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ecovio F23B1 Blown Film Compostable Welding PLA Compound

    • Product Name: ecovio F23B1 Blown Film Compostable Welding PLA Compound
    • 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 517775
    Product Name ecovio F23B1 Blown Film Compostable Welding PLA Compound
    Chemical Base Blend of PBAT (ecoflex) and PLA
    Biodegradability Biodegradable in industrial composting
    Compostability Standard EN 13432
    Certifications DIN CERTCO, OK compost, ASTM D6400
    Processing Method Blown film extrusion
    Weldability Weldable/sealable
    Density 1.25 g/cm³
    Melt Volume Rate 4.0 cm³/10 min (190°C, 2.16 kg)
    Melting Point 110-120°C
    Tensile Strength 22 MPa
    Elongation At Break 300%
    Tensile Modulus 500 MPa
    Vicat Softening Temperature 60°C (A/50)
    Food Contact Compliance EU 10/2011 and FDA
    Moisture Content <0.5%
    Storage Conditions Dry, 5-30°C, avoid direct sunlight
    Film Thickness Range 10-50 µm
    Application Organic waste bags, carrier bags, mulch films, packaging films
    Color Natural/off-white pellets
    Printability Printable

    As an accredited ecovio F23B1 Blown Film Compostable Welding PLA Compound factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing ecovio F23B1 Blown Film Compostable Welding PLA Compound typically supplied in 25 kg moisture-resistant paper sacks, palletized and stretch-wrapped.
    Container Loading (20′ FCL) 20′ FCL loaded with ecovio F23B1 Blown Film Compostable Welding PLA Compound, palletized bags securely stowed and braced for transport.
    Shipping Ecovio F23B1 is shipped as non-hazardous, compostable PLA compound pellets in sealed moisture-barrier bags on pallets. Transport in clean, dry vehicles at ambient temperature, avoiding heat, moisture, and direct sunlight. Not classified as dangerous goods; no UN hazard class or special labeling required. Follow SDS and local regulations.
    Storage Store ecovio F23B1 in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep in tightly sealed original packaging to prevent moisture absorption and contamination. Avoid prolonged storage at elevated temperatures or high humidity. Protect from physical damage. Handle with clean, dry equipment. Maintain stock rotation and use within the manufacturer’s recommended shelf life.
    Shelf Life Shelf life is about 12 months when stored dry, below 30°C, in unopened original packaging, protected from moisture and sunlight.
    Application of ecovio F23B1 Blown Film Compostable Welding PLA Compound

    On single-screw grooved-barrel blown film lines with screw diameters of 50–75 mm and L/D ratios of 30:1, ecovio F23B1 is normally introduced from a desiccant-bed hopper at 70°C for 4–6 h, targeting a residual moisture level below 250 ppm before melt plastication. The barrel profile is set with rear zone 160°C, compression 165–175°C, metering 170–180°C, adapter 175°C, and die 170–178°C; measured melt temperature at the die should not exceed 180°C because prolonged residence above this threshold accelerates PLA segment hydrolysis and lactide reformation. For 10 L kitchen caddy liners in the 12–18 µm thickness range, a die gap of 1.0–1.4 mm and blow-up ratio of 2.6–3.0:1 are employed with double-lip air-ring cooling and internal bubble cooling at 15–20°C to maintain bubble stability at output rates of 80–120 kg/h on 70 mm extruders. Converted side-weld bags are sealed at 115–130°C with dwell times of 0.4–0.8 s; seal strength measured under ASTM F88/F88M-21 typically must exceed 4 N/15 mm for caddy liners carrying 2–4 kg of wet organic waste. Under EN 13432, the compound’s compliance chain includes ISO 14855-1:2012 aerobic biodegradation of at least 90% carbon conversion relative to microcrystalline cellulose within 180 days, ISO 16929:2021 pilot-scale disintegration with 90% of residual fragments passing a 2 mm sieve after 12 weeks in mature compost at 58°C, and ecotoxicity testing under EN 13432 Annex E. The main production failure mode is not bubble instability but seal-bar contamination from PLA oligomer volatiles accumulating on PTFE-coated sealing jaws after 6–8 h of continuous conversion; cleaning of the sealing jaw with brass wire brushes at 80°C is required to prevent channel leakers in the bag bottom weld.

    Why Perforated Produce Bag Conversion Demands Seal Initiation Below 95°C

    High-output rotary bag machines converting 8–12 µm perforated film at 250–350 cycles/min impose a limiting variable that is not extruder throughput but the lower seal bar plateau time available for interfacial melting of the PLA-rich layer. The compound is run at a die gap of 0.8–1.0 mm and BUR of 3.0–3.5:1, which suppresses gauge variation to ±1.5 µm across the web. Perforation punching with needle rollers of 0.4 mm diameter at 15–20 mm pitch reduces transverse tear resistance; therefore the film formulation is processed with 1.0–2.0 wt% erucamide slip masterbatch and 0.5–1.0 wt% synthetic silica antiblock to prevent blocking on the collapsing frame. Seal initiation below 95°C allows the film to wet the sealing jaw and form a continuous weld without fully melting the oriented PLA domains; if seal initiation exceeds 95°C, the dwell time must be extended beyond 0.35 s, causing burn-through at perforation edges and downstream film web breaks. Compliance for direct food contact is not automatic: under Regulation (EU) No 10/2011, overall migration into food simulants must not exceed 10 mg/dm², and specific migration limits for monomers and additives listed in Annex I must be validated for the exact film thickness, temperature, and food simulant. Under FDA 21 CFR 176.170, the finished bag is regulated as indirect food contact through the packaging component; no blanket approval should be inferred from compostability certification. The end product is used for vented flow-wrap of leafy greens and root vegetables where condensation must escape to avoid microbial spoilage; if a moisture vapour transmission rate is required, it should be measured under ISO 15106-1 or ASTM E96/E96M-16 for the converted gauge rather than taken from generic PLA film data.

    Heavy-Duty Retail Carrier Film: Bubble Stability, Embossment, and Handle Weld Integrity

    A 25–40 µm gauge regime for heavy-duty compostable shopping carriers shifts the processing problem from thin-film puncture resistance to bubble sag and die-lip deposition under sustained shear. The extruder is typically a single-screw grooved-feed 60–80 mm diameter with L/D 30:1 and Maddock mixing tip; screw speed of 50–80 rpm generates melt temperatures of 162–172°C. A die gap of 1.2–1.6 mm and BUR of 2.0–2.5:1 produces a stiffness balance needed for patch handles, but lowering BUR below 2.0:1 increases longitudinal tear severity and handle weld peel failure because orientation imbalances localize strain at the die-cut handle root. Embossed patterns are applied on-line with embossing rollers at 70–85°C and nip pressure of 40–60 N/cm²; above 80°C the PLA-rich surface begins to block against the steel embosser, while below 65°C pattern retention after film winding is insufficient. Added post-industrial edge trim of the same grade at up to 15 wt% is tolerated if passed through a 200 µm screen changer and metered gravimetrically; melt pressure before the screen pack should stay below 350 bar to avoid excessive shear heating. Mechanical performance is verified by Elmendorf tear ASTM D1922 in machine and transverse directions, tensile properties by ASTM D882, and dart drop impact by ASTM D1709 Method A. Handle weld integrity is separately tested under ASTM F88/F88M-21 after die-cut handle conversion; commercial specifications typically require a peak seal force not less than 12 N/25 mm for a 25 µm film carrying 8 kg. The welding window is narrower than for LDPE: seal bar setpoints of 120–135°C with 0.6–1.2 s dwell create welded seams, but above 140°C the seam becomes brittle because PLA domain relaxation and film thinning localize failure at the weld edge. Finished bags are certified compostable under EN 13432 only when printing inks, adhesives, and masterbatches cumulatively remain below the organic and heavy metal limits of EN 13432 Annex A.2.

    Field laying of black ecovio F23B1 mulch film in short-cycle lettuce and tomato production on drip-irrigated beds uses 12–20 µm film across bed widths up to 1.2 m; the film is perforated at transplant spacing of 30–50 cm in row. The conversion requires 3–6 wt% carbon black masterbatch, which increases melt viscosity and may require raising the die temperature to 175–180°C but not exceeding 180°C to avoid PLA degradation. Blown film lines with oscillating haul-offs are used to distribute gauge variation; die gap is typically 1.2–1.5 mm and BUR is kept at 2.2–2.8:1 to preserve machine-direction tear strength during mechanical laying. Field disintegration follows EN 17033:2018, which requires that after incorporation into soil the film fragments and mineralizes at a rate specific to the soil reference material, with absence of acute ecotoxicity to plants and earthworms in the prescribed bioassays. Published data for this specific F23B1 formulation in Mediterranean tomato rotations is limited; therefore a batch-specific field disintegration trial under ISO 17556:2019 or ASTM D5988 is advisable before switching a full production block. The critical agronomic failure mode is premature slit propagation from the planting holes; to reduce this, 10–15 wt% talc filler may be added, but above 15 wt% the compound loses bubble stability and develops melt fracture lines visible at the frost line. The film should not be stored in high-humidity warehouses longer than 6 months because PLA hydrolysis shifts the seal-initiation temperature upward and reduces field degradation synchrony; in practice, conversion within 3 months from extrusion is specified.

    When a Compostable Mailer Replaces LDPE Outer Wrap in Logistics

    Non-food logistics film in the 40–80 µm gauge class replaces LDPE/LDPE-EVA mailer stock only after corona, printing, and adhesive-release sequences are re-engineered for the PLA-rich surface. The blown film is produced at die gap 1.5–2.0 mm, BUR 2.0–2.8:1, and melt temperature 165–175°C. Because PLA-rich blown film retains surface energy but is sensitive to ambient moisture, corona treatment is applied in-line immediately after the primary nip at 38–42 mN/m; the surface energy decays by 2–4 mN/m over 72 h if the film is stored at 60–70% RH. Water-based flexo inks with polyurethane binders are used for address windows and branding; solvent-based inks containing ethyl acetate or ketones should be avoided because they swell the PBAT phase and reduce seal strength at the bottom weld. The mailer is converted on bottom-seal machines with seal bar setpoints of 125–135°C and dwell 0.8–1.5 s; seal quality is checked under ASTM F88/F88M-21 with a required minimum of 8 N/25 mm to withstand 3 kg logistics loads. Adhesive closure flaps use compostable hot-melt on the outside surface; compatibility with the film surface requires that the adhesive open time be less than 1.5 s to avoid migration of plasticizer from the adhesive into the film. Unlike LDPE, ecovio F23B1 does not yield to tear propagation in the same manner; the mailer must be designed with tear-initiation notches or perforation lines because puncture resistance measured under ASTM F1306 differs from LDPE and may create uncontrolled tear into the packing list window.

    Downstream segmentStandard designationTest method or clauseRequired endpoint
    Organic waste collection linersEN 13432ISO 16929:202190% of fragments pass 2 mm sieve after 12 weeks at 58°C
    Fresh produce bagsRegulation (EU) No 10/2011Annex I overall and specific migration testingOverall migration limit 10 mg/dm²; SMLs for listed substances
    Agricultural mulch filmEN 17033:2018ISO 17556:2019 or ASTM D5988Soil mineralization and absence of ecotoxicity in prescribed bioassays
    Non-food compostable mailersASTM D6400-21ASTM D5338-15 or ISO 14855-1:201290% carbon conversion relative to cellulose within 180 days
    Paper-film dry-food laminatesEN 13432ISO 14855-1:2012 + ISO 16929:2021Film component meets 90% carbon conversion and disintegration

    Solvent-free laminating of 20–25 µm ecovio F23B1 blown film to clay-coated paper for dry-food pouches uses a two-component polyurethane system at coat weights of 1.5–2.5 g/m². The blown film web enters the lamination nip at unwind tension 20–30 N/100 cm width; excessive tension above 40 N/100 cm triggers primary bubble memory and causes tunnelling after slitting. Lamination speeds of 150–250 m/min are typical on 1.2 m solvent-free laminators, with nip temperature 50–60°C and pressure 3.0–4.5 N/mm². The PLA phase holds the sealant layer flat against the paper but will not accept heat-sealing temperatures above 145°C without edge curl; this limits the pouch to dry products such as tea, soup mix, and powdered beverage sachets, not wet or oil-soaked food. Final pouch seal strength measured under ASTM F88/F88M-21 on the paper/film interface is less relevant than the film-to-film seal, which should exceed 5 N/15 mm after sealing at 120–130°C for 0.5 s. Compliance under EN 13432 requires that the paper, adhesive, and ink jointly fulfill disintegration and biodegradation criteria; because paper dominates the biomass, the film must still meet the 90% carbon conversion threshold under ISO 14855-1:2012 when tested without the paper fraction. If the laminate is sold as home compostable, a separate certification under AS 5810-2010 or equivalent is necessary because EN 13432 alone addresses industrial composting.

    Critical Seal-Bar Temperature Distribution Across 600 mm Wide Side-Weld Tooling

    Side-weld conversion of 15–30 µm blown film produced from ecovio F23B1 exposes a critical temperature distribution across the sealing jaw width that controls weld consistency more than the average setpoint. A 600 mm wide PTFE-coated side-weld bar with cartridge heating typically displays a centre-to-edge differential of 5–12°C when the machine is run at 60–100 cycles/min, because heat is conducted into the unsealed film web at the jaw edges. The recommended control band is 120–135°C at the centre and no less than 110°C at the outermost 50 mm of the jaw; below 110°C, interfacial polymer diffusion is insufficient to produce a continuous weld, and above 140°C at the centre, the PLA phase undergoes additional crystallization during cooling, producing a weld that can fail in brittle mode under ASTM F88/F88M-21 seal strength testing. Dwell time of 0.3–0.7 s and jaw pressure of 3.0–5.0 bar are monitored to keep seal thickness reduction between 10% and 20% of original film thickness; below 10% cold welds occur, and above 20% the seal root becomes the preferred tear path. The weld zone must be cooled to below 50°C before wind-up tension is applied to prevent blocking of the PLA-rich surface in the lay-flat roll. This conversion stage is where the welding character of the compound is most directly exploited: post-seal strength retention after 12 months warehouse storage at 20°C and 50% RH is dependent on the migration of slip additives away from the seal interface, so slip masterbatch addition above 2 wt% should not be specified without re-qualifying seal strength at each quarter of the storage period.

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    Certification & Compliance
    More Introduction

    ecovio F23B1 is a partially bio-based polyester compound for tubular blown film and is built around a polylactic acid continuous phase modified with an aliphatic-aromatic copolyester component, most commonly referred to as polybutylene adipate-co-terephthalate. The F23B1 designation places it within the ecovio F-series for film converting, with specific formulation adjustments intended to support low-temperature weldability and heat-seal response in biodegradable bag structures. Supplier literature reports density in the range of 1.24–1.26 g/cm³ when measured according to ISO 1183-1, and a melt volume rate at 190°C and 2.16 kg of 3–5 cm³/10 min per ISO 1133-1. The compound is supplied as a ready-to-process pellet, not as a masterbatch, so converters do not dilute a carrier resin at the hopper. The material is used in monolayer and coextruded film for soil-biodegradable mulch, organic-waste collection bags, carrier bags, and thin-gage overwrap where industrial compostability under EN 13432 is required. Because the PLA phase dominates the continuous matrix, melt processing is not identical to that of PBAT-rich blown-film grades.

    PropertyTest methodReported envelope
    DensityISO 1183-11.24–1.26 g/cm³
    Melt volume rate at 190°C, 2.16 kgISO 1133-13–5 cm³/10 min
    Tensile modulus, filmISO 527-3250–700 MPa
    Tensile strength at break, filmISO 527-320–35 MPa
    Elongation at break, filmISO 527-3250–500%
    Elmendorf tear resistanceISO 6383-2300–900 mN
    Seal initiation temperatureASTM F8890–115°C

    The reported envelope is compiled from publicly available supplier literature and film-conversion trials; lot-to-lot variation requires verification against the certificate of analysis. Film mechanical values depend strongly on film thickness, blow-up ratio, frost-line height, and orientation.

    What hardware configuration and thermal boundaries permit stable bubble formation with F23B1?

    Stable blown-film production is normally achieved on single-screw extruders in the 45–65 mm diameter range with L/D 28:1–30:1 and a compression ratio of 2.5:1–3.0:1. High-shear barrier screws with aggressive mixing pins are not recommended because local shear heating can drive the melt temperature above the degradation threshold. Barrel temperature profiles are typically set from 150°C in the feed zone to 170–175°C at the adapter, with die temperature held at 170–180°C. Melt temperature should remain below 200°C; excursions above this ceiling accelerate random chain scission of the PLA phase, reduce extensional viscosity, and destabilize the bubble.

    Die gap and bubble geometry require greater attention than with polyolefin film because the melt strength of the compound is lower than that of low-density polyethylene at equivalent melt temperature. Die gaps of 0.8–1.2 mm, blow-up ratios of 2.2:1–3.2:1, and frost-line heights of 3–5 die diameters are common starting points. A dual-lip air ring with adjustable lower-lip flow is preferable for thin-gage operation below 20 µm. Internal bubble cooling may be required when line speed exceeds 30–40 m/min, depending on tower height and ambient humidity.

    Hydrolytic degradation is a more significant process conflict than with polyolefins. The resin should be pre-dried at 75–80°C for 4–6 h, with a desiccant dryer dew point of -40°C or lower, to achieve residual moisture below 250 ppm. At relative humidity above 60%, unshielded resin hoppers absorb atmospheric moisture rapidly, and a hopper dryer rather than a simple hot-air hopper is mandatory. Inadequate drying reduces melt tenacity and produces microvoids at the frost line, which subsequently lower Elmendorf tear resistance and seal consistency. Avoid addition of primary or secondary amine-containing additives because these compounds can promote polyester aminolysis, molecular weight reduction, and premature loss of mechanical integrity.

    Seal initiation thermodynamics and welding-process variables

    The welding response of ecovio F23B1 is governed by chain interdiffusion across the seal interface and partial melting of the PLA crystalline phase. The PBAT-rich modification depresses seal initiation relative to unmodified PLA blown-film grades. Heat-seal tests performed according to ASTM F88 generally place seal initiation between 90°C and 115°C, while hot-tack measurements per ASTM F1921 show a usable plateau from approximately 100°C to 130°C. Below the initiation threshold, failure is predominantly adhesive peel with limited entanglement across the interface. Above the plateau, film shrinkage, pinhole formation, and localized burn-through reduce burst strength.

    In side-weld bag converting, impulse sealers with dwell times of 0.3–0.8 s and jaw pressures in the range of 0.2–0.5 MPa are typical starting conditions. Jaw parallelism is more critical than with LDPE because partial melting of the PLA phase produces a narrow viscoelastic window; misaligned jaws create edge channels that act as tear initiators. Ultrasonic plunge welding is used for thicker sheet and preformed structures, generally at 20 kHz with amplitude of 30–60 µm, trigger force of 50–100 N, and weld time of 0.2–0.6 s for 150–300 µm sheet. Published data for ultrasonic welding of F23B1 specifically is limited, so the stated settings are engineering starting points for PLA-based sheet welding rather than certified grade-specific parameters.

    Weld failure mode should be inspected after production. Cohesive failure in the substrate is preferred for cold-chain bag integrity because it indicates that the weld exceeds the surrounding film strength. Adhesive peel at the seal is associated with insufficient temperature, insufficient dwell, contamination by migratory slip additives, or surface bloom from oligomeric PLA fractions. Overdrying the pellet but then storing converted rolls at high humidity can also shift seal initiation upward because water plasticizes the PLA phase and changes heat transfer during sealing.

    For industrial compostability, monolayer and coextruded films made from ecovio F23B1 are commonly produced at 15–30 µm thickness in side-weld or bottom-seal configurations. The intended use requires a balance between puncture resistance during wet organic-waste loading and tear propagation resistance after floor dragging. The PBAT modification shifts failure from brittle fracture to stable fibrillation, but the film remains more anisotropic than LDPE. In production-scale side-weld bag machines operating near 180 cycles/min, seal consistency is evaluated by burst testing of filled bags after 24 h at 40°C. Because PLA-based films aged above their glass transition can lose seal strength less predictably than LDPE, storage above 60% RH without vapor-barrier packaging may shift seal initiation upward and increase blocking. Converters who pre-dry sealed rolls in tunnel dryers at 45–50°C for 8–12 h before converting report lower scrap rates from seal contamination, but the same practice can embrittle the film if air exchange is insufficient.

    When the compound replaces petroleum-based LDPE in organic-waste bag lines

    The replacement of LDPE with ecovio F23B1 is not a drop-in substitution. Extruder temperature profiles must be reduced from typical LDPE settings by as much as 30–40°C, and screw speed should be lowered to limit viscous dissipation. The film has higher modulus than PBAT-only grades and lower elongation than very high-molecular-weight LDPE, but it provides compostability and a measurable renewable carbon fraction. Compared with unmodified PLA blown-film grades, F23B1 has lower elastic modulus and higher elongation at break because the copolyester phase dissipates strain and suppresses large-scale craze propagation. Compared with PBAT-only film grades, F23B1 offers higher stiffness and reduced blocking, although its seal initiation temperature is higher than pure PBAT and its tear resistance is more direction-dependent.

    The welding character differs from LDPE. LDPE forms seals by viscous flow and chain interdiffusion of a low-crystallinity polyolefin, whereas F23B1 seals by interface softening of the PBAT phase and partial melting of PLA crystalline domains. This means dwell time, jaw parallelism, and surface contamination have a larger influence on seal strength than they do with LDPE. Purging is also required when changing from polyolefin extrusion lines; residual polyethylene or polypropylene contamination can form discrete domains that delaminate under film tension and create visible fish-eye defects. Purging with a low-viscosity biodegradable polyester or a commercial purging compound is preferred because high residence time at elevated temperature degrades the PLA phase and generates lactide deposits at the die lip.

    Thermal degradation of the PLA phase imposes a narrow melt-temperature ceiling

    The continuous PLA phase melts between approximately 150°C and 165°C, while the PBAT-rich phase may exhibit a separate endotherm near 120–130°C. Processing above 200°C accelerates random chain scission and unzipping reactions, releasing lactide and reducing molecular weight. The practical result is a working interval that can be as narrow as 5°C at the die when high line speeds and high shear heating combine. Extensional viscosity decreases rapidly as the melt temperature enters the 190–200°C range, causing bubble sag, gauge variation, and loss of frost-line stability. Conversely, lowering die temperature below 160°C to protect the melt increases die pressure, promotes melt fracture, and can produce visible weld lines in the film.

    Residual lactide generated during processing migrates to the bubble surface and accumulates on the collapsing frame, idler rolls, and sealing jaws. This deposit can lead to seal contamination and periodic line stoppages. The use of processing aids should be limited because migratory additives concentrate at the film surface and alter weld strength. If slip or antiblock is required, non-migratory particulate systems are preferred over fatty acid amide systems. Erucamide addition above 0.3 wt% can reduce seal initiation but also produces inconsistent hot-tack and weakens the sealing plateau. The exact compatibility of a slip additive with F23B1 should be confirmed by seal-strength testing after roll ageing, not only by coefficient-of-friction measurement.

    Compostability certification is not equivalent to food-contact approval

    The grade is designed for industrial compostability, and compliance is typically demonstrated under EN 13432 for the European market. Under EN 13432, the material must achieve at least 90% disintegration after 12 weeks and at least 90% CO₂ conversion after 180 days in controlled composting conditions. Heavy-metal limits are specified in EN 13432 Annex E, with maximum concentrations for zinc, copper, nickel, cadmium, lead, and mercury. The compound may also be tested against ASTM D6400 or ISO 17088 for compostability claims in other jurisdictions, but certification status should be verified with the supplier because certification is grade-specific and may be formulation-specific.

    Regulatory areaStandard or regulationTypical conformance condition
    Industrial compostability, EUEN 1343290% disintegration in 12 weeks; ≥90% CO₂ conversion in 180 days
    Compostability, USASTM D6400Disintegration, biodegradation, and heavy-metal limits per specification
    Heavy metalsEN 13432 Annex EZn, Cu, Ni, Cd, Pb, and Hg below specified maximum concentrations
    Chemical safety, EUREACHPre-registration and substance compliance for the supplied pellet
    Hazardous substancesRoHSLead, mercury, cadmium, hexavalent chromium, PBB, and PBDE below restriction limits

    Food-contact status is a separate regulatory question. Compostability certification does not automatically establish compliance with food-contact plastics regulations such as EU 10/2011 or FDA 21 CFR. Any use in food packaging must be evaluated for migration of oligomeric PLA degradation products, PBAT-related monomers, and processing aids under the intended temperature and food-simulant conditions. Published data for this specific configuration is limited, so converters should request a regulatory statement from the supplier before using F23B1 in direct food-contact structures.

    In agricultural mulch film and organic-waste bag production, the film is typically converted with a minimum of two sealing stations and inspected for weld fracture before wind-up. The operational boundary is set by the balance between pre-drying, melt temperature, and seal dwell. The compound is not certified for anaerobic degradation or home composting unless specifically marked, and it should not be combined with non-compostable polyolefin scrap in recycling streams because incompatible domains delaminate under film tension and reduce seal burst strength.

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