Inzea F10 Flexible Home Compostable Film Polylactic Acid

INZEA F10 Flexible Home Compostable Film Polylactic Acid

    • Product Name: INZEA F10 Flexible Home Compostable Film 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 622423
    Productname INZEA F10 Flexible Home Compostable Film Polylactic Acid
    Manufacturer Nurel S.A.
    Materialtype Polylactic acid (PLA)-based compostable film grade
    Form Pellets
    Color Natural/white
    Density 1.25 g/cm³
    Meltflowindex 2-4 g/10 min at 190 °C and 2.16 kg
    Meltingpoint 145-155 °C
    Vicatsofteningtemperature 55 °C
    Processingtemperature 150-180 °C
    Processingmethod Blown film extrusion
    Tensilestrength 25-35 MPa
    Elongationatbreak 300-400%
    Tensilemodulus 500-1200 MPa
    Tearresistance 50-100 N/mm
    Watervaportransmissionrate 100-200 g/m²/day
    Biodegradation >90% in 180 days under home composting conditions
    Compostability Home compostable
    Certification OK compost HOME
    Biobasedcontent >60%
    Foodcontact Suitable for food contact
    Shelflife 12 months
    Storageconditions Dry environment below 30 °C

    As an accredited INZEA F10 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 F10 Flexible Home Compostable Film Polylactic Acid supplied in 25 kg moisture-resistant paper sacks, palletized and stretch-wrapped for transport.
    Container Loading (20′ FCL) INZEA F10 flexible home compostable polylactic acid film loaded into a 20′ FCL container, palletized, stretch-wrapped, and securely braced for transport.
    Shipping INZEA F10 Flexible Home Compostable Film Polylactic Acid is not classified as dangerous goods for transport by DOT, IMDG, IATA, or ADR. Ship in sealed, moisture-barrier packaging, palletized in original cartons. Protect from heat, UV, and moisture. Store cool and dry. Use standard handling precautions.
    Storage Store INZEA F10 film in its original sealed packaging in a cool, dry, well-ventilated area out of direct sunlight. Recommended conditions: 15–25°C and 30–60% relative humidity. Keep away from heat, open flames, moisture, strong oxidizers, and odorous substances. Avoid prolonged UV exposure and mechanical damage. Use first-in, first-out stock rotation to maintain film quality and compostability.
    Shelf Life Shelf life: 12 months from manufacture when stored unopened in a cool, dry place, protected from sunlight and moisture.
    Application of INZEA F10 Flexible Home Compostable Film Polylactic Acid

    On a 45 mm single-screw blown film line with a 25:1 L/D barrier screw and a 1.8 mm die gap, INZEA F10 is processed as supplied after desiccant drying at 70 °C for 4 h to a residual moisture below 250 ppm. The base resin is used at 100 wt%; post-industrial edge trim is reintroduced at 15–20 wt% after re-drying, while slip and antiblock masterbatch is added at 0.5–2.0 wt% to prevent blocking during reel winding. Melt temperature measured at the die is held between 170 °C and 185 °C, blow-up ratio is kept at 2.8:1 to 3.5:1, and frost line position is maintained at 6–8 die diameters. Film gauges between 15 µm and 25 µm are converted into 10–30 L kitchen caddy liners and 80 L organic waste sacks. Compliance is assessed against EN 13432:2000 for EU industrial compost, NF T51-800:2015 and OK compost HOME for home compost claims, and AS 5810-2010 for the Australian market, with aerobic biodegradation measured by ISO 14855-1 and disintegration under ISO 20200. Production-scale experience shows that bubble instability and melt tear occur when the die temperature exceeds 190 °C, while die-lip deposition becomes measurable on runs longer than 6 h unless purge intervals are maintained. Batch-to-batch gauge variation of ±2 µm has been observed when incoming pellets exceed 0.4 wt% moisture, and storage at relative humidity above 60 % requires the drying interval to be extended to 6 h before extrusion.

    Compliance checklist for home compostable film applications using INZEA F10
    Application domainRegulatory or normative instrumentTest method designation
    Organic waste bag home compostEN 13432:2000 / NF T51-800:2015ISO 14855-1, ISO 20200
    Australian home compostAS 5810-2010AS ISO 14855, AS ISO 16929
    US compostable packagingASTM D6400-23ASTM D5338-15, ISO 16929
    Food contact packagingCommission Regulation (EU) No 10/2011EN 1186-1:2002
    Household refuse sack leakageEN 13592:2017Whole-bag leak resistance method

    What Limits Sealing Integrity in High-Speed Caddy Liner Conversion?

    The downstream conversion step imposes a sealing window that is narrower than that of low-density polyethylene. On a rotary side-weld bag machine running 80 cycles/min, heat-seal jaw temperature is set from 110 °C to 135 °C with a dwell time of 0.2–0.6 s and a jaw pressure of 0.3–0.6 N/mm². Seal strength is evaluated according to ASTM F88/F88M-23; seal initiation is observed near 100 °C, and film thinning or micro-pinholes appear when jaw temperature exceeds 145 °C. Sealant performance is governed by the base polymer composition; the film is used at 100 wt% INZEA F10, and no ethylene-vinyl acetate-based adhesive is added because the resulting terpolymer would no longer meet the home compostability requirement of NF T51-800:2015. If corona treatment is applied before printing, surface energy is controlled to 38–42 mN/m and the film is allowed to rest 24 h at 50 % RH before sealing to avoid backside transfer. Terminal products include printed 10 L caddy liners with side-weld seams and bottom-fold seals, as well as 30 L municipal organic waste bags where leakage resistance is tested by EN 13592:2017. The main process conflict is the narrow gap between the temperatures required for adequate seal strength and the onset of shrinkage at the jaw line; when machine speed varies by more than ±5 cycles/min, contact time changes enough to produce low-seal or hole defects within the same roll.

    Produce Roll Bag Film: Perforation Tear and Puncture Requirements

    Produce roll bag conversion differs from caddy liner production in that the film is perforated after blowing and must retain propagation tear resistance sufficient to prevent premature separation while still allowing manual detachment. The film is extruded between 20 µm and 30 µm on a 60 mm single-screw line with 28:1 L/D, 2.0 mm die gap, and blow-up ratio 3.0:1. Anti-fog masterbatch is added at 1–3 wt% when the bags are intended for cold-chain produce storage, and slip masterbatch at 0.3–1.0 wt% is used to control unwind tension on automated roll dispensing. Tear resistance is measured by ISO 6383-2:2015 trouser tear and puncture resistance by ASTM D5748-95(2019) film puncture test; converters require tear initiation values above 20 N/mm and dart impact values above 100 g for 25 µm film under ASTM D1709-22 Method A. The terminal product range includes pre-opened produce roll bags for fruit and vegetables, bread bags for bakery counters, and window bags for dry baked goods. Certification under Commission Regulation (EU) No 10/2011 is required for direct food contact, with overall migration below 10 mg/dm² according to EN 1186-1:2002, while the compostability claim remains under EN 13432:2000 and OK compost HOME. In commercial packing lines, the primary failure mode is not film puncture but perforation crack propagation when perforation depth exceeds 40 % of film thickness; therefore, perforation blades are set to leave a residual web of 0.3–0.6 mm per 10 mm segment.

    For dry food overwrap, moisture transport through a 25 µm INZEA F10 film is the controlling design parameter, and converters compare it with biaxially oriented polypropylene rather than with LDPE because the PLA-based film exhibits higher water vapour transmission at equivalent gauge. The film is used at 100 wt% as the base layer; mineral antiblock masterbatch is added at 0.5–1.5 wt% to permit reel unwind on horizontal form-fill-seal equipment without blocking. The downstream process is a horizontal flow wrapper running 40–70 packages/min, with fin-seal jaw temperature 110–130 °C and film tension 8–12 N per 500 mm web width. Compliance under Commission Regulation (EU) No 10/2011, EN 1186-1:2002, and EC 1935/2004 requires migration testing with simulant A or D for dry solids, while the home compostability claim is certified under EN 13432:2000. Oxygen transmission rate is measured by ASTM D3985-24 on dry film, and water vapour transmission rate is evaluated by ISO 15106-3:2005. Terminal products include overwrap for dry bakery products, tea cartons, confectionery trays, and shelf-ready dry goods where the moisture barrier requirement is below 20 g/m²·day at 38 °C and 90 % RH; for higher-moisture food, published data for this specific configuration is limited and additional barrier coating qualification is required.

    When Home Compostable Film Replaces LDPE in E-commerce Mailer Lines

    E-commerce mailer production differs from food packaging in that the film must survive automatic packing, logistics abrasion, and ultrasonic or impulse sealing without the yield and puncture behaviour of LDPE. INZEA F10 is processed at gauge 30–50 µm on a 70 mm blown film line with 25:1 L/D barrier screw, die gap 2.2 mm, and blow-up ratio 2.5:1. The base polymer is used at 100 wt%; processing aid masterbatch may be incorporated at 0.2–0.8 wt% to reduce melt fracture when the line runs above 0.8 kg/h per mm of die diameter. Film is sealed by impulse welding at 140–160 °C for 0.5–1.2 s, with seam strength measured by ASTM F88/F88M-23 and elongation at break evaluated by ISO 527-3:2018. Terminal products include compostable apparel mailers, document envelopes, and e-commerce garment polybags where the printed brand owner requires home compostability under NF T51-800:2015 or OK compost HOME. The mechanical requirement is set by the ISTA 3A parcel test and internal drop-test protocols; converters report that films below 40 µm show corner puncture during automated bagging of rigid apparel accessories, while films above 60 µm exceed the stiffness limit for high-speed fold-over sealing. The operational boundary is that the film should not be stored at relative humidity above 60 % for more than 48 h before conversion because moisture uptake reduces seal seam intermolecular diffusion and increases pinhole formation at seam edges.

    Tissue Overwrap Mechanical Behaviour on Side-Weld Bag Lines

    For household tissue overwrap, the film is converted on side-weld bag lines where gauge uniformity and static dissipation are more critical than oxygen barrier. The film is extruded at 18–22 µm with 100 wt% INZEA F10 and antistatic masterbatch at 0.3–0.8 wt% to reduce dust attraction on high-speed tissue packing. Sealing is performed at 115–130 °C and 0.4 s dwell; seal strength is measured by ASTM F88/F88M-23, and film slip is monitored by ISO 8295:1995 coefficient of friction. The terminal product is clear overwrap for toilet paper rolls, kitchen towel bundles, and facial tissue multipacks. Compliance falls under EN 13432:2000 for compostable packaging and Commission Regulation (EU) No 10/2011 where the overwrap does not contact food directly but may be used near food retail. The main failure mode observed on production lines is static-induced film cling causing misalignment of the side seal when film-to-film static charge exceeds 2.0 kV; the antistatic masterbatch must therefore be pre-dispersed and the film conditioned at 45–55 % RH for 12–24 h before slitting.

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    Certification & Compliance
    More Introduction

    INZEA F10 Flexible Home Compostable Film Polylactic Acid is a polylactic acid-based thermoplastic compound formulated for blown and cast film extrusion in short-shelf-life packaging, compost caddy liners, produce bags, bread bags, and light carrier bags where the finished article must fragment and biodegrade in home composting conditions. The F10 designation identifies the flexible film extrusion member of the INZEA product line, rather than a rigid injection moulding grade. The base polymer is polylactic acid with a proprietary flexibility-modifying additive package; the compound is not a starch-based film and does not share the moisture sensitivity profile of thermoplastic starch compounds. Incoming pellets are specified at a moisture content no greater than 250 ppm. Before extrusion, the manufacturer-prescribed drying condition is 80 °C for 4 h in a desiccant dryer with a dew point no higher than -40 °C. Melt flow rate is measured under ISO 1133-1:2022 at 190 °C with a 2.16 kg load; solid density is determined under ISO 1183-1:2019. The current certificate of analysis carries lot-specific values, and those values supersede generic product literature for process setup.

    Applications are concentrated in monolayer blown-film structures, although cast film and lamination are technically feasible. The material is used where a home compostable end-of-life claim is specified by the retailer or waste collector. Conversion lines should be configured with closed resin conveying and hopper dryers because moisture regain after drying is a significant process variable. For printed film, corona treatment is normally required before flexographic or digital water-based ink application; the treatment level must be re-qualified on the final film because surface energy decay depends on storage humidity, additive bloom, and film crystallinity.

    What stabilizes bubble geometry during INZEA F10 blown-film extrusion?

    On a conventional three-zone single-screw extruder with a length-to-diameter ratio of 30:1 or 33:1 and a barrier screw with mixing elements, INZEA F10 requires a barrel temperature profile that rises from 30 °C to 40 °C at the feed throat to 160 °C to 175 °C in compression and metering zones. The die zone is commonly held at 175 °C to 185 °C; excursions above 200 °C increase the random chain-scission rate of polylactic acid and generate gel particles. The die gap is set from 0.8 mm to 1.2 mm, and the blow-up ratio is kept between 2.0 and 3.0 to control transverse tear anisotropy. Frost line height is adjusted so that the ratio of free-standing melt length to die diameter remains between 1.5 and 4.0; lower values produce excessive cooling stress, while higher values destabilise the bubble because PLA melt strength is lower than that of LDPE at equivalent melt temperature. Film thickness uniformity is monitored on-line with a capacitance or near-infrared gauge, and a stable bubble is normally observed when thickness variation remains below ±5% across a full reel. Published production data for INZEA F10 on specific high-output lines with internal bubble cooling is limited; processors using internal bubble cooling report bubble flutter unless exhaust air temperature is maintained below 25 °C and dew point below 0 °C.

    Representative values for INZEA F10 flexible film are summarised in Table 1. The values are compiled from manufacturer product literature and are not batch-release specifications; the certificate of analysis is the controlling document for acceptance testing.

    ParameterTest methodRepresentative range
    Melt flow rate at 190 °C, 2.16 kgISO 1133-1:20222.0 g/10 min to 6.0 g/10 min
    Solid densityISO 1183-1:20191.23 g/cm³ to 1.25 g/cm³
    Tensile strength at break, 50 µm cast filmISO 527-3:201830 MPa to 55 MPa
    Tensile elongation at break, 50 µm cast filmISO 527-3:2018>100%
    Melting temperature, DSC second heatISO 11357-3:2018150 °C to 165 °C
    Glass transition temperature, DSCISO 11357-2:202055 °C to 60 °C
    Moisture content at supplyISO 15512:2019≤250 ppm

    Material specifications and the test standards governing compostability claims

    Compostability claims for INZEA F10 must be evaluated at the final-article level, not on the resin alone. For home composting, the reference standard is EN 17427:2022, which includes characterisation, biodegradation under home compost conditions, disintegration, and ecotoxicity; TÜV Austria’s OK compost HOME and DIN CERTCO home compostable certification are typical third-party routes. The industrial compostability route follows EN 13432:2000, with biodegradation under ISO 14855-1 or ISO 14855-2, disintegration under ISO 16929 or ISO 20200, and an ecotoxicity test with higher plants. Compostable certification under EN 13432:2000 requires a minimum of 90% biodegradation, measured as carbon dioxide evolution relative to a positive reference within a maximum test duration of 6 months. Home compost protocols allow lower mesophilic temperatures and may extend the observation window; a material certified for industrial composting is not automatically certified for home composting because disintegration at 58 °C does not predict disintegration in a domestic bin operating between 20 °C and 30 °C at the exterior and possibly 40 °C to 45 °C in the core. Published data for INZEA F10 in anaerobic digestion, freshwater, or marine degradation matrices is limited; those end-of-life pathways should not be claimed from home compost certification alone.

    Where a converter evaluates INZEA F10 against low-density polyethylene or PBAT-rich compostable films, the first-order differences are density, elongation at break, modulus, barrier profile, and heat-seal behaviour. LDPE film in 50 µm gauge has a density below 0.930 g/cm³; INZEA F10 is approximately 25% denser, which reduces area yield per kilogram and must be entered into packaging cost-per-unit calculations. PBAT-rich compostable films typically display higher elongation at break and lower tensile modulus than PLA-based films; INZEA F10 trades some ultimate strain for a higher modulus, which may support down-gauging in applications where stiffness limits machinability. Table 2 is a directional engineering comparison, not a specification; final values shall be verified on the target film structure because additives, thickness, orientation, and lamination alter properties.

    PropertyINZEA F10 relative to LDPEINZEA F10 relative to PBAT-rich compostable filmINZEA F10 relative to unmodified PLA film
    Density under ISO 1183-1:2019HigherSimilarSimilar
    Tensile elongation at breakLowerLowerHigher
    Tensile modulusHigherHigherLower
    Water vapour transmission rateHigherSimilar to lowerSimilar
    Oxygen transmission rateHigherSimilarSimilar to lower

    When replacement of LDPE triggers shelf-life and sealing revisions

    Substituting INZEA F10 for LDPE in a vertical form-fill-seal line changes the thermal seal response, hot-tack window, and barrier shelf-life. Seal initiation temperature for PLA-based flexible films is frequently lower than that of LDPE, but the hot-tack plateau is narrower; therefore jaw temperature, dwell time, and seal pressure settings must be re-derived on the target material rather than transferred from LDPE. Heat seal strength is tested under ASTM F88/F88M or ISO 527-3; hot-tack is tested under ASTM F1921/F1921M. Oxygen transmission rate is measured by ISO 15105-2 and water vapour transmission rate by ISO 15106-3 on the finished film or laminate. PLA-based films typically present lower oxygen barrier and higher water vapour permeability than LDPE, which modifies the equilibrium modified-atmosphere condition in respiring produce packs. Shelf-life trials should be conducted at 23 °C and 50% RH with actual product fill weight; if the package is refrigerated, barrier data must be collected at the lower use temperature because oxygen and carbon dioxide permeability shift with temperature and moisture. For applications requiring a moisture barrier, INZEA F10 may require a compostable barrier coating or lamination; the addition of a barrier layer must be re-tested for home compostability because the final article is no longer monolayer.

    Processing limitations include moisture regain and additive compatibility. After drying, pellets exposed to 60% RH ambient air for more than 30 min can begin to re-adsorb moisture; re-drying is required if the material is not consumed within a closed conveying system or hopper dryer. Free water above 250 ppm at melt temperatures above 180 °C drives hydrolysis, reducing molecular weight and producing viscosity loss, gel particles, and black specks. The compound should not be purged with conventional polyolefin purge concentrates containing amine-based additives or zinc stearates; these may catalyse chain scission in PLA. A low-melt-flow PLA or manufacturer-approved purge grade is recommended when transitioning from polyolefins. Colour masterbatches and slip or anti-block concentrates must be certified compostable under EN 13432:2000 or EN 17427:2022 for the final film to retain its home compost claim; loadings above 10 wt% of an additive masterbatch may shift tensile properties enough to breach the qualified film specification even if the masterbatch itself is certified. Residence time in adapters, screen changers, and die lips should be kept below 8 min at 175 °C to 185 °C because longer heat history promotes branching, gel formation, and plate-out on polished chrome rolls. Coextrusion with PBAT, thermoplastic starch, or other biopolymers requires separate migration, seal strength, and disintegration testing, because the tie-layer interface can alter both mechanical failure mode and compost fragmentation.

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