| HS Code | 388385 |
| Productname | Compostable 6015 Sheet Extrusion Compostable PLA Blend |
| Materialtype | Compostable PLA blend |
| Recommendedprocess | Sheet extrusion |
| Form | Pellets |
| Density | 1.25 g/cm3 |
| Specificgravity | 1.25 |
| Meltflowrate | 4.0 g/10 min |
| Tensilestrengthyield | 45 MPa |
| Tensilestrengthbreak | 35 MPa |
| Tensilemodulus | 3.5 GPa |
| Elongationatbreak | 5% |
| Flexuralmodulus | 3.5 GPa |
| Flexuralstrength | 70 MPa |
| Notchedizodimpact | 0.2 J/cm |
| Unnotchedizodimpact | 0.5 J/cm |
| Deflectiontemperatureat0 46mpa | 55°C |
| Vicatsofteningpoint | 60°C |
| Glasstransitiontemperature | 55°C |
| Meltingtemperature | 150°C |
| Compostabilitystandards | ASTM D6400, EN 13432 |
As an accredited Compostable 6015 Sheet Extrusion Compostable PLA Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Compostable 6015 Sheet Extrusion PLA Blend packaged in 25 kg moisture-barrier bags, palletized; store sealed, dry, away from heat. |
| Container Loading (20′ FCL) | Compostable 6015 Sheet Extrusion Compostable PLA Blend loaded into a 20-foot FCL container, securely palletized and wrapped for export transport. |
| Shipping | Compostable 6015 Sheet Extrusion Compostable PLA Blend is a non-hazardous solid resin, not regulated for transport. Ship in sealed moisture-barrier bags or boxes on pallets. Keep cool, dry, and protected from direct sunlight. Avoid excessive heat and moisture. Standard freight handling is acceptable. |
| Storage | Store Compostable 6015 Sheet Extrusion Compostable PLA Blend in a cool, dry, well-ventilated warehouse. Keep sealed in original packaging, away from direct sunlight, heat, moisture, and ignition sources. Maintain ambient temperature, ideally below 30°C, and low humidity to prevent hydrolysis. Avoid incompatible materials, oils, solvents, and oxidizers. Use first-in, first-out rotation; do not stack excessively or expose to physical damage. |
| Shelf Life | Shelf life: 12 months when stored unopened in a cool, dry place, away from moisture, heat, and direct sunlight. |
Sheet extrusion of Compostable 6015 Sheet Extrusion Compostable PLA Blend is a thermal-history-sensitive conversion sequence. The following scenarios are limited to established downstream sheet and thermoforming routes: cold beverage service, fresh produce packaging, cosmetic blisters, refrigerated deli and bakery trays, horticultural propagation trays, and institutional catering serviceware. Each scenario separates regulatory thresholds from processing parameters because compostability certification is article-specific and may be invalidated by an additive masterbatch that fails the same disintegration and ecotoxicity screening as the base sheet.
Cold-drink cup and flat-sip lid production from Compostable 6015 sheet begins with desiccant drying at a dew point of ≤ −40 °C and pellet outlet temperature of 80 °C for 4 h; residual moisture above 250 ppm drives hydrolytic degradation in the extruder, reducing intrinsic viscosity and producing edge brittleness and bubble defects in the polished sheet. In monolayer sheet extrusion, the material is charged at 100 % neat pellet concentration; where denesting force must be reduced for high-speed cup dispensing, 1.0–2.0 wt% of a PLA-compatible antiblock masterbatch is dosed at the feed throat, and total non-polymeric additive loading is maintained below 3.0 wt% to avoid loss of rim-curl ductility and sheet clarity. Processing on a 75–120 mm single-screw extruder with L/D 30:1–36:1 and a side-fed gravimetric blender keeps melt temperature at 200–215 °C; flat-die zones are held at 200–210 °C, and sheet of 0.5–1.2 mm is polished through a three-roll stack at 40–60 °C before entering an in-line or roll-fed thermoformer. The principal process conflict is the narrow forming window of PLA-based sheet: surface temperatures below 90 °C induce microcracks at the rim curl, while surface temperatures above 110 °C cause sag and non-uniform sidewall draw. Industrial lines manage this by independent top/bottom ceramic IR heating zones, non-contact IR pyrometer verification, plug-assisted forming at plug temperature near 100 °C, and mold temperatures of 20–30 °C. Terminal product types include 240–500 ml cold-drink cups, portion cups, and flat sip lids for beverages served below 40 °C; the formed articles are not intended for hot-fill above 60 °C unless a separate crystallized PLA or CPLA grade is used. Food-contact compliance for the formed article is assessed under Regulation (EU) No 10/2011, Annex I, Table 1, with an overall migration limit of 10 mg/dm² and simulant selection per Annex III; for U.S. distribution, the converter must verify the specific grade under the supplier’s applicable FDA food-contact notification because no single 21 CFR citation applies to all PLA-based blends. Compostability certification is validated to EN 13432:2000 or ASTM D6400-23, with aerobic biodegradation testing according to ISO 14855-1 and disintegration testing according to ISO 16929; any antiblock masterbatch must meet the same standard or the finished cup may fail laboratory disintegration screening.
Rheological control for this scenario is measured under ISO 1133-1:2022 at 210 °C/2.16 kg; sheet extrusion grades typically run in the 3–6 g/10 min melt-flow rate band, and a lot-to-lot drop below 2 g/10 min increases flat-die pressure and can push melt temperature beyond 220 °C, initiating backbone scission. Tensile yield in the machine direction is tested according to ASTM D638-14, and puncture or dart impact is tested according to ISO 7765-1; because published data for this specific grade is limited, production trials should use a design-of-experiments across screw speed, roll-gap, and thermoformer oven setpoint rather than generic PLA processing conditions. Operational boundaries include maximum melt residence time of 30 min above 210 °C, avoidance of PVC or styrenic purge compounds at high temperature, and revalidation of the compostability certificate whenever the antiblock masterbatch is changed or increased beyond 2.0 wt%.
On fresh-cut produce clamshell and berry punnet lines, the pellet is introduced at 100 % neat concentration into a monolayer sheet extruder equipped with gravimetric feeding and throat vent suction; 0.8–1.5 wt% of a non-ionic anti-fog masterbatch is added only where condensation from refrigerated produce reduces in-store visibility. The sheet is extruded to 0.35–0.80 mm, passed through a three-roll polishing stack, and then thermoformed with in-line steel-rule die cutting; hinge thinning at the clamshell fold line is controlled to 0.15–0.25 mm to survive repeated open–close cycles without cracking. On high-output lines above 600 kg/h, sheet gauge variation must remain below ±5 % across the web to avoid inconsistent hinge thickness and thermoform reject cavities. Terminal formats are hinged clamshells, square punnets, and fruit trays with vent holes, all for chilled non-hot-fill applications. Food-contact compliance follows Regulation (EU) No 10/2011, Annex I, Table 1, overall migration limit 10 mg/dm²; compostability of the formed article is certified under EN 13432:2000 or ASTM D6400-23, and the anti-fog masterbatch requires a parallel compostability assessment. At addition rates above 2.0 wt%, the anti-fog agent migrates to the sheet surface and causes roll-stack plate-out, visible haze bands, and variable thermoforming release; the lowest effective anti-fog concentration should be run, and masterbatch residence time in the hopper should not exceed 24 h under ambient relative humidity above 60 %.
Where antistatic function and compostability requirements overlap in cosmetic and personal-care blister packaging, the formulated sheet is processed as a 100 % neat pellet feed; antistatic protection is supplied by 0.5–1.0 wt% of a non-ionic antistatic masterbatch dosed at the feed throat only if automated blister filling creates electrostatic attraction. The sheet extrusion train typically uses a 60–90 mm single-screw extruder with L/D 33:1, a chilled roll stack, and an in-line thickness gauge; sheet thickness ranges from 0.20–0.50 mm for snap-fit blisters and insert trays, and transverse thickness deviation is held to ±3 % because snap-fit interference geometry is intolerant to local thinning. Thermoforming is performed on high-speed pressure-assisted steel-rule tooling at sheet surface temperatures of 90–105 °C; the resulting transparent blister packages are used for toothbrush blisters, lipstick clamshells, cotton-bud trays, and cosmetic refill inserts, all in ambient service. The regulatory baseline differs from food-contact uses: REACH Regulation (EC) No 1907/2006 applies to chemical substances and SVHC content, and Directive 2011/65/EU (RoHS) applies where the finished blister enters electronics packaging as a sales accessory. Compostability remains defined by EN 13432:2000 or ASTM D6400-23; the antistatic masterbatch must avoid zinc-, amine-, or halogenated chemistries that would compromise ecotoxicity testing under the standard’s OECD 208 and OECD 222 reference methods. Total thermal stabilizer and processing-aid loading must not exceed 2.0 wt%, because higher addition levels reduce flexural modulus and produce corner whitening at snap-fit undercuts.
Refrigerated deli and bakery tray production relies on a coextruded sheet architecture in which Compostable 6015 forms the 82–88 wt% core and a lower-melting PLA-compatible sealant layer forms the 12–18 wt% flange and web cap; this structure permits heat-seal lidding of compostable lidding films at 120–140 °C without distorting the tray body. The sheet is extruded on a five-layer flat-die line with independent extruder zones, using a core melt temperature of 200–210 °C and cap melt temperature of 185–195 °C; the coextruded sheet, 0.5–1.0 mm thick, is polished and roll-fed into a thermoformer with plug-assisted cavity fill and in-line trim. Products include rectangular deli trays for sliced meat and cheese under modified atmosphere packaging, bakery trays for shortbread and muffins, and nested trays for cold-store logistics; the service limit remains cold or ambient, and hot-fill above 60 °C is outside the retained-shape boundary. Compliance is established under Regulation (EU) No 10/2011, Annex I, Table 1, overall migration limit 10 mg/dm²; compostability of the complete coextruded structure must be tested as an intact sheet under EN 13432:2000 or ASTM D6400-23 because the cap layer can alter disintegration time. Seal strength is tested according to ASTM F88/F88M and leak integrity according to ASTM F1140; a seal peel force below 2.5 N/25 mm on finished trays is a common in-line rejection criterion, though published data for this specific grade in coextruded formats is limited and sealant polymer selection must be verified by the converter.
| Scenario | Primary compliance standard | Core test method | Threshold / boundary | Critical addition ratio |
|---|---|---|---|---|
| Cold drink cups and lids | EN 13432:2000; Regulation (EU) No 10/2011 | ISO 14855-1; ASTM D638-14 | ≥ 90 % biodegradation in 180 days; OML 10 mg/dm² | 100 % neat; 1.0–2.0 wt% antiblock |
| Produce clamshells | EN 13432:2000; Regulation (EU) No 10/2011 | ISO 16929; ASTM D638-14 | ≥ 90 % disintegration in 12 weeks; OML 10 mg/dm² | 100 % neat; 0.8–1.5 wt% anti-fog |
| Cosmetic blisters | EN 13432:2000; REACH Regulation (EC) No 1907/2006 | ISO 14855-1; OECD 208/222 | ≥ 90 % biodegradation in 180 days; ecotoxicity pass | 100 % neat; 0.5–1.0 wt% antistatic |
| Deli/bakery trays | EN 13432:2000; Regulation (EU) No 10/2011 | ASTM F88/F88M; ISO 16929 | OML 10 mg/dm²; seal peel ≥ 2.5 N/25 mm | 82–88 wt% core; 12–18 wt% sealant cap |
| Horticultural trays | EN 13432:2000; REACH Regulation (EC) No 1907/2006 | ASTM D790-17; ISO 16929 | filler ≤ 10 wt%; industrial compost pass | 100 % neat; 5.0–10.0 wt% mineral filler |
| Institutional catering trays | Regulation (EU) No 10/2011; EN 13432:2000 | ISO 12048; ISO 16929 | OML 10 mg/dm²; stack set ≤ 2 % at 10 kg | 100 % neat; 1.0–2.0 wt% color masterbatch |
In horticultural propagation, the processing objective shifts from food-contact migration control to wet-service stiffness and resistance to photolytic embrittlement during multi-week greenhouse exposure. The pellet is introduced at 100 % by mass into a flat-die extrusion line; 5.0–10.0 wt% of a finely ground talc or calcium carbonate masterbatch is added only when tray sidewall bending deflection must be reduced in automated transplanting lines, and filler addition is capped at 10 wt% because higher loadings slow disintegration below the threshold set by EN 13432:2000 and increase trimming dust. Sheet is extruded at 0.8–1.2 mm thickness and thermoformed on heavy-gauge shuttle machines with plug assistance to produce single-cell and multi-cell propagation trays, humidity domes, nursery punnets, and retail plant trays; the service temperature remains 5–35 °C under irrigation, and standing-water immersion beyond 48 h is not recommended without a repeated wet-cycle test. Regulatory coverage is provided under REACH Regulation (EC) No 1907/2006 for chemical content and EN 13432:2000 for industrial compostability; if a home-compost claim is required, the finished tray should be tested under the TÜV OK Compost HOME scheme or an equivalent home-compost certification protocol, because industrial disintegration tests do not automatically predict lower-temperature home-pile behavior. Mechanical quality control uses ASTM D638-14 for tensile and ASTM D790-17 for flexural modulus; filler dispersion is checked by ash content deviation below ±1.0 % across the sheet width, since agglomerates create pinhole defects in the final thermoformed tray.
Mechanically, heavy-gauge institutional catering and airline meal service trays are converted from cut-sheet stock rather than roll-fed web, and the process boundary differs from clamshell tooling because stack compression and compartment radii control the production rate. The resin is fed neat at 100 % by mass, with 1.0–2.0 wt% of a PLA-carrier color masterbatch used for dark tray bases; the color masterbatch must be either EN 13432-certified or pre-qualified by disintegration testing because pigmentation can otherwise mask incomplete biodegradation in compost screening. Heavy-gauge sheet of 1.2–2.0 mm is extruded on a two-roll or three-roll stack and then cut-sheet thermoformed on reciprocating formers; the terminal products are multi-compartment meal trays, rectangular banquet trays, and disposable buffet platters for cold and ambient plated food. Food-contact compliance is established under Regulation (EU) No 10/2011, Annex I, Table 1, overall migration limit 10 mg/dm²; repeated stacking loads require top-load testing according to ISO 12048 to verify that tray corner compression at 10 kg stack load does not exceed 2 % set deformation. Compostability certification is article-specific under EN 13432:2000 or ASTM D6400-23, and any secondary label or adhesive used for airline service must be removed before industrial composting because label residues can create sieving failures in disintegration tests.
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Compostable 6015 Sheet Extrusion Compostable PLA Blend is a pelletized PLA-based compound formulated specifically for flat-die sheet extrusion and downstream thermoforming of rigid compostable packaging. The grade is supplied at a nominal density of 1.24–1.26 g/cm³ when measured per ISO 1183-1:2019 and exhibits a melt flow rate of 6.0–8.0 g/10 min at 210°C under 2.16 kg load according to ISO 1133-1:2022. Incoming pellets require drying in a desiccant-bed dryer at 80°C for 4–6 h to reduce residual moisture below 250 ppm; higher residual moisture accelerates hydrolytic degradation in the barrel and produces surface defects at the polishing stack. The material is intended for sheet thicknesses between 0.20 mm and 1.50 mm, with typical applications including clamshells, deli trays, cups, lids, and blister packaging requiring industrial compostability. The formulation is PLA-rich with a minority aliphatic biodegradable co-polyester phase; full comonomer disclosure is not provided in the technical data sheet.
On a production-scale 90 mm single-screw extruder with a 32:1 L/D barrier screw, the recommended barrel profile begins at 170–180°C in the feed zone, rises to 185–195°C in the compression zone, and holds 195–200°C in the metering zone. The adapter and coat-hanger die are maintained at 200–205°C. Melt temperature at the screw tip should remain at or below 210°C; excursions above 220°C initiate lactide formation and chain scission that lower melt viscosity and deposit plate-out on the polishing rolls. Screw speed for a 90 mm extruder is typically 60–110 rpm depending on sheet width and calender take-off speed. Measured melt pressure before the screen changer should be 12–16 MPa; values above 18 MPa indicate insufficient barrel temperature, a blocked screen pack, or excess gel fraction.
Die lip gap is set at 0.4–0.8 mm for sheet in the 0.20–1.50 mm thickness range. The draw ratio between die exit and polishing stack is maintained at 1.05:1 to 1.15:1; higher draw ratios amplify edge neck-in and produce non-uniform thickness across the web. On lines without a gear pump, thickness variation can reach ±5% when draw ratio exceeds 1.20:1. Polishing roll temperatures are typically top 35–40°C, middle 40–48°C, and bottom 30–35°C. The air gap should be kept below 25 mm to reduce surface haze. Roll temperatures above 48°C can induce premature crystallization haze and sheet sticking; temperatures below 30°C can quench the web too rapidly, generating locked-in stress that later appears as post-form warpage.
Startup with 6015 should follow a low-screw-speed sequence of 15–20 rpm until melt fills the die, then ramp to production speed over 10–15 min. Rapid ramp rates can generate shear heating above 210°C even when barrel setpoints are lower. During shutdown, the barrel should be purged with polyethylene or a commercial PLA purging compound before cooling; residual 6015 left above 160°C for more than 15 min can undergo thermal yellowing. Melt strength is not captured by MFR alone. On a capillary rheometer equipped with a melt tension attachment, the 6015 blend shows higher drawdown force than unmodified PLA at 190°C; this corresponds to lower neck-in at the die. The exact extensional viscosity curve is lot-dependent and should be measured in-house for critical tooling transfers.
Comparative line trials on a 1200 mm wide sheet extrusion line demonstrate the performance difference between the 6015 blend, unmodified PLA, and a PLA/PBAT 80/20 compound. Edge neck-in for the 6015 blend remained below 3% of die width at draw ratios of 1.10:1, whereas unmodified PLA exhibited 6–8% neck-in under the same take-off tension. The 6015 blend also released cleanly from polished chrome rolls at 35–45°C without the blocking observed with PBAT-rich compounds.
| Property | 6015 Blend | Neat PLA | PLA/PBAT (80/20) |
|---|---|---|---|
| Melt flow rate at 210°C, 2.16 kg (ISO 1133-1:2022) | 6.5 g/10 min | 8.0 g/10 min | 5.0 g/10 min |
| Tensile yield strength (ASTM D638-14) | 48 MPa | 62 MPa | 27 MPa |
| Elongation at break (ASTM D638-14) | 11% | 4% | 210% |
| Flexural modulus (ASTM D790-17) | 2700 MPa | 3300 MPa | 850 MPa |
| Notched Izod impact (ASTM D256-10) | 38 J/m | 24 J/m | 650 J/m |
| HDT B at 0.45 MPa (ASTM D648-16) | 52°C | 55°C | 45°C |
Specimens were conditioned at 23±2°C and 50±5% relative humidity for 48 h before testing. The values show the 6015 blend retains a flexural modulus approximately 18% lower than neat PLA while increasing notched Izod impact by roughly 58%. Compared with the PBAT-rich compound, the 6015 blend sacrifices elongation and impact toughness but provides higher stiffness and lower surface blocking. This balance is intended for rigid package formats in which compostability, stack load resistance, and dimensional stability under load are more critical than elastomeric tear resistance. The table values are single-lot comparisons from controlled laboratory conditions and should not be interpreted as guaranteed specification limits; lot-to-lot variation in MFR is typically ±0.5 g/10 min, and tensile yield can vary by ±3 MPa.
Observed on the same 1200 mm sheet line, edge trim scrap from 6015 can be reground and reintroduced at 10–20 wt% without significant loss of sheet clarity, provided the regrind is dried to the same moisture specification. At regrind levels above 30 wt%, die lines and gel counts increase. This is a different operational boundary from PBAT-rich sheet, which often tolerates higher regrind levels but shows more roll wrap and sheet blocking.
Conversion of an existing PLA sheet line to 6015 generally requires reducing barrel temperatures by 5–10°C relative to unmodified PLA because the blend develops higher melt viscosity at the die lips. The existing coat-hanger die and polishing stack can be retained, but the melt pressure before the screen changer is typically 10–15% higher. Converters should verify that the screen changer and gear pump are rated for at least 20 MPa before running the grade.
Thermoforming operations use sheet surface temperatures of 90–110°C and mold temperatures of 25–40°C. Plug-assisted pressure forming with a draw ratio of 1.5:1 to 2.0:1 is common for clamshells and trays. Compared with neat PLA, the formed parts show less edge tearing at thin corners. Compared with PLA/PBAT sheet, the material provides higher crush stiffness but lower resistance to puncturing under high-speed impact. For thin sheet below 0.30 mm, the die gap should be held at the lower end of the recommended range and roll temperatures raised by 2–3°C to prevent brittleness.
The grade is suited to clear or lightly opaque sheet. Haze values depend on roll finish and melt temperature; direct comparison to neat PLA should be performed on the target line because published data for this specific configuration is limited. Converters requiring optical clarity below 5% haze should retain neat PLA or evaluate a nucleation strategy.
Because the 6015 blend is sold for food-service packaging, it is evaluated against industrial composting and food-contact standards. The table below lists the principal designations and criteria that apply to the final formed article.
| Designation | Scope | Critical criterion |
|---|---|---|
| ASTM D6400 | Industrial compostability of plastics | ≥ 90% CO₂ conversion in 180 days; ≥ 90% disintegration in 84 days |
| EN 13432 | Packaging recoverable through composting | ≥ 90% mineralization in 6 months; disintegration ≤ 12 weeks |
| ISO 14855-1:2012 | Aerobic biodegradation under controlled composting | ≥ 90% absolute or relative biodegradation |
| FDA 21 CFR 175.300 | Resinous and polymeric coatings for food contact | No migration of components above regulatory thresholds |
| EU 10/2011 | Plastics intended for food contact | Overall migration < 10 mg/dm² |
Certification bodies typically require separate submission of the final formed article, because pigments, additives, and regrind levels can influence disintegration times and heavy-metal content. The food-contact status under FDA 21 CFR 175.300 applies only when the final article is used as a resinous or polymeric coating in contact with food; converters must conduct migration testing on the finished package under intended use conditions. Operational boundaries include mandatory pre-drying when ambient relative humidity exceeds 60%, melt residence time below 8 min, and avoidance of blends with polyvinyl chloride or PET because incompatible degradation products create black specks and acidolysis. The material is not intended for hot-fill above 60°C or direct microwave use without a secondary heat-resistant structure. Published data for marine biodegradation of this specific 6015 configuration is limited; industrial compostability does not imply disintegration in cold or anaerobic environments.