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INZEA FH11 Flexible 40% Bio-Based Retail Bag Film Polylactic Acid

    • Название продукта: INZEA FH11 Flexible 40% Bio-Based Retail Bag Film Polylactic Acid
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
    • Запрос цены: admin@ascent-chem.com
    • Производитель: Ascent Petrochem Holdings Co., Limited
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    Код ТН ВЭД 126883

    Как аккредитованный завод INZEA FH11 Flexible 40% Bio-Based Retail Bag Film Polylactic Acid, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

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    Применение INZEA FH11 Гибкая 40% био-базированная розничная сумка пленка полимолачной кислоты

    High-output conversion of INZEA FH11 Flexible into retail checkout bags begins with pellet moisture control, not melt temperature selection. The material is marketed as a 40% bio-based polylactic acid compound for blown-film extrusion, with the bio-based carbon claim quantified by EN 16640 or ASTM D6866. Residual pellet moisture above 250 ppm, measured by Karl Fischer titration under ISO 15512, accelerates hydrolytic molecular weight loss once melt temperatures exceed 160 °C. A desiccant dryer set to 60–80 °C with a dew point no higher than -40 °C and residence time of 4–6 h is standard practice for flexible PLA compounds before extrusion. On a single-screw extruder with L/D 24:1 to 30:1 and a barrier screw, barrel temperatures from feed to metering are commonly profiled from 150 °C to 170 °C, while the adapter and die are held at 160–180 °C. The die gap is set between 0.8 mm and 1.2 mm, and the blow-up ratio is maintained at 2.0:1 to 2.8:1 to balance machine-direction and transverse-direction tensile strength. Frost line height is adjusted for bubble stability because excessive melt draw resonance creates gauge bands that convert into weak points at the bottom seal. Gauge thickness for checkout bags in this application typically falls between 15 µm and 25 µm, depending on retailer load requirements. The film is corona-treated to a surface energy of 38–42 mN/m measured under ISO 8296, surface-printed with water-based flexographic inks, and sealed at 120–140 °C with 0.3–0.5 s dwell time, followed by die-cutting for handle openings. Converter practice is to verify melt flow index lot-to-lot by ISO 1133-1:2022 at 190 °C/2.16 kg, with the acceptance band set from the supplier certificate. Terminal article compliance for organic recovery rests on EN 13432; disintegration is demonstrated under ISO 20200 or ISO 16929, and ultimate biodegradation under ISO 14855-1 at 58±2 °C for industrial compost. North American distribution may also require ASTM D6400, which sets a biodegradation threshold of 90% absolute or relative to a positive control within 180 days. White masterbatch addition above 8 wt% may alter the certified organic recovery profile and requires revalidation by the certifying body.

    What Limits Gauge Uniformity in High-Speed Produce Roll Bag Film?

    Gauge uniformity in produce roll bags made from INZEA FH11 Flexible is governed by melt strength at the frost line and the consistency of bubble cooling. A single-lip air ring with a dual-flow chilled-air manifold is used on many converter lines; the chilled air temperature is held at 10–20 °C, and the blower output is indexed to the extruder output rather than to ambient conditions. The film is often run at 8–12 µm thickness for high-throughput dispensing, which places exceptional demands on the melt-fracture limit. Polyethylene-grade spirals with abrupt mixing elements are generally unsuitable; a barrier screw with a Maddock mixer is preferred, and the screen pack should not exceed 100 mesh to avoid excessive shear heating. PLA-based compounds are shear-thinning but also hydrolytically sensitive, so residence time in the extruder below 5 min at maximum barrel temperature is maintained. The wound roll is perforated in-line using a rotary pin-perforation system at a repeat length of 200–450 mm, determined by the dispenser geometry. Perforation burr is controlled by blade sharpness and backing roller hardness of 85–90 Shore A. Terminal produce bags must not prematurely split at the perforation, which is verified by tensile testing according to ISO 527-3 or ASTM D882; the perforated film is sampled across the web after 30 min of stable production. Regulatory compliance for food contact is addressed under Regulation (EU) 10/2011 and applicable FDA food-contact notifications for polylactic acid; overall migration testing is performed against the 10 mg/dm² total limit. Because produce is often moist, the film is compounded with an antiblock system such as silica or calcium carbonate at 0.5–2.0 wt%; over-addition increases haze beyond acceptable retail presentation levels and reduces tear resistance. Static dissipation during winding uses passive ionizing bars rather than amine-based antistats because basic nitrogen-containing additives can destabilize PLA during extrusion and worsen odor in the final film.

    In kitchen caddy conversion, the liner made from INZEA FH11 Flexible in the 15–25 µm range is not a simple down-gauged produce bag. The film must tolerate a biphasic environment of humid organic acids and intermittent liquid pooling at the folded edge. The converter runs a blown-film line with a die gap of 0.8–1.5 mm, a blow-up ratio near 2.5:1, and a lower frost line than retail checkout film to reduce internal stress before sealing. Bottom sealing is carried out on a rotary bag machine at 115–135 °C, with the seal bar knurled rather than polished to allow entrapped air to escape during sealing. Seal strength is evaluated using ASTM F88/F88M; a force of 2.5–4.0 N/15 mm is generally the converter acceptance window for hand-loaded organic waste liners. The material is not recommended for prolonged immersion in aqueous liquids above 24 h; although disintegration is intended under composting conditions, water-tight service behavior is outside the technical scope of a compostable bag film. Wet-strength retention is improved by using film layers with higher molecular-weight PLA or by blending with a biodegradable aliphatic-aromatic copolyester in coextrusion, but this must be verified against EN 13432 because not all biodegradable polyesters remain home-compostable. Home compostability claims require certification under a recognized scheme such as TÜV OK compost HOME or EN 17427, which imposes lower-temperature biodegradation and disintegration conditions than industrial compost. The film must also meet the Packaging and Packaging Waste Directive 94/62/EC, including the sum of lead, cadmium, mercury, and hexavalent chromium below 100 ppm by weight. Converters often add a slip agent at 0.1–0.3 wt% to reduce film-to-film friction during automatic dispensing, but excessive slip reduces the coefficient of friction below the level needed to keep the bag open in a caddy.

    When Mailer Film Structures Use 40% Bio-Based PLA in Lamination

    For e-commerce mailers, conversion of INZEA FH11 Flexible frequently involves a monolayer blown film with a self-seal strip, but when the item requires puncture resistance above conventional checkout bag film, a laminated structure is selected. A 25–40 µm print web of INZEA FH11 Flexible is extruded or adhesive-laminated to a second biodegradable film web; in the case of extrusion lamination, melt temperature at the die must not exceed 180 °C for extended periods because PLA-based compounds lose extensional viscosity and can develop gel from thermal degradation. The adhesive used must be a solventless polyurethane that is approved for indirect food contact where required; however, the overall structure must still satisfy EN 13432 if the mailer is marketed as compostable, which limits the adhesive weight to a negligible fraction or requires certification of the complete laminate. Corona treatment of the sealant web to 38–42 mN/m is performed immediately before lamination to achieve interfacial peel adhesion. Mailer closure is a pressure-sensitive strip protected by a siliconized release liner, applied after film is cut into shape; the peel tensile strength of the sealing strip is tested by ASTM D3330, while film tear resistance is measured by ASTM D1922. A mailer film must resist edge-initiated tearing during sorting, but excessive orientation at the frost line introduced to increase stiffness can lower Elmendorf tear propagation. Gauge uniformity across the web is critical because the mailer is converted through a high-speed flexographic press and a heat-seal bottom-folding line. Published data for this specific INZEA FH11 Flexible structure in e-commerce mailers is limited, so converter trials with a pilot blown-film line are necessary to set the exact blow-up ratio and frost line for each grammage. The outer print surface frequently requires a printable topcoat that increases surface energy above 40 mN/m and must not contain nitrile-based pigments that can interfere with industrial compostability.

    Garment Bag Films and Static Dissipation in Automated Insertion

    On textile logistics lines, garment bags made from INZEA FH11 Flexible are converted in Z-fold or roll format for automated insertion machines. The film is extruded at 12–18 µm thickness and perforated for air evacuation; punched vent holes with a diameter of 4–6 mm are spaced 150–300 mm apart to prevent ballooning during high-speed folding. The terminal article is usually a clear or lightly printed bag with a bottom gusset, which requires gauge uniformity better than ±5% across the web to avoid fold misalignment on the insertion machine. Static dissipation is measured according to ASTM D257 or IEC 61340-2-3; a surface resistivity between 106 Ω/sq and 1011 Ω/sq is considered adequate for textile automation, but the chosen antistat must be approved for the final compostability certificate if the bag carries an organic recovery claim. Amine-based antistats are avoided because they can generate odor and contribute to PLA molecular weight loss at processing temperatures. The film is corona treated to 38 mN/m before printing and then folded with mechanical resistance. Compliance for the garment bag as packaging is covered by the heavy metals limits of 94/62/EC and, for chemical substances, by REACH Annex XVII and SVHC screening on the raw material.

    Below 5 °C, Tear Initiation Shifts from Tensile to Impact Mode

    At refrigeration temperatures between 4 °C and 8 °C, cold-chain wrapping of leafy greens and fresh herbs uses INZEA FH11 Flexible in 10–15 µm gauges, but the service temperature is close to the secondary relaxation region of PLA-based films. The film exhibits lower puncture elongation and higher stiffness than at ambient, so the critical failure mode shifts from slow tensile overload to rapid tear initiation at produce stems. The converter compensates by increasing the plasticizer-containing soft phase in the compound, but the exact blend ratio is supplier-controlled and not always disclosed; instead, film property is verified by instrumented impact testing according to ISO 7765-1 or ASTM D3420. A drop-dart impact value that is acceptable at ambient may not remain acceptable at refrigeration temperature, making it essential to sample the film after 24 h conditioning in a cold-room test chamber. The film is perforated with macro holes for respiration and micro perforations for oxygen and carbon dioxide exchange; the hole density is specified by the fresh-cut produce packer based on respiration rate. A high-molecular-weight PLA layer in coextrusion is often combined with INZEA FH11 Flexible as the sealant layer, because the sealant must initiate at 105–125 °C without shrinking the outer layer. Use of the film in direct contact with high-moisture produce requires compliance with relevant food-contact regulation, but published migration data for this particular compound in cold-chain use is limited; therefore, the food-contact compliance statement is based on the raw material manufacturer’s documented certification rather than a universal assumption. Cold-chain films should not be used for deep-freeze applications below -10 °C without validation, because PLA-rich compounds lose elongation rapidly below the glass transition of the soft phases and may shatter on perforation lines.

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    Более подробное введение

    INZEA FH11 Flexible 40% Bio-Based Retail Bag Film Polylactic Acid is a polylactic acid-based thermoplastic compound specified for blown film extrusion of retail bag applications, including carrier bags, produce bags, and short-use lightweight packaging. The designation encodes three classification elements: the INZEA FH11 grade identifier, a flexible film processing window, and a bio-based carbon content of 40% determined by radiocarbon methodology under ASTM D6866-22 or ISO 16620-2:2019. The bio-based carbon value is not equivalent to total renewable mass; it represents the fraction of organic carbon in the compound derived from contemporary biomass rather than fossil carbon. The balance of the carbon pool may originate from fossil-derived modifiers used to reduce brittleness, increase tear resistance, and control heat-seal initiation. Published data for this specific configuration is limited in open technical literature; exact melt flow rate, density, film tensile properties, and moisture limits must be obtained from the current manufacturer technical data sheet before production qualification.

    Polylactic acid homopolymer is commonly reported with a density of 1.24 g/cm³ under ISO 1183-1, a glass transition temperature in the 55 °C to 60 °C range, and a crystalline melting peak between 150 °C and 170 °C for semi-crystalline extrusion grades. These values are material-class reference points and are not grade-specific specifications for INZEA FH11. Flexible PLA compounds typically require a second phase—such as a biodegradable polyester, plasticizer, or rubber-like modifier—to shift the stress-strain response away from the rigid behavior of unmodified PLA. Unmodified PLA film can exhibit tensile elongation at break below 10% under ISO 527-3:2018, whereas commercial flexible PLA compounds are formulated to exceed 100% elongation; however, the exact INZEA FH11 elongation value is controlled by film gauge, orientation, and additive package and must be verified experimentally.

    The intended usage envelope is thin blown film for retail bag formats, with trials generally conducted at 15 µm to 50 µm thickness depending on bag volume and load class. The grade is positioned for converter lines that require a bio-based content claim of 40% while retaining a machine-direction and transverse-direction balance closer to a flexible packaging film than to a rigid sheet.

    Compared with low-density polyethylene, INZEA FH11 belongs to a different regulatory and end-of-life category because PLA is a polyester, not a polyolefin. Processing on LDPE lines is possible only if temperature and moisture controls are tightened. Polyethylene typically offers broader processing tolerance and lower water vapor transmission, while PLA-based flexible film generally transmits water vapor more rapidly and exhibits a narrower heat-seal plateau. Those differences are material-class characteristics and should be evaluated through ISO 15106-2 water vapor transmission and ASTM F2029 heat seal testing on the finished bag film.

    Compared with PBAT/starch film, which may also be compostable but often has lower tensile stiffness, a 40% bio-based PLA compound can provide higher modulus and more stable film handling at the cost of reduced ultimate strain and higher moisture sensitivity unless adequately modified. PBAT is largely fossil-derived but biodegradable; PLA is bio-based but requires industrial composting conditions to degrade. These differences affect shelf-life stability, warehouse humidity tolerance, and downstream converting behavior.

    What Limits the Melt Processing Window for a 40% Bio-Based PLA Compound?

    PLA is a condensation polyester susceptible to hydrolytic chain scission during melt processing. Residual moisture in the pellets reacts with ester linkages, reducing number-average molecular weight and lowering melt viscosity. For most PLA extrusion compounds, including flexible film grades, predrying in a desiccant dryer to less than 250 ppm residual moisture is required before extruder feed. The drying air dew point should be −40 °C or lower, with hopper residence times of 3 h to 5 h at 70 °C to 85 °C. These parameters are standard for PLA resin classes but are not a substitute for the grade-specific drying profile.

    Hydrolysis of PLA in the melt proceeds by random chain scission of ester linkages. The reaction rate is strongly dependent on water concentration; at melt temperatures above the boiling point of water, residual moisture inside pellets is converted into steam, increasing local pressure and accelerating molecular weight reduction. A residual moisture level above 250 ppm is generally associated with reduced melt viscosity and increased generation of lactide oligomers at the die lip. The same mechanism affects reprocessing: edge trim and startup scrap must be dried before reintroduction, and closed-loop trim feed should be designed to avoid moisture uptake above 0.1%.

    Melt temperature at the die lip should not remain above 200 °C for extended periods, because lactide formation and thermal degradation increase sharply at elevated temperatures. Adiabatic shear heating in deep-flight metering sections can cause local temperature overshoot even when barrel setpoints are moderate. Screw configurations with L/D ratios between 25:1 and 33:1, low compression ratios, and water-cooled feed throats reduce the risk of premature melting and hydrolytic degradation. Extruder barrel temperature profiles for PLA-based flexible film generally start near 160 °C to 170 °C in the feed zone, 180 °C to 190 °C in the compression zone, 190 °C to 200 °C in the metering zone, and 190 °C to 200 °C at the die. These are starting-point profiles for material-class qualification and must be adjusted according to the exact melt viscosity and additive package of INZEA FH11.

    Blown Film Extrusion and Bubble Stability Parameters

    Die gaps of 1.0 mm to 2.5 mm and blow-up ratios of 2:1 to 3:1 are typical starting points for flexible PLA film trials. The frost line should be positioned close to the die to limit molecular orientation in the amorphous state. Conversely, if the frost line is too close, the bubble surface cools before adequate relaxation, yielding high dart impact variability and uneven gauge distribution. These operational boundaries arise from PLA’s relatively low zero-shear melt strength and strain-hardening limitations; formulations containing chain extenders or biodegradable polyester phases may shift the bubble stability window, but such additive packages are proprietary.

    Field experience on conventional blown film lines indicates that PLA films often require internal bubble cooling or chilled air because the material has lower melt strength and slower crystallization than HDPE. Bubble fluttering and draw resonance are observed when frost line height is not controlled within a narrow band. Chilled air temperatures below 15 °C, combined with stable external air flow and low nip speed variation, reduce the tendency for transverse gauge bands. The extruder die should be cleaned more frequently than with polyolefin runs because PLA oxidation residues can accumulate at the lip and produce edge wrinkles or film lines.

    For retail bag conversion, gauge uniformity is critical at the gusset fold and seal areas. A variation in thickness above ±5% can concentrate stress at the seal edge and lower bag drop resistance. Blown film lines should be equipped with capacitance or optical gauge scanners and automatic die lip correction if narrow gauge tolerances are specified by the retail bag end user. Post-extrusion slitting should be performed with low-tension winding because flexible PLA can retain orientation stress and develop blocking under tight roll hardness.

    When 40% Bio-Based Carbon Is Specified in Packaging Procurement

    The 40% bio-based carbon value has procurement consequences under ASTM D6866-22 and ISO 16620-2:2019, because it is a carbon-fraction measure rather than a mass-fraction or calorific-value claim. A 40% bio-based carbon content may not satisfy “fully bio-based” claims in jurisdictions where a higher percentage is required, while it may still support a qualified biobased content label under applicable national programs. Converters should retain radiocarbon test reports for each lot or compound batch, because carbon-14 content can vary with feedstock sourcing and reformulation.

    Standards applicable to qualification of a 40% bio-based flexible PLA retail bag film
    Standard reference Purpose Relevant clause or method
    ASTM D6866-22 Bio-based carbon fraction via radiocarbon Method B or C, carbon-14 analysis
    ISO 16620-2:2019 Bio-based carbon content of plastics Clause 8, calculation of biogenic carbon fraction
    ISO 527-3:2018 Tensile properties of film Type 2 specimens, test speed 50 mm/min unless specified
    ASTM D882-18 Tensile properties of thin sheeting Constant-rate-of-grip separation, specimens below 250 µm
    ISO 6383-2 Tear resistance, Elmendorf Pendulum-type tear on notched film specimens
    EN 13432:2000 Compostability and biodegradability of packaging Clause 5 chemical characterization, Clause 6 biodegradation, Clause 7 disintegration, Clause 8 ecotoxicity
    ASTM D6400-23 Compostable plastic labeling Section 6 disintegration, Section 7 biodegradation, Section 8 toxicity

    Compostability certification is based on the final film thickness, ink coverage, and adhesive load, not merely on the base resin. EN 13432:2000 requires at least 90% biodegradation within 6 months under controlled composting conditions, disintegration within 12 weeks, and ecotoxicity testing. A 40% bio-based carbon content does not automatically satisfy these requirements; the fossil-derived modifier fraction may be biodegradable or non-biodegradable depending on chemistry. Converters must obtain a certification for the specific final article, not merely for the base resin.

    Food-contact status is also grade-specific. PLA homopolymers may be permitted in EU Regulation No 10/2011 and in specific FDA food-contact notifications, but fillers, modifiers, and processing aids determine final compliance. The converter must obtain the manufacturer’s regulatory statement for INZEA FH11 and evaluate overall migration under EN 1186-2 or FDA 21 CFR 177 conditions relevant to the intended food type and contact time.

    Printing and heat sealing introduce further operational boundaries. PLA film surfaces are often corona treated to a wetting tension of at least 38 mN/m under ISO 8296:2003; ink adhesion failures may occur when surface energy falls below 42 mN/m after storage. Water-based inks are typically used because polar solvents can plasticize PLA surfaces and lower heat-seal strength. Heat seal initiation for PLA-based flexible films is generally between 80 °C and 100 °C, but the seal window can be narrower than 20 °C wide, requiring tighter jaw temperature control than polyolefin bag lines. Hot-tack force under ASTM F1921 is lower than LDPE; cooling bars and controlled jaw dwell reduce film tearing at the seal edge.

    Lamination, solvent-based inks, and high-solvent adhesives should be evaluated for compatibility with PLA because polar solvents can plasticize the film surface and lower heat seal strength. Converters should also avoid exposing the compound to amine-containing additives or strongly alkaline cleaning media because PLA is susceptible to alkaline hydrolysis at the surface, producing subsequent loss of clarity and seal integrity. These limitations are common to PLA-based films and do not constitute a product-specific defect.

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