| HS Code | 766437 |
| Product Name | INZEA F19 Transparent Flexible Food Packaging Film Polylactic Acid |
| Material Type | Polylactic Acid (PLA) |
| Form | Film |
| Appearance | Transparent |
| Flexibility | Flexible |
| Primary Application | Food packaging |
| Food Contact Suitability | Suitable for food contact |
| Biobased Origin | Renewable plant-based |
| Biodegradability | Compostable under industrial composting conditions |
| Density | Approximately 1.25 g/cm³ |
| Melt Flow Rate | Approximately 2-6 g/10 min at 190 °C/2.16 kg |
| Melting Temperature | Approximately 150-160 °C |
| Glass Transition Temperature | Approximately 55-60 °C |
| Tensile Strength | Approximately 30-50 MPa |
| Elongation At Break | High, typical of flexible PLA film |
| Optical Transparency | High transparency |
| Heat Sealability | Heat sealable |
| Processing Method | Blown film extrusion |
| Moisture Sensitivity | Requires drying before processing |
| Barrier Properties | Moderate oxygen and moisture barrier typical of PLA films |
As an accredited INZEA F19 Transparent Flexible Food Packaging Film Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INZEA F19 transparent flexible food packaging film, polylactic acid, supplied in 25 kg rolls, wrapped in protective film on pallets. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): INZEA F19 transparent flexible PLA food packaging film, palletized, shrink-wrapped, moisture-protected, and secured for safe ocean transport. |
| Shipping | INZEA F19 Transparent Flexible Food Packaging Film (Polylactic Acid) is non-hazardous and not regulated for transport. Ship in original sealed packaging, protected from moisture, heat, and direct sunlight. No UN number, hazard class, or special transport label required. Suitable for road, sea, and air freight under standard dry conditions. |
| Storage | Store in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and moisture. Keep in original sealed packaging, palletized, off floor. Avoid prolonged high temperatures and UV exposure to prevent degradation. Maintain 15–25°C and low humidity. Do not stack excessively; protect from physical damage. Store separately from incompatible chemicals and strong oxidizers. Use first-in, first-out stock rotation. |
| Shelf Life | INZEA F19 PLA film shelf life: typically 12 months when stored cool, dry, sealed, protected from sunlight, moisture, heat; confirm supplier specifications. |
INZEA F19, a polylactic acid film grade for transparent flexible food packaging, is used in cold-chain produce applications where the film functions as a gas-exchange membrane rather than as a hermetic barrier. A 20–25 μm monolayer PLA film produced by cast extrusion on a 25:1 L/D single-screw extruder at a melt temperature of 190–210 °C with a chill roll set to 15–25 °C retains an amorphous morphology that favours optical clarity; pre-drying the resin at 80 °C for 4 h to a residual moisture below 250 ppm reduces hydrolytic chain scission and lactide reformation, which otherwise generates haze and acetaldehyde taint in the packed product. The oxygen transmission rate of unmodified PLA at this gauge measured according to ASTM D3985-17 at 23 °C and 50% relative humidity is reported in the 400–800 cm³/m²·day·atm range for laboratory-cast film, with the higher values corresponding to low-crystallinity film and the lower values to film that has undergone heat-setting or partial orientation. Because carbon dioxide permeates PLA 3–5 times faster than oxygen, the package maintains an equilibrium modified atmosphere that slows enzymatic browning in cut lettuce and cabbage without inducing anaerobic fermentation; however, the actual oxygen and carbon dioxide steady states depend on product respiration rate, fill weight, headspace volume, and storage temperature, so no single film gauge is universally suitable across salad formats. On high-speed vertical form-fill-seal machines running at 40–70 packages per minute, seal jaw temperatures are maintained at 95–110 °C with a dwell of 0.3–0.5 s and a sealing pressure of 0.3 MPa; the narrow window is due to PLA’s tendency to shrink and distort when heated above its glass transition temperature of approximately 55–60 °C. Terminal formats include pillow packs for 120–250 g salad portions, gusseted slaw packs, and microgreen pouches. Compliance at food-contact level is governed by EU Regulation (EU) No 10/2011 overall migration limits of 10 mg/dm² or 60 mg/kg, depending on package geometry, and by EN 13432 when industrial compostability is claimed; the specific additive masterbatch used in a fresh-cut application must be verified because antifog and slip additives influence porosity of the seal interface. At relative humidity above 60% on the converting floor, pre-dried PLA reabsorbs surface moisture within 30–60 minutes, so hopper loading must be coupled with closed-loop dried-air conveying rather than open hoppers.
| Compliance reference | Measured parameter | Limit or criterion | Relevant application |
| EU Regulation (EU) No 10/2011 | Overall migration | 10 mg/dm² or 60 mg/kg | All direct food-contact structures |
| EU Regulation (EU) No 10/2011, Annex I/II | Specific migration of authorised additives | Additive-specific SML | Antifog masterbatch |
| EN 13432 | Disintegration in industrial compost | ≥90% in 12 weeks | Compostability claim |
| EN 13432 | Biodegradation | ≥90% in 180 days | Compostability claim |
| ISO 14855-1:2012 | Aerobic biodegradation test method | Reported as % mineralization | Compostability verification |
| FDA 21 CFR / FCN | Food-contact status | Valid FCN or 21 CFR citation | United States market |
Antifog masterbatches based on glycerol esters or sorbitan derivatives are incorporated at 1–3 wt% into fresh-cut salad film to lower the water contact angle on the inner film surface below 40° after migration begins; at the same time, the additive shifts the heat-seal initiation temperature and may create a low-molecular-weight boundary layer at the seal interface. On a horizontal pouch line sealing 40 μm films at 0.35 MPa and 105–115 °C, seal strengths from 6–12 N/15 mm are obtained with a 2 wt% masterbatch after a 48 h migration period under refrigerated storage at 4 °C; measurements are performed under ASTM F88/F88M. However, raising the masterbatch to 4–5 wt% to achieve faster antifog action typically reduces seal strength by 20–35% and deposits a waxy film on the sealing jaw after fewer than 8 h of continuous production, increasing seal failures and requiring cold-solvent jaw cleaning. This conflict is partly resolved by using a coextruded three-layer film with the antifog additive confined to the inner food-contact layer at 1.5–2.0 wt%, while the sealant layer remains low in migrating additives; such structures are run on three-extruder blown-film lines with layer ratios of 15/70/15 and die temperatures of 195–205 °C. The terminal bag formats are tubular salad sleeves, side-seal pouches, and zip-reclosable packs for 100–500 g portions. Food-contact compliance requires that the migrating additive have a specific migration limit listed in Annex I of (EU) No 10/2011 or a valid FDA FCN; when the antifog is a multi-component blend, the additive supplier’s migration data must cover all constituents. Because PLA softens near 55–60 °C, the seal jaw must not exceed 120 °C or the film neck will stretch in the cross-direction and produce smile-shaped distortions at the pouch mouth.
Monolayer PLA film at 20 μm gauge functions as a moisture barrier of last resort in dry snack packaging; tested at 38 °C and 90% relative humidity under ISO 15106-3:2005 or ASTM F1249-20, the unmodified film typically exhibits a water vapour transmission rate above 200 g/m²·day. That value is an order of magnitude higher than a metallised biaxially oriented polypropylene laminate, making monolayer PLA unsuitable for potato chips, crackers with hygroscopic seasonings, or dried fruit containing less than 10% moisture by mass. The practical manufacturing response is adhesive lamination of 20 μm PLA to a 30–40 g/m² paper or cellulose web on a solventless laminator at 1.5–2.5 g/m² coating weight, followed by 48 h of curing at 30–35 °C. The paper layer consumes moisture absorbed through the printing surface and adds puncture resistance, while the PLA layer provides transparency, sealability, and the renewable-carbon fraction required for EN 13432 claims. Terminal pouches are typically three-side-seal or stand-up formats for granola, oatmeal clusters, and low-moisture cereal snacks; headspace oxygen is eliminated by nitrogen flushing to below 1% residual oxygen in the filling tunnel. Because the laminate is not a homogeneous plastic, the converter must verify that the adhesive does not migrate as a non-intentionally added substance; migration testing is performed under (EU) No 10/2011 with the intended food simulant. Failure modes observed on converting equipment include tunnelling along the lamination nip when the paper moisture exceeds 12%, and curl when the PLA web tension differs from the paper tension by more than 0.25 N/25 mm. These limitations should be treated as process boundary conditions rather than absolute barriers; published data for this specific grade in dry snack laminations is limited, and pilot trials on the target packaging line remain mandatory.
Confectionery twist wrap is one of the few packaging operations where the dead-fold and twist-retention properties of PLA are technically advantageous relative to oriented polyolefins. Film of 25–30 μm gauge is cast and then biaxially oriented in a tenter frame at draw ratios of 2.5–3.5 in the machine direction and 3.0–4.0 in the transverse direction. On a horizontal flow-wrap line running at 300–600 pieces per minute, the material forms a tight twist with a 540–720° rotation and holds closure without adhesive; this eliminates cold-seal pattern registration used for BOPP. The narrow heat-seal window of PLA means that many confectionery converters prefer to apply a 1.0–1.5 g/m² cohesive cold-seal coating on the inner surface and seal by pressure only, avoiding heat entirely. The cold-seal adhesive must be derived from natural rubber latex or synthetic dispersion and must not migrate through the film into chocolate; migration testing follows (EU) No 10/2011. Terminal articles are individually wrapped hard candies, chocolate miniatures, and toffees. The main processing constraints are static build-up below 30% relative humidity and a tendency for the film to become brittle if stored below 15 °C prior to wrapping; converters condition reels for 24 h at 23 °C and 50% relative humidity before loading. Because twist retention depends on crystalline orientation rather than thickness, slitting and winding must maintain edge tension below 0.4 N/25 mm to avoid telescoping of the reels.
PLA film below its glass transition loses ductility, and the loss is measurable in standard dart impact testing. At 23 °C and 50% relative humidity, a 40 μm cast PLA film may exhibit elongation at break of 3–5% under ISO 527-3:2018; at -18 °C, elongation at break commonly drops below 2%, and dart drop impact resistance under ASTM D1709-22 declines by 40–60% relative to room-temperature values. The failure mode in frozen vegetable bag applications is not seal failure but puncture from broccoli florets, corn kernels, and diced carrot edges after the package strikes hard surfaces during distribution. A monolayer 30–40 μm PLA bag is therefore limited to smooth-flowing frozen products such as peas, sweet corn, or sliced green beans with a fill temperature below 5 °C and storage at -20 °C or warmer. Heavy, irregular products require coextruded structures in which PLA is blended with PBAT or PHA at 10–20 wt% to shift the ductile-brittle transition downward; however, published data for this specific INZEA F19 configuration in frozen packaging is limited. The vertical form-fill-seal machine must run with a lower forming shoulder angle than polyethylene to avoid stress whitening, and the unwind path should be shortened to reduce cold-film flexing. Because PLA does not maintain barrier at freezer door temperature cycling, packages are typically overwrapped or packed in secondary cartons to prevent surface condensation that accelerates freezer burn. The relevant compliance framework for frozen vegetables remains (EU) No 10/2011 and EN 13432; a claim of industrial compostability for the package does not imply that the frozen food itself is compostable.
Extrusion coating of PLA onto virgin-fibre board requires corona pretreatment above 40 mN/m and close control of paper moisture between 4% and 8%. A 15–20 μm PLA layer is extruded at 8–20 g/m² onto 180–250 g/m² kraft or virgin-fibre board through a flat die at 225–245 °C; the melt curtain is drawn down at a line speed of 80–150 m/min with an air gap of 150–300 mm. The backside coolant is maintained at 15–20 °C to control curl, while the molten PLA wets the fibre surface after corona treatment. The resulting cupstock is heat-sealable for bottom and side-seam forming on cup machines using heated mandrels at 110–130 °C. The cup is suitable for cold beverages below 50 °C; exposure to boiling water above 90 °C deforms the PLA and fails under the cup rim, so hot-fill tea and coffee are outside the operational boundary. Industrial compostability of the finished cup requires that the paperboard be uncoated or coated with a compostable barrier, and that inks and varnishes also meet EN 13432 criteria; a PLA-laminated cup with petroleum-based printing may still be certified but the testing burden is higher. Field data from converting trials show that inconsistent paper moisture below 4% or above 8% causes pinholing in the PLA layer, while a corona level below 40 mN/m produces delamination at the cup side seam. Because the melt index of PLA changes with moisture, predrying of the resin must keep residual moisture below 250 ppm; wet resin causes bubbles in the melt curtain and thin spots below 10 g/m² that burst on mandrel expansion.
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INZEA F19 Transparent Flexible Food Packaging Film Polylactic Acid is a flexible polylactic acid film grade intended for food-contact web converting. The material is supplied as a transparent-to-translucent film and is used in monolayer form or as a sealant layer in coextruded structures for flow-wrap, twist-wrap, lidding, and pouch applications. The designation places it within the flexible PLA film class because it exhibits lower tensile modulus and higher elongation at break than unmodified biaxially oriented PLA film. Unlike LDPE blown film, the grade is based on renewable carbon and carries a different profile of heat-seal temperature, moisture barrier, and dead-fold. The exact flexibilization approach for INZEA F19 is product-specific and may include copolymerized components or permitted plasticizer systems; for migration assessment, the converter must obtain additive and residual monomer data from the supplier. All numerical values in this document are drawn from public literature for flexible PLA films and standard test methods unless a specific lot certificate is referenced. Lot-to-lot variability in melt viscosity, seal initiation, and optical quality must be controlled through the supplier’s certificate of analysis and incoming film testing.
Film properties are measured under standardized conditions. Tensile properties are determined according to ISO 527-3; haze is tested by ISO 14782; melt flow rate of the base resin may be determined by ISO 1133-1:2022 at 210°C with 2.16 kg load; density is measured by ISO 1183-1. The flexible PLA film class is typically characterized by density of 1.24 g/cm³ to 1.26 g/cm³, tensile modulus of 800 MPa to 1500 MPa, elongation at break of 100% to 250%, and haze of 2% to 8% at a thickness near 25 µm. Published F19-specific values are limited; the current technical data sheet should be used for specification. Seal initiation temperature measured with the method of ASTM F1921 is usually reported between 75°C and 85°C for flexible PLA sealant webs. Plateau seal strength and hot-tack force depend on jaw temperature, dwell time, pressure, and coating thickness. Oxygen transmission rate measured at 23°C and 0% RH according to ASTM F1927 or ISO 15105-2 is typically between 250 cm³·µm/m²·day·atm and 450 cm³·µm/m²·day·atm for PLA film when normalized to thickness, but oxygen barrier declines at elevated humidity. Testing should therefore be conducted at both 0% RH and 80% RH when the package will encounter high-moisture conditions. The renewable carbon content of PLA is above 95% when measured by ASTM D6866-22. Typical melt flow rates for film-grade PLA are 4 g/10 min to 8 g/10 min at 210°C/2.16 kg; higher-flow variants may seal more easily but can exhibit lower melt strength.
| Property / test method | Rigid PLA film | Flexible PLA film class, INZEA F19 position | LDPE blown film |
|---|---|---|---|
| Tensile modulus, ISO 527-3 | 3000 MPa to 3500 MPa | 800 MPa to 1500 MPa | 150 MPa to 300 MPa |
| Elongation at break, ISO 527-3 | 3% to 10% | 100% to 250% | 300% to 600% |
| Haze, ISO 14782 | 1% to 3% | 2% to 8% | 5% to 15% |
| Seal initiation, ASTM F1921 | 80°C to 95°C | 75°C to 85°C | 100°C to 115°C |
| Oxygen transmission rate, 23°C, 0% RH, ASTM F1927 | 250 µm·cm³/m²·day·atm to 450 µm·cm³/m²·day·atm | 250 µm·cm³/m²·day·atm to 450 µm·cm³/m²·day·atm | 2000 µm·cm³/m²·day·atm to 3000 µm·cm³/m²·day·atm |
| Bio-based carbon, ASTM D6866-22 | >95% | >95% | <5% |
Values in Table 1 are representative literature ranges for film classes and do not constitute a specification for any single lot of INZEA F19. Lot-release limits should be taken from the manufacturer certificate of analysis.
In practice, the film is typically converted at thicknesses between 20 µm and 50 µm for monofilm applications. Confectionery twist-wrap lines use the higher stiffness-to-thickness ratio of PLA to retain the twist without adhesive; dead-fold retention is higher than LDPE because of the higher tensile modulus shown in Table 1. Bakery flow-wrap requires a balance of clarity and toughness; if the product contains nuts or sharp dried inclusions, puncture resistance should be screened with ASTM F1306 and the sealant web selected at the upper end of the thickness range. Lidding films for trays of cut fruit or leafy produce require seal-through-contamination robustness and antifog performance; antifog integration must be validated because some antifog additives raise surface energy and may reduce peel performance. Print applications use corona treatment to achieve a surface energy of 38 mN/m to 42 mN/m measured with ISO 8296; water-based inks may require higher treatment or a primer. If the film is used in a coextruded structure with EVOH, tie layers must be selected for adhesion to both PLA and EVOH, and the structure should be tested for interlayer adhesion under ASTM F904.
Line conversion from rigid PLA to a flexible PLA grade is not neutral. Winding tension and dancer-roller pressure must be reduced because the web elongates more under load. Machine-direction stretch in printing presses and slitter rewinders can alter gauge and register if tension is held at values optimized for rigid PLA. Sealing jaw setpoint is lowered relative to rigid PLA. When replacing LDPE, the difference is greater. LDPE seal initiation is generally above 100°C; flexible PLA may initiate at 75°C to 85°C. The usable PLA seal window is commonly 25 K to 35 K wide, so temperature variation across seal jaws should be maintained within ±3 K, preferably with heated-jaw geometry that reduces edge effects. Dwell time should be short enough to limit crystallization at the seal; overcrystallization can produce a brittle seal and low hot-tack. Packaging lines with long dwell times or high seal pressures may need to reduce jaw pressure to 0.3 MPa to 0.6 MPa. Because PLA has lower melt strength than LDPE in many blown-film processes, bubble stability at low thickness is improved by lowering melt temperature and using a blow-up ratio within the 2:1 to 3:1 range. Tear-initiation resistance measured by ASTM D1004 is lower for thin PLA films than for LDPE; sharp-edged products may require thicker gauge or blended structures. Compared with PBAT/starch blends, the F19 class retains higher stiffness and lower haze but may exhibit lower puncture deformation; for high-abuse applications, lamination or blending may be necessary. The F19 class is therefore best positioned for lines that can operate at lower seal temperatures and with precise tension control, rather than as a direct drop-in replacement on high-slip LDPE packaging machines.
Before extrusion, PLA resin and reclaimed film must be dried. The target residual moisture is below 250 ppm, achieved in a desiccant dryer with a dew point of −40°C or lower. Drying at 80°C for 4 h is typical; higher temperatures can cause clumping and should be avoided unless the dryer is designed for low-temperature crystalline resins. Single-screw extruders with length-to-diameter ratios between 24:1 and 30:1 are employed. Barrel zones are often set with a flat or reverse profile: feed zone 160°C to 170°C, compression zone 170°C to 190°C, metering zone 180°C to 200°C, and die at 190°C to 210°C. Melt temperatures at the die range from 180°C to 210°C for cast film and 170°C to 200°C for blown film. Temperatures above 230°C should be avoided because PLA undergoes thermal degradation and molecular weight loss. Cast film die gaps are normally 0.8 mm to 1.2 mm; chill roll temperatures of 15°C to 25°C are used to avoid blocking and to manage crystallinity. For blown film, blow-up ratios between 2:1 and 3:1 are applied, and the collapsing frame should have low friction because the film can block or scratch. Regrind levels up to 20 wt% are used when the scrap is clean and dry; repeated extrusion histories reduce melt viscosity and narrow the processing window. Converters should monitor melt pressure and motor load as indirect measures of molecular weight retention. Corona treatment may be applied in-line or off-line; if off-line, surface treatment should be repeated immediately before printing or lamination because treated PLA surface energy decays over time.
Food-contact compliance for INZEA F19 must be determined on the final food-contact article. Under EU Regulation (EC) No 10/2011, the overall migration limit must be met in the correct simulant for the food type and contact time. For many refrigerated or ambient packaging uses, migration testing is performed at 40°C for 10 days; fatty and acidic foods may require simulants D1 and B according to Annex III. In the United States, the supplier should identify the applicable Food Contact Substance Notification or FDA citation; general reliance on 21 CFR 175.300 or 177.1520 is not automatically valid for PLA. The converter must also assess the migration of plasticizers, slip agents, antiblock agents, printing inks, laminating adhesives, and coatings. Industrial composting certification may be available under EN 13432 or ASTM D6400. Testing requirements include 90% biodegradation within 180 days per ISO 14855-1 and 90% disintegration after 12 weeks through a 2 mm screen. Home composting and marine degradation are not automatically satisfied. REACH registration and REACH Article 33 SVHC disclosure should be provided by the supplier; RoHS Directive 2011/65/EU may not apply to packaging film, but heavy-metal limits in packaging are normally covered by packaging regulations such as 94/62/EC in the EU.
| Requirement | Standard or method | Typical threshold / status |
|---|---|---|
| EU food-contact overall migration | EU 10/2011 Annex III, Annex V | Final article testing required |
| US FDA food contact | Supplier FCN / 21 CFR citation | Product-specific statement required |
| Biodegradation | ISO 14855-1 / EN 13432 | 90% in 180 days |
| Disintegration | EN 13432 | 90% through 2 mm screen |
| Bio-based carbon | ASTM D6866-22 | >95% typical PLA |
| SVHC disclosure | REACH EC 1907/2006 Article 33 | Supplier declaration required |
| Packaging heavy metals | 94/62/EC or national law | Sum below 100 ppm for Pb, Cd, Hg, Cr(VI) |
Table 2 is a compliance checklist. Exact status depends on the final film construction, additives, inks, coatings, and adhesives.
The oxygen and water vapour barrier of the F19 film class is moderate compared with EVOH or metallized films. PLA oxygen permeability increases with relative humidity because water plasticizes the matrix; therefore, dry-food barrier testing at 0% RH does not represent high-humidity conditions. For products requiring low oxygen ingress or high moisture retention, a coextruded or laminated barrier layer is necessary. Water vapour transmission rate measured by ASTM E96/E96M is higher than that of polyethylene-based structures at equal thickness. Heat-seal strength of flexible PLA films is typically lower than LDPE at the same thickness. Sealed-seam strength measured by ASTM F88/F88M may be in the range of 5 N/15 mm to 10 N/15 mm for flexible PLA monolayer webs, but F19-specific values should be confirmed. Hot-tack force measured by ASTM F1921 is lower than LDPE and may require longer cooling bars on vertical form-fill-seal equipment. Continuous service temperature is limited by the glass transition of PLA near 55°C to 60°C; amorphous films can deform at temperatures above 40°C to 45°C. Hot-fill, retort, and steam sterilization are not recommended unless the article is crystallized and validated. For disposal, industrial composting may be possible where the film is certified under EN 13432 or ASTM D6400, but the presence of laminates, inks, or adhesives can inhibit compostability. Mechanical recycling of PLA requires segregation from conventional polymer streams; near-infrared sorters may be needed because PLA density can overlap with other polymers and is incompatible with PET recycling. The material should not be introduced into polyolefin or PET reclaim streams without a dedicated waste-management agreement.