-component epoxy. Terminal articles include PP clamshell packaging tools, PET blister tray plug assists, and trim-blank forming tools for automotive door panels. The process limitation is a tool face temperature above 100 °C during continuous cycle operation, which risks localized indentation under clamp load; published long-term creep data for this exact configuration is limited.

    Carbon-fiber wet layup cells impose a different combination of vacuum bagging pressure and exothermic cure, a condition where printed mandrel surfaces are less tolerant than steel or Invar but offer lead time and mass advantages. The material is validated through ASTM D638-14 tensile coupons printed in the Z-build orientation, with acceptance values drawn from the supplier data sheet; the manufacturing cell is controlled under AS9100D first-article inspection for tooling release. Feedstock proportion is 100% PRO HT shell, 8 perimeters thick at the tool face, with 40% cubic infill in the core and an aluminium backing frame mechanically fastened rather than co-molded. The downstream process uses a 1.0 mm nozzle at 250–260 °C, chamber at 70–80 °C, layer height 0.35 mm, followed by annealing at 100 °C for 2 h and vacuum groove machining. Tool faces are prepared with epoxy sealer and release agent; the mold is used only for out-of-autoclave cure cycles below 95 °C or wet layup with room-temperature epoxy systems. Terminal articles include out-of-autoclave carbon/epoxy rib tooling, drone airfoil layup mandrels, and carbon-fiber sports equipment templates. The operational boundary is explicit: autoclave cycles above 110 °C are not recommended because the heat deflection margin is insufficient; published data for PRO HT in 121 °C autoclave tooling is limited.

    Robotic cells attach printed vacuum gripper bodies to automatic tool changers, and the component must survive repeated cantilever loads, robot acceleration transients, and occasional impact from part ejection. The mounting interface is machined to ISO 9409-1:2004, while notch sensitivity and impact screening follow ISO 179-1:2010 Charpy specimens conditioned at 23 °C. Additive fraction for the body is 100% PRO HT; brass insert boss regions are printed at 85% infill density, and the remaining structure uses 35% triangular infill with 6 perimeter walls. The downstream process prints at 260–270 °C with a 0.6 mm nozzle and 0.20 mm layer height, after which threaded brass inserts are heat-staked at 220 °C into holes sized at 2.5 times the nominal screw diameter. Terminal products include suction gripper frames for injection-molded bumper fascias, robot end-of-arm bracket assemblies, and sensor mounting arms for assembly line pick-and-place operations. The pressure-sensitive vacuum plane must not exceed 12 kg total assembled mass at 3 g acceleration; direct exposure to methyl ethyl ketone-based cutting fluids is not permitted because surface stress cracking has been observed in production cells.

    When Low-Volume Interior Trim Replaces Injection Molded ABS

    Interior trim programs with volumes below 500 units per year provide a process window where printed PRO HT parts avoid injection tooling amortization, but the dimensional stability requirement is driven by cabin solar soak. The regulatory reference for flammability is FMVSS 302, with a customer-specific horizontal burn rate target of ≤100 mm/min; color and lightfastness after topcoat are screened under ISO 105-B06. Material usage ratio is 100% PRO HT, with 5 perimeter walls in clip retention zones and 45% triangular infill in the central volume; no talc-filled PP diluent or secondary polymer is added. Downstream production runs at 260 °C nozzle temperature, 60 °C chamber setpoint, and 0.25 mm layer height on a large-format printer, followed by light sanding, adhesion promoter, and a two-component polyurethane coating. The annealing step at 100 °C for 2 h introduces approximately 0.4% Z-axis shrinkage, which is compensated in the CAD model before clip-fit surfaces are machined. Terminal article classes include seat belt guide covers, HVAC duct outlet vanes, door panel switch bezels, and instrument cluster surrounds. The limitation is direct windshield demist ducting where discharge air can exceed 110 °C; such locations are excluded from the PRO HT material envelope because creep under clip preload becomes measurable above the HDT-B inflection.

    Washdown packaging lines sort and position primary containers through starwheel cams and timing screws that are regularly exposed to quaternary ammonium detergents, a chemical environment that rules out many unfilled PLA feedstocks but can be tolerated by PRO HT if cleaning temperature and pH are controlled. The compliance reference for repeated-use food equipment is FDA 21 CFR 174.5, with machine hygiene zoning controlled under EN 1672-2:2020; uncoated PRO HT is not a direct food-contact resin, so product-contact surfaces require a separately validated barrier coating. Charge proportion is 100% PRO HT, 50% rectilinear infill, and a solid 3 mm bearing surface depth at wear points. The downstream process uses 255 °C extrusion, 110 °C heated bed, 45 °C chamber, layer height 0.30 mm, and a post-print annealing step at 100 °C for 3 h to reduce internal stress; CAD compensation for 0.6% Z-axis shrinkage is applied before toolpath generation. Terminal articles include conveyor wear strips, starwheel cams, guide rails, and filler bowl timing screws. The operational window is restricted to cleaning solutions from pH 2–11 at temperatures below 60 °C; peracetic acid solutions above 0.5% concentration cause surface yellowing and should be avoided.

    Medical Device Fixture Sterilization Behavior Under Vaporized H2O2

    Medical device assembly fixtures made from PRO HT are qualified for vaporized hydrogen peroxide cycles, not for steam autoclave exposure, because the material’s heat deflection value at 0.45 MPa leaves insufficient margin at 121 °C. The governing quality system is ISO 13485:2016, with sterilant characterization aligned to ISO 14937:2009 and the VHP cycle operated at 50 °C. Feed composition is 100% PRO HT at 70% triangular infill, 8 perimeters, and a 0.6 mm nozzle with 0.15 mm layer height; after printing, a degassing step at 100 °C for 2 h reduces outgassing and stabilizes critical dimensions. Downstream production includes ultrasonic horn nests, tray dividers, and ESD-safe assembly sockets, with all part designs avoiding blind holes that would retain sterilant. Ethylene oxide cycles at 55 °C are acceptable if aeration time is extended by 30% relative to standard resins, but steam autoclave at 121 °C is outside the documented material envelope due to deflection and residual stress relaxation. The final terminal articles are Class II and Class III device manufacturing aids, not patient-contact implants; biocompatibility testing under ISO 10993 is the responsibility of the device manufacturer and is not claimed for the printed fixture resin itself.

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    Сертификация и соответствие требованиям
    Более подробное введение

    The BigRep PRO HT BioPolymer Filament is a 2.85 mm diameter, polylactic acid-based engineering compound supplied in 2.5 kg, 4.5 kg, and 8.0 kg spool formats for large-format fused filament fabrication. It is qualified on the BigRep PRO direct-drive platform with a nominal 1.0 m³ build volume and is compatible with open-material extrusion systems using 0.6 mm to 1.0 mm nozzles. The material is differentiated from standard BigRep PLA by a mineral nucleation package that raises the heat deflection temperature under 0.45 MPa load to approximately 100 °C when tested according to ISO 75-2:2013 method B. Manufacturer-published typical tensile strength is 39 MPa under ISO 527-2:2012 type 1A specimens. The compound is intended for large-format tools, fixtures, and short-run thermoforming aids where service temperatures exceed the practical limit of standard PLA but do not justify the drying and chamber demands of PA6/66. Because the feedstock is bio-sourced, the material is positioned for industrial settings that require lower warpage than unfilled ABS while maintaining compatibility with established PLA waste streams; published data for this specific recycling configuration is limited.

    What thermal and hygroscopic boundaries govern extrusion of this bio-based engineering filament?

    Extrusion of the PRO HT BioPolymer filament is bounded by a defined thermal window. Manufacturer-published processing data specify a nozzle set point between 190 °C and 230 °C and a heated bed temperature between 50 °C and 70 °C; the BigRep PRO enclosed chamber is typically held at 30 °C to 60 °C for parts exceeding 400 mm in the longest axis. At nozzle temperatures above 240 °C, the PLA-based matrix undergoes chain scission and viscosity reduction, producing stringing and over-adhesion during rapid travel moves. Below 185 °C, interlayer diffusion is insufficient, and large parts develop delamination at sharp geometric transitions. The mineral filler package increases thermal conductivity relative to unfilled PLA, which shortens the interlayer re-melt window and requires tighter toolpath cooling control. Layer heights from 0.15 mm to 0.30 mm with a 0.6 mm nozzle and up to 0.40 mm with a 1.0 mm nozzle fall within manufacturer operating limits. Moisture uptake is moderate but process-relevant; spools exposed to relative humidity above 60 % for more than 48 h should be dried in a forced-air dryer at 50 °C for 4 h to 6 h before extrusion. Failure to pre-dry can produce surface blistering on long tool paths because water vapor egress at the nozzle generates microvoids at the interlayer boundary. No amine-based compatibilizers or high-alkalinity cleaning agents should be used in post-process washing, as residual alkaline conditions accelerate hydrolysis of the PLA ester backbone at service temperatures above 60 °C.

    Standardized mechanical data and comparative portfolio position

    Typical properties from manufacturer technical data are summarized below. All mechanical values are conditioned at 23 °C and 50 % relative humidity according to ISO 291. These values are not design allowables; they represent single-point data for quality control and portfolio comparison.

    Property / ProcessBigRep PRO HT BioPolymerBigRep PLABigRep PETG
    Density, ISO 1183-1:20191.24 g/cm³1.24 g/cm³1.27 g/cm³
    Tensile strength, ISO 527-2:201239 MPa60 MPa47 MPa
    Flexural modulus, ISO 178:20192400 MPa3200 MPa1900 MPa
    Heat deflection temperature, HDT B, 0.45 MPa, ISO 75-2:2013100 °C55 °C70 °C
    Nozzle set point190–230 °C190–220 °C230–250 °C
    Heated bed set point50–70 °C45–60 °C60–80 °C

    The comparative data show a deliberate property trade-off. PRO HT BioPolymer is approximately 35 % lower in tensile strength than BigRep PLA but provides an 82 % higher HDT B. Flexural modulus is reduced by 25 % relative to PLA, which lowers fixture stiffness but improves corner-section compliance in large printed tools. Compared with BigRep PETG, the HDT B is higher by 30 °C, while flexural modulus is higher by approximately 26 %. This property combination positions the material for dimensionally stable tooling that must survive short thermal excursions without the moisture-handling burden of PA6/66. Applications requiring maximum tensile strength should remain with BigRep PLA. Applications requiring broader chemical resistance to oils and solvents should consider PA6/66 or PETG, because the PLA-based PRO HT BioPolymer is susceptible to ester hydrolysis under prolonged exposure to hot aqueous alkaline solutions.

    Thermoforming and vacuum-forming fixtures represent the primary processing advantage. In typical semi-crystalline sheet forming with polypropylene at sheet temperatures of 140 °C to 160 °C, a solid printed tool made from PRO HT BioPolymer should not be placed in continuous direct contact with the sheet without a thermal break; its 100 °C HDT B is below the sheet temperature, and sustained contact can produce surface creep. The material is better suited to thin amorphous sheet such as ABS or polystyrene at contact temperatures below 90 °C, or to fixture zones outside direct radiant heating. Spray-paint masking jigs, assembly nests, and end-of-arm tooling for low-cost collaborative robots are additional production-scale applications where the 100 °C HDT B permits short oven pre-heat exposure. On a BigRep PRO equipped with a 1.0 mm nozzle, a representative production profile uses a 0.30 mm layer height and 70 mm/s infill speed to balance interlayer adhesion with build time; published data for this specific configuration is limited to internal process-development reports. Corner lifting remains a failure mode when the bed temperature is below 50 °C and the part footprint exceeds 800 mm in both X and Y axes. A 10 mm brim with 0.1 mm z-offset reduces edge peel without post-machining.

    When build volumes approach 1.0 m³, which process parameters control warp and interlayer strength?

    On a BigRep PRO with a nominal 1000 mm × 1000 mm × 1000 mm build envelope, residual stress in PRO HT BioPolymer is managed by controlling the first-layer adhesion zone and the chamber cooling gradient. The heated bed is set to 60 °C for footprints above 500 mm × 500 mm; lower bed temperatures produce edge curl because the PLA-based matrix contracts during solidification while the filled compound exhibits linear solidification shrinkage in the range of 0.4 % to 0.6 %. The chamber is ramped from ambient to 35 °C during the first 5 layers and held for the remainder of the build; this reduces the gradient between the heated bed and the upper layers. Part cooling fans are disabled for the first 10 layers and limited to 30 % duty cycle thereafter to prevent rapid surface quenching. A sacrificial brim of 8 mm to 12 mm width is recommended on all corners with included angles below 45°. In long runs above 72 h, spool changes on the BigRep PRO automatic material bay should be staged before the filament reaches the encoder junction; a run-out pause mid-layer can produce a visible weld line because localized cooling at the pause point alters crystallization kinetics. No single interlayer tensile strength standard exists specifically for large-format fused filament, but transverse tensile tests adapted from ISO 527-2 are used to evaluate Z-axis strength; typical Z-axis strength for PLA-based engineering compounds falls between 60 % and 75 % of the XY tensile strength.

    Chemical resistance is limited by the PLA ester backbone. The filament is not suitable for continuous immersion in hot water above 60 °C, strong alkaline cleaning baths above pH 10, or aromatic and chlorinated solvents. Compatibility with mineral oil is moderate, but long-term dimensional stability under oil exposure has not been published for this formulation. For compliance-sensitive applications, the manufacturer supplies REACH and RoHS declarations; food-contact suitability is not claimed under EU 10/2011 or FDA 21 CFR absent a specific migration test. The material should be stored in sealed containers with desiccant when not in use, and spools left on the machine for more than 7 days in an uncontrolled environment should be re-dried before high-duty tooling prints. Printed parts can be machined with standard woodworking tools, but the mineral filler accelerates tool wear relative to unfilled PLA; carbide-tipped cutting tools are recommended for edge trimming operations above 500 mm/min linear feed.

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