| HS Code | 590619 |
| Material Type | Biodegradable PLA blend |
| Density | 1.25–1.28 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 3–5 g/10 min |
| Melting Temperature | 150–155 °C |
| Vicat Softening Temperature | 55–60 °C |
| Tensile Strength | 30–35 MPa |
| Elongation At Break | 300–350% |
| Tensile Modulus | 1500–1800 MPa |
| Biobased Carbon Content | >50% |
| Biodegradability Certification | EN 13432 |
| Processing Method | Blown film extrusion |
| Processing Temperature | 160–180 °C |
| Recommended Film Thickness | 20–60 µm |
| Moisture Content | <0.2% |
As an accredited Bio-Flex F 1110 Blown Film Biodegradable PLA Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Bio-Flex F 1110 Blown Film Biodegradable PLA Blend supplied in 25 kg polyethylene-lined paper bags, 40 bags per pallet, shrink-wrapped. |
| Container Loading (20′ FCL) | 20′ FCL: approximately 18–20 MT of Bio-Flex F 1110 pellets, packaged in 25 kg bags or big bags. |
| Shipping | Bio-Flex F 1110 Blown Film Biodegradable PLA Blend ships as non-hazardous solid pellets in moisture-barrier 25 kg sacks or 1000 kg bulk bags, palletized and stretch-wrapped. Store dry, cool, ventilated, away from direct sunlight, heat, and moisture. Handle with standard PPE; avoid dust generation and prolonged skin contact. |
| Storage | Store Bio-Flex F 1110 in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and incompatible materials. Keep original packaging sealed to prevent moisture absorption. Recommended conditions: below 30°C and low humidity. Use first-in, first-out stock rotation. Inspect containers regularly, protect from dust and contamination, and follow supplier SDS/local regulations. Avoid excessive stacking and rough handling to prevent bag damage. |
| Shelf Life | Shelf life is typically 12 months when stored in original unopened packaging in a cool, dry environment; avoid moisture and high temperatures. |
The conversion of Bio-Flex F 1110 into single-ply compostable retail carrier film on high-output blown-film lines is constrained by the compound’s narrow processing window and lower melt strength relative to LDPE; the material is processed as supplied at 100% compound without the addition of regrind above 20 wt%, because recycled PLA-dominant film reintroduces hydrolytically degraded chains that lower bubble stability. Melt temperature measured at the die exit is maintained between 155 °C and 170 °C; exceeding 180 °C for more than 3 min residence time triggers measurable random chain scission, observable as a rise in melt flow rate under ISO 1133-1:2022 and a loss of dart drop puncture energy. The monolayer film, typically 18–30 µm, falls under the harmonized industrial composting standard EN 13432:2000, with clause 4.2.2 requiring 90% ultimate biodegradation within 180 days, clause 4.2.3 requiring physical disintegration of >90% of fragments to <2 mm after 12 weeks, and clause 4.2.4 mandating absence of ecotoxicity in plant growth tests; parallel certifications under ASTM D6400-19 and ISO 17088:2021 are recognized for North American and global markets. Tensile acceptance values for finished bags are determined by EN ISO 527-3:2018, dart drop by ISO 7765-1:1988, and Elmendorf tear by ASTM D1922-15; converters typically require minimum dart drop impact of 600 g for a 25 µm monolayer film and machine-direction tear resistance of at least 20 N/mm to survive automatic bag insertion in retail self-checkout lanes. Production on a single-screw blown-film extruder with an L/D ratio of 30:1 to 36:1, a barrier screw with Maddock mixing elements, and a die gap of 0.8–1.4 mm permits stable bubble formation at blow-up ratios of 2.5:1 to 4.0:1. Use of a dual-lip air ring is mandatory when line speeds exceed 80 m/min; above this threshold, the low melt strength of the PLA-rich matrix creates asymmetric frost line positions and causes gauge deviations above ±8%. Internal bubble cooling (IBC) reduces this deviation to ±4% and stabilizes the bubble for in-line conversion. Exact melt flow rate and moisture uptake limits must be taken from the supplier’s technical datasheet; the general requirement for PLA-dominant blown film compounds is pre-drying to below 400 ppm moisture when ambient relative humidity exceeds 60% RH. Terminal products include vest-style carrier bags, bottom-seal checkout bags, and roll-mounted produce bags; die-face cutters and rotary bag machines require 2–5 wt% of a slip/antiblock masterbatch to maintain dynamic coefficient of friction below 0.35 under ISO 8295:1995 and to suppress film-to-film blocking at storage temperatures above 35 °C.
For kerbside organic waste caddy liners and kitchen countertop collection bags, Bio-Flex F 1110 is converted into film thicknesses between 20 µm and 35 µm. The compound is run neat at 100% in most certified home-compostable constructions; however, when downstream filling lines impose puncture energies above 3 J on wet, compacted feedstock, converters may incorporate 5–12 wt% of a PBAT-rich impact modifier masterbatch. Such dilution shifts the stiffness-to-tear balance and requires re-validation of the finished article under the intended certification scheme because the addition of PBAT changes the ultimate biodegradation profile under EN 13432:2000 clause 4.2.2 and under the home-composting standard NF T 51-800:2015 where the temperature plateau is 25 ± 5 °C rather than 58 ± 2 °C. The dominant mechanical failure mode in these liners is not tensile yield but slow tear propagation initiated at pinholes formed during collection; Elmendorf tear resistance measured by ASTM D1922-15 on machine-direction specimens should remain above 30 N/mm for 25 µm film, while puncture resistance under EN 14477:2004 should exceed 800 mN for the same gauge. Blown-film processing for this application uses barrel temperature profiles from 150 °C in the feed throat to 170–175 °C at the die, with an actual melt temperature not exceeding 178 °C. A grooved feed section is recommended because the compound’s granule surface friction under high screw speeds exceeds that of LDPE and can cause feed-block bridging in smooth-bore barrels. Die gap is set at 0.9–1.5 mm, blow-up ratio at 3.0:1 to 4.5:1, and frost line height at 5–7 die diameters; higher BUR values increase transverse direction tear resistance but reduce machine-direction output stability, manifesting as sag-induced bubble wander after 6 h of continuous operation. Operational boundary: liners should not be used for waste streams containing standing water above 55 °C; sustained contact with such hot wet loads accelerates hydrolytic chain scission and reduces tear resistance by more than 40% within 72 h. Terminal products include vented kerbside caddy liners, tie-handle kitchen waste bags, and certified compostable waste sacks for organic waste streams; pinhole testing per ASTM F1306-21 is applied at a minimum threshold of 0.4 N/15 mm slow puncture force to eliminate premature rupture during transport.
| Application segment | Primary biodegradation/compostability standard | Food-contact / chemical safety basis | Key mechanical test method |
|---|---|---|---|
| Retail checkout bags | EN 13432:2000, ASTM D6400-19 | Not food-contact; REACH | ISO 7765-1:1988, ASTM D1922-15 |
| Organic waste liners | EN 13432:2000, NF T 51-800:2015 | Not food-contact; REACH | EN 14477:2004, ASTM F1306-21 |
| Agricultural mulch | EN 17033:2018, ISO 17556 | Not food-contact; REACH; USDA BioPreferred optional | ISO 4892-3:2016, ASTM D638-14 |
| Produce overwrap | EN 13432:2000 optional | EU 10/2011, FDA 21 CFR 175.300 | ASTM F2029-16, ISO 15106-3:2009 |
| Apparel polybags | EN 13432:2000 optional | Not food-contact; REACH | IEC 61340-2-3:2016, ISO 8295:1995 |
| Magazine wrap | EN 13432:2000, AS 4736:2006 | Not food-contact; REACH | ISO 8295:1995, ASTM D1922-15 |
Soil-biodegradable mulch film made from Bio-Flex F 1110 is used in annual row-crop systems where retrieval and landfill disposal of conventional polyethylene mulch would impose mechanical labor costs and where fragments left in soil must not accumulate as secondary microplastics. The governing standard is EN 17033:2018, which requires 90% ultimate soil biodegradation within 24 months under ISO 17556 test conditions at 20–28 °C, and which prohibits any negative effects on plant germination or invertebrate survival in ecotoxicity assays; the corresponding U.S. approach relies on ASTM D5988-18 and the USDA BioPreferred voluntary certification rather than a federal compostability mandate. For black mulch, 2–5 wt% of a carbon black masterbatch with a soil-biodegradable carrier resin is incorporated to reduce photo-oxidative chain scission on the film surface; the effect is quantified by tensile elongation retention after QUV exposure under ISO 4892-3:2016, with pass/fail thresholds fixed by the crop service-life requirement rather than by a universal numeric value. The blown-film conversion runs at 10–20 µm final thickness, which is thinner than retail carrier film and therefore demands a lower blow-up ratio of 2.0:1 to 3.0:1 and a die gap of 0.8–1.2 mm to avoid excessive transverse orientation that would raise moisture vapor transmission above the crop’s soil-warming requirement. Melt temperature is held at 155–165 °C, and barrel residence time is limited to <4 min because prolonged exposure above 165 °C pre-hydrolyzes the polymer before soil burial, reducing the molecular weight to below the entanglement threshold and causing premature slitting failures during mechanical laying. Specialty equipment includes a rotating die or an oscillating haul-off for layflat widths up to 1,200 mm, and a surface treater for printing plant rows and brand identification; corona treatment is maintained at 38–42 mN/m to prevent ink rub-off during machine installation. Terminal products include black and transparent soil-biodegradable mulch film for tomato, pepper, melon, and strawberry cultivation, as well as ridge covers for asparagus beds. Operational boundaries are explicit: the film must be incorporated into microbially active soil with moisture above 30% water-holding capacity and soil temperature above 10 °C for meaningful biodegradation; in arid or permanently cold soils, fragmentation may occur but ultimate biodegradation will be retarded beyond the 24-month window, leaving visible residues that violate the intended end-of-life profile.
Flow-wrap overwrap for fresh-cut produce, herbs, and bakery items formulated from Bio-Flex F 1110 requires a different set of conversion parameters than retail carrier film because optical clarity and seal integrity on horizontal form-fill-seal machines dominate performance. The film is run at 100% compound in monolayer structures between 12 µm and 25 µm for pillow packs, or as a coextruded skin layer at 10–25% of total thickness over a PBAT-rich core when a seal initiation temperature below 90 °C is required by high-speed flow-wrap lines. Food-contact compliance is anchored to EU Regulation 10/2011 with overall migration testing per EN 1186-1:2002 using simulant D1 for aqueous produce and simulant A for dry bakery goods; U.S. applications fall under FDA 21 CFR 175.300 for resinous and polymeric coatings, with migration data generated per FDA Guidance for Industry 2007. Because PLA-dominant blends exhibit higher water vapor transmission than LDPE, the film is applicable to products requiring respiring packaging: water vapor transmission rate measured by ISO 15106-3:2009 at 23 °C and 85% RH typically ranges from 120 g/(m²·day) to 180 g/(m²·day) for 20 µm film, which reduces condensation events under cold-chain storage compared to LDPE of equivalent gauge. Blown-film processing uses a polished air ring and a lower blow-up ratio of 2.0:1 to 2.5:1 to minimize surface haze; die gap is 0.8–1.2 mm, melt temperature 165–175 °C, and the film is post-treated with 2–4 wt% of a food-contact-approved antifog masterbatch to suppress droplet formation on the inner surface. Seal initiation temperature is characterized by ASTM F2029-16 hot-tack testing and typically lies between 85 °C and 95 °C, which restricts the film from use in boil-in-the-bag or retort applications. Terminal products include flow-wrap bags for lettuce, spinach, fresh herbs, cut fruit trays, and bakery over-wrap; the film is not suitable for modified-atmosphere packaging requiring oxygen transmission rates below 500 cm³/(m²·day·atm) unless an additional barrier layer is incorporated.
| Application segment | Melt temperature | Die gap | Blow-up ratio | Film thickness | Typical additive loading |
|---|---|---|---|---|---|
| Retail checkout bags | 155–170 °C | 0.8–1.4 mm | 2.5:1–4.0:1 | 18–30 µm | 2–5 wt% slip/antiblock |
| Organic waste liners | 150–175 °C | 0.9–1.5 mm | 3.0:1–4.5:1 | 20–35 µm | Neat, or 5–12 wt% PBAT-rich modifier |
| Agricultural mulch | 155–165 °C | 0.8–1.2 mm | 2.0:1–3.0:1 | 10–20 µm | 2–5 wt% carbon black masterbatch |
| Produce overwrap | 165–175 °C | 0.8–1.2 mm | 2.0:1–2.5:1 | 12–25 µm | 2–4 wt% antifog, or 10–25% coextruded PBAT skin |
| Apparel polybags | 155–170 °C | 0.9–1.3 mm | 2.5:1–3.5:1 | 25–40 µm | 1–3 wt% antistatic, 3–8 wt% slip/antiblock |
| Magazine wrap | 150–175 °C | 0.9–1.4 mm | 2.0:1–3.0:1 | 30–50 µm | 1–2 wt% antistatic, 2–5 wt% slip |
In e-commerce and garment packaging, Bio-Flex F 1110 replaces polyethylene polybags in operations where the finished film must be compostable under EN 13432:2000 or at minimum satisfy REACH Article 33 reporting obligations for substances of very high concern; the compound is processed neat at 100%, with 1–3 wt% of a non-ionic antistatic masterbatch and 3–8 wt% of a slip/antiblock masterbatch added to meet automated bag-machine throughput. Static decay time measured under IEC 61340-2-3:2016 from 1,000 V to 100 V must remain below 2 seconds at 23 °C and 12% RH; otherwise, film-to-film adhesion causes misfeeds in side-weld bag machines running above 250 cycles/min. The blown-film extrusion uses a 30:1 L/D barrier screw without a Maddock mixer to reduce shear heating, a die gap of 0.9–1.3 mm, and a blow-up ratio of 2.5:1 to 3.5:1; melt temperatures are maintained between 155 °C and 170 °C, and the bubble is collapsed through a hardwood or aluminum nip at a layflat width up to 1,500 mm. Corona treatment at 40–44 mN/m is applied before printing; however, the treated surface loses 4–6 mN/m within 48 h if the roll is stored in high humidity above 60% RH, requiring inline treatment on the bag machine rather than offline batch treatment. Terminal products include side-weld garment bags, self-adhesive strip polybags for e-commerce, dust covers for hanging textiles, and heat-sealed accessory pouches. The operational boundary is defined by heat resistance: sustained exposure to temperatures above 55 °C, such as in containerized ocean freight through equatorial routes, causes the film to block and the seal area to creep; use of ventilated containers or silica gel desiccants is required for long-haul shipments.
Magazine and direct mail polywrapping has shifted toward compostable substrates in regions where municipal programs accept printed paper with compostable film, and Bio-Flex F 1110 is extruded into 30–50 µm monolayer films for this converting segment. The compound is used neat with 1–2 wt% antistatic masterbatch to prevent dust attraction in high-speed mailhouses and 2–5 wt% slip masterbatch to reduce coefficient of friction below 0.30 under ISO 8295:1995 on polished steel. Compliance for non-food mail film is governed primarily by REACH and by voluntary industrial composting standards EN 13432:2000 or AS 4736:2006; print adhesion requires surface energy above 38 mN/m, achieved by corona discharge at 2.0 kW across a 1,000 mm web at 30 m/min. Blown-film processing lines configured with a 25:1 or greater L/D screw, die gap of 0.9–1.4 mm, and BUR of 2.0:1 to 3.0:1 produce layflat widths from 150 mm to 600 mm; the melt temperature is capped at 175 °C to minimize thermal degradation that would brown the film and reduce ink contrast. Inline perforation and cold-seal adhesive application are performed on the bag machine rather than the extrusion line, because cold-seal registration tolerances of ±0.5 mm are easier to maintain when the film is not wound under tension exceeding 80 N/m. Terminal products include magazine wraps, newspaper sleeves, direct mail enclosures, and postal outer bags for flat-pack items. The material is not suitable for applications requiring prolonged outdoor weathering; published data for this specific configuration is limited, and converters must generate outdoor exposure data according to ISO 877-1:2009 before claiming UV resistance beyond 200 h.
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Bio-Flex F 1110 is a PLA-based thermoplastic compound supplied for blown film extrusion in short-use and compostable packaging applications. The pelletized grade is a melt-compounded blend of polylactic acid and a biodegradable copolyester phase, formulated to reduce the inherent brittleness of neat PLA while retaining sufficient melt strength for bubble stability. Published flow data place the melt volume-flow rate at 190 °C under 2.16 kg piston load in the range 3–6 cm³/10 min when tested to ISO 1133-1:2022; density is reported at 1.24–1.26 g/cm³ under ISO 1183-1:2019. The material is characterized by a high renewable carbon fraction and is usually certified by the compounder for industrial compostability under EN 13432:2000; direct reliance on certification requires confirmation of the exact additive masterbatch and final film thickness used downstream.
Processing latitude is narrower than that of fossil LDPE. Pre-drying in a desiccant-air dryer at 70–80 °C for 4–6 h is required to reduce pellet moisture below 0.025 %. Residual moisture above that threshold hydrolyzes PLA during extrusion, lowering melt viscosity and producing unstable bubble geometry, die-lip plate-out, and surface sharkskin on film. On a production line with a 45 mm single-screw extruder having 30 L/D and a three-zone screw with a Maddock mixing element, the barrel profile is generally set between 150 °C and 185 °C from feed to metering, with the die held at 180–200 °C. Feed-throat cooling should remain active to prevent pellet bridging.
Bubble geometry differs from LDPE because the melt exhibits lower elongational viscosity and less strain-hardening. Die gaps of 0.8–1.2 mm, blow-up ratios between 1.8 and 2.6, and frost-line heights of 4–8 die diameters are typical starting conditions. The lower melt strength makes the bubble sensitive to high air-ring velocities and to rapid cooling; unstable boundary layers or helical instability are observed when the frost line is raised too far or the melt temperature exceeds 200 °C. Output is limited by bubble stability rather than drive load. Regrind levels above 20 % may reduce dart impact and should be qualified on the target line.
Short-use shopping bags and fruit and vegetable films are the primary application window. Film in the 20–40 µm range can be heat-sealed using impulse or constant-heat sealing; seal strength reaches useful levels when the jaw temperature is maintained at 110–130 °C and dwell time is at least 0.5 s. The seal window is narrower than LDPE and is sensitive to film orientation. Bags produced from unmodified film may tear at the seal perimeter if the seal bar pressure is excessive. Because the grade has higher stiffness than flexible copolyester-rich biodegradable compounds, it is better suited to crisp, oriented films than to stretch films or elastic packaging.
Compared with LLDPE, Bio-Flex F 1110 typically delivers higher tensile modulus and lower puncture resistance at equal gauge. Tensile properties measured according to ISO 527-3:2018 on 30 µm mono-layer blown film tend to be in the range 25–40 MPa tensile strength and 150–250 % elongation at break; published data for the specific film configuration is limited and depends on draw-down ratio. Dart impact, measured by ISO 7765-1, is generally lower than LLDPE at the same thickness, so package design must compensate by increasing gauge or reducing stress concentration. Tear propagation resistance measured by ISO 6383-2 is directional; machine-direction tear is often lower once the film has been oriented at high take-up speed.
Haze and clarity are close to PLA but not identical to LDPE. For 25–35 µm film, light transmission measured by ASTM D1003 typically exceeds 85 %, while haze may be higher than LLDPE but acceptable for produce packaging. These values shift with frost-line height and blow-up ratio. Surface energy of freshly formed film is usually adequate for water-based flexographic inks after corona treatment to 38–42 mN/m. However, PLA surfaces age faster than polyethylene; adhesion loss occurs if treated film is stored above 30 °C or at relative humidity above 60 % for more than 48 h. The grade is sensitive to extended UV exposure and is not intended for durable outdoor films.
Edge trim and start-up scrap can be re-processed if kept dry and free of polyethylene contamination. In production-scale converting, contamination with LDPE as low as 2–5 % can cause visible gels, delamination, and reduced transverse-direction tear because the two phases are thermodynamically incompatible. PET and PVC contamination create severe degradation: PLA hydrolyzes in the presence of PVC thermal degradation products, leading to carbonized deposits and bubble holes. The recommended regrind fraction is usually 10–20 % for printable film and 20–30 % for waste liners; higher fractions decrease puncture impact and increase gel counts. If regrind has been stored in humid conditions, it must be re-dried at 70 °C for at least 4 h.
Residence time above 200 °C should be minimized. Prolonged hold-up in the die, adapter, or screen pack promotes lactide reformation, which is observed as acidic odor, lower bubble strength, and white die-lip deposits. Frequent purging with low-MFR polyethylene before shutdown is not compatible; dedicated purging compounds for PLA-based materials are recommended.
| Parameter | Bio-Flex F 1110 trial window | Typical LLDPE reference | Critical deviation |
|---|---|---|---|
| Barrel zone temperature | 150–185 °C | 180–220 °C | Feed zone above 165 °C causes bridging |
| Melt temperature | 175–195 °C | 190–230 °C | Above 200 °C lowers melt strength |
| Die gap | 0.8–1.2 mm | 1.5–2.5 mm | Above 1.5 mm increases draw resonance risk |
| Blow-up ratio | 1.8–2.6 | 2.0–3.5 | Above 3.0 weakens bubble |
| Frost-line height | 4–8 die diameters | 6–12 die diameters | Excessive height raises haze and instability |
Within the Bio-Flex film portfolio, F 1110 is normally differentiated by its higher PLA content, which raises tensile modulus and lowers elongation at break relative to grades designed for elastic agricultural films. Higher-flexibility biodegradable blown-film compounds may exhibit elongation at break above 400 % and lower modulus, whereas F 1110 remains in the 150–250 % elongation range. This stiffness improves bubble collapse and downstream converting at the cost of limited stretch and lower puncture resistance. The grade is therefore selected for short-use bags, lamination films, and compostable packaging requiring dimensional stability, rather than elastic cling or high-dart applications.
Compostability claims are only valid when the complete film, including pigments, inks, and adhesives, has been assessed as an article. The base resin is normally evaluated under EN 13432:2000, which requires biodegradation of at least 90 % within 180 days, disintegration residues above 2 mm below 10 % after 12 weeks, and absence of ecotoxicity. Corresponding test methods include ISO 14855-1 for aerobic biodegradation, ISO 16929 for disintegration, and OECD 208 for ecotoxicity. Under ASTM D6400, the material is intended for industrial composting facilities, not home compost or soil burial. The presence of conventional plastic contaminants above 1 % may cause failure at sorting or disintegration stages.
| Standard | Scope | Key criteria |
|---|---|---|
| EN 13432:2000 | Packaging recoverable through composting and biodegradation | ≥90 % biodegradation in 180 days; ≤10 % residue above 2 mm after 12 weeks |
| ASTM D6400 | Compostable plastics for municipal or industrial facilities | Similar mineralization and disintegration thresholds |
| ISO 17088:2021 | Specification for compostable plastics | Defines test methods and pass/fail values |
Storage at 20–30 °C in sealed original bags is required. Pellets exposed to ambient air above 60 % RH can reach moisture content above 0.025 % within 24 h, making immediate drying before extrusion necessary. Masterbatch loading must be kept low. Color concentrates based on PE carriers are incompatible; only PLA or biodegradable copolyester carriers should be used at 2–4 % addition. Above 5 %, masterbatch incompatibility creates gels and lowers transverse-direction tear. Slip and antiblock additives should be selected from compostable approved sources.
High-speed bagmaking imposes different constraints from film blowing. The material has a lower coefficient of friction than LDPE, which can cause slippage on roller nip systems; corona treatment and antistatic masterbatches may be required. Sealing temperature sensitivity is higher than LDPE; the difference between acceptable seal strength and burn-through or film shrinkage is often 5–10 °C. Because the film begins to shrink near the seal bar at 120–130 °C, jaw temperature must be profiled and dwell time minimized. Rotary sealing lines achieve better results than flat-bar sealers because the film web is not stationary over the heated element. These limitations define the practical speed ceiling and require line-specific optimization.
Field data from film producers indicate that edge trim recovery is most successful when the trim is granulated immediately after extrusion rather than stored as loose film. Loose film absorbs ambient moisture and creates feeding irregularities. Dedicated granulator knives should be maintained to avoid fines above 3 %, because fines can cause screw slippage and melt-temperature variation. On high-output lines, an automated edge-trim feedback system with gravimetric dosing of regrind at 12–18 % is commonly used to maintain bubble stability without manual feed fluctuation. Batch-to-batch variance in melt flow can shift the frost line by several centimeters; the air ring and internal bubble cooling settings must be adjusted continuously when changing production lots.