| HS Code | 881385 |
| Productname | Bio-Flex F 1140 Blown Film Industrial Compostable PLA Blend |
| Manufacturer | FKuR |
| Materialtype | PLA blend |
| Form | Pellets |
| Application | Blown film |
| Compostability | Industrial compostable |
| Certification | EN 13432; ASTM D6400 |
| Density | 1.25 g/cm³ |
| Meltflowrate | 3 g/10 min (190°C/2.16 kg) |
| Tensilestrength | 30 MPa |
| Elongationatbreak | 250% |
| Tensilemodulus | 1500 MPa |
| Charpynotchedimpactstrength | 4 kJ/m² |
| Meltingtemperature | 150°C |
| Vicatsofteningtemperature | 60°C |
| Processingtemperature | 160-190°C |
| Filmthickness | 15-50 µm |
| Biobasedcontent | >50% |
As an accredited Bio-Flex F 1140 Blown Film Industrial Compostable PLA Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Bio-Flex F 1140 Blown Film Industrial Compostable PLA Blend is supplied in 25 kg moisture-resistant bags, 40 bags per pallet (1,000 kg). |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Bio-Flex F 1140, industrial compostable PLA blend for blown film, securely stowed and sealed. |
| Shipping | Bio-Flex F 1140 Blown Film Industrial Compostable PLA Blend is typically shipped as solid, non-hazardous pellets in 25 kg moisture-barrier bags, palletized and stretch-wrapped. Transport in clean, dry trucks or containers. Store below 30°C, protected from moisture, heat, and direct sunlight; follow standard industrial hygiene. |
| Storage | Store Bio-Flex F 1140 Blown Film Industrial Compostable PLA Blend in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep sealed in original packaging on pallets. Recommended conditions: 15–25°C and low humidity. Avoid prolonged storage near strong odors or contaminants. Do not expose to open flames. Maintain first-in, first-out stock rotation. |
| Shelf Life | Shelf life is approximately 12 months when stored unopened, dry, below 30°C, away from moisture and heat in original packaging. |
Bio-Flex F 1140 is introduced as a 100 % as-supplied granulate on high-output LDPE bag lines only after the feed system has been reviewed for moisture regain, because the PLA phase in the compound is susceptible to hydrolysis at the feed throat. Pre-drying in a desiccant drier at 70–80 °C for 4–6 h with a dew point of ≤ -40 °C reduces residual moisture to < 0.025 % by mass; hopper residence time should not exceed 2 h if ambient relative humidity is above 60 %. Film-grade extruders with screw diameter 50–75 mm and L/D 30:1 are preferred, using a two-stage screw with a mild mixing section rather than high-shear Maddock elements that can raise melt temperature by viscous dissipation. Melt temperature measured at the die adapter is held between 160 °C and 180 °C; die zones are set no higher than 175 °C because prolonged residence time above 190 °C produces lactide decomposition and leads to gel flecks at the die lip. A die gap of 0.8–1.2 mm and a blow-up ratio of 2.8:1–3.2:1 produce a bubble that retains enough melt strength for continuous operation; frost-line height is kept between 1.5 and 2.5 die diameters to balance orientation and tear resistance. The film is converted into perforated or heat-sealed T-shirt bags at 20–35 µm. Compliance for the finished article is demonstrated under EN 13432:2000 for the European Economic Area and ASTM D6400-23 for North American claims; where packaging waste regulations apply, the certificate must be supported by ISO 16929 disintegration data showing ≥ 90 % fragmentation after 12 weeks and OECD 208 ecotoxicity testing. Blocking is the dominant line failure; when roll blocking is observed, a certified compostable anti-block masterbatch is metered at 1–2 wt% rather than increasing the film gauge. Tensile properties on film samples are measured by ISO 527-3; Elmendorf tear strength is measured by ISO 6383-2.
In municipal organic waste diversion programs, the same compound is processed as a monolayer film at 100 % unmodified pellet feed. The extruder configuration is less aggressive than in retail bag production: a die gap of 0.6–0.9 mm, a blow-up ratio of 2.5:1–3.0:1, and a frost-line height of 2.0–2.5 die diameters are used to hold gauge between 15 µm and 30 µm. The terminal product is a kitchen caddy liner or curbside organic waste bag perforated for easy closure. Certification is assessed under EN 13432:2000 and, where accepted in North America, ASTM D6400-23; the full compostability file must include aerobic biodegradation per ISO 14855-1 at ≥ 90 % within 180 days, disintegration per ISO 16929, and ecotoxicity per OECD 208 and EN 13432 Annex A heavy-metal limits. Since municipal customers frequently print collection instructions on the bag, any ink or antistatic concentrate added to the 100 % compound must itself carry a compostability conformity certificate; otherwise the final product may fail the heavy-metal or ecotoxicity screening.
Extrusion of dry-goods liners shifts the critical control point from tear propagation to seal initiation and film-to-film slip. The formulation is run at 100 % Bio-Flex F 1140; an anti-block masterbatch at 1–2 wt% is added only if the coefficient of friction measured by ISO 8295 exceeds 0.35 on the outer surface. The downstream process uses a monolayer blown-film line with a die gap of 0.8–1.0 mm and a blow-up ratio of 2.5:1–3.0:1 to produce film of 25–40 µm. After extrusion and corona treatment at 38–42 dyn/cm, the film is printed or sealed to itself; heat-seal parameters are established by differential scanning calorimetry on the exact film, and seal-bar temperature is set 15–25 °C above the measured crystalline melting endotherm, followed by seal strength testing per ASTM F88. Published data for this specific compound at food-contact seal conditions is limited, so converter trials must validate hot-tack performance on the specific bag-making machine. Terminal finished products include cereal liner bags, cracker and biscuit inner liners, and dry snack pouches. Regulatory compliance for dry food contact in the European Union is based on Regulation (EC) No 1935/2004 and Regulation (EU) No 10/2011; overall migration into simulants must remain below 10 mg/dm² according to EN 1186-1. In the United States, a valid food-contact notification for the compound or the manufactured film must cover the application. The operational boundary is moisture barrier: PLA-based blown film without an additional certified compostable barrier layer is not suitable for long-shelf-life products requiring moisture protection equivalent to oriented PET or aluminum foil.
E-commerce mailers impose puncture and tear requirements that cannot be met by increasing gauge alone, because excessive gauge increases film stiffness and makes the mailer difficult to seal and convert. The starting construction is 100 % Bio-Flex F 1140 in a monolayer blown-film line with a die gap of 1.2–1.8 mm and internal bubble cooling. Blow-up ratio is set at 2.5:1–3.0:1 to maintain impact strength without excessive transverse direction shrinkage; the collapsed film is gusseted on the sides and converted into shipping envelopes at 60–100 µm. Compliance for industrial compostability is tested under EN 13432:2000 and ASTM D6400-23, with a certificate that also references ISO 17088. Because mailers are often printed, corona treatment at 40–44 dyn/cm is applied before flexographic or digital printing. Puncture performance is evaluated by dart drop impact per ASTM D1709 Method A and Elmendorf tear per ISO 6383-2; if the monolayer fails the converter's minimum tear value, a certified compostable PBAT-rich compound may be incorporated as a separate layer or at a specified weight percentage. Published data for coextruded structures containing Bio-Flex F 1140 in the mailer segment is limited, so the addition ratio of the PBAT-rich layer must be established through a design-of-experiments study that maintains the final structure's EN 13432 certification. Terminal products are printed shipping mailers, logistics envelopes, and return-package pouches.
| Application segment | Industrial compostability standard | Food-contact or packaging regulation | Primary mechanical test |
|---|---|---|---|
| Retail checkout bags | EN 13432:2000, ASTM D6400-23 | Directive 94/62/EC, EU 2019/904 | ISO 527-3, ISO 6383-2 |
| Bio-waste liners | EN 13432:2000, ASTM D6400-23 | EN 13432 Annex A heavy-metal limits | ISO 527-3 |
| Dry-goods liners | EN 13432:2000 | Regulation (EC) No 1935/2004, EU 10/2011 | ASTM F88, ISO 8295 |
| E-commerce mailers | EN 13432:2000, ASTM D6400-23, ISO 17088 | Directive 94/62/EC | ASTM D1709, ISO 6383-2 |
| Apparel polybags | EN 13432:2000 | REACH Annex XVII | ISO 527-3, ASTM F88 |
| Produce roll bags | EN 13432:2000 | EU 2019/904 | ISO 527-3, ISO 7765-1 |
| Paper over-wrap | EN 13432:2000 | ISO 14021 | ISO 6383-2, ASTM D1003 |
In apparel and textile packaging, the 100 % compound is processed on a standard monolayer blown-film line at a die gap of 0.6–0.9 mm, a blow-up ratio of 2.5:1–3.0:1, and a melt temperature of 160–175 °C; the 20–30 µm film is slit and converted into garment polybags. The finished article remains under the scope of EN 13432:2000 because no synthetic slip agent is added; converters that require reduced static charge must use a certified compostable antistatic masterbatch and re-test the polybag for disintegration under ISO 16929. Mechanical acceptance is usually limited to tensile elongation at break per ISO 527-3 and seal integrity per ASTM F88.
Produce roll bags are a demanding thin-gauge segment because the film must remain open at the perforation and survive high-speed roll-to-roll conversion. The compound is fed at 100 % as-supplied granulate; a compostable anti-block masterbatch at 1 wt% is metered only when film-to-film blocking appears after corona treatment. The downstream process uses a monolayer blown-film line with a die gap of 0.6–0.8 mm, a blow-up ratio of 3.0:1–3.5:1, and a gauge range of 12–20 µm. Bubble vibration becomes the primary processing failure at this gauge, and is suppressed by increasing frost-line height to 2.5–3.0 die diameters and reducing extruder output until the bubble's optical thickness variation measured by an online gauge scanner falls below the converter's specification. Terminal products are tear-off produce roll bags for fresh fruit and vegetable counters. Industrial compostability is certified under EN 13432:2000; the Single-Use Plastics Directive EU 2019/904 should be reviewed for national labeling or marketing restrictions, but the material itself is outside the non-compostable problematic plastic categories when the bag is certified. Tensile property acceptance follows ISO 527-3, and dart drop impact is measured by ISO 7765-1 at 23 °C and 50 % relative humidity.
Secondary packaging for paper ream logistics runs the compound as a 100 % monolayer film of 30–50 µm, typically at a blow-up ratio of 2.0:1–2.5:1 to produce a flatter web for the wrapping unit. The process includes a low-intensity corona treatment at 38–42 dyn/cm on the print side and, if necessary, a 1 wt% compostable anti-block masterbatch on the seal side to reduce blocking during roll storage. Terminal products are paper ream wrap and tissue bundle wrap. The compliance assessment is EN 13432:2000 for composting and ISO 14021 for any self-declared environmental claims printed on the film. In this end-use, optical haze and print adhesion are inspected according to ASTM D1003 and ISO 2409, respectively. The operational boundary is that a paper wrap film based on a PLA blend has lower tear resistance than a conventional LDPE overwrap of the same gauge; therefore tear strength is controlled by ISO 6383-2 after winding and should not be tested only on flat samples.
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Bio-Flex F 1140 is a PLA-based compound engineered for blown film extrusion and classified as industrially compostable. The grade is supplied in pellet form with a solid density of 1.25 g/cm³ under ISO 1183-1. Melt volume-flow rate is specified as 3.0 cm³/10 min at 190 °C and 2.16 kg load under ISO 1133-1:2022. Tensile modulus of blown film typically falls between 2500 MPa and 3200 MPa, and machine-direction tensile elongation at break falls between 5% and 8%, measured on 100 µm film according to ISO 527-3. These values shift with blow-up ratio, frost-line height, and film gauge; the certificate of analysis for the specific lot governs. The material is intended for industrial composting under EN 13432 and ASTM D6400, but is not automatically home compostable. It is used in mono-layer and coextruded blown film lines for compostable packaging, lamination film, and carry-out applications.
In blown film, unmodified PLA exhibits a narrow processing window and limited bubble stability because its extensional viscosity is insufficient at the low melt temperatures required to avoid thermal degradation. F 1140 is differentiated by a molecular architecture and compostable copolyester fraction that raise melt strength and permit a blow-up ratio of 2.5:1 to 3.5:1 without immediate bubble collapse. The result is a stiffness-elongation balance that is not obtainable with either unmodified PLA or PBAT-dominant films. Unmodified PLA film can exceed 3000 MPa in tensile modulus but fractures at low elongation; PBAT-rich blown film usually exhibits tensile modulus below 150 MPa and elongation at break above 400%. F 1140 occupies a middle position, with tensile modulus in the 2500–3200 MPa range and elongation in the single-digit percentage range under ISO 527-3. This means F 1140 retains enough stiffness for machine-direction tension control and print registration while avoiding the brittle pinhole failure mode observed in unmodified PLA.
| Property | Test method | Indicative F 1140 value | Processing implication |
|---|---|---|---|
| Density | ISO 1183-1 | 1.25 g/cm³ | Yield per kilogram is lower than polyolefins; downgauging is constrained by stiffness targeting. |
| Melt volume-flow rate | ISO 1133-1:2022 | 3.0 cm³/10 min at 190 °C/2.16 kg | Requires sufficient melt pressure in grooved-feed sections; not suitable for very low-head-pressure dies. |
| Tensile modulus | ISO 527-3 | 2500–3200 MPa | High stiffness supports VFFS reel handling; can cause excessive film curl if gauge non-uniformity exceeds 5%. |
| Tensile elongation at break | ISO 527-3 | 5–8% | Sufficient for moderate creasing but not for deep-draw vacuum forming. |
Pre-drying is mandatory. The pellets must be dried in a desiccant dryer with a dew point below -30 °C at 70 °C for 4 h to reach a residual moisture below 250 ppm (0.025%). If ambient relative humidity exceeds 60%, extrusion should be performed with a closed hopper, and regrind should be dried again because PLA-based blends reabsorb moisture rapidly. Failure to maintain moisture below 250 ppm causes hydrolytic chain scission in the melt, reducing molecular weight and increasing melt flow. On a 45 mm single-screw blown film line with 30:1 L/D and a barrier screw, the barrel profile should begin at 150 °C in the feed zone and rise to 160–165 °C in the metering and mixing zones. Die body temperature should be held at 155–165 °C. Melt temperature must not remain above 170 °C for more than a few minutes during start-up; at 175 °C, viscosity decay accelerates and lactic acid generation increases. Use screen packs of 80–120 mesh and an automatic screen changer for long runs.
Bubble stability is improved with a dual-lip air ring and chilled air at 15–20 °C. The frost line is normally set at 2–4 die diameters above the air ring. Film thickness below 15 µm requires a blow-up ratio of at least 2.5:1 and a die gap of 0.8–1.2 mm to prevent gauge variation from exceeding 5%. Internal bubble cooling is advised when output exceeds 80 kg/h on a 250 mm die, because without it the heat transfer rate becomes limiting and bubble flutter appears.
The upper process temperature limit is governed by the thermal decomposition of the PLA fraction. At melt temperatures above 170 °C, the molecular weight distribution broadens and the melt strength drops; above 180 °C, gel bodies develop as degradation products condense or crosslink in low-shear zones at the adapter and die inner surfaces. The pressure profile across the screen pack should not fluctuate more than 5%; larger fluctuations indicate feed-block partial melting or hydrolytic degradation. Avoid amine-based additives, which can promote ester cleavage and shift the pH of the melt, and avoid PVC residue in the extruder because hydrochloric acid generated at processing temperatures accelerates polymer hydrolysis. Purging with a dedicated PLA-compatible purge compound is required after running polyolefins; polyolefin residue causes interfacial delamination and film haze. If gel flecks appear, reduce the melt temperature by 5–10 °C and increase screw speed slightly to reduce residence time before shutting the line down for disassembly.
On vertical form-fill-seal equipment, F 1140 film can be sealed when jaw temperatures are set between 115 °C and 130 °C, with a dwell time of 0.5–1.0 s at 200 N seal force on a flat-bar 10 mm jaw. The hot-tack strength is lower than that of PE, so the seal-cooling air should be activated immediately after the jaw opens; otherwise the weight of the product will pull the seal apart. Corona treatment to 38–42 mN/m is required for water-based flexo and inkjet printing. Lamination with cellulose or paper substrates is possible with starch-based or polyurethane-free compostable adhesives; solvent-based polyurethane systems should not be assumed compatible with the industrial composting certificate. Film blocking can be managed with a compostable anti-block masterbatch at 0.1–0.3 wt%, but overdosing above 0.5 wt% lowers clarity and raises haze.
The relevant standard is EN 13432:2000. It requires 90% disintegration after 12 weeks in a controlled industrial composting environment at 58 °C ± 2 °C, and 90% biodegradation as CO₂ within 180 days. The standard also sets limits for heavy metals and requires ecotoxicity testing of the final compost. In North America, ASTM D6400 applies. Certification is valid for the specific film formulation and must be reconfirmed when inks, coatings, or sealants exceed the nominal weight percentages used in the original test. Converters should retain batch certificates and maintain traceability of the base resin lot because blending post-industrial regrind beyond 10 wt% may require additional testing. The material is not certified for home composting under AS 5810 or NF T51-800 unless the converter has obtained separate certification. Disposal through industrial composting is not permitted in anaerobic digesters, because methane yield and residence time differ from the aerobic test protocol.
Compared with other PLA blend grades, F 1140 is differentiated by blown film melt strength and higher stiffness. It should not be used in injection moulding or thermoforming, where the high melt strength and low elongation can generate frozen-in orientation stress and wall-thickness variation. The material is also not suited for stretch film, because the elongation at break in the 5–8% range is insufficient for high-stretch wrapping. Its density of 1.25 g/cm³ should be entered into film-weight calculations; replacing an LDPE film of equal gauge increases the weight per square meter by approximately 36%. For seal-layer applications, coextrusion with a PBAT-rich grade is possible if the two melts are viscosity-matched at the die shear rate; otherwise layer instability produces visible ridge defects. The recommended regrind content is 10–20 wt% maximum for dry edge trim and start-up scrap, provided the scrap is free of polyolefin contamination and has been re-dried.