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Natur-Tec BF3002HT High Heat Injection Molding Compostable Polylactic Acid

    • Название продукта: Natur-Tec BF3002HT High Heat Injection Molding Compostable Polylactic Acid
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
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    • Производитель: Ascent Petrochem Holdings Co., Limited
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    Спецификации
    Код ТН ВЭД 619187

    Будучи аккредитованным заводом Natur-Tec BF3002HT для высокотемпературного впрыска, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

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    Применение Natur-Tec BF3002HT высокотеплового литья под впрыском компостируемой полимелочной кислоты

    In hot beverage lid and hot-fill portion-pack production, the Natur-Tec BF3002HT high-heat injection moulding compostable polylactic acid compound enters the injection moulding cell only after closed-loop desiccant drying at 80 °C for 4 h to a pellet moisture content below 250 ppm. Plants that introduce open hopper loading in ambient relative humidity above 60% observe splay on the cavity surface within 15–20 min of exposed residence. The material is processed on electric toggle injection presses with clamp force between 800 kN and 1,600 kN, using melt temperatures of 185–200 °C and tool surfaces held at 80–100 °C to complete crystallisation prior to ejection. A two-stage holding profile with injection peak at 120–160 MPa and packing pressure at 60–70% of that peak prevents sink and dimensional drift opposite valve-gated hot-runner entry points. The terminal part field includes hot cup lids, portion cups, single-serve dessert bowls, and hinged lid-shoulder closures. Regulatory compliance is governed by EN 13432:2000 for organic recovery, ASTM D6400-21 for North American compostability claims, EU Regulation (EU) No 10/2011 for overall migration into food simulants, and the applicable U.S. FDA food-contact notification for the compounded grade. Dosing practice keeps the virgin compound at 100% with post-industrial regrind from sprues and runners blended at 10–15 wt%; regrind above 20 wt% is excluded in hot-fill service because chain scission shifts the crystallisation exotherm and depresses heat deflection under ASTM D648 Method B at 0.455 MPa below the thermal load applied by continuous 85 °C hot-fill lines.

    Compliance matrix for hot-beverage lid and hot-fill portion-pack production
    Standard or regulationScopeCritical acceptance criterion
    EN 13432:2000Packaging recoverable through composting and biodegradation90% biodegradation by ISO 14855-1 within 180 days; disintegration residue ≤10% above 2 mm within 12 weeks; ecotoxicity negative
    ASTM D6400-21North American industrial compostabilityBiodegradation via ASTM D5338; disintegration via ISO 16929; no adverse effect on compost quality
    EU Regulation (EU) No 10/2011Plastic materials intended for food contactOverall migration ≤10 mg/dm² in simulants selected by contact temperature and duration
    ISO 17088:2021Compostability specification for plasticsAlignment with ISO 14855-1, ISO 16929, and ISO 20200

    The dominant thermal failure in lid production is not lip burn but post-ejection shrinkage. In thin-wall cavity sections below 1.0 mm, premature ejection at high mould temperatures leaves the part with residual amorphous polylactic acid that later crystallises during pallet stacking, producing an ovality deviation of 0.2–0.5 mm across the curled rim. Tooling therefore uses mechanical slide actions on the full rim circumference, and ejection plate motion is delayed until cavity pressure at the gate location has decayed below 20 bar. The crystallising mould temperature requires water lines sized for a ΔT of 5–10 °C between inlet and outlet; if the ΔT exceeds 12 °C, crystallinity gradients across the lid create differential shrinkage visible as radial haze. Local exhaust ventilation at the machine throat and hot-runner area is maintained because melt residence above 200 °C for more than 5 min raises lactide concentration and increases surface vehicle defects in the formed lid.

    How Does a 20 wt% Regrind Fraction Move the Crystallinity Window in Disposable Cutlery?

    Disposable cutlery tools place the thermal load at the boundary between hot soup contact and mechanical bending. The BF3002HT feedstock is typically let down with 15–20 wt% sprue-free regrind, but the exact ceiling is set by ISO 1133-1:2022 melt flow testing on the blended batch; when the melt volume-flow rate drifts by more than 5% against the virgin certificate of analysis, tine filling in fork cavities shorter than 1.8 mm becomes non-uniform. High-cavitation moulds of 32–64 cavities are run on electric or hydraulic presses with clamp force from 1,600 kN to 3,200 kN, and valve-gated hot runners are preferred to reduce sprue mass and deliver uniform melt pressure to each cavity. The mould surface temperature is held at 90–100 °C, and post-mould crystallisation annealing in circulated-air racks at 90 °C for 20–30 min is applied to knife handles and spoon bowls above 3 mm wall thickness; the annealing step raises heat deflection but can consume 8–12% of total cycle time. The relevant conformity markers are EN 13432:2000, ASTM D6400-21, the BPI certification mark where North American commercial composting is specified, and EU Regulation (EU) No 10/2011 where cutlery is sold into direct food contact. Finished part types include forks, soup spoons, knives, stirrers, and sporks.

    Mould-release strategy shifts with the cutlery profile. Knife handles with thick cross-sections above 4 mm benefit from a two-step ejection sequence: first the blade portion is released from the cavity, then the handle is pushed from the core after a 0.5–1.0 s delay to reduce ejector pin depth. Venting is placed at the last fill point in the spoon bowl; inadequate vent depth below 0.02 mm produces diesel burns and local acetaldehyde odour. Thermal stability at the nozzle is checked by purging at 190 °C with 5 min residence; a colour shift beyond Δb* 1.5 against virgin pellets is rejected. A recorded field failure mode is flexural whitening at the spoon neck under high-speed filling; the problem is mitigated by increasing holding pressure to 70% of peak and reducing regrind to the lower 10 wt% band when ambient warehouse humidity exceeds 70%.

    Cosmetic Jar Warpage After Hot-Fill Wax Pouring

    In cosmetics and personal-care packaging, BF3002HT is applied to injection-moulded jars and cups that receive hot-poured balms, waxes, and butters at filling temperatures between 70 °C and 85 °C. The moulding process differs from food service because the part wall is typically 2.0–4.0 mm, and screw recovery must keep melt temperature below 200 °C while the tool is run at 80–95 °C; cooling time per wall thickness often reaches 8–10 s/mm in a mirror-finish cavity, making cycle-time management the dominant production bottleneck. Dosing comprises 100% virgin BF3002HT with 2–4 wt% masterbatch colorant and up to 10 wt% post-industrial regrind; higher regrind levels create black specks and reduce the surface quality required for transparent or soft-touch overmoulding. The terminal product range includes facial cream jars, lip balm pockets, solid perfume compact bases, and refill cups. The applicable conformity set is EU Regulation (EC) No 1223/2009 for the cosmetic product inside the container, REACH Regulation (EC) No 1907/2006 for substance registration, EU Directive 94/62/EC for heavy metals and packaging minimisation, and EN 13432:2000 where the empty pack is claimed as compostable. A process boundary is necessary for fragrance-loaded formulations; published data specific to BF3002HT in continuous contact with ethanol-based fragrances is limited, and the ester linkages of polylactic acid can undergo environmental stress cracking under flexural strain above 1% after 48 h of 70/30 ethanol/water contact. Packaging engineers must not substitute BF3002HT for PETG or PP in high-solvent perfume closures without preliminary fitness-for-contact testing.

    Warpage in cream jars after hot-fill is traced to asymmetric gate location and uneven post-mould crystallisation. For a cylindrical jar of 50 mm diameter and 3 mm wall, a single edge gate produces a shell-core crystallinity gradient; the part bows outward by 0.3–0.8 mm after 24 h at 45 °C. Tooling correction uses three pin-point gates spaced at 120° around the base or a valve gate into the base centre, with the cavity wall held at 90 °C and the core at 75 °C to direct shrinkage to the inner surface. Finished part dimension is checked under ISO 291 after conditioning for 48 h at 23 °C and 50% relative humidity.

    Horticultural propagation trays, vine clips, and nursery identification stakes use BF3002HT where thermal load arises from solar gain inside greenhouse tunnels rather than direct hot liquid contact. Production lines use thin-wall moulds with part thickness from 1.2 mm to 2.5 mm and melt temperatures of 180–195 °C; screw designs with L/D of 20:1–24:1 and low-compression feed sections are applied to avoid excessive shear heating. In dosing, the compound is blended with 0–10 wt% post-industrial regrind; if UV opacity for exterior nursery use is demanded, 1–2 wt% carbon black masterbatch is dispersed, but the resulting compound is not home-compostable and must not be labelled as soil-biodegradable because polylactic acid requires industrial composting conditions. Terminal products include grapevine clips, tomato clips, tree-label stakes, plug trays, and seedling markers. The conformity landmark for compost moulding is EN 13432:2000 or ASTM D6400-21, with ISO 17088:2021 serving as the global specification; under ISO 16929 disintegration testing, full part thickness above 2.5 mm may require extended residence to meet the 10% residue ceiling within 12 weeks. In field service, unstabilised polylactic acid clips become brittle after one or two greenhouse seasons; fracture typically initiates at thin living hinges, which is the primary reason why hinge depth is held below 0.8 mm in tooling.

    Part ejection from thin-wall horticultural tools is stabilised by using peripheral gate locations and parting-line vents at 0.01–0.03 mm depth. Because the melt is more shear-sensitive at thin wall, injection speeds above 300 mm/s can create flow marks on label stakes; the accepted control window is 150–250 mm/s screw advance, with cavity pressure at end of fill held below 600 bar to avoid jetting. After moulding, clips are not annealed except where clamp creep under warm greenhouse conditions is expected; a short annealing step at 80 °C for 15 min improves dimensional set but can cause ejection pin marks to deepen if applied before the part is fully cooled below 45 °C. Terminal parts remain industrial compostable only; soil burial tests are not a valid substitute for ISO 16929.

    While a 1.0 mm Pen Barrel Wall Must Still Pass Dimensional Stability After 48 h at 60 °C

    Writing-instrument and stationery applications use BF3002HT for long, thin-walled components where ejection deformation and warehouse heat are more critical than hot liquid contact. The injection process demands high injection speeds into flow paths exceeding 100 mm, with wall thicknesses from 1.0 mm to 1.8 mm; cycle times of 20–35 s are achieved only when tool temperature is maintained at 80–90 °C and melt temperature is kept between 190 °C and 205 °C. Dosing uses 100% virgin BF3002HT with 2–3 wt% pigment masterbatch and up to 10 wt% closed-loop regrind; if regrind exceeds 10 wt%, melt viscosity drift measured by ISO 1133-1:2022 causes die drool at hot-runner nozzle tips and visible clouding in transparent barrels. The finished component range comprises pen barrels, mechanical pencil bodies, ruler bodies, pencil sharpener housings, and desk accessory shells. The relevant chemical conformity set includes REACH Regulation (EC) No 1907/2006, EN 71-3 where the article may be handled by children, and EN 13432:2000 where the finished item carries a compostable end-of-life claim. The principal operational boundary is sustained service above 60 °C; although the annealed material withstands short excursions, prolonged thermal soak softens thin-wall geometry and causes dimensional drift in pen barrels stored in a closed vehicle in summer. Published data for BF3002HT in writing-tool grade applications is limited; production validation should include oven-aging at 60 °C for 48 h under 0.2 MPa flexural load.

    Drooling at the hot runner is a known bottleneck when colour masterbatch at 3 wt% or above reduces melt elasticity. To maintain nozzle shutoff, the hot-runner tip is specified with a thermal profile 10–15 °C below the barrel front zone, and the decompression stroke is limited to 3–5 mm; longer suck-back draws air into the melt stream and creates silver streaks along the longitudinal pen barrel wall. After injection, the parts are placed immediately into oriented stacking trays to prevent crosswise bending during the first 30 min of crystallisation. The dimensional stability criterion is measured by ISO 178 flexural modulus after conditioning for 48 h at 23 °C and 50% relative humidity; a decline of more than 10% in flexural modulus after the 60 °C soak is treated as a batch failure.

    Building Blocks and the EN 71-3 Mass Balance Case Against Regrind

    Toys and educational components made from BF3002HT are injection-moulded where the compostable claim and mechanical stiffness matter but the component is not a safety-critical load-bearing part. The formulation uses 100% virgin compound with 2–4 wt% of an EN 71-3-compliant pigment masterbatch; post-industrial regrind is avoided in toys intended for children under 36 months, because contaminant mass balance under EN 71-3:2019 requires traceable feedstock and regrind introduces an uncontrolled source of heavy-metal migration risk. Processing conditions are deliberately low-shear: melt temperature is held at 185–195 °C, back pressure at 2–5 bar, and screw speed below 150 rpm to minimize lactide generation and maintain the low residual monomer profile expected in children’s products. Moulds are vented at the end of fill, with tool temperature at 80–100 °C to develop crystallinity before ejection. Terminal products include building blocks, educational shapes, puzzle bases, counting frames, and stackable manipulative components. Conformity is assessed under EN 71-3:2019 for migration of 19 elements, ASTM F963-23 for the U.S. toy market, REACH Regulation (EC) No 1907/2006 for substances of very high concern, and EN 13432:2000 if the final article is labelled compostable. A sharp operational boundary appears in small-part design: polylactic acid-based compounds exhibit lower impact strength than ABS and are not used for safety-test items that must pass EN 71-1 drop tests from heights above 1.0 m; building-block designs therefore maintain wall thicknesses above 2.0 mm and avoid snap-fit undercuts with radii below 0.5 mm.

    Tool surface temperature in block moulds is ramped from 80 °C to 100 °C over the first 5–10 shots; cold-tool startup produces a mottled crystalline skin that fails visual acceptance criteria under ISO 105-A02 grey scale reference for colour change. Because the material is not toughened like ABS, ejector pin placement is moved away from thin feature bases and the part is removed only after core temperature falls below 60 °C. A particular challenge in educational toys is cavity fill at the top of a block boss; when wall thickness falls below 1.5 mm, gas entrapment at the boss end is prevented by a porous sintered vent insert rather than increased injection pressure, which would otherwise raise shear and generate lactide. The finished components are not labelled as home compostable; the industrial compost claim follows EN 13432:2000 disintegration and ecotoxicity criteria.

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    Более подробное введение

    Natur-Tec BF3002HT High Heat Injection Molding Compostable Polylactic Acid is a nucleated, semicrystalline PLA-based compound supplied in pellet form for conventional injection molding of rigid compostable articles. The grade is specified where unmodified PLA has insufficient heat resistance because of heat deflection below 60 °C; target components include compostable cutlery, coffee cup lids, serving trays, and hot-food contact accessories. The material relies on a thermally activated crystallization mechanism. When the mold is held above 90 °C, the resulting crystalline network raises the heat deflection temperature measured at 0.455 MPa by ASTM D648 into the elevated range required for short hot-beverage and hot-fill contacts. Representative values for the product class are summarized below; the manufacturer’s lot-specific certificate of analysis remains the controlling document for production qualification.

    PropertyTest MethodRepresentative RangeUnit
    DensityASTM D7921.24–1.26g/cm³
    Melt Flow Rate at 210 °C, 2.16 kgASTM D123810–20g/10 min
    Tensile Strength at YieldASTM D63858–65MPa
    Tensile Elongation at BreakASTM D6382–4%
    Flexural ModulusASTM D7903.2–3.6GPa
    Notched Izod Impact at 23 °CASTM D25620–30J/m
    Heat Deflection Temperature, as-molded annealed at 100 °CASTM D64888–98°C
    Vicat Softening TemperatureASTM D1525130–145°C

    Data in the table are not batch guarantees; melt flow rate, tensile values, and heat deflection temperature shift with crystallinity, moisture, regrind content, and part thickness.

    What Distinguishes BF3002HT from Unmodified PLA Injection Grades?

    The functional boundary between general-purpose PLA and BF3002HT appears in heat deflection temperature after the part exits the mold. Unmodified amorphous PLA typically exhibits heat deflection below 60 °C at 0.455 MPa because the glass transition temperature of PLA is near 55–60 °C. A nucleated high-heat PLA compound develops crystallinity during a high-temperature mold cycle and can reach 88–98 °C at 0.455 MPa under ASTM D648 when crystallization is complete. This shift is the basis for rigid compostable cutlery and lids that withstand hot soup, coffee, and short dishwashing contact.

    Compared with unmodified PLA, BF3002HT exhibits higher flexural modulus retention at 80 °C; amorphous PLA loses stiffness above its glass transition, while crystalline domains retain mechanical integrity for short thermomechanical loads. Compared with soft PBAT/PLA blend products, the grade orders at the rigid end of the compostable polyester spectrum: flexural modulus is elevated, but tensile elongation at break typically remains below 5% by ASTM D638. Compared with unreinforced polypropylene, density is approximately 1.24–1.26 g/cm³ by ASTM D792, roughly 35% higher, and notched Izod impact is lower, while flexural modulus is higher. The material is therefore appropriate for stiff, low-strain, hot-contact disposables rather than ductile or snap-fit loads.

    Melt Residence Time and Hydrolytic Degradation Are Not Independent Variables

    Processing of PLA-based compounds is controlled by hydrolysis and thermal depolymerization of ester linkages. Moisture in the pellets attacks polylactic acid during melting, producing chain scission, molecular weight loss, viscosity reduction, and mechanical property decay. Hydrolysis follows an autocatalytic mechanism: carboxylic acid end groups generated by chain scission accelerate further degradation unless the material is dried and melt temperature is controlled. At 210 °C, PLA-based melts of this class commonly show apparent zero-shear viscosity in the range of 1000–3000 Pa·s, making melt flow rate by ASTM D1238 or ISO 1133-1:2022 an indirect indicator of molecular weight retention in incoming lots and regrind. For BF3002HT, the supplier’s general PLA processing window recommends desiccant drying at 80 °C for 4 h with a dry-air dew point of -40 °C or lower to reduce final moisture below 250 ppm. Moisture above 0.025 wt% produces measurable molecular weight loss in the barrel and may increase melt flow rate by more than 20% relative to dry resin.

    Melt temperatures should remain between 190 °C and 210 °C at the nozzle, with an upper excursion limit near 220 °C. Extended residence time above this temperature promotes lactide formation, discoloration, and loss of notched Izod impact. Injection molding machines with 20:1 to 24:1 L/D general-purpose screws and a reverse-cut or smearing screw tip are suitable when the shot size is kept between 30% and 70% of barrel capacity. Total melt residence time should not exceed 20 min; hold-up points in the barrel, nozzle, and hot runner should be minimized. Where a hot runner is used, externally heated manifolds with low-dead-spot flow channels and fast valve-gate actuation are preferred. Internally heated systems with stagnant zones have been associated with yellowing and black specks in high-heat PLA compounds.

    At the gate, shear rates commonly fall between 103 s−1 and 104 s−1; the melt is pseudoplastic, and higher injection velocity may be needed to fill thin sections. Excessive shear heating above 220 °C should be avoided. Vent depth is typically 0.02–0.04 mm to remove volatiles without flash. Regrind ratios up to 20% may be used if the regrind is dried and free of contamination; higher ratios accelerate yellowing and reduce impact strength.

    When Mold Temperature Falls Below the Crystallization Onset

    The intended heat resistance of BF3002HT is not achieved if the mold is run as a cold-water tool. At mold temperatures below 80 °C, crystallization is kinetically suppressed, and the part remains largely amorphous; heat deflection temperature by ASTM D648 can remain below 65 °C even though the compound contains a nucleation package. The processing solution is to hold mold surface temperatures between 90 °C and 110 °C using pressurized water or oil temperature control units rated for 120 °C. At 100 °C mold temperature, cooling is extended relative to polypropylene because the part must pass through a crystallization exotherm while the tool is hot. Cycle time increases of 20–40% over equivalent cold-runner PP have been observed in production trials.

    Where high mold temperatures are not available, post-mold annealing can be performed in fixtures at 100 °C for 20–30 min, but this introduces warpage risk, dimensional change, and secondary labor. Published data for this specific configuration in BF3002HT is limited; trials should define shrinkage and flatness against the part’s critical dimensions. Gate size is also a factor: gates below 60% of part wall thickness have been associated with gate freeze-off before packing, generating sink marks and incomplete crystallization at the gate region. Typical gate diameters for thin-wall articles are 0.8–1.5 mm. Mold shrinkage for high-heat PLA compounds after crystallization is typically 0.3–0.5% in the flow direction and 0.5–0.8% transverse, lower than typical polypropylene shrinkage.

    Impact performance in the high-heat PLA class remains the main mechanical limitation. Notched Izod values near 20–30 J/m at 23 °C by ASTM D256 are below those of impact-modified polypropylene, which can exceed 100 J/m in typical automotive compounds. Elongation at break below 5% means that snap-fit features, living hinges, and high-strain geometry should be redesigned or avoided. At service temperatures below 0 °C, brittleness increases further. Compared with PHA-based compostable injection grades, BF3002HT may exhibit higher flexural modulus but lower ultimate elongation and different melt-stability limits. These trade-offs define the application envelope: rigid, low-strain, hot-contact disposable articles that can tolerate the lower impact resistance of a semicrystalline PLA matrix.

    Compostability Certification Matrix

    End-of-life claims for BF3002HT are governed by industrial compostability standards rather than marine or home compost conditions. The grade is within the class of PLA compounds tested under ASTM D6400-23, EN 13432:2000, and ISO 17088:2021. Ultimate aerobic biodegradation is measured by ISO 14855-1:2012 and ASTM D5338-15, in which organic carbon is converted to carbon dioxide under controlled composting conditions. Disintegration is assessed by ISO 20200:2015 or ISO 16929:2021. These tests are conducted at 58 °C in actively aerated static reactors, not at ambient soil or seawater temperatures. The product is not marketed as marine biodegradable; disposal must be routed to an industrial composting facility operating at thermophilic conditions. For food-contact applications, the processor must obtain lot-specific conformity documentation for the final article under the relevant regulatory framework, such as Regulation (EC) No 10/2011 or applicable FDA food-contact clearances. Biobased carbon content is measured by ASTM D6866; typical PLA resin exhibits biobased carbon content above 95%.

    StandardScopeRepresentative Test Method
    ASTM D6400-23Specification for compostable plasticsASTM D5338-15, ASTM D6866
    EN 13432:2000Packaging recoverable through composting and biodegradationISO 14855-1:2012, ISO 20200:2015, ISO 16929:2021
    ISO 17088:2021Specification for compostable plasticsISO 14855-1:2012, ISO 20200:2015

    Application routes reported for high-heat PLA compounds of this type include single-use compostable cutlery, coffee cup lids, hot soup spoons, salad bowls, deli trays, and rigid packaging for catering and institutional food service. In such parts, the material selection is justified only when an industrial composting stream is available and when the article geometry provides sufficient wall thickness for crystallization. Thin-wall parts below 1 mm may not retain enough heat during mold filling to complete crystallization before ejection; published data for this specific configuration in BF3002HT is limited. Operational boundaries include a maximum hot-food contact condition near 95 °C for short durations, no dry-heat oven use, and no prolonged boiling-water immersion. Continuous exposure above 60 °C in amorphous zones can induce dimensional change because the PLA glass transition is traversed. Opened bags should not be stored at relative humidity above 50% for longer than 8 h without redrying.

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