| HS Code | 505292 |
| Material Type | PLA Blend |
| Density | 1.25 g/cm³ |
| Melt Flow Rate | 3-5 g/10 min (190°C/2.16 kg) |
| Melting Point | 150-155°C |
| Vicat Softening Temperature | 55-60°C |
| Tensile Strength | 40-50 MPa |
| Elongation At Break | 250-350% |
| Tensile Modulus | 1400-1600 MPa |
| Clarity | High |
| Haze | Low |
| Biodegradability | Compostable (EN 13432) |
| Processing Method | Blown Film Extrusion |
| Recommended Film Thickness | 20-50 µm |
| Bio Based Carbon Content | >50% |
As an accredited Bio-Flex F 2201 CL High Clarity Blown Film PLA Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Bio-Flex F 2201 CL High Clarity Blown Film PLA Blend comes in 25 kg sealed moisture-resistant foil-lined bags on pallets. |
| Container Loading (20′ FCL) | 20′ FCL: Bio-Flex F 2201 CL High Clarity Blown Film PLA Blend, palletized, stretch-wrapped, and securely loaded for export. |
| Shipping | Bio-Flex F 2201 CL High Clarity Blown Film PLA Blend is shipped as moisture-sensitive thermoplastic pellets in sealed, foil-lined bags, octabins, or bulk sacks. Keep dry, below 30°C, away from heat and sunlight. Handle with normal PPE. Normally not classified as dangerous goods; follow local transport regulations. |
| Storage | Store Bio-Flex F 2201 CL High Clarity Blown Film PLA Blend in a cool, dry, well-ventilated warehouse. Keep sealed in original packaging, on pallets, off the floor. Protect from moisture, direct sunlight, heat, contamination, and ignition sources. Recommended storage is below 30°C with low humidity. Use FIFO stock rotation and avoid excessive stacking or incompatible materials. |
| Shelf Life | Shelf life is typically 12 months when stored unopened in a cool, dry place, protected from moisture, heat, and direct sunlight. |
In fresh produce film converting, Bio-Flex F 2201 CL is processed as a monolayer web for leafy greens, berry fixtures, and herb sleeves. The pellets require desiccant drying at 60 °C to 70 °C for 4 h to 6 h with a dew point no higher than -40 °C. At ambient relative humidity above 60%, the dryer outlet air must be maintained at -40 °C dew point and the hopper must be sealed. Residual moisture above 250 ppm leads to hydrolytic chain scission in the extruder. A single-screw blown film line with 25:1 L/D and a three-zone screw having compression ratio 2.8:1 to 3.2:1 is typical. Barrel temperatures are set from 140 °C at the feed zone to 155 °C at the die. Melt temperature must not exceed 180 °C for residence times longer than 90 s. A die gap of 0.8 mm to 1.2 mm and a blow-up ratio of 2.0:1 to 2.5:1 produce a 25 µm to 35 µm gauge. Optical haze is measured under ASTM D1003. Values below 12% are achievable only when the frost line is held steady at 4 to 6 die diameters above the die; frost-line oscillation increases surface roughness and raises haze. Laser microperforation is applied when the produce respiration rate demands gas exchange. The perforation pattern is determined by storage-trial shelf life, not by extrusion conditions. An antifog masterbatch is added at 1 wt% to 3 wt% when condensation control is required. Addition above 3 wt% may lower seal initiation temperature and tensile modulus. Tensile properties are checked under ISO 527-3 after any additive change because published data for specific masterbatch combinations is limited. Food-contact compliance is governed by EU Regulation 10/2011; migration testing of the final bag is performed under EN 1186-2 with overall migration not exceeding 10 mg/dm². Compostability is verified by EN 13432:2000 when the article is intended for organic waste collection. Terminal articles are clear compostable produce bags, herb sleeves, or berry display packs.
Operational boundaries for this segment are defined by bubble stability and tension. Winder tension is kept at 15 N/m to 25 N/m. Higher tension blocks film flatness and produces gauge bands. Lower tension causes telescoping. The film is not recommended for direct contact with high-fat produce dressings or hot food because the PLA-rich structure softens above 55 °C. If produce is prepackaged with sharp stems, a thicker 35 µm gauge is used; puncture resistance is measured by a slow-puncture test according to ISO 7765-2 or an equivalent in-house method. Published data for this precise configuration is limited; converters should establish puncture thresholds using the final produce item, not a generic probe.
Bakery pouches and bread bags use this grade at 20 µm to 30 µm because the blown web has lower bending stiffness than a cast PLA sheet of comparable gauge. The bubble is produced with a 2.2:1 to 2.8:1 BUR and a die gap of 0.8 mm to 1.0 mm. Online microperforation is introduced after the nip. The perforation pattern is selected from bread moisture loss trials. Below 30 µm, residual film stress before perforation can cause hole elongation in the machine direction. The resulting uneven venting reduces shelf-life repeatability. Heat sealing on hot-bar rotary bag machines is performed at 90 °C to 110 °C with a dwell time of 0.8 s to 1.5 s. Seal strength is tested by ASTM F88/F88M. A minimum of 2.5 N/15 mm is maintained on automated packaging lines. If seal strength falls below this value, the film is checked for surface slip additive migration. A two-layer film with the anti-fog masterbatch concentrated in the inner layer at 2 wt% delays condensation at 4 °C display temperatures. The outer layer remains neat to preserve clarity. Food-contact status is validated by EU Regulation 10/2011. Overall migration tests are run under EN 1186-2 with isooctane or 95% ethanol substitutes for fatty bakery goods. Compostability of printed bags follows EN 13432:2000; printing inks must independently meet the 90% biodegradation threshold. The terminal article is a clear or printed compostable bread bag with venting and anti-fog function.
On bakery lines, starch dust from the packaging environment contaminates seal jaws. The dust reduces heat transfer and creates microchannels in the seal. If jaw surfaces are not cleaned at 30-minute intervals, seal strength measured by ASTM F88/F88M can vary by more than 20%. This is a production-line effect observed on converted machines; it is not a resin property. The film retains only limited retention of trapped moisture; bread with a water activity above 0.95 will produce visible condensation unless sufficient perforation area is provided. The necessary perforation area is determined by water activity and bag volume.
| Segment | Die melt temperature | Blow-up ratio | Die gap | Thickness | Post-extrusion step |
|---|---|---|---|---|---|
| Fresh produce monolayer | 150 °C–160 °C | 2.0:1–2.5:1 | 0.8–1.2 mm | 25–35 µm | Laser microperforation |
| Bakery pouch | 148 °C–158 °C | 2.2:1–2.8:1 | 0.8–1.0 mm | 20–30 µm | Inline perforation and anti-fog |
| Shrink sleeve | 155 °C–165 °C | 3.0:1–3.8:1 | 0.8–1.0 mm | 40–60 µm | Solvent seaming and shrink tunnel |
| Kitchen caddy liner | 150 °C–160 °C | 2.0:1–2.5:1 | 1.0–1.4 mm | 25–50 µm | Bottom seal and gusset forming |
| Dry-goods laminate | 152 °C–162 °C | 2.0:1–2.5:1 | 0.8–1.0 mm | 25–40 µm | Corona and adhesive lamination |
| Label facestock | 154 °C–162 °C | 2.8:1–3.2:1 | 0.8–1.0 mm | 30–50 µm | Corona and slitting |
When a high-stalk bubble is blown at 3.0:1 to 3.8:1 BUR, the web retains sufficient transverse orientation for clear shrink sleeves and tamper-evident bands on dry goods. The die temperature is held between 155 °C and 165 °C, and the die gap is set to 0.8 mm to 1.0 mm. A narrower gap increases shear and lowers haze, but the associated pressure rise must stay below the maximum specified by the die manufacturer. The frost line is raised to 6 to 8 die diameters above the die to stabilise the stalk. The blown tube is slit and then converted on a sleeve seaming line. Solvent seaming is performed with a commercial PLA-compatible solvent mixture; forced extraction is mandatory. Shrinkage is measured by ISO 11501 or ASTM D2732. Published data for this exact grade in shrink configuration is limited; converters must generate a shrinkage curve in a water bath at 85 °C to 95 °C. Dry-goods shrink tunnels are set at 95 °C to 105 °C for 5 s to 10 s. Because the PLA-rich structure loses shrink force near its glass transition, the sleeve should not be used on products with surface temperature above 60 °C. Terminal articles are clear compostable shrink bands for dry food containers.
Side-seam strength is measured after solvent bonding by ASTM F88/F88M. On a 12 mm overlapped seam, a value above 1.5 N/15 mm is required for high-speed application. If seam strength is lower, the solvent mixture, pressure, or belt speed is adjusted before tunnel profiling. Sleeve splitting occurs when the seam is exposed to uneven tunnel heat above 95 °C. The line should be profiled with a thermocouple placed inside the sleeve; temperature variation greater than 5 °C across the tunnel width creates asymmetric shrink and seam curl. Hot-water shrink baths are not used because PLA hydrolyses under prolonged wet heat. Immersion in 85 °C water is limited to below 30 s; longer exposure weakens the film and increases splitting. Food-contact status is judged under EU Regulation 10/2011; printed and seamed sleeves require final migration screening under EN 1186-2. Compostability is established by EN 13432:2000, including the solvent loading after drying.
For organic waste collection, the film is extruded at 25 µm to 50 µm with a 2.0:1 to 2.5:1 BUR and a die gap of 1.0 mm to 1.4 mm. Thicker gauges are preferred because the liner contacts wet kitchen waste with a pH of 4 to 6. Under these conditions acid-catalyzed hydrolysis of the PLA fraction controls the serviceable life. A 25 µm liner retains acceptable wet strength for a 3-day to 5-day collection cycle at room temperature. Longer exposure, hot liquid effluents, or fatty waste are outside the operational window. Tensile properties are measured by ISO 527-3 after contact with a synthetic waste leachate. An accelerated screening medium of 0.1 N hydrochloric acid at 40 °C is used by converters to compare batch-to-batch degradation resistance. Impact resistance is measured by ASTM D1709. A dart drop below 35 g for 25 µm film indicates excessive moisture at the die or polymer degradation. For compostability, disintegration is validated by ISO 16929 under aerobic composting conditions. Ultimate biodegradation is measured by ISO 14855-1 with a 90% minimum conversion relative to the cellulose reference after 180 days. Heavy metal limits are specified in EN 13432:2000 Annex A.4. The terminal article is a clear or printed compostable kitchen caddy liner.
On twin-station bag machines, bottom seals are formed with a thermal impulse sealer at 95 °C to 115 °C. Higher settings cause stringing and edge tear. The side gussets are the weak point because folds create stress concentration and local moisture entrapment. Converters observe that wet caddy liners fail at the gusset before the bottom seal; therefore corner reinforcement with a wider seal area or additional film pleats is used. Static load testing with up to 8 kg of wet waste is applied to 30 µm liners. Failure above this load is reported in field trials, not established as a standard limit. Because the grade is incompatible with PVC or PET residue in regrind, purge transitions must be confirmed by melt pressure stabilisation before production starts.
Dry-goods lamination uses the blown web as a reverse-printed outer ply or as the inner heat-seal ply for low-moisture products. The base film is corona treated to 38 mN/m to 42 mN/m surface energy; wetting tension is measured by ISO 8296. Treatment must be confirmed immediately before lamination because surface energy decays within 48 h on untreated storage. A water-based polyurethane adhesive is applied at a dry coat weight of 2.0 g/m² to 3.0 g/m². Solventless isocyanate systems are not specified for direct food contact under EU Regulation 10/2011 because primary aromatic amines require explicit migration screening. The laminate is used only when the filled product has water activity below 0.60; the film is not a high oxygen barrier. Moisture vapour transmission rate is measured by ASTM F1249 at 23 °C and 50% RH. Converters set pass/fail targets from the product moisture isotherm data. Seal strength is checked by ASTM F88/F88M; a value above 2.0 N/15 mm is required for pouch converting. The terminal article is a compostable dry-food pouch or single-wall bag. Compostability is governed by EN 13432:2000; each adhesive, ink, and primer must independently meet the 90% biodegradation threshold.
Failure in this segment occurs mainly as delamination when web tension is above 20 N/m during coating. The blown film relaxes after winding; excessive tension creates curl and tunnel edges. On the laminating nip, roll temperature is held below 40 °C because the film softens and can lose gauge. If a metallised barrier layer is needed, it is not applied directly to Bio-Flex F 2201 CL without an anchor coat; published data for this configuration is limited.
Label facestock made from Bio-Flex F 2201 CL uses a film thickness of 30 µm to 50 µm and a high-stalk bubble with 2.8:1 to 3.2:1 BUR. The stalk height is maintained at 200 mm to 400 mm above the die depending on die diameter. A chilled upper nip roll below 25 °C sets the final structure. Web tension after slitting is held at 15 N/m to 20 N/m to prevent telescoping. Slit edge quality is critical because ragged edges create dust that reduces print quality. The film is corona treated to 38 mN/m to 44 mN/m using ISO 8296. Print adhesion is verified by ISO 2409 cross-cut; a classification of 1 or better is required for UV flexo inks. Dimensional stability is measured by ISO 11501 at 60 °C for 10 min. Freestanding films with transverse shrinkage above 3% cause label curl and press misregistration. The terminal article is a clear compostable label applied to produce crates, bakery packaging, or compostable mailers. Compostability follows EN 13432:2000; the pressure-sensitive adhesive must meet the same standard.
Migration of adhesive components into the PLA-rich facestock can plasticise the film and reduce die-cutting accuracy. Converters screen adhesive migration by ageing the laminate at 40 °C for 7 days, followed by dimensional measurement under ISO 11501. If transverse shrinkage after ageing exceeds 1.5%, the facestock is downgraded to direct-print banding without pressure-sensitive adhesive. This operational boundary prevents field failures on high-speed label lines. Published data for this specific grade as label facestock is limited; each adhesive system must be validated on the finished construction.
| Standard or regulation | Property / test | Application relevance | Typical acceptance criterion |
|---|---|---|---|
| EN 13432:2000 Annex A.4 | Regulated metals and hazardous substances | All compostable articles | Sum of Pb, Cd, Hg, Cr(VI) below 100 mg/kg |
| ISO 14855-1 | Ultimate aerobic biodegradation | All compostable articles | 90% conversion in 180 days |
| ISO 16929 | Disintegration under composting | All compostable articles | 90% dry mass < 2 mm |
| ISO 527-3 | Tensile properties of film | All film applications | Converter-defined |
| ASTM D1003 | Haze and light transmission | Clear produce, bakery, window | Below 12% haze |
| ASTM F88/F88M | Seal strength | Bag and pouch seals | 2.0–2.5 N/15 mm minimum |
| ISO 8296 | Wetting tension | Lamination, printing, adhesive | 38–44 mN/m |
| ISO 11501 | Shrinkage under heat | Label facestock, window patch | < 3% at 60 °C for 10 min |
| EU Regulation 10/2011 | Overall migration | All food-contact articles | 10 mg/dm² via EN 1186-2 |
| ASTM F1249 | Water vapour transmission rate | Dry-goods laminate | Product-specific |
| ASTM D1709 | Dart drop impact | Kitchen caddy liner | Above 35 g for 25 µm |
Inside a paper-based window patch line, the clear film is die-cut and applied to the board opening with a starch-based or water-based adhesive at a wet coat weight of 1.5 g/m² to 2.5 g/m². The film thickness is 20 µm to 30 µm; a thicker gauge increases bending stiffness and causes board curl after drying. The unwinding tension is held at 10 N/m to 15 N/m because the film is not a high-modulus web. Haze is measured by ASTM D1003; the window must remain below 12% haze to meet display criteria. Hot-air adhesive drying is set at 60 °C for 20 s; the film must not shrink beyond 1.0% in either direction during this step. Dimensional stability is checked by ISO 11501 at 60 °C for 10 min. The terminal article is a transparent window in compostable food cartons. Compliance is governed by EU Regulation 10/2011 for food contact and by EN 13432:2000 for compostable packaging. The printed board and the window film must biodegrade in the same industrial composting cycle.
Operationally, the film is incompatible with high-solvent adhesives because ketone-containing systems can etch the surface and reduce clarity. Water-based adhesives are selected on the basis of wetting tension measured by ISO 8296; a minimum of 38 mN/m is required for adhesive spread. Published data for this specific window-patch configuration is limited. Converters should run a 48 h block test on the finished carton to confirm that the adhesive does not migrate into the film and create visible patches. The window is not recommended for hot-filled cartons because the film softens above 55 °C.
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Bio-Flex F 2201 CL High Clarity Blown Film PLA Blend is a polylactic-acid-based thermoplastic compound formulated for tubular blown film extrusion where optical transparency, bio-based carbon content, and industrial compostability are specified. The grade belongs to the Bio-Flex family and carries the CL designation for the high-clarity optical package. The blend is designed to be processed on conventional polyethylene blown film lines with grooved feed sections, a barrier screw, and a dual-lip air ring. Two processing conflicts define the extrusion window: the tendency of unmodified PLA to form large spherulites that scatter visible light, and the narrow thermal interval between adequate melt fluidity and lactide generation. The material is supplied in pellet form; exact formulation is proprietary, but the matrix is PLA-based with a melt-strength modifier and a nucleating package. The high-clarity attribute is therefore not a surface treatment but a bulk morphology effect combined with surface slip and anti-blocking additives.
Published typical values are not specification limits. Density is 1.25 g/cm³ when tested according to ISO 1183-1:2019; melt-volume rate is 4.0 cm³/10 min at 190 °C and 2.16 kg when tested according to ISO 1133-1:2022. For 50 µm blown film produced at a 3.0:1 blow-up ratio, tensile strength is 30–35 MPa machine direction and 25–30 MPa transverse direction under ISO 527-3. Haze is typically below 8% per ASTM D1003-13; gloss at 60° is typically above 75 GU per ASTM D2457-13. Dart drop impact for 30 µm film is generally 150–250 g per ISO 7765-1. All values should be confirmed against the manufacturer’s batch certificate.
Die melt temperature must be maintained between 155 °C and 175 °C. Temperatures above 185 °C accelerate PLA chain scission, lactide formation, and melt-strength loss; temperatures below 150 °C increase melt pressure, promote melt fracture, and leave unmolten gel fragments that appear as optical defects. A single-screw extruder of 25:1 to 30:1 L/D with a compression ratio of 2.5:1 to 3.0:1 and a grooved feed section is recommended. Barrel set points are typically 150 °C feed, 160 °C compression, 165 °C metering, and 165 °C die. Melt residence time at temperature should remain below 15 min. For a 50 mm extruder with a 0.8 mm die gap, die melt pressure is typically 180–260 bar; sustained pressures above 350 bar indicate a blocked screen pack or insufficient temperature. Screw speed should be limited to avoid melt temperature over-run; start at 20–30 rpm and adjust based on melt pressure.
The melt exhibits pseudoplastic behavior. At processing shear rates from 10 s⁻¹ to 1000 s⁻¹, viscosity decreases with increasing shear rate; a power-law index of 0.3–0.5 can be used for initial screw-design calculations. Excessive shear in a mismatched high-compression screw can generate viscous heating and chain scission; barrier screws with a Maddock mixing section are therefore preferred over general-purpose PE screws with deep inlet channels and high compression ratios.
On a 55 mm grooved-feed blown film line with a 0.8 mm die gap, stable bubble geometry was obtained at blow-up ratios of 2.5:1 to 3.5:1. Frost-line height should be held at 2–4 die diameters. If frost-line height exceeds 4.0 die diameters, the bubble wanders and gauge variation increases because melt strength is lower than that of LLDPE. Chilled air at 10–18 °C is preferred; air temperatures above 25 °C delay crystallization and increase tackiness. Die lip attachment or drool is managed by die-temperature adjustments of ±5 °C and by maintaining a clean die lip. Internal bubble cooling can raise output but should only be used after stable ambient-air operation is established. On high-output lines, a 60/100/60 mesh screen pack is used to remove gel particles and protect the die gap; no screen pack should be used if the pressure drop exceeds 80 bar, because elevated melt pressure reduces throughput and increases shear heating.
The high-clarity designation derives from spherulite-size control and phase-morphology management. Unmodified PLA films can develop spherulites of 10–50 µm at conventional cooling rates, scattering visible light. The CL formulation increases nucleation density and reduces spherulite diameter below 1 µm. A refractive-index-matched copolyester or compatibilizer phase lowers interfacial scattering and improves distinctness of image. As a result, 50 µm film can exhibit haze below 8% under ASTM D1003-13 and gloss above 75 GU under ASTM D2457-13, while opaque compostable films may show 15–30% haze at equivalent thickness. The trade-off is a lower dart impact; nucleation increases stiffness and can reduce impact resistance by 10–20% relative to opaque grades. Ultraviolet or thermal post-crystallization should be avoided because it increases spherulite size and haze. Transverse direction haze is often more sensitive to die-lip lines and melt fracture; die-lip polish must be maintained.
Pre-drying is mandatory before extrusion. Pellet moisture must be below 0.025% (250 ppm). A desiccant dryer set at 60–80 °C for 4–6 h with a dew point of −40 °C or lower is specified. Moisture above 0.05% leads to hydrolytic degradation, lower melt viscosity, bubble instability, and film brittleness. At relative humidity above 60%, hopper residence should not exceed 30 min, or a closed feed hopper with dry-air sweep should be used. Unopened bags should be stored below 35 °C and 60% RH. Pellets exposed to ambient air for more than 12 h should be re-dried.
During start-up on a 45 mm extruder, an LDPE purge is used at 160 °C until melt pressure stabilizes below 200 bar. The hopper is then switched to Bio-Flex F 2201 CL. When transitioning from other PLA grades, purging with low-MFR PP is not recommended; a dedicated PLA purge compound is preferred. Shutdown requires reducing barrel temperatures to 150 °C before stopping the screw. If the line stops for more than 5 min, melt in the die should be purged before restart to avoid gel formation. Batch-to-batch variation in melt-volume rate should be monitored at incoming QC; a shift from 4.0 cm³/10 min to 5.5 cm³/10 min may require a 5–10 °C reduction in melt temperature to maintain bubble stability, while a decrease to 3.0 cm³/10 min may require a 5 °C increase in die temperature within the stated window.
Certification of the final film is article-dependent. The raw material is not intrinsically certified as compostable; the converted structure must pass disintegration, biodegradation, and ecotoxicity testing according to EN 13432:2000 or ASTM D6400. Food-contact compliance must be established on the actual film, including printing inks, adhesives, and coatings, under EU Regulation 10/2011 or component-specific FDA 21 CFR citations. The table below summarizes applicable frameworks.
| Framework | Scope | Typical Test or Requirement |
|---|---|---|
| EN 13432:2000 | Packaging recoverable through composting and biodegradation | Disintegration, biodegradation, ecotoxicity |
| ASTM D6400 | Compostable plastics for municipal or industrial aerobic composting | Biodegradation and disintegration |
| EU Regulation 10/2011 | Plastic food contact materials | Overall migration limits and specific migration |
| FDA 21 CFR 175.300 | Resinous and polymeric coatings for food contact | Component-specific compliance |
| REACH | Registration, authorization, SVHC communication | Article 33 SVHC notification |
Published data for this specific configuration is limited where all food-contact simulant and time/temperature combinations are considered. Converters must perform migration testing on the actual film structure and thickness. Incompatibilities with certain acidic or high-fat simulants are not covered by generic raw-material certifications.
Typical applications include high-clarity compostable produce bags, over-wrap film, garment bags, and retail carrier bags. On ambient-air blown film lines, thickness from 15 µm to 80 µm is attainable. Below 15 µm, gauge uniformity depends on die concentricity and melt-temperature homogeneity; above 80 µm, cooling limitations increase haze and lower output. The film is not recommended for frozen-food packaging without impact modification, because the PLA phase embrittles below −20 °C. A 100 mm die with a 3.0:1 blow-up ratio produces approximately 471 mm lay-flat width.
Relative to standard Bio-Flex blown film grades without the CL package, the optical gain is significant, but the nucleating system reduces dart impact by 10–20% at equal thickness. Relative to PBAT-rich compostable films, the PLA-containing F 2201 CL has higher tensile modulus and lower elongation at break. Tensile modulus is in the range of 2.5–3.5 GPa, and elongation at break is between 200% and 400% depending on orientation. Sealing initiation temperature is generally 85–105 °C, and seal strength is determined by ISO 527-3. Unlike petroleum-based LLDPE film, the grade has lower melt strength and a narrower operating window; it cannot be processed on high-stalk extrusion configurations designed for LLDPE. Corona treatment to 38–42 mN/m per ISO 8296 is used to maintain print adhesion for water-based inks; surface energy decays over time, so inline treatment is preferred.