Inzea F58 Al30 Rigid Thermoforming Injection Biodegradable Polylactic Acid

INZEA F58 AL30 Rigid Thermoforming/Injection Biodegradable Polylactic Acid

    • Product Name: INZEA F58 AL30 Rigid Thermoforming/Injection Biodegradable Polylactic Acid
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 426242
    Product Name INZEA F58 AL30
    Product Type Rigid Thermoforming/Injection Biodegradable Polylactic Acid
    Polymer Base Polylactic Acid (PLA)
    Biodegradability Biodegradable
    Compostability Compostable (EN 13432)
    Biobased Yes
    Processing Methods Thermoforming, Injection Molding
    Form Pellets
    Color Natural
    Melting Temperature Typical C 150-160

    As an accredited INZEA F58 AL30 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 AL30 biodegradable PLA is supplied in 25 kg moisture-resistant paper bags, palletized and stretch-wrapped for transport.
    Container Loading (20′ FCL) Container loading (20′ FCL): INZEA F58 AL30 biodegradable polylactic acid resin, packed in 25 kg bags, for rigid thermoforming/injection molding.
    Shipping INZEA F58 AL30 Rigid Thermoforming/Injection Biodegradable Polylactic Acid is non-hazardous. Ship in sealed, moisture-resistant bags or containers under dry, ambient conditions, away from heat, sunlight, and contamination. Standard freight applies; no dangerous goods declaration required. Follow local transport, storage, and environmental regulations. Handle with normal industrial hygiene.
    Storage Store INZEA F58 AL30 Rigid Thermoforming/Injection Biodegradable Polylactic Acid in original sealed packaging in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Prevent moisture absorption; maintain low humidity and temperatures below 30°C. Avoid strong acids, bases, and oxidizers. Follow FIFO rotation and keep away from food, drink, and incompatible materials. Protect packaging from physical damage.
    Shelf Life Shelf life: 12–24 months when stored sealed, dry, below 30°C, away from moisture, heat, and UV in original packaging.
    Application of INZEA F58 AL30 Rigid Thermoforming/Injection Biodegradable Polylactic Acid

    Thermoformed rigid fresh-produce clamshells, hinged bakery containers, and cold deli bases produced from INZEA F58 AL30 are processed as extruded sheet with a thickness range of 0.25 mm to 0.80 mm. The compound is pre-dried at 80 °C for 4–6 h to a residual moisture content below 250 ppm, measured by halogen moisture balance or inline NIR; hopper dryer dew point is maintained below -40 °C during continuous sheet extrusion on a single-screw line with 30:1 L/D barrier screw and screen pack 60/80/100 mesh. Formulation addition ratio in this segment is 96.0–100.0 wt% INZEA F58 AL30, with 0.5–2.0 wt% of a PLA-compatible slip/antiblock masterbatch and 0.5–1.5 wt% of a nucleating masterbatch; the exact loading is adjusted to the sheet line throughput and haze target measured under ASTM D1003-21. Food-contact compliance is governed by EU No 10/2011 with an overall migration limit of 10 mg/dm² and specific migration testing according to the fatty and aqueous simulants assigned to the packaged food type. The sheet is then thermoformed on contact-heat machines where upper and lower sheet surface temperatures are held between 90 °C and 125 °C, with forming air pressure 4–7 bar and mould temperature 30–60 °C for low-crystallinity, low-haze clamshells; for crystallised trays requiring higher heat resistance, the mould temperature is raised to 80–110 °C, but cycle time increases by 1.5–3 s. The most frequent production-scale failure modes are sag deeper than 12% of sheet width at the plug-assist station and web splitting at the clamp frame when sheet temperature deviates by more than ±4 °C from the forming window; both defects are controlled by zoning the infrared heaters and monitoring sheet surface temperature with a contact pyrometer at the oven exit. Terminal products include fruit punnets, hinged salad bowls, mushroom trays, and bakery dome lids. Compostability claims for these articles are validated under EN 13432:2000, which requires ≥90% aerobic biodegradation of the organic fraction within 180 days, disintegration to ≤10% residue on a 2 mm sieve within 12 weeks, and compliance with the ecotoxicity tests set out in the standard.

    Regulatory area Standard designation Requirement
    Food contact overall migration EU No 10/2011 10 mg/dm²
    Aerobic biodegradation EN 13432:2000, ASTM D6400-23 ≥90% in 180 days
    Disintegration ISO 16929:2021 ≤10% remaining on 2 mm sieve after 12 weeks
    Sheet haze ASTM D1003-21 Target set by processor, typically 3–15%

    Can a 32-cavity cutlery tool maintain shot consistency below 0.12 g variance at 8-second cycles?

    In injection moulded disposable cutlery and beverage stirrers, INZEA F58 AL30 is usually dosed at 98.0–99.5 wt% with 0.5–2.0 wt% colour or nucleating masterbatch; the resin must be pre-dried to below 200 ppm moisture using a desiccant dryer with a dew point below -40 °C. The process is carried out in cold-runner 32-cavity tools with mechanical sprue break and air ejection, because PLA solidifies sharply and is prone to stringing if nozzle temperature exceeds 205 °C. Barrel temperature profile from feed to nozzle is set at 165 °C, 185 °C, 195 °C, 200 °C, and 195 °C, with back pressure 5–10 bar hydraulic and screw rotation kept below 120 rpm to limit shear heating. Injection speed is set at 35–70 mm/s and holding pressure at 600–900 bar hydraulic for a shot weight of 12–18 g across the tool; mould temperature is held at 15–25 °C with turbulent-flow water channels to achieve cycle times of 8–12 s. Production-scale bottleneck data show that shot-to-shot weight variance should be maintained below 0.12 g; if variance exceeds this threshold, tine thickness drift and sink marks at the spoon bowl become measurable. Terminal products include teaspoons, soup spoons, forks, and coffee stirrers; knife geometries are typically avoided because the material’s notched Charpy impact under ISO 179-1:2023 is in the range of 3–5 kJ/m², and thin serrated edges fracture during ejection or packing. The material is not suitable for service above 60 °C; heat deflection temperature under ISO 75-2:2013 for 0.45 MPa is generally reported at 50–55 °C for low-crystallinity injection moulded PLA. Compostability claims follow EN 13432:2000 or ASTM D6400-23, and distributors are advised to confirm the specific lot certificate for mineralisation percentage measured under ASTM D5338-15; published data for this specific configuration is limited to supplier technical datasheets and mould trials.

    Where dairy portion lids are thermoformed inline after cast sheet extrusion, the process conflict is not polymer degradation but post-forming curl and thickness variation in the sealing flange area. INZEA F58 AL30 is processed at 98.5–100.0 wt% with 0–1.5 wt% titanium dioxide white masterbatch for light-shielding cream and dairy applications; the melt is extruded through a 0.8–1.2 mm die gap with an automatic gauge control system, and the sheet is cooled on polished chill rolls at 35–45 °C to limit crystallinity while retaining dimensional stability. Sheet thickness for inline forming is maintained at 0.35–0.60 mm, with a thickness standard deviation below 0.02 mm across the web, verified by on-line beta gauge. Forming takes place at sheet surface temperatures of 85–105 °C using plug-assisted pressure forming at 3–5 bar; the mould is held at 20–35 °C for amorphous lids. The critical quality parameter is flatness after conditioning at 4 °C for 24 h, where flange warpage must remain below 1.5 mm over an 85 mm diameter lid; excess orientation from undersized plugs or cold sheet causes lid curl that disrupts heat-seal integrity. Food-contact compliance is required under EU No 10/2011, with overall migration below 10 mg/dm² in simulant D1 50% ethanol for dairy desserts and 3% acetic acid for acidic fruit preparations. Terminal products include dairy dessert lids, coffee shot cup lids, and portion cup closures. Industrial compostability of the formed lids is evaluated according to EN 13432:2000, but the sealing coating or adhesive used on the lid must be separately assessed because it may affect disintegration.

    Injection moulded cosmetic packaging fails not in the press but under 30-day contact with fatty emollients

    Injection moulded cosmetic jars, caps, and inner platforms produced from INZEA F58 AL30 are typically moulded from resin dried to below 200 ppm moisture, dosed at 100 wt% or with 1–3 wt% of an opacifying mineral masterbatch to achieve the required visual barrier and reduce light transmission through the sidewall. The material is processed in hot-runner valve-gate tools with 1–4 cavities, because valve gates minimise gate blush and stringing at melt temperatures below 210 °C; barrel profile is set at 175 °C, 190 °C, 200 °C, 205 °C, and nozzle 200 °C. Mould temperature is maintained at 25–40 °C, injection speed at 20–50 mm/s, and holding pressure at 400–700 bar for wall sections between 1.2 mm and 2.0 mm. Regulatory compliance for cosmetic packaging supplied to EU markets falls under REACH EC No 1907/2006 for chemical safety, with no intentionally added SVHCs above the communication threshold of 0.1 wt%; packaging compatibility with the cosmetic formulation is assessed under ISO 22716:2007 fill-line GMP and packaging stability tests. The operational boundary is chemical resistance: PLA is sensitive to ester-rich oils, terpene-based fragrances, and ketone solvents. Long-term contact tests according to ISO 175:2020 with almond oil at 40 °C for 30 days should be run before approving thick-walled jars for leave-on creams; published data for this specific configuration is limited, but stress whitening and environmental stress cracking may occur if incompatible emollients are filled above 25 wt% in the formulation without an inner barrier component. Terminal products include cosmetic cream jars, loose powder platforms, and caps for lip balm or solid perfume jars, excluding products requiring autoclaving or hot-fill above 60 °C.

    Horticultural propagation trays and plant clips under EN 13432:2000 with a processing-window constraint of 195 °C to 210 °C melt temperature

    Horticultural propagation trays, cell inserts, and plant clips are injection moulded or thermoformed from INZEA F58 AL30 at 100 wt% resin without fillers; the addition of lignocellulosic fillers is avoided in thin-walled cell configurations because it increases brittleness at gate-adjacent sections and reduces melt flow under ISO 1133-1:2022. The melt temperature is restricted to 195–210 °C because thermal degradation accelerates above 210 °C, producing lactic acid oligomers that deposit on mould vents and increase ejection force. Injection moulded plant clips are produced in multi-cavity cold-runner tools with tunnel gates and mould temperatures of 15–25 °C; clip hinge sections are designed with a minimum radius of 0.8 mm and a maximum strain at living hinge below 5% to avoid fracture during repeated closure. Thermoformed propagation trays use sheet thickness of 0.35–0.70 mm, forming at sheet surface temperatures of 90–110 °C, with drainage holes punched after forming rather than in the forming station because punching below 20 °C can initiate microcracks at hole edges. Regulatory and end-of-life compliance for these horticultural articles is referenced to EN 13432:2000, ISO 17088:2021, and, for the United States, ASTM D6400-23; the material is industrially compostable under these standards but should not be described as soil-biodegradable or home-compostable unless separately certified. Terminal products include propagation cell trays, plant clips, greenhouse identification tags, and root-rainer parts. These articles must be collected and sent to an operating industrial composting facility; in-field soil incorporation is not a supported end-of-life claim for this grade.

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    Certification & Compliance
    More Introduction

    INZEA F58 AL30 is a rigid polylactic acid compound supplied by Nurel Biopolymers for sheet extrusion, roll-fed or sheet-fed thermoforming, and injection molding of rigid disposable packaging. The grade is formulated for applications requiring industrial compostability under EN 13432 or ASTM D6400, with a property envelope typical of high-stiffness PLA rather than flexible PBAT or PBS. Manufacturer literature lists a melt flow rate of 6 g/10 min at 190 °C/2.16 kg according to ISO 1133-1, a density of 1.24 g/cm³ according to ISO 1183-1, a tensile yield strength of 60 MPa according to ISO 527-2, and a tensile modulus of 3600 MPa according to ISO 527-2. The notched Charpy impact value is approximately 3.5 kJ/m² (ISO 179-1/1eA), indicating rigid failure behavior rather than ductile deformation. The product is intended for use in cooled tools; continuous service above the Vicat softening temperature of approximately 58 °C (ISO 306/B50) must be avoided.

    Drying and hydrolytic degradation thresholds before melt processing

    Moisture control is the controlling variable for melt processing of this PLA-based grade. PLA undergoes hydrolytic chain scission when residual moisture exceeds 0.025 wt%, and the reaction rate increases with residence time and melt temperature. Drying in a dehumidifying hopper dryer with a dew point of -40 °C to -50 °C at 70–80 °C for 4–6 h is required. If incoming granulate moisture exceeds 0.4 %, drying time is extended to at least 8 h and dryer airflow must be sufficient to maintain hopper outlet temperature. Residual moisture should be verified by Karl Fischer titration or a calibrated moisture analyzer to below 250 ppm before melt processing. On production-scale twin-screw sheet extrusion lines with L/D 30:1 to 44:1, incomplete drying is observed as edge instability, gear pump surging, and falling melt pressure. Melt pressure variance above ±0.5 MPa at constant screw speed is commonly traced to residual moisture or bypass of the drying system.

    Melt temperature is maintained at 190–210 °C for sheet extrusion and 190–205 °C for injection molding. Prolonged residence above 220 °C generates lactide and oligomeric deposits on die lips and vent ports; the condition appears as white plate-out and increased screw torque. Screw speed is kept in the moderate range of 80–150 rpm on 30:1 to 40:1 L/D extruders, depending on barrel diameter, to limit shear heating. Injection unit back pressure is set at 5–15 bar gauge to maintain stable shot size without overworking the melt.

    In sheet-fed thermoforming, the extruded sheet is typically produced at a thickness of 0.3–1.5 mm and processed on plug-assisted or pressure-forming lines with sheet surface temperatures of 90–120 °C. The forming window is narrower than amorphous PET. Below 90 °C the sheet develops stress whitening at corner radii, while above 120 °C sag becomes excessive. The AL30 formulation is designed to reduce sag during index heating; however, draw ratios above 3:1 still require a heated plug at 90–110 °C and forming air pressure of 4–6 bar to prevent wall thinning below 0.15 mm in cup sidewalls. Thermoforming operations running multi-cavity trays with 32 or 48 cavities can reintroduce edge regrind at up to 30 wt% when the regrind is re-dried and the sheet is not used as a direct food-contact sealing layer.

    What separates the AL30 formulation from unmodified PLA, PET and PBAT?

    The differentiation from unmodified PLA is most visible in melt tension during sheet take-off. Unmodified PLA grades of similar melt flow rate show greater neck-in and web flutter on polished three-roll stacks, whereas the AL30 package increases melt strength and allows higher line speeds. The formulated grade maintains a tensile modulus near 3600 MPa, which is approximately 3–5 % higher than several unfilled PLA injection grades and more than an order of magnitude above PBAT film grades in the 50–500 MPa modulus range. Compared with PET, the density is lower by approximately 0.13 g/cm³, but the heat deflection temperature under load is approximately 55 °C (ISO 75-2/B), below that of PET. Oxygen barrier is also inferior to oriented PET; published oxygen transmission values for PLA sheet at 250 µm are commonly in the range 20–40 cm³/(m²·day·bar) at 23 °C and 50 % RH (ASTM D3985), whereas oriented PET of similar thickness is typically below 5 cm³/(m²·day·bar). This grade is therefore not a drop-in replacement for barrier trays unless additional coatings or multilayer structures are used.

    Against PBAT and PBS, rigidity is the decisive difference. PBAT has a tensile modulus near 100 MPa and yields flexible film, while PBS occupies a flexural modulus range of approximately 300–700 MPa. INZEA F58 AL30 occupies a stiff plateau suitable for rigid tray geometries without reinforcing fibers. The trade-off is impact: PBAT remains ductile at low temperature, while this PLA grade exhibits Charpy notched impact below 5 kJ/m² and should not be specified for snap-fit or living-hinge components.

    Compostability certification boundaries and barrier data

    Compostability claims for this product are valid only in industrial composting facilities meeting the temperature and moisture conditions of the test standard. Disintegration is evaluated under EN 13432 or ASTM D6400 using compost at 58 °C and approximately 50 % moisture; these conditions are not replicated in ambient soil or marine water. Certification under one standard does not automatically confer certification under the other, and country-specific conformity programs such as DIN CERTCO or TÜV Austria require separate assessment. For food-contact applications, compliance must be confirmed against 21 CFR 175.300 or Regulation (EU) No 10/2011 as applicable; the grade is not self-certified for all food types and all alcohol or fat levels.

    Standard or methodParameterThreshold or value
    EN 13432Aerobic biodegradation of packaging≥ 90 % conversion to CO₂ in 6 months
    ASTM D6400Aerobic biodegradation of compostable plastics≥ 90 % mineralization within 180 days
    ISO 1133-1:2022Melt flow rate6 g/10 min at 190 °C/2.16 kg
    ISO 1183-1Density1.24 g/cm³
    ISO 527-2Tensile yield strength / modulus60 MPa / 3600 MPa
    ISO 306/B50Vicat softening temperature58 °C

    Injection molding of the grade is carried out with a general-purpose or low-compression screw having a compression ratio of 2.0:1 to 2.5:1 and a check ring suitable for shear-sensitive melts. Mold temperatures between 15 °C and 30 °C are used to shorten cycle time; mold temperatures above 40 °C increase crystallinity but extend cycle and can cause sticking in unpolished cavities. The material solidifies rapidly, so injection speeds are set to fill thin-wall cavities in 0.5–1.5 s, with holding pressure at 60–80 % of injection pressure. Shrinkage after molding is in the range 0.3–0.7 % (ISO 294-4), and tool dimensions are calculated accordingly. For multi-cavity closures or trays, clamp force requirement is approximately 3–5 kN/cm² of projected part area.

    When cold-wall molds and high injection speeds become process risks

    Cold-wall molds below 15 °C can generate jetting and surface flow marks because the melt freezes before the cavity is fully packed. High injection speeds above 150 mm/s generate shear heating that may exceed the 220 °C degradation threshold even when the barrel set temperature is 195 °C. In valve-gated hot-runner systems, dead spots above 10 s residence time lead to yellowing and black specks; hot-runner manifolds are therefore maintained at 190–200 °C with free-flow shutoff nozzles. The product should not be compounded with amine-based antistatic or slip additives without compatibility testing because basic additives can accelerate PLA chain scission in the melt. If regrind is used, it must be re-dried to 250 ppm and limited to 30 wt% in direct food-contact parts unless migration testing under Regulation (EU) No 10/2011 demonstrates compliance.

    Long-term dimensional stability is bounded by the glass transition of PLA near 55–60 °C and by moisture-induced hydrolysis at elevated relative humidity. In high-humidity storage above 85 % RH, tensile strength retention after 60 days may fall below 80 % of the conditioned value. Applications requiring sustained load at 45 °C or above should be validated in the specific geometry and wall thickness, because published data for this specific grade under combined thermal and mechanical load is limited.

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