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INZEA F10BC40S Flexible Home Compostable Film Polylactic Acid

    • Product Name: INZEA F10BC40S Flexible Home Compostable Film 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 324761
    Product Name INZEA F10BC40S Flexible Home Compostable Film Polylactic Acid
    Manufacturer Nurel S.A.
    Polymer Type Polylactic Acid (PLA) based compound
    Form Pellets
    Color Natural
    Density 1.24 g/cm3
    Melt Flow Rate 4.5 g/10 min at 190°C and 2.16 kg
    Melting Point 150°C
    Vicat Softening Temperature 55°C
    Tensile Strength 25 MPa
    Elongation At Break 350%
    Tensile Modulus 500 MPa
    Tear Resistance 60 N/mm
    Dart Drop Impact 200 g
    Haze 5%
    Gloss 85 at 45°
    Biobased Content 40%
    Compostability Certification OK compost HOME; EN 13432
    Food Contact Suitable for food contact
    Processing Method Blown film extrusion
    Recommended Film Thickness 20-50 µm

    As an accredited INZEA F10BC40S Flexible Home Compostable Film Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing INZEA F10BC40S Flexible Home Compostable Film Polylactic Acid packaged in 25 kg polyethylene-lined paper bags, shipped on pallets.
    Container Loading (20′ FCL) 20′ FCL container loaded with INZEA F10BC40S flexible home compostable polylactic acid film, palletized, wrapped, and secured for ocean shipment.
    Shipping INZEA F10BC40S Flexible Home Compostable Film Polylactic Acid is not classified as dangerous goods for road, rail, sea, or air transport. No UN number, hazard class, or packing group applies. Ship dry, sealed, and at ambient temperature, protected from moisture, direct sunlight, contamination, and physical damage. Follow local regulations and manufacturer instructions.
    Storage Store INZEA F10BC40S in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep in original sealed packaging on pallets, off the floor, and separated from strong oxidizers, acids, and bases. Avoid prolonged high humidity or temperatures above recommended limits to prevent degradation, blocking, or loss of film properties. Follow FIFO stock rotation.
    Shelf Life Typical shelf life is 12 months when stored unopened, dry, at ambient temperature, protected from direct sunlight, heat, and moisture.
    Application of INZEA F10BC40S Flexible Home Compostable Film Polylactic Acid

    Blown film operations for home-compostable fresh-produce packaging based on INZEA F10BC40S flexible polylactic acid typically begin with desiccant drying at 70°C for 4 h until residual moisture falls below 250 ppm. On a 55 mm single-screw extruder with L/D 30:1 and a barrier screw, barrel temperatures are set at 165°C, 170°C, 175°C, 180°C, and adapter/die at 180°C. The die gap is held at 1.0 mm, the blow-up ratio at 2.8:1, and the lay-flat width at 330 mm for a 25 µm film. Slip and antiblock masterbatch is added at 3–5 wt% because PLA film surfaces develop blocking under roll compression when rewind tension exceeds 0.15 N/mm. The converted flow pack for cherry tomatoes or washed lettuce is verified for food-contact migration under Commission Regulation (EU) No 10/2011 and for organic recovery under EN 13432:2000; the final film must also pass the 12-week disintegration threshold and ecotoxicity criteria before a home compost claim is used. Home compostability under TÜV Austria OK compost Home requires a separate certification scope because the ambient pile remains below 45°C for extended periods. Haze, dart impact to ASTM D1709 Method A, and tensile properties to ASTM D882 are applied as incoming quality gates. Melt temperatures above 190°C or residual moisture above 400 ppm produce molecular weight reduction, gel specks, and unstable bubble geometry.

    StandardParameterCriterion
    EN 13432:2000Ultimate aerobic biodegradation≥90% within 180 days relative to cellulose reference
    EN 13432:2000Disintegration after 12 weeks≥90% of fragments <2 mm
    EN 13432:2000EcotoxicityPlant growth and germination ≥90% of blank compost
    EN 13432:2000Heavy metalsBelow Annex A limits

    Can a 12 µm Agricultural Mulch Film Survive Mechanical Laying Without Orientation Tear?

    Black agricultural mulch film based on INZEA F10BC40S is generally produced at 12–25 µm on a 45 mm blown film line with L/D 24:1 and a double-flighted barrier screw. Carbon black masterbatch is added at 6–8 wt% for light exclusion; the carrier resin must be PLA-compatible to avoid bubble instability and melt fracture at the 1.2 mm die gap. Mechanical transplanters and mulch layers operating at 5–7 km/h tear the film at the planting shoe if directional tear resistance is below the machine's peak acceleration force. Elmendorf tear is therefore measured to ASTM D1922 and dart impact to ASTM D1709 Method B as acceptance tests. Home compostability under EN 13432:2000 does not by itself satisfy agricultural soil performance; soil biodegradable mulch film is qualified under EN 17033:2018, which requires ≥90% aerobic biodegradation within 24 months, ecotoxicity testing by OECD 208, and no adverse impact on soil organisms. Published data for this specific soil application is limited, so the film must be qualified on the target crop row spacing and soil temperature. The terminal product is a perforated black ground cover for tomato and pepper cultivation, with 20 mm holes at 300 mm intervals. Processing above 190°C or re-extrusion of post-use field film above 10 wt% causes viscosity loss that prevents uniform gauge control on clay-coated soils with high surface friction.

    Shopping Bag Film from 20 µm Tubular Stock with 25% Post-Industrial Edge Trim

    Conversion of INZEA F10BC40S into checkout bags uses a 50 mm single-screw extruder with L/D 30:1, a continuous screen changer fitted with 100 µm mesh, and a die gap of 0.9 mm. In-line edge trim is ground on a low-shear granulator and re-fed at 25 wt% maximum because higher regrind concentrations lower melt viscosity and cause bubble sag before the frost line. The regrind fraction is dried with virgin pellets to below 300 ppm moisture; a separate infrared drying step at 65°C for 3 h is required when edge trim has absorbed ambient moisture in unheated storage areas. Melt temperature is maintained at 175–185°C and blow-up ratio at 3.0:1; these settings balance transverse direction tear against machine direction dart impact in the finished bag. Bottom sealing is performed at 120–130°C with 0.8 s dwell, and chilled rollers are positioned after the seal bars to prevent blocking. The end product is a home-compostable fruit bag or shopping bag with a wall thickness of 20 µm. Compliance is verified under EN 13432:2000 and REACH for the finished article; food contact suitability for unpackaged produce is assessed under Regulation (EU) No 10/2011 on the sealant side. If surface resistivity exceeds 10¹² Ω/sq by ASTM D257, antistatic masterbatch is added at 1–2 wt% to prevent bag-machine misfeeds.

    Extrusion coating of INZEA F10BC40S onto 40 g/m² kraft paperboard for home-compostable foodservice articles is run on a coating line with a 75 mm extruder, L/D 30:1, and a 900 mm slot die. Melt temperature is kept between 180°C and 190°C; the coating weight is set at 15 g/m² at a line speed of 120 m/min. The paperboard is corona-treated in-line to 42–46 mN/m; without this treatment, adhesion falls below the required 1.5 N/15 mm peel strength measured by TAPPI T540. A water-based polyurethane primer at 0.3–0.5 g/m² dry coat is used on boards with high ash content or dense calendering. The coated board is formed into sandwich wedges, cups, and plates; heat sealing of the PLA coating to itself is achieved at 120–140°C with 0.5 s dwell. Food-contact compliance for the coated article is tested under Regulation (EU) No 10/2011 with total migration below 10 mg/dm²; the home compost claim requires EN 13432:2000 and confirmation of the final laminate in the TÜV Austria OK compost Home certificate register. Processing above 200°C generates volatile lactide, visible smoke, and edge instability at the coating nip.

    When the Same Grade Is Processed as a 30 µm Twist-Wrap Web

    Twist-wrap confectionery film is produced with a 30 µm thickness on a 45 mm blown film or cast film line; blown film uses a 0.8 mm die gap and a 2.5:1 blow-up ratio, while cast film requires a chill roll at 20–25°C. The grade is processed without external plasticizer; where additional twist retention is required, a bio-based slip masterbatch is added at 1–2 wt%. Deadfold angle retention is measured by a 180° fold test after 30 s at 23°C and 50% RH; a retention angle below 60° causes unwinding on high-speed twist wrappers. Tensile elongation in the machine direction is monitored to ASTM D882 because elongation below 150% produces fracture at the wrapper's necking station. Flexographic printing is performed with low-voc water-based inks; the film surface is treated to 38–40 mN/m before the print deck. The end product is a printed twist wrap for candies and chocolate pieces. Compliance includes Regulation (EU) No 10/2011 for food contact and EuPIA GMP for the ink system; compostability of the printed film is verified under EN 13432:2000 on the final printed article, not solely on the unprinted film.

    Home-compostable window patches for rigid paperboard cartons are produced from INZEA F10BC40S on a 35 mm cast film line with L/D 25:1, a 0.5 mm die gap, and a chill roll at 20°C. The film is laminated to the interior of the paperboard window using a starch-based adhesive at 3–5 g/m² wet laydown with tunnel temperature at 70°C. The window film thickness is 25 µm; haze measured to ASTM D1003 is controlled below 8% to preserve visual product inspection through the window. The end product is a compostable window carton for dry goods such as tea bags, solid cosmetics, or confectionery. Compliance for the laminate includes EN 13432:2000 and Regulation (EU) No 10/2011 where the window contacts food; the adhesive system must be selected from positive lists within the same food-contact framework. Dimensional stability during tunnel lamination is the primary control: film shrinkage above 1% in the machine direction causes window distortion and poor registration on the window patcher.

    Seal initiation below 100°C is obtained when the sealant layer is coextruded with a home-compostable copolyester

    Heat-sealed lidding film for PLA food trays uses a two-layer coextruded structure in which INZEA F10BC40S forms the core and print skin, and a low-melting home-compostable copolyester forms the sealant layer. The total film thickness is 25–30 µm; the sealant layer is held at 15–20% of total thickness. On a 55 mm coextrusion line with L/D 30:1, the sealant extruder is run at 145–155°C, while the INZEA layer is run at 170–180°C; the die is held at 180°C. Seal initiation temperature is measured by ASTM F1921 on a heat-seal tester with 0.5 s dwell and 40 psi pressure; the target heat-seal strength is 3 N/15 mm at 100–110°C for tray lidding by ASTM F88. The end product is used for chilled ready-meal trays made from home-compostable PLA or paperboard. Compliance is verified under Regulation (EU) No 10/2011 for fatty and aqueous food simulants, and the complete lidding film is certified under EN 13432:2000. Seal contamination by surface oil from the tray rim reduces seal strength below 2 N/15 mm; therefore tray rims are cleaned or selected with low surface oil migration.

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    Certification & Compliance
    More Introduction

    INZEA F10BC40S is a flexible film extrusion grade based on polylactic acid and modified with a biodegradable copolyester/plasticiser fraction to reduce the brittleness associated with PLA homopolymer. The product is supplied in pellet form for continuous conversion on blown-film and cast-film equipment. Intended end uses include home-compostable produce bags, organic-waste liners, lightweight carrier films, and thin-gauge overwrap where ambient-temperature biological disintegration is specified. The designation F10BC40S identifies a film-specific PLA formulation with a flexibility profile distinct from standard rigid PLA grades. Because lot-to-lot variation affects melt rheology and film properties, the values provided in this document are representative conversion-control data and should be verified against the active supplier certificate of analysis before barrel-profile programming.

    Prior to melt extrusion, the pellet feedstock is dried in a desiccant dryer at 60–70 °C for 4–6 h. The target residual moisture is below 0.025 wt%, as determined by Karl Fischer titration or a calibrated moisture balance. At plant relative humidity above 60 %, hopper residence time should be minimised because PLA-based systems are susceptible to hydrolysis-induced molecular weight loss at melt temperature. A closed feed hopper with a dry-air purge at a dew point of −40 °C or lower is recommended for unconditioned production areas. Pellets exposed to ambient air for more than 30 min before entering the extruder should be re-dried when viscosity drift or bubble defects are observed.

    A typical blown-film line uses a single-screw extruder with an L/D ratio of 28:1 to 33:1 and a compression ratio of 2.5:1 to 3.0:1. The barrel profile begins with a feed throat temperature of 30–40 °C, followed by barrel zones increasing from 145 °C to 165 °C. Adapter and die zones are generally held at 155–165 °C. Melt temperature at the die is maintained between 150 °C and 170 °C; excursions above 180 °C accelerate chain scission and reduce bubble tension. Die gap settings from 0.8 mm to 1.2 mm and blow-up ratios from 2.0:1 to 3.5:1 provide a stable bubble with sufficient transverse orientation on conventional single-lip air rings.

    What Limits the Bubble Stability of F10BC40S in High-Draw-Down Thin-Film Production?

    Bubble stability in F10BC40S is controlled by the temperature-dependent elongational viscosity of the PLA-rich phase and the compatibility of the copolyester/plasticiser fraction. At melt temperatures below 150 °C, higher-viscosity PLA domains can produce melt fracture at the die lip and visible die lines at elevated screw speeds. Above 180 °C, the biodegradable copolyester fraction can begin to degrade thermally, and the bubble loses melt tension, resulting in sag and gauge-band formation. Frost-line height is typically set between 1.5 and 3.0 die diameters; a higher frost line can increase crystallinity development but may reduce transverse toughness if the bubble is drawn too rapidly. A draw-down ratio above 5:1 can cause asymmetric necking and poor transverse-direction gauge uniformity on single-lip air rings. On a 45 mm single-screw extruder with a 30 L/D barrel and a 200 mm spiral mandrel die, melt-pressure variation at the screen changer is typically kept below 10 % to avoid bubble pumping and film thickness oscillation. Dual-lip air rings or internal bubble stabilisation are generally required when producing film below 25 µm.

    Mechanical, Thermal, and Barrier Data from Standardized Test Methods

    The following values are representative of 50 µm monolayer blown film produced under the processing conditions described above. They are not specification limits and may shift with gauge, orientation, additive package, lamination structure, and post-extrusion ageing.

    PropertyUnitTest methodTypical range or value
    Melt flow rate, 190 °C / 2.16 kgg/10 minISO 1133-1:20223.0–5.0
    Densityg/cm³ISO 1183-1:20191.24–1.27
    Melting temperature, DSC second heating°CISO 11357-3:2018148–155
    Glass transition temperature°CISO 11357-2:202045–55
    Tensile stress at break, machine directionMPaISO 527-3:201815–22
    Tensile strain at break, machine direction%ISO 527-3:2018300–500
    Tensile modulus, machine directionMPaISO 527-3:2018150–300
    Elmendorf tear resistance, transverse directionN/mmISO 6383-2:198315–35
    Water vapour transmission rate, 23 °C, 85 % RHg/(m²·day)ISO 15106-2:2005150–350
    Oxygen transmission rate, 23 °C, 0 % RHcm³/(m²·day·bar)ISO 15105-2:2003300–700

    The water vapour transmission rate of F10BC40S is higher than that of polyolefin films and is an inherent consequence of the PLA-based chemistry. Applications requiring desiccated shelf-life conditions should be evaluated with barrier testing of the complete laminate rather than with single-film data.

    When Comparative Selection Against PLA Homopolymer and PBAT-Rich Films Determines Grade Choice

    Against unmodified PLA homopolymer film, F10BC40S shifts the failure mode from brittle cracking to ductile deformation. The tensile modulus is roughly one-tenth to one-eighth that of PLA homopolymer, while elongation at break rises from below 10 % to the 300–500 % range. This change makes the grade suitable for bag applications requiring fold resistance and puncture tolerance rather than rigid thermoformed structures. The comparative data below are representative and are provided to guide polymer selection, not as a substitute for finished-film verification.

    ParameterINZEA F10BC40SUnmodified PLA homopolymer filmPBAT-rich home-compostable film
    Tensile modulus, machine direction150–300 MPa2000–3500 MPa50–150 MPa
    Elongation at break, machine direction300–500 %3–10 %400–800 %
    Melt processing window150–170 °C170–210 °C130–160 °C
    Home compostabilityDeclared for the gradeNot typicalCommonly certified
    Water vapour barrierModerateModerateModerate-to-high transmission

    Compared with PBAT-rich home-compostable compounds, F10BC40S retains higher stiffness and a more PLA-like thermal profile. These characteristics can improve film-opening behaviour on automated bag machines but reduce ultimate elongation and low-temperature impact resistance relative to softer PBAT-dominant systems. The selection between F10BC40S and a PBAT-rich compound therefore depends on whether the converter prioritises stiffness, gauge control, and renewable-carbon positioning over maximum stretch and puncture propagation at very high deformation rates.

    On the converting floor, F10BC40S is corona-treated before printing because the as-extruded surface energy is typically below 35 mN/m. Treatment to 40–42 mN/m is commonly required for water-based ink adhesion. Kinetic coefficient of friction, measured under ISO 8295:1995, is usually maintained in the 0.25–0.45 range with the slip additive package. If the film is used on vertical form-fill-seal equipment, the heat-seal temperature and dwell time should be mapped against gauge because the PLA-rich phase narrows the seal plateau relative to low-density polyethylene. Heat-seal jaw temperatures are generally set between 90 °C and 110 °C, but seal strength is strongly dependent on dwell time, jaw pressure, and film thickness. Unsupported films below 15 µm may require internal bubble stabilisation and reduced melt temperatures to prevent puncture and wrinkle defects during slitting.

    Home-compostable claims for INZEA F10BC40S are assessed through certification schemes rather than inferred from polymer composition alone. The grade is positioned for ambient-temperature disintegration under certification schemes such as TÜV AUSTRIA OK compost HOME. Where industrial compostability is also declared, compliance with EN 13432:2000/AC:2005 is documented through biodegradation, disintegration, and ecotoxicity testing. Relevant test methods include ISO 14855-2:2018 for controlled aerobic biodegradation, ISO 16929:2021 for disintegration, and OECD 208 terrestrial plant growth tests for ecotoxicity. The converter should obtain the current certificate number and confirm that the final film, including inks, adhesives, and coatings, falls within the certified formulation envelope. Raw-pellet data alone do not establish final-article home-compostable or food-contact compliance.

    F10BC40S is suitable for low-temperature and ambient-temperature flexible packaging where the use temperature does not exceed 40–50 °C. The film is not appropriate for hot-fill, boil-in-bag, or heat-assisted cooking applications unless the complete structure has been tested for dimensional stability, seal integrity, and migration under the intended time-temperature profile. If food contact is required, migration testing under Regulation (EU) No 10/2011 or the relevant local legislation should be performed on the finished laminate because low-molecular-weight plasticiser and copolyester components can migrate into fatty food simulants. Film structures containing reactive inks, high-acid food simulants, or aggressive cleaning agents should be validated under the intended packaging conditions before commercial release.

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