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INZEA F58 AL40 Rigid Thermoforming/Injection Biodegradable Polylactic Acid

    • Product Name: INZEA F58 AL40 Rigid Thermoforming/Injection Biodegradable Polylactic Acid
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 131125
    Product Name INZEA F58 AL40
    Material Type Biodegradable Polylactic Acid (PLA)
    Processing Methods Rigid Thermoforming, Injection Molding
    Density 1.25 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 15-25 g/10 min
    Melting Temperature 150-160 °C
    Vicat Softening Temperature 60 °C
    Tensile Strength At Break 35-40 MPa
    Tensile Modulus 2500-3500 MPa
    Elongation At Break 3-5 %
    Flexural Modulus 3000-3500 MPa
    Notched Charpy Impact Strength 2-3 kJ/m²
    Biobased Content > 40 %
    Biodegradability Compostable according to EN 13432
    Food Contact Suitable for food contact
    Color Natural

    As an accredited INZEA F58 AL40 Rigid Thermoforming/Injection Biodegradable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INZEA F58 AL40 is packaged in 25 kg moisture-resistant paper sacks, palletized, suitable for rigid thermoforming and injection biodegradable PLA processing.
    Container Loading (20′ FCL) INZEA F58 AL40: loaded in 20′ FCL in 25 kg bags on pallets, approximately 18–20 MT net, shrink-wrapped and strapped.
    Shipping INZEA F58 AL40 rigid thermoforming/injection biodegradable polylactic acid is shipped as non-hazardous solid pellets in sealed moisture-barrier bags, typically 25 kg bags or octabins on pallets. Transport at ambient temperature in dry, clean conditions, avoiding direct sunlight, excessive heat, and moisture. No special dangerous-goods classification; keep packaging closed until use.
    Storage Store INZEA F58 AL40 in a cool, dry, well-ventilated area, away from heat, direct sunlight, moisture, and ignition sources. Keep original packaging tightly sealed to prevent hydrolysis and contamination. Maintain low humidity and stable temperature; avoid strong oxidizers. Use first-in, first-out stock rotation and observe shelf-life recommendations. Keep containers clean, labeled, and closed when not in use.
    Shelf Life Typically 12 months when stored unopened in original packaging, cool, dry, and protected from moisture, heat, and direct sunlight.
    Application of INZEA F58 AL40 Rigid Thermoforming/Injection Biodegradable Polylactic Acid

    Thermoforming conditions that preserve 0.8 mm wall thickness at moisture levels under 250 ppm

    Sheet extrusion operators running refrigerated dairy portion packs with INZEA F58 AL40 typically condition the resin in a desiccant wheel drier with a dew point of -40 °C and an air flow of 0.3 m³/h/kg for 4 h at 70–80 °C, because moisture above 250 ppm triggers hydrolytic chain scission at the die lip and produces edge haze that cannot be recovered downstream. The melt temperature is held between 190 °C and 205 °C on a single-screw extruder with a 30D L/D barrier screw and a screen pack no finer than 100 µm; higher melt temperatures increase lactide formation and lower melt strength at the plug, while lower temperatures raise shear heating in the metering zone and produce unmelted gel bodies in sheet. The chill roll stack is operated at 25–35 °C with a roll gap adjusted to the sheet thickness, and sheet of 0.8–1.2 mm is wound with edge trim recycle limited to 20 wt% of the feed stream because higher amorphous PLA regrind fractions shorten the thermal stability envelope during sheet re-extrusion.

    ParameterSheet extrusionPlug-assist thermoforming
    Residual moisture< 250 ppm< 250 ppm
    Melt or sheet surface temperature190–205 °C95–110 °C
    Tool or roll temperature25–35 °C chill roll25–35 °C mould
    Pressure or cycleDie pressure monitored4–6 bar forming air, 6–9 s cycle

    At the forming station, the sheet surface is brought to 95–110 °C by ceramic or quartz contact heating, and a plug-assisted tool with an aluminium plug radius of 0.5 mm and plug temperature 80–90 °C distributes material before air pressure at 4–6 bar presses the sheet against a mould held at 25–35 °C. The forming cycle is normally 6–9 s. The final container is rated for short contact with refrigerated dairy products up to 45 °C; hot-fill above this threshold produces wall distortion at the base radius and lid seat. Compliance for the food-contact application is assessed under EU Regulation (EU) No 10/2011, Annex I, with overall migration below 10 mg/dm², and compostability claims are validated by EN 13432:2000, including disintegration under ISO 16929:2021 and aerobic biodegradation under ISO 14855-1:2021. The formulation addition ratio in clear applications is 100 wt% INZEA F58 AL40; if a slip agent is required for denesting, a masterbatch loading of 2–4 wt% is used only after the modified compound is revalidated for migration and compostability. Terminal product types include 125–200 ml dairy dessert cups, portion packs for cream or sauce, and cold soup containers sealed with peelable compostable lidding film.

    On fresh-produce packing lines where berry clamshells must survive cold-chain washdown and automatic lidding, INZEA F58 AL40 is converted as a 0.35–0.5 mm sheet with a post-extruder regrind cap of 15 wt% to preserve hinge flexural fatigue life; regrind above that threshold increases gel reflection in the hinge and lowers the number of open-close cycles before snap failure, an effect observed on high-speed thermoforming lines operating at 30–45 strokes/min. The downstream process uses a contact-heated sandwich oven with a surface temperature of 90–105 °C, a plug-assist tool with a syntactic foam plug, and a water-cooled aluminium mould set at 20–25 °C to freeze the hinge without creating stress whitening. The hinge is produced by a scoring die that leaves a residual web thickness of 0.12–0.15 mm; if the web is compressed below 0.08 mm, the hinge loses ductility at 4 °C and fails during pack-out. Ventilation slots are punched in-line after forming, and the cut parts are robot-stacked to avoid blocking. The compliance framework for export markets is ASTM D6400-23 for compostable packaging, EU Regulation (EU) No 10/2011 for food-contact migration, and a supplier-confirmed U.S. FDA 21 CFR Part 177 food additive status for the specific lot; no generic 21 CFR citation should be used without the grade-specific clearing. The formulation addition ratio for clear fruit packaging is 100 wt% INZEA F58 AL40; if an anti-fog masterbatch is required to prevent condensation across the lid, it is added at 2–5 wt% only after revalidation of haze, hinge toughness, and ISO 14855-1:2021 biodegradation. Terminal product types include 125 g to 750 g berry clamshells, salad herb packs with micro-perforated lids, and cherry tomato punnets with interlocking corner closures. Published data for the exact INZEA F58 AL40 hinge-fatigue limit under this specific configuration is limited; the residual web values above are general PLA sheet guidance and should be confirmed on the production line.

    When screw recovery speed becomes the limiting variable in injection-moulded cutlery production

    Injection-moulded disposable cutlery manufactured from INZEA F58 AL40 tests a different boundary than thermoformed sheet because the melt spends its entire residence time inside a heated barrel and hot runner system, where prolonged exposure re-forms lactide and reduces molecular weight. On a 120-tonne hydraulic injection moulding machine with a 40 mm screw and 22D L/D, a shot weight of 250 g across a 16-cavity spoon tool may require a plasticising time of 8–12 s; if screw recovery exceeds 12 s for a tool with 1.8 mm nominal wall, the material can remain above 180 °C in the barrel for more than 4 min, generating viscosity loss and brown specks in the gate area. The barrel profile is reverse-set from 180 °C at the rear to 195 °C at the front and 200 °C at the nozzle; the mould is water-regulated at 30–35 °C, because lower temperatures quench the surface too rapidly and produce high gate stress, while higher temperatures extend cooling time and cause sticking on the core. Injection speed is held at 60–90 mm/s with a switch-over at 90–95% of stroke, and hold pressure is set at 450–650 bar for 1.5–2.5 s to pack the handle and bowl of the cutlery. The formulation addition ratio is 100 wt% virgin INZEA F58 AL40 for cutlery exported as compostable foodservice ware, with clean post-industrial regrind limited to 10 wt% for knife handles because knife stiffness under cantilever loading drops when regrind raises gel content. Compliance for food-contact serviceware is evaluated under EU Regulation (EU) No 10/2011, Annex I, with migration testing according to EN 1186-1:2002, and compostability assessed under EN 13432:2000; claims for U.S. food-contact status require the exact supplier FCN or 21 CFR Part 177 clearing. Terminal product types are 160–170 mm spoons, forks, knives, and sporks, normally sold in bulk or wrapped sets; use is limited to cold or warm food below 55 °C, and dishwasher use is not recommended because wet heat above 55 °C causes deformation at load-bearing sections.

    For non-food transit packaging where cosmetic cartons and consumer-electronics cushions require static dissipation without flammability concerns, INZEA F58 AL40 sheet is extruded at 0.3–0.6 mm with a blend ratio of 97–99 wt% INZEA F58 AL40 and 1–3 wt% antistatic masterbatch; higher additive loadings raise surface haze and reduce thermoforming melt strength at the edges of deep-draw trays, a defect visible on platen machines running draw ratios above 1:1.5. The antistatic target is a surface resistivity of 1010–1012 Ω/sq measured according to IEC 61340-2-3:2016. Colour masterbatch for opaque cosmetic inserts is added at 3–5 wt%, but the combined additive package must not exceed 6 wt% unless the converter verifies that the masterbatch carrier does not shift the compostability marker under EN 13432:2000. Downstream processing uses a twin-screw compounding step only when masterbatch dispersion is required; otherwise direct sheet extrusion is preferred to avoid an additional heat history. The sheet is thermoformed on an intermittent chain-fed machine with a top oven temperature of 85–100 °C, a female mould held at 20–30 °C, and steel-rule cutting after the sheet leaves the forming area. Incorrect oven zoning produces wrinkling at the tray flange; because amorphous PLA has a narrow stretch window, the difference between the centre and edge sheet temperature must be held below 5 °C during heating. Compliance is documented through REACH Regulation (EC) No 1907/2006 for the supplied compound and RoHS Directive 2011/65/EU for electrical/electronic accessory packaging, while compostability claims require ASTM D6400-23 for the U.S. market. Terminal product types are cosmetic inner trays, transit cushions for small electrical assemblies, and non-food clamshells for retail security seals. The material is not suitable for heavy components above 2 kg in long-term warehouse storage because compressive creep at temperatures above 40 °C can allow tray deformation.

    Regrind ratios above 20 wt% in horticultural pot moulding and the onset of rim cracking

    Horticultural injection moulders running thin-wall seedling pots and plant clips from INZEA F58 AL40 encounter a distinct failure shift when post-industrial regrind exceeds 20 wt%, because each regrind pass shortens the chain length and concentrates gel fragments at the rim weld line and gate vestige. At 20–30 wt% regrind, the melt pressure trend on a 120-tonne hydraulic machine monitored with a nozzle transducer moves below the virgin-material control band and becomes more sensitive to screw recovery speed; however, the more reliable upper regrind limit is established from batch-to-batch variance in notched Charpy impact energy under ISO 179-1:2010, which declines as gel content increases. The preferred formulation addition ratio is therefore 100 wt% virgin INZEA F58 AL40 for thin-wall pots below 0.8 mm nominal wall, and up to 20 wt% clean internal regrind for heavy plant clips where the wall section exceeds 1.5 mm. For black nursery pots, a black masterbatch is added at 2 wt%; filler addition above 5 wt% is not recommended for clips because impact toughness measured by ISO 179-1:2010 on notched specimens falls sharply relative to the unfilled grade, and failure occurs at the clip hinge before the intended service load is reached. The injection process uses a 50 mm screw with 20D L/D, a reverse barrel profile from 180 °C to 200 °C, and a mould temperature of 20–30 °C; injection velocity is set at 120–160 mm/s for 0.8 mm wall pots to prevent freeze-off before fill. After ejection, clips are annealed at 60–70 °C for 15–20 min to reduce residual orientation and improve dimensional stability during outdoor use; without annealing, a clip loaded in direct sunlight may creep and lose clamping force. Compliance for industrial compostability is assessed under EN 13432:2000, and mechanical property conformance is checked by ISO 527-2:2012 for tensile strength and ISO 178:2019 for flexural modulus; there is no food-contact requirement for this application. Terminal product types include 8–12 cm nursery pots, propagation trays, and injection-moulded plant clips for vine training. UV exposure does not cause immediate loss of shape, but outdoor service life should be limited to one growing cycle unless the formulation is specifically UV-stabilized.

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    Certification & Compliance
    More Introduction

    INZEA F58 AL40 is a biodegradable polylactic acid grade manufactured for rigid thermoforming and injection moulding. The grade is classified within PLA-based compounds that are assessed for industrial compostability under EN 13432 or ASTM D6400, and renewable-carbon content may be characterized by ASTM D6866 when a biobased carbon claim is required. Because published data for this specific configuration are limited, lot-specific values from the manufacturer’s certificate of analysis should govern design and acceptance. Unfilled semi-crystalline PLA grades used in comparable rigid packaging typically exhibit density near 1.24 g/cm³ under ISO 1183-1, tensile yield strength of 40–65 MPa under ISO 527-2, and flexural modulus of 3.0–4.0 GPa under ISO 178. Typical article geometries include transparent or opaque cups, trays, clamshell containers, thin-wall pots, and cutlery, with injection-moulded wall sections below 1.5 mm and thermoformed sheet thickness from 0.2 mm to 1.2 mm.

    What processing parameters govern sheet extrusion and thermoforming stability?

    Before extrusion, desiccant drying at 80 °C for 4 h to a residual moisture below 0.025 wt% is required; moisture above this threshold accelerates hydrolytic chain scission, with a measurable reduction in melt viscosity and an increase in edge brittleness. Sheet extrusion lines with a barrel length-to-diameter ratio of 24:1 to 32:1 and a compression ratio of 2.5:1 to 3:1 are common. Barrel profiles are set from 180 °C at the feed zone to 200–210 °C at metering and die zones; the upper melt-temperature limit is constrained by lactide reformation and yellowing above 220 °C. Chill-roll temperatures between 30 °C and 60 °C control crystallinity and sheet curl. Thermoforming requires sheet surface temperatures of 90–120 °C for predominantly amorphous PLA, measured with an infrared pyrometer set at emissivity 0.90–0.95. Below 90 °C, stress whitening and microcracking appear during plug-assisted stretching; above 120 °C, sag becomes excessive and wall-thickness variation on deep-draw tools can exceed ±10%. In production-scale sheet extrusion, regrind fractions above 20 wt% lower melt strength and increase gel counts unless the reclaimed sheet is dried, dust-free, and blended with virgin material. The safe forming window for unmodified PLA can be less than ±5 °C; maintaining uniform sheet temperature across the forming area is therefore a critical control point.

    In injection-moulding campaigns with clamp force from 800 kN to 2000 kN, the same drying specification is mandatory because molten PLA undergoes rapid hydrolytic degradation when residual moisture exceeds 0.025 wt%. Cylinder temperatures from 190 °C to 210 °C, nozzle at 200 °C, and mould temperatures of 15–30 °C favour short cycles and low crystallinity; mould temperatures near 80 °C increase crystalline content and heat-deflection temperature but extend cycle time and may increase warpage if cooling is non-uniform. Hot-runner systems must avoid dead spots and keep total residence time below 5 min at melt temperature; longer residence times promote lactide reformation and a measurable drop in molecular weight. Gates for thin-wall containers should be sized for shear rates below 1 × 10⁵ s⁻¹ to prevent melt fracture and jetting; land lengths below 0.8 mm and adequate cold-well geometry are preferred. Shrinkage for amorphous PLA is typically 0.2–0.6% in the flow direction and 0.2–0.4% transverse, with higher values when nucleated or moulded above 80 °C. On production lines, batch-to-batch variation in melt viscosity can appear if drying conditions drift; melt pressure at the nozzle should be monitored as a real-time indication of hydrolytic degradation.

    Melt rheology and mechanical benchmarks referenced to ISO 527-2 and ISO 178

    Rigid PLA-based grades in this class typically show melt volume-flow rates of 5–20 cm³/10 min at 190 °C and 2.16 kg under ISO 1133-1. Tensile yield strength is commonly 40–65 MPa, tensile modulus 3.0–4.0 GPa, and elongation at break 2–6% under ISO 527-2; flexural modulus is 3.0–4.0 GPa under ISO 178. Notched impact strength for unfilled PLA is generally 2–4 kJ/m² under ISO 179-1/1eA, significantly below that of impact-modified PLA or polyolefins. The rigid designation indicates high modulus and low elongation, making the grade unsuitable for flexible film or stretch applications. Published data for the specific F58 AL40 configuration are limited; design validation should use the supplier’s certificate of analysis rather than generic PLA values. Differential scanning calorimetry under ISO 11357-1 may show a glass transition near 55–60 °C and a cold-crystallization exotherm; for semi-crystalline PLA, the melting endotherm can appear at 150–165 °C. Heat-deflection temperature of amorphous PLA is typically below 60 °C at 0.45 MPa, which constrains use in hot-fill packaging unless crystallinity is induced by mould temperature, nucleating agents, or post-annealing.

    Indicative property envelope for rigid PLA-based compounds
    PropertyTest methodIndicative range
    DensityISO 1183-11.24 g/cm³
    Melt flow rateISO 1133-1 at 190 °C, 2.16 kg5–20 cm³/10 min
    Tensile yield strengthISO 527-240–65 MPa
    Flexural modulusISO 1783.0–4.0 GPa
    Notched impact strengthISO 179-1/1eA2–4 kJ/m²

    Unlike PBAT-rich film grades, which are formulated for elongation at break above 500% and tensile modulus below 0.1 GPa, INZEA F58 AL40 is positioned for rigid, non-impact-modified packaging. Compared with standard PLA homopolymer injection grades, the F58 series may include melt-strength modification or mineral fillers; the AL40 designation identifies a rigid formulation within the series, but exact filler type and loading must be confirmed from the supplier. The operational difference is most evident in thermoforming: unmodified PLA exhibits pronounced sag and non-uniform wall thickness at sheet temperatures above 100 °C, whereas a rigid thermoforming grade is expected to retain a broader forming window through higher zero-shear viscosity and rubbery-plateau storage modulus. The material should not be used as a drop-in replacement for PET in hot-fill applications because its thermal resistance at 0.45 MPa is lower unless crystallinity is fully developed. For contact with fatty or acidic foods, migration resistance and hydrolytic stability must be verified on the finished article, as PLA can undergo ester hydrolysis under high humidity and elevated temperature. Unlike aromatic polyester grades, PLA requires stricter moisture control at every processing stage and shows lower gas-barrier properties, which limits shelf-life performance in oxygen-sensitive packaging unless a barrier coating or multilayer structure is used.

    Hydrolytic degradation during processing behaves as a cliff-edge rather than a linear loss: at moisture contents below 0.025 wt%, melt-viscosity loss is negligible, but above 0.05 wt%, intrinsic viscosity can drop by more than 10% within one residence time. On production-scale twin-screw compounding lines with L/D 40:1, vacuum venting at -0.08 MPa and barrel temperatures not exceeding 210 °C are used to limit lactide reformation. When regrind content exceeds 30 wt%, sheet surface haze and gel counts increase because reprocessing reduces molecular weight and promotes crystallization during drying. In contact-plate thermoforming, a temperature gradient greater than 5 °C across the forming area causes uneven stretching and local thinning. Plug materials should have low thermal conductivity and low friction; syntactic foam or POM-C plugs are typical, and plug speed is adjusted to prevent premature cooling of the sheet before vacuum is applied. Sheet extrusion melt pumps between extruder and die improve thickness consistency to approximately ±2% at throughputs above 100 kg/h. Vacuum holes in the tool should be 0.4–0.6 mm in diameter, and hole spacing should be less than 15 mm in high-stretch areas. These processing boundaries are standard for rigid PLA and are inferred from industrial practice rather than from a product-specific dataset.

    When compostability certification and EU food-contact migration limits are evaluated simultaneously

    Compostability claims under EN 13432 or ASTM D6400 require independent evidence of disintegration, ultimate biodegradation, and ecotoxicity; they do not by themselves establish food-contact suitability. In the EU, the final article must comply with Regulation (EU) No 10/2011, including overall migration below 10 mg/dm² unless specific migration limits apply to individual monomers or additives. Many PLA grades are evaluated under FDA 21 CFR 175.300 or Food Contact Notifications, but the exact F58 AL40 grade must be covered by a valid supplier declaration of compliance. REACH and RoHS obligations apply only where relevant to the finished article and its placement on the market. Storage before processing should be maintained below 60% relative humidity in unopened bags; opened material should be re-dried before use. Contact with alkaline cleaning agents, esters, ketones, and chlorinated solvents is contraindicated, as these chemicals accelerate stress cracking and surface degradation. The product is intended for industrial composting, not for uncontrolled home composting or marine biodegradation.

    Compliance verification matrix
    ClaimStandard or regulationMeasurement or evidence
    Industrial compostabilityEN 13432 / ASTM D6400Disintegration, biodegradation, ecotoxicity
    Food contactRegulation (EU) No 10/2011Overall migration 10 mg/dm²
    Renewable carbonASTM D6866 or EN 16640Biobased carbon fraction
    Moisture contentISO 15512< 0.025 wt%
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