| HS Code | 367845 |
| Density | 1.25 g/cm³ |
| Melt Flow Rate | 3.0 g/10 min at 190°C/2.16 kg |
| Tensile Strength At Yield | 34.5 MPa |
| Tensile Strength At Break | 34.5 MPa |
| Tensile Modulus | 2.41 GPa |
| Elongation At Break | 3.5% |
| Flexural Strength | 55.2 MPa |
| Flexural Modulus | 2.41 GPa |
| Notched Izod Impact | 0.267 J/cm |
| Unnotched Izod Impact | 1.60 J/cm |
| Heat Deflection Temperature | 51.7°C at 0.46 MPa |
| Vicat Softening Point | 56.1°C |
| Melting Point | 150°C |
| Processing Temperature | 160-190°C |
| Drying Temperature | 70°C |
As an accredited Compostable 1002 Sheet Extrusion Compostable PLA Blend factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg moisture-barrier bags, palletized and stretch-wrapped, labeled with batch, safety, and compostability information for Compostable 1002 Sheet Extrusion PLA Blend. |
| Container Loading (20′ FCL) | 20′ FCL container loading for Compostable 1002 Sheet Extrusion Compostable PLA Blend, securely palletized and stowed for safe ocean transport. |
| Shipping | Compostable 1002 Sheet Extrusion Compostable PLA Blend ships as a non-hazardous solid resin in moisture-barrier bags, lined cartons, or drums on pallets. Store and transport in a cool, dry, ventilated area away from heat, sunlight, and moisture. Follow the SDS and local regulations. Handle carefully to prevent package damage. |
| Storage | Store Compostable 1002 Sheet Extrusion Compostable PLA Blend in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep original containers tightly closed and palletized off the floor. Maintain moderate temperatures and low humidity to prevent hydrolysis or degradation. Follow first-in, first-out stock rotation; avoid prolonged storage near incompatible materials. |
| Shelf Life | Typical shelf life is 12 months when stored sealed in cool, dry conditions, away from moisture, heat, and direct sunlight. |
When the 1002 sheet extrusion grade is directed into chilled ready-meal tray and lidstock conversion, the line is configured as follows: the resin and any reclaimed edge trim are dried in a desiccant dryer with a dew point of -40 °C at 70 °C for 4 h, producing residual moisture below 250 ppm before the material enters the extruder throat. Melt is processed in a 30:1 L/D single-screw extruder with a barrier screw, barrel zones of 180 °C, 195 °C, and 200 °C, and melt temperature maintained between 190 °C and 205 °C. Screen changer pressure is typically 90–140 bar; the melt passes a coat-hanger sheet die with lip gap 0.8–1.2 mm and is polished on a three-roll calendering stack at 25–40 °C. Final sheet gauge is 400–800 µm, with draw ratio held between 1.9 and 2.2 to limit orientation and maintain consistent plug forming. Edge trim is ground through a low-shear granulator and reintroduced at 20–30 wt% after drying; above 30 wt%, melt flow index increases by 0.5–1.0 g/10 min and sheet sag becomes measurable on the roll stack. Thermoforming uses heated syntactic foam plug assist with plug temperature 90–110 °C, sheet surface temperature 90–110 °C, mold temperature 30–50 °C, forming air 6–8 bar, and cycle time 2.5–4.0 s. Terminal products include lidded trays for chilled ready meals, cold dairy desserts, and prepared fruit portions. Food-contact compliance under EU Regulation (EU) No 10/2011 requires overall migration below 10 mg/dm² using EN 1186-1; industrial compostability is evaluated to EN 13432, with disintegration below 10% residue on a 2 mm sieve after 12 weeks and biodegradation at or above 90% within 180 days under controlled aerobic composting. Published data for this specific 1002 configuration is limited, but these processing windows are representative of PLA-based sheet grades in the same MFI range.
High-speed cold drink cup and portion cup lines impose a narrower thermoforming window than shallow tray lines. The PLA matrix exhibits a glass transition temperature of 55–60 °C by ISO 11357-2:2020, and the sheet is formed in its amorphous state to preserve clarity; crystallization half-time at 110 °C is sufficiently long that the sheet surface must not remain at that temperature for more than a few seconds. Virgin 1002 sheet at 300–600 µm gauge is formed with a sheet surface temperature of 85–105 °C; below 85 °C, stress whitening appears at the cup base radius and sidewall microcracks develop during rim curling. Above 105 °C, web formation and sidewall thinning become non-correctable because melt strength falls sharply. The plug, machined from syntactic foam or low-thermal-mass HDPE, is held at 80–100 °C; the female aluminum mold is controlled at 30–50 °C with 5–8 bar pre-blow and final blow air. Melt flow index is measured by ISO 1133-1:2022 at 210 °C/2.16 kg and is 2–6 g/10 min for virgin feedstock. Each 10 wt% increment of edge trim regrind raises MFI by 0.2–0.5 g/10 min and reduces sag resistance; at 30 wt% regrind, sidewall thickness distribution across a 6-point profile degrades from ±8% to ±14%. The relationship is shown below.
| Regrind loading (wt%) | Melt flow index (g/10 min, 210°C/2.16 kg) | Sheet surface forming window (°C) | Sidewall thickness variation (%) |
|---|---|---|---|
| 0 | 2.0–4.0 | 88–105 | ±6–8 |
| 20 | 2.5–4.8 | 86–103 | ±8–10 |
| 30 | 3.0–5.5 | 85–100 | ±10–14 |
| 40 | 3.5–6.5 | 83–96 | ±14–18 |
Above 30 wt% regrind, the process window narrows to ≤20 °C, and rim curl consistency falls because melt strength decreases. Ribbed sidewalls or embossed bases increase local draw and expose instabilities. Terminal products include 200 mL–500 mL cold dessert cups, portion cups, and cold drink tumblers for fill temperatures below 40 °C. Splash filling above 40 °C is outside the amorphous PLA service limit because the article softens near the glass transition. Compliance is governed by EN 13432 for compostability and EU Regulation 10/2011 for food contact; converters are advised to verify specific migration of lactic acid using EN 1186-14 and simulant B for aqueous foods. The 0 °C cold-chain lid fit should be validated on-line, because PLA dimensional change after 24 h at 4 °C can reduce lid snap retention by 2–5% when the lid is directly thermoformed from the same sheet.
For dry-goods clamshells with an integrally hinged closure, the 1002 sheet is extruded at 250–500 µm and converted on in-line thermoformers with infrared ceramic heating. Impact modification is pre-compounded at 5–15 wt% PBAT or an equivalent compostable polyester to maintain hinge fold endurance; the hinge is then scored and folded 180° for not fewer than 50 cycles at 23 °C and 50% RH. The sheet is trimmed by matched-metal cutting in the same indexing cycle, with punch-and-die clearance below 0.05 mm to avoid delamination at the hinge. Haze is measured by ASTM D1003-13 and remains below 8% on 300 µm sheet, while Gardner impact by ASTM D5420-21 exceeds 1.5 J at 23 °C. Terminal products include transparent cosmetic accessory clamshells, toy packaging, and dry electronics accessory trays. For non-food cosmetic and retail packaging, the finished article is subject to REACH Regulation (EC) No 1907/2006 for Substances of Very High Concern screening and EU Directive 94/62/EC on packaging and packaging waste; industrial compostability is verified to EN 13432. Regrind limits for transparent clamshells are lower than for opaque tray stock, typically 10–20 wt%, because above 20 wt% yellowness index by ASTM E313-20 can exceed 4 under repeated heat history from the regrind loop.
The 1002 sheet is processed into propagation trays, soil-block trays, and plant transport carriers at 350–700 µm gauge using flat-bed roll-fed thermoformers. Black or green trays are produced with 1–3 wt% compostable color masterbatch; each colorant must independently satisfy EN 13432 heavy metal limits and aerobic degradation, because the finished article is evaluated as a whole and not by base resin only. Regrind loads of 20–40 wt% are common in horticultural products because surface aesthetics are secondary; however, above 40 wt%, brittleness temperature measured by ASTM D1790-14 rises toward 5 °C, and propagation tray corner cracking increases during automated filling, stacking, and transport. The terminal products—cell trays, propagation flats, soil-block trays, and plant transport carriers—are not intended for direct soil burial. PLA blends that meet EN 13432 are industrially compostable, but the same article does not automatically meet ISO 17088 or EN 17033 for soil biodegradable mulch claims, and home compost certification is subject to a separate TÜV Austria OK compost Home or equivalent scheme. The relevant compliance matrix is shown below.
| Requirement | Standard / method | Typical pass criterion |
|---|---|---|
| Industrial compostability | EN 13432 | ≥90% biodegradation in 180 days, disintegration <10% residue on 2 mm after 12 weeks |
| Heavy metal limits | EN 13432 Annex A | Below specified mg/kg dry solids; no uncontrolled additives |
| Packaging waste recovery | EU Directive 94/62/EC | Material must not impede compost recovery stream |
| Low-temperature brittleness | ASTM D1790-14 | No fracture at 5°C under specified impact condition |
Because the sheet can be pressure formed into shallow cavities at 350–500 µm, low-moisture pharmaceutical blister trays and non-sterile medical device clamshells are converted on contact plate machines under controlled dust conditions. The sheet surface is brought to 85–100 °C by contact heating for 4–8 s; cavity depth is limited to 10–15 mm to avoid corner thinning below 60% of nominal sheet gauge. Regrind is excluded from patient-contact packaging unless a 0–10 wt% closed-loop stream is validated free of ink, adhesive, silicone, and cross-contamination. Terminal products include low-moisture nutraceutical blister trays, vial locators, and non-sterile device clamshells. Packaging validation under ISO 11607-1:2019 covers seal strength, integrity, and material compatibility; biological assessment follows ISO 10993-5:2009 and ISO 10993-10:2021 when the material is designated as a medical device packaging component. Moisture barrier is not equivalent to Aclar or PCTFE; published data for this specific PLA blend configuration is limited, so converters should measure moisture vapour transmission rate by ASTM F1249-20 before switching high-sensitivity drug formulations.
Closed-loop edge trim reclamation begins at the calendering stack, where slitting removes 10–15% of sheet width. The trim is fed through a low-shear granulator with 4–6 mm screen, passed over a magnetic separator, and dried to 250 ppm residual moisture before gravimetric feeding into the extruder throat. In-line reclaim at 20–35 wt% operates on a 25:1 L/D co-rotating twin-screw extruder with side feed; however, above 30 wt%, melt temperature heterogeneity between virgin and regrind fractions is documented by infrared barrel monitoring to exceed 3 °C, increasing gauge variation along the web. Sheet gauge variation measured by beta gauge after the roll stack should remain within ±5%; above 30 wt% regrind, variation shifts to ±7–9% unless the gravimetric system controls each component within 0.5% feed accuracy. Terminal applications are short-run specialty lids, display trays, and non-food insert trays. Industrial compostability is retained only when the reclaimed material has not been contaminated with pressure-sensitive adhesive labels or crosslinked polymers; quality control should include FTIR spectra screening according to ASTM E1252-98(2021) and melt flow testing by ISO 1133-1:2022. The 1002 grade, when run with this reclaim setup, should not be diverted to food-contact sheet unless the converter verifies that all reclaimed material originates from the same food-contact-grade production and is subject to the same EU Regulation 10/2011 compliance records.
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Compostable 1002 Sheet Extrusion Compostable PLA Blend is a compounded polylactide-based thermoplastic supplied as cylindrical pellets for flat-die sheet extrusion and inline thermoforming. The product designation 1002 identifies a melt-strengthened sheet grade containing a renewable impact-modifier package and an inorganic nucleating system. The compound is intended for rigid compostable packaging, food-service trays, clamshell containers, and thin-walled inserts where EN 13432:2000 or ASTM D6400 certification may be required. On production lines equipped with a 45 mm single-screw extruder having an L/D ratio of 30:1 to 36:1 and a 600 mm coat-hanger die, the material is typically processed at a melt temperature of 195–205°C and a die set point of 200–210°C. A desiccant drying step is mandatory before extrusion: residual moisture is reduced to ≤250 mg/kg as measured by ISO 15512:2019; drying for 4–6 h at 80±5°C with a supply-air dew point of −40°C is the standard set-up. Because melt viscosity changes sharply with temperature, the die-temperature band should be controlled within ±5°C to avoid sheet-width variation and edge tear. The compound is not a drop-in replacement for HIPS or APET in every tool; it is intended for converters requiring a certified compostable sheet resin with higher melt strength than unmodified PLA. Published data for this specific 1002 configuration is limited in peer-reviewed form; the values that follow are typical ranges for melt-strengthened PLA sheet compounds and should be confirmed against lot-specific certificates of analysis.
Unlike unmodified polylactide, the 1002 grade incorporates a chain-extension architecture that stabilizes extensional viscosity during draw-down from a flat die. In practical terms, edge-bead formation and roll-stack transfer are improved; reported neck-in values for melt-strengthened PLA compounds in this class are 8–14 mm per side on a 600 mm die at 0.35 mm target sheet, whereas unmodified PLA can exhibit 18–25 mm per side under the same die configuration. The nucleating system also accelerates crystallization, permitting faster quenching on a vertical three-roll stack: roll temperatures of 25–40°C produce amorphous clarity, while 45–60°C favor higher thermal resistance at the expense of haze. These processing differences are not universal properties of all PLA blends and must be re-established on the target die because die-gap, lip-land length, and draw-down rate dominate edge-bead response.
| Property | Test method | Compostable 1002 PLA blend | Unmodified PLA sheet grade | HIPS sheet grade |
|---|---|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022, 210°C/2.16 kg | 3–6 g/10 min | 5–10 g/10 min | 2–4 g/10 min (200°C/5.00 kg) |
| Density | ISO 1183-1:2019 | 1.24–1.27 g/cm³ | 1.24–1.26 g/cm³ | 1.03–1.05 g/cm³ |
| Tensile yield strength | ISO 527-2:2012 | 45–55 MPa | 52–65 MPa | 20–32 MPa |
| Tensile modulus | ISO 527-2:2012 | 3.0–3.5 GPa | 3.2–3.8 GPa | 1.8–2.4 GPa |
| Notched Izod impact strength, 23°C | ISO 180/A | 4–7 kJ/m² | 2–4 kJ/m² | 8–14 kJ/m² |
| Heat deflection temperature, 1.8 MPa | ISO 75-2:2013 | 50–60°C | 50–55°C | 75–85°C |
These comparative data illustrate the structural difference: the 1002 grade retains the tensile modulus advantage of PLA, but its impact strength sits between unmodified PLA and HIPS. Heat deflection is the primary restriction. The improvement in notched Izod impact over unmodified PLA is attributable to the renewable impact-modifier phase, which must be dispersed in the twin-screw compounding step; poor dispersion produces surface pits and a loss of clarity in 0.25–0.50 mm sheet. A separate drying and compounding operation is therefore critical to lot-to-lot consistency. Property values are typical ranges only and do not represent guaranteed lot-certified specifications.
At melt temperatures above 210°C in the screw tip or die, PLA undergoes β-scission and intramolecular transesterification; lactide generation appears as acrid emissions, screw deposit formation, and loss of melt strength. Below 180°C, the nucleated compound may not fully plastinate, producing micro-gels and surface pits in 0.3 mm sheet. The recommended melt-temperature set points are therefore 190–205°C at the metering zone and 200–210°C at the die. Because the melt mass-flow rate changes by approximately 7–12% for every 5°C shift in melt temperature, sheet gauge uniformity degrades rapidly outside the ±5°C control band.
Moisture is an equally critical boundary condition. PLA is hydrolytically sensitive at processing temperatures; residual moisture above 250 mg/kg causes molecular weight reduction, a drop in melt viscosity, edge tear, and lamination defects. Compostable 1002 should be dried in a desiccant hopper dryer with a supply-air dew point of −40°C or lower. At ambient relative humidity above 60%, the recommended drying duration is extended from 4 h to 6–8 h because pellet moisture uptake during storage can exceed 500 mg/kg within 24 h. Inline moisture verification using ISO 15512:2019 is recommended for lot release. Regrind addition is permitted only when flake moisture is similarly controlled and the flake bulk density is above 0.45 g/cm³. Processors should limit regrind to 20–30 wt%; above this level, batch-to-batch MFR drift and notched impact loss have been observed on production lines. The compound should not be blended with amine-containing additives or masterbatches unless explicitly approved, because amine species can accelerate ester cleavage and negate the chain-extension architecture.
For compostability certification, the 1002 grade is intended to satisfy industrial composting requirements under EN 13432:2000 and ASTM D6400. Certification is a system-level assessment requiring the final article, print, adhesive, and gauge to be included. Under EN 13432:2000, the material must demonstrate ≥90% aerobic biodegradation within 180 days relative to a positive control when tested according to ISO 14855-1:2012; disintegration must exceed 90% in a controlled composting pilot after 12 weeks; and the resulting compost must pass an ecotoxicity test, typically OECD 208. 1002 without printing or lamination generally satisfies the chemical characterization requirements of clause 4.2 of EN 13432:2000, but complete certification must be confirmed on the final article because gauge and surface area affect disintegration kinetics. Food-contact suitability requires article-specific migration testing under EU (EU) No 10/2011; overall migration must be ≤10 mg/dm² in the appropriate food simulant, and specific migration of lactic acid and oligomeric species should be assessed. In the United States, compliance with 21 CFR 175.300 is not a blanket approval for all PLA compounds; individual components must be cleared for the intended condition of use.
| Standard/Regulation | Scope | Clause or test designation | Position for 1002 |
|---|---|---|---|
| EN 13432:2000 | Industrial compostability of packaging | Clause 4.2; Annex A; OECD 208 | Designed to comply; final-article certification required |
| ISO 14855-1:2012 | Aerobic biodegradation of plastics | ≥90% in 180 d | Typical melt-strengthened PLA blends meet; 1002 lot certification must be confirmed |
| ASTM D6400 | Compostable plastics specification | ASTM D5338-15; disintegration; ecotoxicity | Intended for certification; final article governs |
| EU (EU) No 10/2011 | Plastic food-contact materials | Overall migration <10 mg/dm²; specific migration limits | Requires article-specific migration testing |
| 21 CFR 175.300 | Resinous and polymeric coatings | Food-contact substance status | Subject to component inventory and conditions of use |
| ISO 15512:2019 | Moisture content | ≤250 mg/kg before processing | Mandatory in-process verification |
When a converter substitutes 1002 for HIPS on an existing thermoforming line, the conversion to a compostable PLA compound is accompanied by lower thermal resistance and a different brittle-failure mode. The tensile modulus of 1002 is approximately 30–60% higher than HIPS, permitting down-gauging in some rigid tray designs; however, the heat deflection temperature at 1.8 MPa is 50–60°C, whereas HIPS typically ranges from 75–85°C. 1002 is therefore not suitable for hot-fill applications above 60°C or for microwave reheating unless the package is vented and the food load remains below 55°C. The notched Izod impact strength of 1002 is lower than HIPS, so sidewall radii and corner geometries must be redesigned to avoid brittle fracture during trimming. On the other hand, 1002 has a density of 1.24–1.27 g/cm³, increasing part weight relative to HIPS by approximately 20% for the same gauge. This mass increase may be offset by using 10–15% thinner sheet in low-load lids; however, such down-gauging requires a thermoforming mold with tighter plug-assist tolerances because the sheet’s hot-tensile strength below 80°C is less forgiving. When compared with APET, 1002 has lower clarity and different gas-barrier behavior. Published data for 1002-specific oxygen and water-vapour transmission is limited; the barrier performance must be generated on the final article using ISO 15105-2 or ASTM D3985 for oxygen and ISO 15106-1 or ASTM E96 for water vapour. In general, PLA sheet has lower oxygen permeability than HIPS and higher water-vapour permeability than APET, so the package design must account for moisture gain or loss in the product life cycle.
Edge tear, die-lip deposit, and gauge bands on a production-scale sheet line are usually attributable to one of three causes: moisture above 250 mg/kg, die-temperature drift beyond ±5°C, or regrind content above 30 wt%. In a documented thermoforming qualification, a 0.35 mm black food-service tray was produced on a 700 kg/h sheet line using a 120 mm single-screw extruder and a 1,200 mm flat die; the acceptable operating envelope was maintained only when the melt temperature was kept between 195°C and 205°C and the polish-stack roll gaps were set to a nip pressure of 40–50 N/mm. At 215°C, the sheet exhibited lactide odor and a 9% loss of notched Izod impact. At 185°C, surface haze increased from 7% to 14% per ASTM D1003-13. These observations are line-specific and are reported as industrial experience rather than as product specifications. The compound should be qualified on the target line with the intended regrind ratio, die configuration, and final article thickness; no universal processing condition should be assumed.