| HS Code | 928614 |
| Product Name | INZEA FH0850S Flexible 50% Bio-Based Film Polylactic Acid |
| Material Type | Polylactic Acid (PLA) based flexible film compound |
| Bio Based Content | 50% |
| Form | Pellets |
| Processing Method | Film extrusion |
| Density | 1.24-1.25 g/cm³ |
| Melt Flow Rate | 6-8 g/10 min (190°C/2.16 kg) |
| Melting Temperature | 150-160 °C |
| Glass Transition Temperature | 55-60 °C |
| Tensile Strength | 35-40 MPa |
| Elongation At Break | 250-350% |
| Tensile Modulus | 1000-1200 MPa |
| Flexural Modulus | 1200-1500 MPa |
| Vicat Softening Temperature | 60 °C |
| Heat Deflection Temperature | 50 °C |
| Color | Natural |
As an accredited INZEA FH0850S Flexible 50% Bio-Based Film Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INZEA FH0850S Flexible 50% Bio-Based Film Polylactic Acid is supplied in 25 kg moisture-barrier foil-lined bags, palletized for industrial use. |
| Container Loading (20′ FCL) | Palletized INZEA FH0850S PLA film loaded in 20′ FCL; keep dry, ambient, secured, within weight limits, protected from heat/moisture. |
| Shipping | INZEA FH0850S Flexible 50% Bio-Based Film Polylactic Acid is shipped as a non-hazardous solid in sealed, moisture-barrier packaging on pallets. Keep dry, cool, and away from direct heat. Typically not regulated for DOT/IMDG/IATA unless local rules specify otherwise. Follow supplier SDS and transport regulations. |
| Storage | Store INZEA FH0850S Flexible 50% Bio-Based Film Polylactic Acid in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep in original sealed packaging, protect from dust, UV, and physical damage. Avoid prolonged high temperatures, humidity, and strong oxidizing agents. Follow supplier SDS and local regulations. |
| Shelf Life | Shelf life is 12 months when stored in original unopened packaging, cool, dry, and protected from sunlight and moisture. |
Residual moisture in INZEA FH0850S pellets is reduced to below 250 ppm before melt processing because the ester backbone undergoes hydrolytic chain scission at typical extrusion residence times if water is present above 400 ppm. A desiccant-bed dryer with a −40 °C dew point air supply and 75–80 °C hopper temperature for 4–6 h is used; when ambient relative humidity exceeds 60 %, the drying cycle is extended by 2 h and the inlet air is maintained at 80 °C. Melt flow rate is checked by ISO 1133-1:2022 at 190 °C/2.16 kg; typical flexible PLA film grades fall between 4 g/10 min and 8 g/10 min, but FH0850S-specific lot values govern acceptance. On a 50 mm mono-layer blown-film line with a 30:1 L/D barrier screw, 2.5:1 compression ratio, and 60/80/100 mesh screen pack, barrel set points are ramped from 160 °C at the feed throat to 185 °C at the metering section; the spiral mandrel die is held at 180–190 °C with a 1.2 mm lip gap. A blow-up ratio of 2.2:1 to 2.8:1 and a frost-line height of 4–6 die diameters are balanced to maintain transverse direction orientation while preventing excessive haze; reducing the frost line to below 3 die diameters increases bubble stability but produces measurable thickness bands and lower dart impact.
Slip and antiblock masterbatch is pre-compounded at 1.0–2.0 wt%; addition above 3.0 wt% depresses tensile modulus and tear propagation but improves unrolling on automated bagging machines. The 20–30 µm film is intended for perforated or unperforated produce bags and bakery films where high transparency and industrial compostability are required. Bio-based carbon fraction is verified according to ISO 16620-2:2019 or ASTM D6866-22 as 50 % biogenic carbon. Industrial compostability is assessed under EN 13432:2000/AC:2005 with 58 ± 2 °C thermophilic incubation; ASTM D6400-23 is applied for US municipal composting claims. Food contact is tested to EU Regulation No 10/2011 Annex I with a 10 mg/dm² overall migration limit using simulant B for 10 days at 40 °C; for US use, compliance with FDA 21 CFR 177.1500 or a valid food-contact notification is required. Film tensile properties are measured by ISO 527-3:2018 at 200 mm/min; typical values for flexible PLA film of this thickness range fall between 35 MPa and 45 MPa machine-direction tensile strength, but published FH0850S-specific data on this exact line configuration is limited and converter trials are required before setting acceptance limits. Dart impact by ASTM D1709-16a Method A on 25 µm film is expected in the 30–50 g range, and tear propagation by ASTM D1922-19 can be lower than polyolefin film, which must be considered in bag design.
Seal initiation for FH0850S on a heat-seal jaw begins between 105 °C and 115 °C; below 100 °C, peel strength measured by ASTM F88/F88M-23 drops below 3 N/25 mm because the thermal interface does not reach the melt-solid transition required for chain interdiffusion. At jaw temperatures above 125 °C, film thinning at the seal root and shrinkback reduce burst resistance; the practical sealing window is therefore 10–20 °C wide, which is narrower than for low-density polyethylene and demands closed-loop temperature control. Dwell time is set at 0.3–0.6 s with 0.4 MPa jaw pressure. For dry snack and granola pouches run on a vertical form-fill-seal machine at 1.2 m/s linear film speed, dancer tension of 10 kg and a serrated sealing jaw profile produce machine-direction seal strengths of 6–9 N/25 mm when the film has been corona treated to 42–46 mN/m prior to printing. Storage above 45 °C decreases seal strength retention because the oriented amorphous fraction relaxes, so the configuration is limited to ambient or chilled product distribution and is not suitable for hot-fill, retort, or microwave-assisted reheating. Oxygen transmission at 23 °C and 0 % RH by ASTM D3985-17 for a 25 µm mono-layer is typically 500–800 cc/m²·day, which is sufficient for dry goods with limited oxidative shelf-life requirements but insufficient for high-fat snacks without an additional barrier layer. Laminate construction with compostable adhesives at 1.5–2.0 g/m² dry coat weight improves puncture resistance; however, lamination with PE or PP layers would prevent disintegration because the final package would not meet the EN 13432 requirement of 90 % fragmentation after 12 weeks in the thermophilic phase.
Molten FH0850S at 200–210 °C is delivered through a 0.6 mm flexible-lip flat die as a 15–25 µm coating onto one-side clay-coated paperboard for cold beverage cups and food trays. Adhesion relies on mechanical anchoring into the clay coating and surface oxidation; corona pre-treatment of the paperboard to 44–48 mN/m or the use of a waterborne primer improves peel adhesion above 200 g/25 mm under ASTM D1876-08. A chill roll temperature of 15–20 °C is maintained to reduce post-extrusion crystallization and maintain flexural crack resistance when the coated board is die-cut and folded. Coating weight below 12 µm leads to pinhole defects at fold lines; above 30 µm the composite becomes excessively stiff and may delaminate during blanking. The extrusion lamination line is equipped with a 120 mm screw and 28:1 L/D, screen pack 100/120/150 mesh, and barrel temperatures from 180 °C to 205 °C. Because the process operates near the upper thermal stability limit of PLA, residence time at temperature is kept below 15 min and barrel purging is performed before shutdown; the polyester backbone crosslinks and forms gels when held above 210 °C with residual water above 100 ppm. The resulting paperboard composite is used for cold beverage cups, salad bowls, and grab-and-go food cartons; certification under EN 13432:2000/AC:2005 applies to the coating as a compostable component, while the board itself must also comply or the entire structure is assessed as a composite. For food contact, the paperboard is food-grade and the FH0850S coating is evaluated to EU Regulation No 10/2011 with 10 mg/dm² overall migration; hot-fill above 50 °C is excluded because warp and seal relaxation occur.
| Parameter | Blown produce bags | VFFS side-gusset pouches | Extrusion lamination | Thermoforming sheet |
|---|---|---|---|---|
| Melt temperature (°C) | 170–190 | 180–195 | 200–210 | 185–205 |
| Die gap / coating weight | 1.2 mm | 0.8–1.0 mm | 0.6 mm die, 15–25 µm coat | 0.4–0.8 mm sheet die |
| Chill roll / frost line | Frost line 4–6 die diameters | N/A | Chill roll 15–20 °C | Chill roll 25–40 °C |
| Thickness (µm) | 20–30 | 40–70 | 15–25 | 300–800 |
Sheet extrusion for FH0850S uses a chill-roll stack with roll temperatures of 25 °C, 35 °C, and 40 °C to control crystallinity and residual stress. At sheet gauges below 0.8 mm, the heat capacity of the sheet is low, and plug-assist thermoforming requires differential oven zone set points of 80 °C, 90 °C, and 95 °C to bring the core surface to 85–95 °C without overheating the edges; edge fold-over and bridging occur if the bottom zone exceeds 100 °C. The plug assist is heated to 60–80 °C and the cavity mold is held at 30 °C. Draw ratios above 3:1 lead to uneven wall thickness and stress whitening at the bottom corners, so draft angles of 5–8° and cavity depths below 60 mm are specified for deli containers and hinged clamshells. Compliance with EU Regulation No 10/2011 and FDA 21 CFR food-contact provisions is required for refrigerated deli containers, fruit clamshells, and cold food tubs; the containers are not suitable for hot fill above 50 °C or domestic microwave reheating because wall deformation occurs near the glass transition. Post-trimming regrind can be re-extruded into the sheet core at 15–20 wt% if the flake is dried to below 250 ppm moisture; higher regrind levels reduce sheet ductility and increase gel specks. Published dart impact data for FH0850S thermoformed containers under ASTM D1709 are limited; converter-specific drop tests are recommended.
| Requirement | Standard | Test condition / limit |
|---|---|---|
| Industrial compostability | EN 13432:2000/AC:2005 | ≥ 90 % disintegration in 12 weeks at 58 ± 2 °C; ≥ 90 % biodegradation by 180 days |
| US compostability | ASTM D6400-23 | Conforms to ASTM D6868-21 provisions for coatings |
| Food contact overall migration | EU Regulation No 10/2011 | 10 mg/dm² simulant B, 10 days @ 40 °C |
| US food contact | FDA 21 CFR 177.1500 or applicable FCN | End-use condition A–H depending on food type |
| Bio-based carbon content | ISO 16620-2:2019 or ASTM D6866-22 | 50 % biogenic carbon fraction |
Addition of post-industrial regrind to FH0850S carrier bag extrusion is limited to 15–20 wt% because repeated thermal processing lowers melt viscosity and darkens the melt. On a 65 mm grooved-barrel blown-film line with 28:1 L/D, the melt pressure upstream of the screen changer increases from 220 bar at 0 % regrind to 280 bar at 20 % regrind; a continuous melt filter with 200 µm mesh is used to remove gel streaks. The die lip gap is 1.4 mm, the blow-up ratio is 2.5:1, and the frost line is 5 die diameters. Carrier bag conversion at 80 bags/min uses seal temperature 115 °C and 0.4 s dwell. Film thickness of 35–50 µm is selected for retail carrier bags; thin gauges below 30 µm show splitting at the side seal on automatic bag opener machines. Mechanical properties per ISO 527-3:2018 for 40 µm film are expected to show machine-direction tensile strength in the 35–45 MPa range and elongation at break between 200 % and 300 %, but FH0850S-specific certificate data should be used. The bag is designed for industrial composting under EN 13432:2000/AC:2005 and not for home composting unless a separate home composting certification is obtained. The film must not be compounded with amine-based stabilizers because amine groups accelerate ester chain scission; aromatic or aliphatic diisocyanates are also excluded due to migration risk and loss of food-contact suitability.
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INZEA FH0850S Flexible 50% Bio-Based Film Polylactic Acid is a compounded film extrusion grade in which renewable carbon is declared as 50% under radiocarbon accounting. The product is intended for cast and blown film lines where polylactic acid is combined with a flexible non-PLA phase to overcome the low elongation and tear resistance of unmodified PLA homopolymer. The material is supplied as pellets and should be read as a film-grade compound rather than a neat PLA resin. The exact formulation is proprietary and may include bio-based or fossil-derived polymeric modifiers, processing stabilizers, slip additives, and nucleating agents. Because the term “bio-based” is a carbon-fraction designation and not necessarily a mass-fraction claim, converters should use the supplier’s certificate of analysis for lot-specific renewable carbon values.
The FH prefix identifies a flexible film grade. The 0850 digits may encode melt-flow range, additive package, or product generation according to the manufacturer’s internal nomenclature. An S suffix is commonly associated in film resins with slip or surface-modification additives, but the specific composition of INZEA FH0850S is not fully disclosed in public literature. Published data for the exact melt mass-flow rate, thermal transitions, and mechanical properties of this grade should therefore be obtained from the manufacturer’s current technical datasheet or measured on arrival. This qualification step is necessary because PLA compounds can shift through additive hydrolysis, stabilizer depletion, or lot-to-lot molecular weight variation.
The renewable carbon fraction is not equivalent to renewable mass fraction. A 50% bio-based carbon result under ASTM D6866-22 or EN 16785-1:2015 means that half of the total organic carbon in the sample contains contemporary radiocarbon. The PLA backbone contributes the majority of renewable carbon in this class; non-PLA modifiers may be fully or partially fossil-derived without reducing the carbon fraction below the declared level. If the formulation contains inorganic fillers, the mass-based bio-content can differ substantially. For formal compliance, the report should specify the standard, sample preparation, and radiocarbon result expressed as percent modern carbon or percent bio-based carbon. ISO 16620-2:2019 provides a corresponding framework for bio-based carbon in plastics, while EN 16785-1:2015 uses radiocarbon plus elemental analysis to correct for carbon from inorganic sources. This distinction matters in packaging procurement because a 50% bio-based carbon claim cannot be directly compared with a 50% renewable mass claim or a 50% biomass content under ISO 14040-based life-cycle accounting.
For film converters, the practical consequence is that the grade retains only part of the end-of-life attributes of a high-purity PLA. Industrial compostability is not an automatic property of a 50% bio-based carbon compound; it must be demonstrated under EN 13432:2000 or ASTM D6400-21. Final-film biodegradability is governed by all organic constituents, including non-PLA phases. The 50% designation is therefore an input-material specification, not a finished-film biodegradability certificate.
Moisture control is the first process constraint. PLA-based film grades are hydrolytically degraded when heated with excessive water; the reaction reduces molecular weight, lowers melt viscosity, and produces film defects such as fisheyes, gauge bands, and reduced tensile impact strength. On production-scale desiccant-dryer systems, a dew point of −40 °C is normally accepted for PLA compounds. Hopper residence times of 4–6 h at 70–80 °C are typical for pelletized semi-flexible PLA film compounds, but the exact profile for INZEA FH0850S should be confirmed against the manufacturer’s processing guide. Target residual moisture before extrusion is below 250 ppm measured by ISO 15512:2019. Higher moisture levels are a common root cause of intermittent pressure fluctuations and film gels.
For blown film, single-screw extruders with length-to-diameter ratios of 24:1 to 30:1 and barrier or Maddock mixing sections are used to complete melting before the die. Melt temperatures between 170 °C and 190 °C are commonly reported for semi-flexible PLA film grades; excursions above 200 °C accelerate thermal degradation of the PLA segment and can shift melt viscosity, causing bubble instability. Die temperature setpoints are typically kept within ±5 °C across the circumference to prevent helical gauge variation. A die gap of 0.8–1.2 mm and a blow-up ratio of 1.5–2.5 are representative for flexible PLA compounds on conventional polyolefin lines, though the exact frost-line height is line-specific and is set to balance bubble stability with transverse orientation. On cast film lines, the melt curtain is pinned to a chill roll at 15–30 °C; the air gap is minimized to reduce neck-in and preserve web flatness.
Unlike semi-crystalline PLA homopolymer, flexible film compounds may show lower melt strength. Bubble stability is therefore more sensitive to screw speed and die pressure than to the thermal profile alone. A melt filtration stage with screen packs from 100 mesh upward is often inserted before the die to remove partially melted or crosslinked agglomerates. Processors commonly observe that sudden reductions in melt pressure at constant screw speed without changes in temperature indicate molecular weight loss from hydrolysis or thermal chain scission. The corrective action is to reduce throughput and verify dryer performance before raising temperatures. Suppliers of PLA compounds typically recommend purging with a stable polyolefin or a dedicated PLA purge compound after shutdown because material left in the barrel at processing temperature can degrade and form black specks during subsequent starts.
For monolayer film evaluation, the key mechanical distinction is elongation behavior. Unmodified PLA film typically exhibits low elongation at break in the machine direction, often below 10% under ASTM D882-18, whereas flexible PLA compounds are formulated to yield tensile elongation values above 200%. INZEA FH0850S is positioned in the flexible range of this spectrum. Published data for the exact tensile modulus, tear strength, and seal strength of this specific compound are limited and should be verified per lot. Tear propagation resistance is assessed under ASTM D1922-15; the flexible phase improves resistance to brittle tear. Impact energy measured by free-falling dart under ASTM D1709-16 is similarly higher than for rigid PLA but remains below that of high-molecular-weight LDPE in many formulations.
Heat-seal response is a defining converting property. Flexible PLA film grades generally show seal initiation at lower temperatures than rigid PLA because the non-PLA phase softens before the PLA crystalline melting point. For validation, a heat-seal curve should be generated on the actual packaging line using seal-strength measurement under ASTM F88. A single seal temperature is insufficient because seal initiation, plateau strength, and hot tack involve different failure mechanisms. Typical conditions for flexible PLA compounds fall within seal-bar temperatures of 90–130 °C and dwell times of 0.5–1.0 s at moderate pressure, but these are not material constants. Hot-tack performance depends on melt rheology more than seal strength and should be evaluated if vertical form-fill-seal operation is intended.
| Property | Test method | Rigid PLA | Flexible PLA compound class, including INZEA FH0850S | LDPE |
|---|---|---|---|---|
| Bio-based carbon | ASTM D6866-22 | 90–100% | 50% declared | 0% |
| Film elongation at break | ASTM D882-18 | 2–10% | Generally above 200%; verify per lot | 200–600% |
| Density | ISO 1183-1:2019 | 1.24–1.26 g/cm³ | 1.22–1.26 g/cm³ class | 0.918–0.930 g/cm³ |
| Softening temperature | ISO 306 | Higher | Controlled by PLA glass transition | Lower than PP but broad |
| Compostability | EN 13432:2000 | Usually certified | Requires formulation-specific certification | Not compostable |
The product is selected when the film must combine a partial renewable carbon contribution with flexibility that neat PLA cannot provide. Compared with a rigid PLA film, INZEA FH0850S sacrifices some bio-based carbon and stiffness. Rigid PLA grades routinely exceed 90% bio-based carbon and display higher tensile modulus and higher heat resistance, but they fail by brittle fracture at low elongation. Polybutylene adipate terephthalate blends may offer high elongation and compostability, but they often contain little or no renewable carbon unless specifically formulated with starch or PLA. Compared with LDPE, INZEA FH0850S offers a renewable carbon fraction but generally lower tear strength, lower seal strength, and a narrower heat-seal operating window. It is therefore not a drop-in replacement for LDPE in demanding applications such as heavy-gauge trash liners or frozen-food pouches without redesigning the film structure. Compared with high-purity PLA/PBAT compostable films, the 50% bio-based carbon value suggests that the formulation may contain a significant fossil-derived or non-compostable phase; end-of-life claims must be verified against EN 13432:2000 or ASTM D6400-21.
Within the INZEA grade range, the FH prefix differentiates flexible film products from grades designated for rigid film, sheet, or injection molding. The 50% bio-based carbon value of FH0850S should not be confused with higher-renewability grades that may approach 90–100% bio-based carbon but exhibit lower elongation. The S suffix may indicate surface modification; if slip properties are required, coefficient of friction should be checked under ASTM D1894-14 because slip additives can change with ageing and temperature. The exact composition and additive package should be obtained from the manufacturer’s safety data sheet and technical data sheet before using the film in food contact or high-speed converting.
In application terms, the grade is suited to film structures where moderate flexibility, transparency potential, and partial renewable carbon are required. Typical uses include light-duty shopping bags, dry-goods overwrap, magazine or mailing wrap, and industrial liners not exposed to wet or hot contents. The material is less appropriate for microwaveable packages, hot-fill pouches, retort pouches, or sustained outdoor exposure. Continuous service near or above the PLA glass-transition temperature of approximately 55–60 °C can produce progressive dimensional change, and the hydrolytic sensitivity of the PLA phase limits direct contact with high-moisture foods unless a barrier layer or lamination is used. Film stiffness and seal strength should be confirmed for vertical form-fill-seal lines with short dwell times.
Water-vapour transmission rate and oxygen transmission rate are also relevant. PLA-based films are moderate gas barriers but are more hydrophilic than polyolefins; measured WVTR is higher than LDPE at equivalent thickness. For applications requiring shelf-life extension, a barrier coating or coextruded layer may be required. Barrier data should be obtained under ASTM F1249-20 for water vapour and ASTM D3985-17 for oxygen at controlled relative humidity. The flexible non-PLA phase can either increase or decrease WVTR depending on its polarity and crystallinity. Published data for this specific configuration is limited and should be measured on the final film structure rather than inferred from neat PLA values.
For regulatory compliance, the base PLA fraction may fall under FDA 21 CFR 177.1520 if the resin complies with applicable specifications, but the compounded grade as supplied may not have a global food-contact clearance. EU food-contact compliance must be demonstrated on the finished film under Regulation EU 10/2011, with overall migration below 10 mg/dm² and specific migration limits for additives. REACH Article 33 communication applies only if the product contains substances of very high concern above 0.1% w/w. RoHS restrictions apply mainly to electrical and electronic equipment components and not to packaging films unless incorporated into EEE. For industrial compostability, EN 13432:2000 requires at least 90% disintegration after 12 weeks, at least 90% biodegradation within 180 days, and no adverse ecotoxicity. A 50% bio-based carbon compound does not automatically satisfy these criteria; certification of the exact film structure is required.