| HS Code | 517791 |
| Material Type | Polylactic Acid (PLA) |
| Form | Extrusion/Thermoforming Sheet |
| Appearance | Clear |
| Density | 1.24 g/cm³ |
| Melt Flow Rate | 6.0 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 55.0 MPa |
| Tensile Strength At Break | 45.0 MPa |
| Tensile Modulus | 3.50 GPa |
| Elongation At Break | 3.5 % |
| Flexural Strength | 90.0 MPa |
| Flexural Modulus | 3.50 GPa |
| Notched Izod Impact Strength | 2.5 kJ/m² |
| Vicat Softening Point | 55.0 °C |
| Glass Transition Temperature | 55.0 °C |
| Melting Point | 150 °C |
| Haze | 2.0 % |
| Light Transmission | 90 % |
As an accredited Futerro PLA Extrusion Clear Extrusion/Thermoforming Sheet Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Futerro PLA clear extrusion/thermoforming sheet is packaged in 25 kg rolls, protective-film wrapped, and stacked on shipping pallets. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): palletized Futerro PLA clear extrusion/thermoforming sheet, secured, moisture-protected, and transported under dry, ambient conditions. |
| Shipping | Futerro PLA Extrusion Clear Extrusion/Thermoforming Sheet Polylactic Acid ships on pallets, securely wrapped against moisture, dust, and UV. Transport and store cool, dry, ideally below 30°C, away from direct sunlight and heat. Handle carefully to prevent scratching, warping, or bending. Not classified as hazardous for shipping. |
| Storage | Store in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and moisture. Keep in original sealed packaging or moisture-barrier wrap. Maintain flat, supported storage to prevent warping; avoid heavy stacking. Keep away from incompatible chemicals, strong alkalis, and solvents. Recommended conditions: 10–30°C, relative humidity below 50%. Do not expose to prolonged heat above 50°C. Rotate stock, use FIFO. |
| Shelf Life | Shelf life is typically 12 months when stored in original packaging in a cool, dry place, away from moisture, heat, and sunlight. |
Because PLA sheet is quenched to an amorphous condition on a polishing stack with chrome roll surface temperature held below 50 °C, the Futerro PLA Extrusion Clear Extrusion/Thermoforming Sheet grade can be converted into berry punnets and cut-fruit clamshells with haze values measured according to ASTM D1003-13 in the range 2% to 5% at 300 µm thickness. Where the Futerro grade-specific datasheet is not publicly available, the numerical ranges are drawn from commercial PLA extrusion/thermoforming production practice and should be validated on the target line. Drying prior to extrusion uses a desiccant dryer delivering -40 °C dew point air at 80 °C for 4 h, reducing pellet moisture to below 250 ppm; if regrind exceeds 15%, a second drying hopper is used because edge-trim fines reabsorb moisture within 30 min in plant floor air above 60% relative humidity. Sheet extrusion on a 32:1 single-screw extruder with barrel temperatures 180 °C to 200 °C and a gear pump inlet pressure of 80 bar to 120 bar feeds a flex-lip die with gap 0.5 mm to 1.0 mm. Thermoforming into produce punnets is initiated when sheet surface reaches 85 °C to 92 °C; lower surface temperature causes corner stress-whitening in draws deeper than 35 mm, while higher temperature causes sag exceeding 20 mm on 500 mm sheet width. Hole perforation for berry respiration is cut in-line with needle diameters 1.0 mm to 1.5 mm, giving open area 1% to 2% without reducing crush resistance more than 10% when measured under ISO 12048 top-load compression. Finished punnets are used for strawberries, blueberries, blackberries and mixed cut fruit at fill temperatures below 15 °C and storage below 8 °C; above 45 °C air temperature, stacking distortion occurs because PLA heat deflection temperature under 0.455 MPa load is approximately 50 °C to 55 °C per ASTM D648-18. Food-contact compliance is verified by overall migration testing to EN 1186-1:2002 under EU Regulation 10/2011, with a limit of 10 mg/dm²; specific migration of lactic acid is checked by EN 13130-1:2005 where applicable. The main operational boundary is not oxygen barrier: PLA permeability is higher than PET, so the punnets suit short shelf-life berries rather than modified-atmosphere applications requiring oxygen transmission rate below 10 cm³/m²/day unless an additional barrier coating is applied.
At 185 °C to 200 °C melt temperature, the Futerro PLA extrusion grade exhibits a melt-flow index in the 4 g/10 min to 8 g/10 min range when tested at 210 °C with 2.16 kg load per ISO 1133-1:2022; this viscosity window permits lid sheet extrusion at 250 µm to 350 µm on a 30:1 single-screw extruder with a barrier screw and a screen pack of 60/80/100 mesh. Cup and lid pair sealing is not governed solely by bulk polymer flow but by interfacial temperature and pressure at the rim. A natural PLA-to-PLA heat seal typically requires interface temperature of 105 °C to 120 °C, applied dwell 0.8 s to 1.5 s, and rim pressure 2 bar to 3 bar. However, when lid-forming scrap is reincorporated above 20%, molecular weight reduction caused by hydrolytic chain scission shifts seal initiation temperature upward by 3 °C to 5 °C and reduces seal strength measured under ASTM F88/F88M-21 by 15% to 25%. For cold beverage cups, the lid flange must retain a thickness of 150 µm to 200 µm after plug-assisted forming; thickness variation below -0.05 mm creates rim leaking at the seal because compression force is not uniformly distributed. An anti-block masterbatch dosage of 0.3% to 0.7% is common for block resistance, but slip additive migration from a lower-cost masterbatch can contaminate the seal region after 48 h, reducing burst pressure by 10% to 15%. Finished products include cold-fill tumblers, flat lids with straw crosses, and dome lids for iced beverages; the maximum sustained service temperature is limited to 55 °C in the lid skirt area, so use with hot coffee or tea is excluded unless the lid is separated by a barrier ring from the cup mouth. Compliance under EU Regulation 10/2011 must be re-established after any change in slip or anti-block masterbatch supplier because migration of non-monomer additives is not automatically covered by the base resin listing.
Maintaining sheet surface temperature within 88 °C to 96 °C is the critical control parameter for square and rectangular deli containers with draw ratios above 1.5:1. Below 88 °C, the amorphous PLA sheet behaves elastically enough to produce corner stress-whitening and microcracks at the container base radius when sidewall draw extends beyond 40 mm; the haze increase measured under ASTM D1003-13 can exceed 8% absolute. Above 96 °C, sheet sag on 600 mm width exceeds 25 mm, generating floor thickness below 120 µm and reducing falling-dart puncture resistance under ISO 6603-1:2000 by more than 30%. Plug-assisted forming uses a syntactic polybutylene terephthalate plug heated to 55 °C to 65 °C; plug speed should be set at 150 mm/s to 250 mm/s, because slower speeds permit premature sheet cooling against the plug, while faster speeds induce local draw marks on the sidewall. Mold temperature is normally held at 25 °C to 35 °C, with a differential of 5 °C to 10 °C between male and female sections to control release without causing rim curl. Cycle time for 400 µm sheet is 3.0 s to 5.0 s; longer residence in the oven above 100 °C increases crystallinity above 5% and creates visible milkiness. Deli containers are tempered by inclusion of 10% to 15% clean regrind, but regrind above 15% reduces sheet extensibility because repeated thermal history increases carboxylic acid end-group concentration above 20 meq/kg. Finished goods include rectangular salad containers, compartment trays, and cold-fill pasta snap-close bases. Compliance for fatty food contact under EU Regulation 10/2011 requires overall migration testing with simulant D2 for oil-in-water emulsion products, not only aqueous simulant A, because lactic acid oligomers have greater partitioning into slightly lipophilic media. The operational boundary is that air-tight clarity cannot be maintained if sheet is annealed for hot-fill performance above 70 °C, as PLA spherulitic growth causes a haze increase above 15% by ASTM D1003-13.
| Forming parameter | Below critical value | Observed defect | Above critical value | Observed defect |
|---|---|---|---|---|
| Sheet surface temperature | 88 °C | Corner stress-whitening, haze > 8% | 96 °C | Sheet sag > 25 mm, floor thickness < 120 µm |
| Plug temperature | 55 °C | Premature sheet chill, uneven draw | 65 °C | Sidewall sticking, gloss loss |
| Regrind content | 10% | Minimal property shift, stable viscosity | 15% | End-group increase > 20 meq/kg, reduced extensibility |
When a clear hinged bakery box is formed from 300 µm PLA sheet, hinge scoring must be set to 55% to 65% of the original thickness and the hinge radius kept above 1.0 mm because PLA has notched impact strength below 5 kJ/m² under ISO 179-1:2010 at 23 °C. A multilayer or laminated anti-fog coating applied at 0.5 g/m² to 1.5 g/m² is required for high-moisture patisserie items; without it, condensation droplets coalesce on the dome within 20 min of filling at 30 °C internal air temperature. The sheet is produced at 250 µm to 400 µm thickness and die gap 0.6 mm to 0.9 mm, with polish roll temperature 45 °C to 50 °C and lehr roll temperature 20 °C to 25 °C to prevent curl. Thermoforming uses a female cavity with plug assist; the plug depth is programmed to 70% of the cavity depth before vacuum release, which distributes sidewall thickness to a minimum of 140 µm. Bakery applications include dome boxes for muffins, palmiers, and small patisserie, but not whole cakes with a warm-fill above 40 °C because the hinge loses sealing force after repeated flexing if the package is held in a display cabinet above 35 °C. Clean bakery regrind may be incorporated up to 25%, but only if the trim is collected within 2 h and fed through a closed-loop dedusting bin, as flour dust on the sheet surface increases visible specks and reduces local seal strength under ASTM F88/F88M-21 by 10%.
Typical PLA sheet from the Futerro grade can be converted into clear hinged clamshells and snap-fit display blocks for cosmetics, electronics accessories, and stationery when the packaging is not exposed to sub-zero distribution temperatures. Instrumented falling-dart testing under ISO 6603-1:2000 on 350 µm sheet reports a puncture energy of 2 J to 4 J at 23 °C, dropping below 1 J at 0 °C; consequently, the hinged corners are radiused to at least 1.5 mm and nominal wall thickness after forming is maintained above 250 µm to prevent freight damage in unheated cargo holds. The clear folding structure is die-cut after extrusion using matched metal rules with tip angle 42° to 50°; because PLA shear edges will chip if the rule is dull, the cutting kiss pressure is limited to 0.3 MPa to 0.5 MPa on the platen. Snap-fit closure undercuts are formed at 8° to 12° draft angle and not reverse draft, because the amorphous PLA sheet has elongation at yield below 5% at 23 °C per ISO 527-2:2012, making undercut ejection difficult without stress-whitening. Additive practice for this sector restricts anti-block to 0.5% to 1.0% and avoids impact modifiers above 2%, because core-shell rubber dispersions cause a haze increase above 4% at 300 µm sheet thickness and reduce printability of the flat front panel. Compliance for packaging sold in the European Union requires the heavy-metal ceiling of 100 mg/kg for lead, cadmium, mercury, and chromium VI combined under EU Directive 94/62/EC, while electronic accessories packaging must also satisfy RoHS Directive 2011/65/EU for the packaged article rather than the polymer alone. In the United States, food-contact status is not derived from a general 21 CFR 177.1520 listing; PLA resin is cleared through a supplier-specific food contact notification under 21 CFR 170.100, so brand owners must retain the notification number for audit. Finished products include snap-fit phone-case trays, USB-cable clamshells, cosmetic gift sets, and transparent magnet boxes replacing rigid PVC or PETG.
| Requirement | Standard or directive | Acceptance or relevance |
|---|---|---|
| Heavy metals in packaging | EU Directive 94/62/EC | Sum of lead, cadmium, mercury, chromium VI < 100 mg/kg |
| Electronic article restriction | RoHS Directive 2011/65/EU | Applies to packaged article, not polymer alone |
| U.S. food-contact notification | 21 CFR 170.100 | Supplier-specific FCN required |
For chocolate cavity trays, the cooling tunnel return air temperature must be held between 10 °C and 15 °C, and the formed tray must be ejected at a sheet core temperature below 35 °C to avoid embossing collapse on the cavity floor under the weight of successive trays. The shallow cavities are formed from 200 µm to 300 µm sheet with draw depth below 20 mm; above 20 mm, the clear PLA tray can exhibit thinning at the cavity base to 80 µm, reducing chocolate containment rigidity. In contrast to deep deli draws, the confectionery tray cycle time can be shortened to 2.0 s to 3.5 s because the low draw does not require plug penetration beyond 40% of cavity depth. The critical surface property is coefficient of friction; an anti-block dose of 0.4% to 0.8% and a slip additive dose of 0.2% to 0.5% prevent nesting of trays in the magazine feed without affecting chocolate release, measured as a release angle below 5° from the cavity after conditioning at 18 °C for 24 h. However, lipophilic cocoa butter can selectively absorb low-molecular-weight lactide oligomers when the tray directly contacts couverture for more than 30 days at 25 °C; this makes migration testing under EN 13130-1:2005 with simulant D2 more indicative of real risk than an aqueous simulant A test. The final product is used as an insert inside folding cartons for pralines, individual chocolates, or chocolate truffles; barrier to oxygen and moisture is not sufficient for unrefrigerated shelf life beyond 6 months without an inner flow wrap. Regrind loading is limited to 10% because visual scoring from black specks is unacceptable in white or pastel carton interiors, and edge-trim contamination with cocoa dust lowers tear strength of the web by 8% to 12% when measured under ASTM D638-14.
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Futerro PLA Extrusion Clear Extrusion/Thermoforming Sheet Polylactic Acid is a semicrystalline polylactide product designation for monolayer clear sheet extrusion and subsequent roll-fed or cut-sheet thermoforming of rigid articles. The product is based on poly(L-lactic acid) with the linear aliphatic polyester repeat unit [–O–CH(CH₃)–CO–]ₙ, obtained by ring-opening polymerization of lactide. The designation refers to a clear sheet/resin system, not an injection-molding or fiber grade. Published data for this specific Futerro grade configuration is limited; the processing and property boundaries below are drawn from public technical data for semicrystalline PLA extrusion/thermoforming resins and should be confirmed against lot-specific Futerro documentation. The material is applied to clear clamshells, blister trays, portion cups, lids, bakery containers, produce punnets, and cosmetic blisters. Sheet for these formats is commonly specified at 150 µm–2 mm gauge, with optical transmission above 90 % and haze below 3 % on 1.0 mm sheet measured according to ASTM D1003. Density is in the range of 1.24 g/cm³ per ISO 1183-1; melt mass-flow rate for extrusion/thermoforming grades is generally 2–8 g/10 min at 210 °C/2.16 kg per ISO 1133-1:2022. Tensile yield strength is in the range of 50–65 MPa and tensile modulus 3.0–3.5 GPa per ISO 527-2; flexural modulus is 3.0–3.6 GPa per ISO 178; notched Izod impact is 2–4 kJ/m² per ISO 180/A. Glass transition occurs at 55–60 °C and melting endotherm at 145–160 °C per ISO 11357-2/3. These values separate the sheet extrusion grade from Futerro injection-molding and fiber grades, which are formulated with different melt-flow and crystallization kinetics.
Hydrolysis is the dominant melt-processing failure mode. PLA is hygroscopic, and moisture in the pellet feed reacts through ester cleavage, reducing molecular weight, increasing melt mass-flow rate, and lowering melt strength. On production lines, insufficient drying is observed first as die-lip drool, melt curtain instability, microbubbles, or random haze bands. The resin is pre-dried in a desiccant bed at 80 °C for 4 h to residual moisture below 250 ppm, measured by ISO 15512 Karl Fischer titration. A dry-air hopper with dew point below -40 °C is required; unprotected transfer at 23 °C and 50 % RH can reintroduce process-limiting moisture within minutes. Regrind is limited to 30 % by weight and re-dried under identical conditions, because multiple heat histories reduce molecular weight and raise carboxylic acid end-group concentration. If pellet moisture exceeds 500 ppm, drying time is extended beyond 4 h, and melt viscosity loss becomes measurable as an upward shift in melt mass-flow rate.
Flat-sheet extrusion is performed on single-screw extruders with 30:1 to 36:1 L/D, barrier-flight screws, and vacuum venting. Barrel temperatures are generally set from 180 °C to 210 °C, with adapter and sheet die temperatures near 200 °C. Sustained melt temperatures above 230 °C accelerate lactide reformation, yellowing, and thermal degradation. The melt is shear-sensitive; high screw speed or restrictive die gaps can generate frictional heating that is not reflected in barrel set-points. Melt pressure at the die lip is maintained below the onset of melt fracture, and polished die lips are used to preserve surface smoothness. The melt is cast onto a chrome-plated three-roll stack with roll temperatures held at 20–40 °C to quench the web to an amorphous state. Roll temperatures above approximately 60 °C can induce cold crystallization and haze. Edge bead control, vacuum trim, and independently heated die zones are used to maintain sheet gauge variation below ±5 % of nominal for stable thermoforming.
The upper processing limit is lower than that of PET. PLA sheet typically processes near 200 °C, whereas PET sheet extrusion normally operates at 270–300 °C. This lower melt-temperature ceiling requires tighter thermal control and places greater demand on screw design to avoid unmelted polymer at low stock temperatures and local overheating at high shear.
On roll-fed thermoforming lines with zoned ceramic or quartz IR ovens, clear extruded sheet is heated to a surface temperature of 90–120 °C depending on gauge, orientation state, and line speed. The forming window is narrower than amorphous PET because PLA undergoes rapid cold crystallization above 100 °C, which can freeze orientation and produce visible haze. Plug-assist tools made from syntactic foam or PEEK are used to reduce surface sticking and heat transfer from the plug. For amorphous clear parts, mold temperatures are held at 20–40 °C to preserve optical clarity and reduce cycle time. When heat-set thermoforming is specified, mold temperature is raised to 100–110 °C to permit lamellar thickening and improve dimensional stability at the expense of haze. Published data for this specific Futerro grade is limited; heat-set PLA resins generally require low D-lactide content, often below 2 mol%, because stereochemical defects depress the maximum obtainable crystalline fraction. Unannealed sheet has a heat deflection temperature of 50–60 °C at 0.455 MPa per ISO 75-2/B, so continuous service above 45–50 °C is not recommended for clear amorphous parts. Draw ratios above 3:1 can create localized thinning at pinch points and hinge regions; plug displacement, pre-blow timing, and mold venting are adjusted to avoid orientation-induced stress concentration. The notched Izod impact of 2–4 kJ/m² per ISO 180/A indicates brittle failure in thin-wall parts; living hinges and snap-fit features should be radiused and aligned to avoid crack propagation perpendicular to the extrusion direction.
Regulatory status is not determined solely by resin composition. For European food-contact use, the finished article must comply with Commission Regulation (EU) No 10/2011, including overall migration limits of 10 mg/dm² or 60 mg/kg depending on the food simulant and contact ratio. Specific migration of residual lactide, lactic acid, and any processing aids is assessed under the intended time–temperature conditions. In the United States, PLA is not automatically covered by 21 CFR 177.1520, which addresses olefin polymers; food-contact status for PLA resins is generally established through a Food Contact Notification or other FDA clearance for the specific grade and conditions of use. The converter must verify that the final sheet and formed article meet the relevant migration limits under the actual food type, temperature, and contact duration.
Industrial compostability claims for PLA packaging should be based on certification of the finished article to EN 13432 or ASTM D6400. These standards require aerobic biodegradation of at least 90 % of organic carbon to CO₂ within 180 days, disintegration with at least 90 % of material passing a 2 mm sieve after 12 weeks, and compliance with ecotoxicity and heavy metal limits. Home compostability should not be assumed; separate certification to a standard such as AS 5810 or NFT 51-800 is required. Under REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU, the product is supplied with substance declarations and does not require the cadmium- or lead-based stabilizers typical of some PVC formulations.
Barrier performance in formed articles is not directly equivalent to flat-sheet data because thermoforming induces variable wall thinning and localized orientation. Oxygen permeability of PLA at 23 °C and 0 % RH is typically 40–60 cm³·mm/m²·day·atm per ASTM D3985; at 50 % RH, permeability may rise to 80–120 cm³·mm/m²·day·atm as water plasticizes the amorphous regions. Water vapour transmission rate at 23 °C and 85 % RH is commonly 15–25 g·mm/m²·day per ISO 15106-2. Carbon dioxide permeability is typically 3–5 times the oxygen permeability, which is relevant for respiring produce packaging. Permeability coefficients increase sharply as service temperature approaches the glass transition; at 40 °C, oxygen permeability can be substantially higher than at 23 °C. These properties place the material between PET and PS for oxygen barrier and below PET for moisture barrier. Shelf-life modelling for food packaging therefore requires normalized transmission rate data integrated over the actual time–temperature distribution rather than single-point values at ambient room temperature. Formed articles with wall thickness below 200 µm may require additional barrier coatings or multilayer structures if shelf-life targets exceed the intrinsic permeability of PLA.
The combination of lower density, moderate stiffness, and renewable carbon differentiates this PLA extrusion/thermoforming sheet from comparative clear rigid packaging substrates. Compared with PET, the PLA density is lower (1.24 g/cm³ versus 1.33 g/cm³), but heat deflection temperature is substantially lower, limiting hot-fill and retort use. Compared with polypropylene, the tensile modulus is higher, but notched impact strength is lower, making PP more ductile in thin-wall closures. Compared with polystyrene, PLA provides lower oxygen permeability at chilled temperatures but has lower water-vapour resistance than PET. Compared with amorphous PLA injection grades, the extrusion/thermoforming designation uses a lower melt mass-flow rate and higher melt strength to resist draw resonance; however, the resin remains unsuitable for extrusion blow molding or stretch blow molding unless a dedicated high-melt-strength or crystallizable grade is selected. The table below summarizes representative public property ranges for clear rigid packaging substrates.
| Property | PLA extrusion/thermoforming class | PET sheet | PP sheet | PS sheet |
|---|---|---|---|---|
| Density (g/cm³) | 1.24 | 1.33 | 0.90 | 1.05 |
| Tensile modulus (GPa) | 3.0–3.5 | 2.8–3.4 | 1.2–1.6 | 2.8–3.5 |
| HDT at 0.455 MPa (°C) | 50–60 | 70–80 | 90–110 | 75–90 |
| Industrial compostability | Certifiable under EN 13432/ASTM D6400 | Not industrially compostable | Not industrially compostable | Not industrially compostable |
These comparative values are representative general ranges from public polymer data; the Futerro grade-specific values should be taken from the technical data sheet and not from the table alone.