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BigRep HI-TEMP Biodegradable Polymer Filament

    • Название продукта: BigRep HI-TEMP Biodegradable Polymer Filament
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
    • Запрос цены: admin@ascent-chem.com
    • Производитель: Ascent Petrochem Holdings Co., Limited
    • Свяжитесь сейчас
    Спецификации
    Код ТН ВЭД 748501

    Как аккредитованный завод BigRep HI-TEMP Biodegradable Polymer Filament, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

    Упаковка и хранение
    Упаковка BigRep HI-TEMP Biodegradable Polymer Filament, 1 kg spool, vacuum-sealed in moisture-barrier bag with desiccant, inside recyclable branded cardboard box.
    Погрузка контейнера (20-футовый контейнер) 20′ FCL: Palletized BigRep HI-TEMP biodegradable polymer filament spools loaded into dry container, secured, climate-protected, maximizing payload for export.
    Доставка BigRep HI-TEMP Biodegradable Polymer Filament ships on a spool in a sealed moisture-barrier bag with desiccant, packed in a rigid cardboard box. It is non-hazardous, requires no special transport controls, and should be kept dry, away from heat, moisture, and direct sunlight.
    Хранение Store BigRep HI-TEMP Biodegradable Polymer Filament in its original sealed packaging with fresh desiccant, in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Maintain ambient conditions around 15–25 °C and low humidity. Keep away from strong oxidizers, acids, and bases. For opened spools, use an airtight dry box or vacuum bag to prevent hydrolysis and print-quality degradation.
    Срок годности Shelf life: 12 months unopened, stored sealed in a cool, dry place, away from moisture, heat, and UV light.
    Применение биоразлагаемой полимерной нити BigRep HI-TEMP

    In thin-gauge vacuum forming of food-adjacent packaging prototypes, the high-temperature biodegradable polymer compound is processed as a dense tool shell rather than as a printed prototype part. The spool is dried at 40 °C for 8 h when ambient exposure has exceeded 60 % relative humidity; extrusion is held at 215 ± 5 °C, the build plate at 60 ± 5 °C, and the enclosed chamber at 35–40 °C. A 0.3 mm layer height with 0.4 mm extrusion width, 4 perimeters, 6 top and bottom skins, and 45 % triangular infill produces a shell that withstands vacuum pressure of −0.85 bar without visible creep at sheet-contact temperatures up to 85 °C. Shell wall thickness below 8 mm at the vacuum box flange cracks during toggle clamping; minimum flange thickness is set to 10 mm and the flange zone is printed with 8 perimeters. Vacuum slots are post-machined at 0.8–1.2 mm diameter and 45° orientation to the forming surface to prevent visible marking on 0.35–0.50 mm PET sheet. The tool is annealed at 80 °C for 2 h in a forced-air oven before use; after annealing, HDT-B under ISO 75-2:2013 method B is reported by the material supplier as >85 °C, and Vicat A50 under ISO 306:2022 reaches 115 °C. Terminal parts are PET and HIPS trays and blisters formed in pilot runs of 150–400 units for packaging line trials. The tool is limited to short-run simulation: continuous surface exposure above 90 °C at vacuum slots causes localised softening and slot collapse. Food-contact compliance is indirect; the printed tool is not itself a food-contact article, but formed packaging intended for food use must meet overall migration limits under EU 10/2011. Release agents are selected to avoid silicone transfer onto PET surfaces: a dry-film, silicone-free release is used because silicone migration can interfere with subsequent heat-seal adhesion. Printed tensile verification is performed under ISO 527-2:2012 using specimens printed in the same build orientation as the tool surface.

    Wax Injection Dies in Low-Pressure Investment Casting

    Low-pressure wax injection for investment casting relies on aluminium or steel dies in production; the high-temperature biodegradable filament functions as a short-run die set for pattern trials when cavity temperatures remain below 70 °C. The die body is printed with 80 % gyroid infill, 6 perimeters, and 0.2 mm layer height to reduce stair-stepping on contoured core surfaces. After printing, the cavity is sealed with a filled two-component epoxy coating applied at 150–250 µm dry film thickness and hand-polished to Ra 1.6 µm; the barrier prevents paraffin wax penetration into layer lines. Injection is run at 0.4–0.6 MPa and wax temperature 65–68 °C. Draft angles of 1.5–3° are added to vertical walls because the printed polymer has lower notched impact strength than tool steel. Ejector pins are replaced by compressed air poppets operating at 0.3 MPa to avoid point loading on thin die walls. Terminal outputs are unfilled paraffin and water-soluble wax patterns for small impeller, valve-body, and orthopaedic preform shells. Notched Izod values for this material class under ASTM D256-10 are below unmodified ABS; therefore cavity corners are radiused to a minimum of 4 mm. Dimensional verification of the die cavity is completed on a coordinate measuring machine under ISO 10360-2:2009 with a target tolerance of ±0.1 % of nominal cavity size. The die has two operational boundaries. It is not suitable for flash-dewax autoclaves above 100 °C or for solvent-borne wax removal at elevated temperature; pattern removal is limited to cold chlorinated solvent immersion or warm water for water-soluble wax. The epoxy sealer is checked with an ultrasonic thickness gauge at five points; any reading outside 150–250 µm requires local rework before the next injection cycle to avoid wax penetration and die-face delamination.

    On body-in-white assembly lines, checking fixtures and weld-cell gauges produced from high-temperature biodegradable print stock reduce lead time relative to cast aluminium while remaining dimensionally stable at ambient production temperatures up to 70 °C. The print recipe uses a 1.0 mm nozzle, 0.55 mm layer height, 70 % rectilinear infill, 5 perimeters, and 6 top and bottom skins. The build plate is set to 65 °C and the chamber to 35 °C; spools are dried at 40 °C for 12 h before printing to limit moisture-induced microvoiding near the locating pin seats. Heat-set brass threaded inserts of size M8 are installed at 180 °C into reamed pilot holes of 7.0 mm; insertion speed is kept below 5 mm/s to prevent local melting of the surrounding polymer matrix. Terminal parts include a left-hand door inner panel checking fixture with locating pins, clamp pads, and CMM reference spheres; the fixture is used for 80–120 inspection cycles per shift over an eight-week pilot window. Fixture repeatability is evaluated under AIAG MSA 4th edition with a gauge R&R result below 10 %; CMM verification follows ISO 10360-2:2009. The coefficient of linear thermal expansion for this compound is higher than aluminium by a factor of 3–4, so dimensional checks are initiated only after the fixture and part have soaked in the measurement room at 20 ± 2 °C for 4 h. Direct MIG weld spatter contact is prohibited; guard plates or ceramic cloth shielding are required within 300 mm of the weld point. Continuous surface temperature above 80 °C or localised clamp force above 250 N per point causes indentation creep and loss of datum repeatability.

    Can a Biodegradable Core Support Vacuum-Bagged Prepreg at 80 °C?

    Low-temperature carbon-fibre/epoxy prepreg systems cure between 70 °C and 85 °C; a mineral-modified PLA-based core survives these cycles if the bag-side skin does not exceed 85 °C for more than 6 h. The core is printed at 35 % gyroid infill, 4 perimeters, 5 top and bottom skins, and 15 mm nominal wall thickness to resist vacuum consolidation under −0.80 bar. The mandrel is extracted after cure through the open end of the composite runner, so no soluble tooling is required. Release compatibility is critical. Use a solvent-free PVA film and an epoxy-compatible semi-permanent release agent; avoid amine-containing tool sealers because they inhibit prepreg cure at the tool interface. Vacuum bag leak rate is held below 0.05 bar over 10 min; a breached bag allows local exothermic excursion above 95 °C and initiates core softening. Terminal components are hollow carbon-fibre/epoxy intake runners and duct sections for motorsport or UAV development. The mandrel surface is sealed to Ra 3.2 µm before release film layup; surface roughness above Ra 6.3 µm causes resin bleed into layer lines and increases extraction force after cure. Dimensional verification of printed core sections is performed under ISO 527-2:2012 tensile testing of specimens printed in the same build orientation; published data for this specific configuration is limited, so process qualification on a representative 1:1 core coupon is required before production. Continuous cure above 90 °C or autoclave pressure above 1.5 bar exceeds the operational boundary of the polymer. REACH conformity for the printed resin is supplied at batch level under EC 1907/2006; the composite processor must assess the full mandrel-release-resin system for workplace exposure under EC 1907/2006 Annex XVII.

    When Tooling Must Be Sealed Before Addition-Cure Silicone Work

    Addition-cure platinum silicone RTV-2 reproduction on printed tooling is limited by two factors: catalyst inhibition and demoulding stress. The high-temperature biodegradable filament is used for prototype moulds only when the printed surface is sealed with an amine-free aliphatic epoxy or acrylic lacquer of 150–250 µm dry film thickness. The sealer blocks unpolymerised ester residues and mineral filler from contaminating the platinum catalyst. Mould geometry is printed at 0.25 mm layer height, 45 % gyroid infill, and 3 perimeters; wall thickness is kept below 10 mm to reduce thermal mass during silicone exothermic cure. Silicone is degassed at −0.9 bar for 5 min, poured, and cured at 25 °C for 24 h followed by post-cure at 60 °C for 4 h. Terminal components are polymer cushions, short-run vibration dampers, and prototype seals for medical or industrial equipment. Demoulding is performed only after cooling to 30 °C; forcing ejection at higher temperature tears the silicone because the printed mould has lower tear strength retention at the mould-silicone interface. Continuous mould surface temperature must not exceed 80 °C during post-cure; ovens with hot spots above 90 °C cause warpage in the mould base. The filament’s biodegradation potential under DIN EN 13432 does not transfer to the cured silicone part and does not replace medical-grade validation; for skin-contact prototypes, the silicone elastomer is assessed under ISO 10993-5 and ISO 10993-10. The printed tool itself is not autoclaved, not washed with ethanol above 40 °C, and not combined with tin-cure silicone systems because acetic acid release attacks the epoxy sealer. Re-sealing is required when coating thickness falls below 150 µm anywhere on the cavity.

    Sealing Wet Concrete Formwork Without Solvent-Borne Release Agents

    GFRC and architectural precast panels cast against large-format printed formwork expose the polymer to wet alkaline concrete, formwork pressure, and cyclic demoulding. The formwork is printed at 35 % triangular infill, 6 top and bottom skins, and 4 perimeters; vertical walls are drafted at 3–5°. The surface is sealed with a two-component polyurethane clear coat applied at 200–300 µm dry film thickness to achieve Ra 3.2 µm and prevent water absorption into layer lines. After coating, the surfaces are block-sanded with 400-grit abrasive and re-checked for roughness. Concrete is a glass-fibre reinforced mixture with 3 % by weight alkali-resistant glass fibres, water-cement ratio 0.35, and superplasticiser dosage 0.8 % by cement weight. Pour height is limited to 500 mm to keep hydrostatic pressure below 12 kPa; higher heads require external steel stiffening. Curing proceeds at 20 °C and >90 % RH for 24 h before demoulding. Terminal outputs are 1.2 m × 0.6 m architectural cladding panels and mock-up formliners in runs of 5–20 casts. Release is based on water-emulsified vegetable-oil agents; solvent-based mineral-oil release agents are not used because they soften the polyurethane sealer and the printed outer layers. Formwork pressure calculation follows DIN 18218; cast panel flatness is verified with a 600 mm straightedge under EN 12390-1. The main failure mode is alkaline surface attack when the polyurethane barrier is scratched or worn below 150 µm; coating thickness is inspected after each cast with a wet-film gauge and any spot below the threshold is recoated before the next pour. The polymer formwork is not rated for steam curing above 60 °C, nor for repeated exposure to pH above 11 without the intact barrier.

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    Более подробное введение

    BigRep HI-TEMP Biodegradable Polymer Filament

    BigRep HI-TEMP Biodegradable Polymer Filament is supplied as a large-format fused filament fabrication feedstock with a nominal diameter of 2.85 mm and a roundness tolerance of ±0.05 mm. The formulation belongs to the biodegradable polyester class, but the designation HI-TEMP indicates a nucleated or modified structure that shifts the thermal deformation envelope beyond that of amorphous PLA. The material is not a general-purpose PLA; it is intended for applications in which a part must hold shape under moderate thermal load during tooling use, downstream processing, or short-term service, while still meeting industrial compostability criteria under EN 13432 or ASTM D6400-23. The exact transition temperatures, melt flow index, and mechanical values are batch dependent and must be read from the current certificate of analysis. Large-format extrusion platforms with build dimensions above 500 mm × 500 mm impose greater thermal gradients than desktop systems, and the material’s practical performance is therefore influenced by chamber temperature, part geometry, and annealing history.

    How does the thermal response differ from conventional biodegradable polyesters?

    The primary thermal distinction is measured under ISO 75-2:2013 method B and ISO 306:2022 method B50. Amorphous PLA filaments typically exhibit heat deflection temperature values in the 50–60 °C range at 0.45 MPa. High-temperature biodegradable polyester grades that rely on nucleating agents and controlled crystallization can shift the HDT B value into the 80–110 °C range after annealing at 80–100 °C for 30–120 min in a dimensionally stable fixture. The annealed condition is critical: as-printed parts may not exhibit the full heat resistance because extrusion cooling suppresses crystallinity. Differential scanning calorimetry under ISO 11357-3 should be used to verify the cold-crystallization peak and to establish an annealing setpoint without inducing excessive shrinkage. Vicat softening temperature under ISO 306 method B50 is commonly reported for the annealed grade; published data for this specific configuration is limited, and a batch-specific datasheet should be requested.

    Mechanical values must be evaluated with respect to print orientation. Fused filament fabrication produces anisotropic properties; Z-axis tensile strength is commonly 30–60 % lower than XY tensile strength depending on interlayer fusion. Tensile test results under ISO 527-2:2012 type 1A and flexural modulus under ISO 178:2019 should be reported together with print orientation. Large-format parts with 0.4 mm layer height and 1.0 mm nozzle diameter can show local porosity at sharp direction changes, which reduces Z-strength. Users should not transfer desktop-grade mechanical values to large-format builds without verifying interlayer weld strength on the actual machine.

    Dimensional change during annealing is a critical constraint. A flat plate annealed at 100 °C can shrink by 0.2–0.8 % along the print direction and by 0.1–0.4 % across the raster direction, depending on infill density and extrusion temperature. Tooling features with tolerances tighter than ISO 286-1 IT12 should be printed oversize and post-annealed in a fixture that restricts warpage. Published data for this specific configuration is limited; the dimensional change rate must be characterized on the production machine before committing to precision tooling.

    When drying and melt residence time are not controlled

    The most frequent production failure with biodegradable polyester filaments is hydrolytic degradation during extrusion. Polyester feedstock absorbs moisture from ambient air; at relative humidity above 60 %, surface moisture can reach levels sufficient to generate steam and chain scission in the melt. The filament should be dried in a desiccant dryer at 55–70 °C for 4–8 h to a dew point below -40 °C. A moisture content below 0.025 % is a conservative control limit. On production lines, moisture-related degradation appears as a rising melt flow index under ISO 1133-1:2022, excessive nozzle oozing, surface roughness, or loss of interlayer adhesion. Melt pressure in the hot end should be monitored; fluctuations above 0.5 MPa at constant speed often indicate feed inconsistency, partially degraded resin, or spool tangling.

    The melt processing window is bounded at the lower end by insufficient fusion and at the upper end by chain scission. Large-format hot ends with 0.8–1.2 mm nozzles may require a setpoint offset of 5–10 °C above the datasheet mid-range when hardened steel nozzles are used, because thermal conductivity differs from brass. Nozzle temperatures above the supplier’s upper limit should be avoided; residence times longer than 15 min at maximum barrel temperature can shift the molecular weight distribution. Production stops should be followed by purging with virgin material before resuming a build. Chamber air temperature should be held at 35–50 °C, and the build plate at 60–80 °C to reduce edge lift in parts taller than 200 mm. Without active chamber heating, temperature stratification above 5 °C between bed and upper layers can cause visible delamination in large rectangular sections.

    Rheological data measured by capillary rheometry at 210 °C can be used to predict die swell and nozzle pressure. Biodegradable polyester melts with high molecular weight often show shear-thinning behavior; at apparent shear rates above 100 s−1, viscosity is sufficiently low for large nozzle extrusion, but at low shear rates melt strength may be insufficient for unsupported spans. Bridging and overhang performance should be tuned by adjusting print speed rather than raising melt temperature, because higher melt temperature lowers zero-shear viscosity and increases sag. In large-format deposition, the bead width may exceed 1.0 mm, and the extrusion multiplier must be validated with a single-wall calibration cube; overextrusion above 2–5 % creates layer ridges and trapped porosity, while underextrusion produces visible gaps at direction changes.

    For sacrificial tooling, washout cores, and low-temperature composite layup mandrels, the material is typically printed at layer heights between 0.2 mm and 0.4 mm. The extruded bead is deposited onto a heated bed with a polyimide or PEI surface; adhesion aids may be required for long, thin features. After printing, dimensional accuracy of tooling features is influenced by shrinkage anisotropy and should be verified against the machine’s capability study, not assumed from CAD. In hollow composite applications, the polymer is selected because it can be broken out mechanically or processed for industrial composting after service, provided that contamination from resins, release agents, and adhesives does not violate the compostability criteria of EN 13432. The material is not recommended for continuous load-bearing applications above the annealed heat deflection temperature, and cyclic loading requires component-specific fatigue testing under ISO 527-5 or ASTM D790 with environmental conditioning.

    Comparative Mechanical and Thermal Property Matrix against PLA, PETG, ABS and PA6/66

    The following table summarizes representative published ranges for unfilled FFF-grade materials. Values for the BigRep HI-TEMP grade are representative of high-temperature biodegradable polyester formulations and must be confirmed against the current technical data sheet. Industrial composting refers to EN 13432 or ASTM D6400-23 certification, not ambient soil degradation.

    Material family HDT B typical Tensile strength XY Flexural modulus Industrial compostability Typical FFF extrusion range
    BigRep HI-TEMP Biodegradable 80–110 °C annealed 45–60 MPa 2.8–3.5 GPa Yes under EN 13432/ASTM D6400-23 200–230 °C
    PLA 50–60 °C 50–65 MPa 2.3–3.5 GPa Yes under EN 13432/ASTM D6400-23 190–220 °C
    PETG 65–75 °C 45–50 MPa 1.8–2.1 GPa No 230–250 °C
    ABS 90–100 °C 35–45 MPa 1.8–2.5 GPa No 240–260 °C
    PA6/66 110–150 °C 60–70 MPa 2.0–3.0 GPa No 260–280 °C

    The matrix shows the primary substitution logic: compared with PLA, the HI-TEMP biodegradable grade moves into the service territory of PETG and unfilled ABS while retaining industrial compostability. Compared with PETG, the thermal performance may be higher after annealing, but the processing window is narrower and more sensitive to moisture. Compared with ABS, the material avoids styrene monomer volatility and offers a biodegradability pathway, but it may require more careful drying and lower chamber temperatures. Compared with PA6/66, the biodegradable polyester cannot match the high-temperature service range of polyamide, and it is not a drop-in replacement where continuous service above 120 °C is required.

    Colorant masterbatches and nucleating agents can shift the cold-crystallization temperature by 5–15 °C. A black production lot may therefore require a different annealing profile than a natural lot. Process engineers should maintain a lot-specific datasheet and not transfer parameters without verifying the melt flow index and thermal transitions. On gantry-style large-format machines with direct-drive extruders, batch-to-batch viscosity variation above ±5 % can be observed when colorant masterbatch is changed; this can require extrusion multiplier adjustment.

    Hydrolytic degradation is accelerated by moisture, heat, and reprocessing cycles

    Hydrolytic degradation proceeds by ester bond cleavage, and its rate increases with melt temperature, residence time, and dissolved water. Dry filament stored in sealed containers with desiccant below 20 % RH retains processability; opened spools should be returned to storage or dried before use if ambient humidity exceeds 60 % RH. Regrind from failed prints is not automatically equivalent to virgin material. If a production facility grinds and reprocesses large-format scrap, the regrind fraction should be limited to 20 wt% and the blend re-dried before feeding. Each heat history increases the melt flow index and reduces impact strength; adding regrind above 30 wt% can produce unacceptable Z-axis tensile loss in large parts.

    End-of-life claims must be separated from uncontrolled environmental degradation. Industrial composting certification under EN 13432 requires a minimum disintegration and biodegradation level under controlled conditions; it does not imply rapid breakdown in marine or soil environments. Waste handling should therefore be routed to an industrial composting facility or a specialized biodegradable polymer recycling stream. The material should not be mixed with PET recycling streams because it can act as a contaminant in rPET granulate. For regulatory compliance, users must verify that the final printed article meets the applicable requirements for REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU Annex II restrictions; these regulations apply to the finished article, not only to the feedstock. The manufacturer’s current safety data sheet should be consulted for decomposition products during printing, ventilation requirements, and exposure limits.

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