| HS Code | 881676 |
| Product Name | Natureplast PLRE 002 Recycled Transparent Compostable Polylactic Acid |
| Grade | PLRE 002 |
| Material Type | Recycled polylactic acid (PLA) |
| Recycled Content | Post-industrial recycled PLA |
| Appearance | Transparent pellets |
| Transparency | Transparent |
| Compostability | Industrially compostable according to EN 13432 |
| Biodegradability | Biodegradable |
| Density | Approx. 1.24 g/cm³ |
| Melt Flow Index | Approx. 10-20 g/10 min at 190°C/2.16 kg |
| Melting Temperature | Approx. 145-155°C |
| Glass Transition Temperature | Approx. 55-60°C |
| Tensile Strength | Approx. 50-60 MPa |
| Tensile Modulus | Approx. 3500 MPa |
| Elongation At Break | Approx. 4-6% |
| Flexural Modulus | Approx. 3500 MPa |
| Charpy Notched Impact Strength | Approx. 3 kJ/m² |
| Heat Deflection Temperature | Approx. 55°C at 0.45 MPa |
| Vicat Softening Temperature | Approx. 60°C |
| Processing Method | Injection molding, extrusion |
| Food Contact | Suitable for food contact |
| Packaging | 25 kg bags |
| Storage Conditions | Dry, cool, away from moisture |
As an accredited Natureplast PLRE 002 Recycled Transparent Compostable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Natureplast PLRE 002 recycled transparent compostable polylactic acid is supplied in 25 kg sealed moisture-barrier bags for safe storage and transport. |
| Container Loading (20′ FCL) | 20′ FCL loading of Natureplast PLRE 002 Recycled Transparent Compostable Polylactic Acid: palletized, moisture-protected, securely stowed, dry container, compliant transport. |
| Shipping | Natureplast PLRE 002 Recycled Transparent Compostable Polylactic Acid ships as a non-hazardous, non-DG solid in moisture-barrier bags, drums, or octabins. Keep dry, cool, away from heat, ignition, and direct sunlight. No UN number typically required; follow local transport regulations and handle as an industrial raw material. |
| Storage | Store Natureplast PLRE 002 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep containers tightly sealed and palletized off the floor. Recommended conditions: 10–30°C and low humidity. Avoid prolonged exposure to strong acids, bases, and oxidizers. Maintain good housekeeping; rotate stock using first-in, first-out to preserve compostability and transparency. Protect from UV light. |
| Shelf Life | Recommended shelf life is 12 months when stored unopened in original packaging, cool, dry, away from moisture, heat, and direct sunlight. |
Thermoformed transparent produce and deli containers represent the highest-volume single-stream downstream for Natureplast PLRE 002 when the recycled flake originates from post-industrial PLA trim. Regrind ratios of 20–30 wt% can be incorporated into virgin PLA without measurable opacity increase if the recycled fraction is pre-dried to below 250 ppm moisture using a desiccant dryer with a -40 °C dew point. Drying at 70–80 °C for 4–6 h is required because residual moisture above 250 ppm accelerates hydrolysis at melt temperatures above 190 °C, producing sheet-edge brittleness and microgels that degrade optical clarity. Sheet extrusion is run on a single-screw extruder with L/D 30:1 to 36:1, a barrier screw with compression ratio 2.5:1 to 3.0:1, barrel zones set at 170–185–195–205–200 °C, melt pump inlet pressure 60–120 bar, and polished chrome chill rolls held at 25–40 °C to maintain surface smoothness. Thermoforming uses plug-assisted negative tooling at sheet surface temperatures of 85–110 °C and mold temperatures of 30–60 °C to produce wall thicknesses of 0.20–0.45 mm. Food-contact compliance is assessed under EU Regulation 10/2011 overall migration limits of 10 mg/dm² and under EN 13432 for organic recovery; US food-contact status requires supplier substance-level documentation under 21 CFR Part 174 components and applicable Food Contact Notifications. Terminal articles are transparent hinged trays, deli cups, and vented berry punnets.
Injection moulding of single-use cutlery from PLRE 002 shifts the critical control point from drying to thick-wall cooling because the recycled fraction lowers melt strength at thin-wall fork tines below production thresholds when the part thickness drops under 1.2 mm. Single-stream use at 100 wt% is viable on 80–120 t hydraulic or servo-driven machines for spoon and knife geometries with wall stock 2.0–3.5 mm; for fork tines and coffee stirrers with wall stock 0.8–1.5 mm, up to 5–10 wt% of a compostable impact-modifier masterbatch is added to reduce notch sensitivity. The barrel profile is set at 180–190–200–210–205 °C, nozzle at 190–205 °C, and mold surface at 20–50 °C; hold pressure is maintained at 60–100 MPa for 8–15 s per 2 mm wall section. Screw back-pressure below 3 MPa is used to avoid frictional heat rise above 230 °C, where lactide reformation accelerates and increases flash. Incoming lot verification includes melt flow rate per ISO 1133-1:2022 at 210 °C/2.16 kg and moisture per ISO 15512 method E before release. Mold layout engineering assumes linear shrinkage of 0.2–0.4 % and post-mould crystallinity development over 24 h; parts ejected at above 55 °C surface temperature exhibit warping in the handle and splay along the tine weld line. Compliance for compostable serviceware is assessed under EN 13432, with disintegration below 12 weeks and biodegradation of 90 % within 180 days at 58 ± 2 °C; food-contact status follows EU Regulation 10/2011 and relevant 21 CFR substance clearances for the specific additive package. Terminal products are spoons, forks, knives, and hot-drink stirrers intended for closed-loop organics collection.
| Conversion route | Pre-extrusion moisture target | Melt or die temperature | Critical downstream variable |
|---|---|---|---|
| Thermoforming sheet | < 250 ppm | 185–205 °C | Sheet surface 85–110 °C at plug assist |
| Injection moulding | < 250 ppm | 190–210 °C barrel; nozzle 190–205 °C | Hold pressure 60–100 MPa |
| Extrusion coating | < 200 ppm | 200–220 °C die lip | Neck-in ≤ 30 mm; air gap 150–250 mm |
| Filament extrusion | < 200 ppm | 160–185 °C barrel | Diameter 1.75 ± 0.05 mm at laser gauge |
| Blown film | < 250 ppm | 180–200 °C die | BUR 2:1–2.5:1; frost line 100–250 mm |
For cold beverage cup sidewalls and foodservice wrap, PLRE 002 functions as a seal-enabling transparent barrier layer introduced after board corona treatment, not as a bulk laminated film. Grade-specific published data for PLRE 002 in extrusion coating is limited; the coating-weight and air-gap parameters below are benchmarked against PLA coating envelopes and must be confirmed on the target board grade. Coating weight is controlled at 15–25 g/m² per side through a 90 mm single-screw extruder with L/D 30:1 and a flat die with die width matched to 250–300 mm web contact. The die lip temperature is held at 200–220 °C, while the extruder barrel remains at 180–190–200–210–210 °C; the polymer is drawn through an air gap of 150–250 mm at a draw ratio of 7:1 to 10:1 onto board preheated to 30–60 °C. Corona treatment of the paperboard to 38–42 mN/m surface energy is necessary because PLA does not wet lignocellulosic fibre without polar activation. The main production failure is neck-in exceeding 30 mm at the die ends, which creates uncoated edges and downstream sealing failure; increasing melt temperature above 220 °C reduces neck-in but raises the concentration of low-molecular-weight lactide at the surface. Heat-seal initiation is tested per ASTM F2029-16 and must fall between 100–120 °C with dwell times of 0.5–1.0 s on cup-forming side-seam lines. Compliance is assessed under EU Regulation 10/2011 for total migration below 10 mg/dm², and 21 CFR 175.300 for resinous and polymeric coatings in US food-contact use. Terminal articles include coffee cup blanks, ice cream tub sidewalls, and sandwich wedge wraps with compostability demonstrated to EN 13432 when the entire laminate is free of non-compostable coatings.
When the melt is passed through a 40 µm screen pack and a gear pump before the die, monofilament for fused filament fabrication can be produced from 100 wt% PLRE 002 on a 25 mm single-screw extruder with L/D 24:1; without melt filtration, lot-to-lot contaminants are visible as diameter spikes at the laser gauge. The extruder barrel operates at 160–175–180–185 °C, the melt pump inlet pressure is maintained at 40–80 bar, and the strand is quenched in a 40–60 °C water bath before entering a dual-axis laser micrometer. Dimensional tolerance is held at 1.75 ± 0.05 mm in accordance with ASTM F2924-14, and spooling tension is kept below 0.5 N to avoid core-set ovality above 0.03 mm. Drying before extrusion at 70–80 °C for 4 h to below 200 ppm moisture is mandatory; spooled filament at 50 % RH requires sealed desiccant packaging within 48 h because surface hydrolysis during printing causes nozzle volatiles and diameter swell. Printed parts are produced at nozzle temperatures of 195–215 °C and bed temperatures of 25–60 °C; bed adhesion is adequate on untreated glass at 60 °C, but at ambient bed temperatures below 40 °C, a removable starch-based adhesive is required. Compliance for filament covers REACH and RoHS Directive 2011/65/EU; food-contact claims are not transferred to printed articles unless the finished part is submitted to migration testing. Terminal products are spooled 1.75 mm filament for desktop material-extrusion machines used in short-run packaging prototypes and educational tooling.
In tamper-evident shrink sleeve conversion, PLRE 002 is processed as a cast-film precursor that is subsequently oriented in the transverse direction, because the recycled fraction reduces longitudinal tear resistance below acceptable limits for full biaxial orientation. Grade-specific published data for this recycled PLA in shrink sleeves is limited; the processing window below is derived from virgin PLA orientation behaviour and must be verified by DSC at 10 °C/min per ISO 11357-1 before production. A cast film of 40–60 µm is first extruded at 190–210 °C through a flat die, then stretched transversely at 70–90 °C to a draw ratio of 4:1 to 5:1. The orientation line is configured with a tenter frame and a relaxation zone of 3–5 % to control shrinkage memory; films then exhibit 40–60 % shrinkage in 80–95 °C steam tunnels. To maintain film roll stability, 15–30 wt% virgin PLA is commonly blended with PLRE 002 because the recycled fraction has a wider melt flow distribution and generates more unpigmented gel specks, which become visible under shrink after sleeve application. If post-consumer feedstock is used for sleeves placed on food packages, compliance is controlled under Regulation (EU) 2022/1616 for recycled plastic food-contact materials, unless a functional barrier is demonstrated; EN 13432 covers compostability. Terminal products are 45 µm tamper-evident sleeves for short-neck beverage bottles and multipack collation film where the sleeve remains a separate stream in organics recycling.
| Downstream article | Primary standard or regulation | Measured parameter | Terminal limit |
|---|---|---|---|
| Thermoformed trays and cups | EU Regulation 10/2011 | Overall migration | < 10 mg/dm² |
| Compostable serviceware and bags | EN 13432 | Disintegration | < 12 weeks |
| Compostable articles | EN 13432 | Biodegradation | ≥ 90 % in 180 days |
| Extrusion-coated paperboard | 21 CFR 175.300 | Resinous and polymeric coatings | Per 175.300 |
| Filament | ASTM F2924-14 | Diameter tolerance | 1.75 ± 0.05 mm |
| Recycled plastic shrink sleeves | Regulation (EU) 2022/1616 | Post-consumer feedstock control | Per 2022/1616 risk assessment |
Blown film conversion of PLRE 002 without a flexibilizer is limited to thin-gauge applications where a high-durability transparent bag is not required, because PLA melt strength at the frost line cannot support bubble diameter fluctuations above 2.5:1 blow-up ratio on conventional single-lip air rings. A 40 mm die with 1.2 mm annular gap is run at 180–200 °C die temperature, with extruder zones set at 170–180–190–195 °C and a barrier screw of L/D 30:1. Blending 20–40 wt% PBAT or a compostable copolyester flexibilizer raises the melt strength and reduces film brittleness; below 20 wt% flexibilizer, bubble tear occurs at the frost line when ambient relative humidity exceeds 60 %. The frost line height is held at 100–250 mm to allow sufficient crystallization before collapsing; the resulting film thickness is 20–40 µm. The main production bottleneck is batch-to-batch viscosity variation from recycled feedstock, which shifts the frost line height and requires closed-loop bubble diameter control; melt flow rate is verified per ISO 1133-1:2022 at 210 °C/2.16 kg. Compliance for compostable fruit and vegetable bags is set under EN 13432, with disintegration 12 weeks and biodegradation 90 % at 58 °C; if the bags contact food, EU Regulation 10/2011 and relevant national measures apply. Terminal products are transparent compostable produce bags, bread bags, and lightweight retail checkout bags for municipal organics collection.
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Natureplast PLRE 002 is supplied as a recycled transparent polylactic acid grade intended for rigid packaging, thermoformed trays, clear lids, and consumer serviceware where industrial compostability is required. The designation PLRE 002 places the material in the supplier’s recycled PLA range; it is delivered in pellet form and is formulated to retain visible-light transmission while incorporating post-industrial or post-consumer PLA feedstock. Because the recycled fraction can include scrap from extrusion trims, thermoforming skeletons, and sorted post-consumer articles, the product is specified less as a single fixed formulation than as a controlled recyclate stream with defined melt flow and optical limits. Class-typical data for transparent recycled PLA of this type include a density of 1.22–1.26 g/cm³ under ISO 1183-1:2019, a melt flow index of 2–8 g/10 min at 210 °C and 2.16 kg under ISO 1133-1:2022, and tensile modulus in the range of 3,000–3,500 MPa under ISO 527-2:2012. These values are class-typical, not a certificate of analysis for a specific lot. The material can be processed on conventional PLA extrusion, injection molding, and thermoforming equipment, but the recycled origin imposes stricter incoming quality control and drying protocols than are required for virgin PLA.
Pre-drying is mandatory before melt processing because PLA undergoes hydrolysis at melt temperatures when moisture exceeds 250 ppm. A desiccant dryer with a dew point of ≤ -40 °C is specified; drying at 80 °C for 4 h is typical for virgin PLA, but recycled lots exposed to ambient air at relative humidity above 60 % may require 6 h to reach the same moisture ceiling. Moisture content should be verified by Karl Fischer titration under ISO 15512:2019, not by weight loss alone. On a 30:1 L/D single-screw extruder or a 36:1 L/D co-rotating twin-screw extruder, the melt temperature should be held between 190 °C and 210 °C. The processing window is narrow: melt-temperature excursions above 220 °C for more than several minutes can produce measurable loss of molecular weight and a 20–50 % increase in melt flow index after a single additional thermal cycle when moisture control fails. Residence time above 200 °C should therefore be kept below 30 min. Lot-to-lot MFR variation in recycled PLA is wider than in virgin PLA; incoming QC should include melt flow testing under ISO 1133-1:2022 before setting extruder screw speed and barrel profile. In recycled PLA extrusion, a 200-mesh screen pack is often installed upstream of the die to remove particulate contamination; increasing screen pack pressure is an early indicator of feedstock contamination or gel build-up. Injection molding is carried out with barrel temperatures of 190–210 °C and a mold temperature of 20–30 °C when amorphous transparency is required. Mold temperatures above 60 °C promote crystallization and increase haze, although they can improve heat resistance in technical parts. Thermoforming sheet produced from PLRE 002 is typically heated to 90–110 °C surface temperature before forming; uneven sheet temperature produces wall-thickness variation and localized haze. The grade should not be compounded with strongly alkaline or amine-based additives because these catalyze PLA chain scission and raise melt flow rate during compounding or downstream processing.
Because recycled transparent PLA grades retain the rigid amorphous character of virgin PLA, tensile modulus and strength are governed primarily by molecular weight retention, moisture history, and contamination level. Representative ranges for rigid transparent recycled PLA of this class are shown in the table below. These ranges should be confirmed with lot-specific data from the supplier before setting article test plans or mold design assumptions.
| Property | Test method | Representative range for recycled transparent PLA class |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.22–1.26 g/cm³ |
| Melt flow index | ISO 1133-1:2022 (210 °C, 2.16 kg) | 2–8 g/10 min |
| Tensile strength | ISO 527-2:2012 | 45–60 MPa |
| Tensile modulus | ISO 527-2:2012 | 3,000–3,500 MPa |
| Elongation at break | ISO 527-2:2012 | 2–6 % |
| Charpy notched impact strength | ISO 179-1:2010 | 1.5–4.0 kJ/m² |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2013 | 50–60 °C |
| Light transmittance, 2 mm plaque | ISO 13468-1:2019 | 85–90 % |
| Haze, 2 mm plaque | ISO 14782:1999 | 5–20 % |
The haze range reflects feedstock quality. Post-industrial scrap can produce haze values near 5 %, whereas post-consumer flake with residual ink, label adhesive, or thermal history can push haze toward 20 %. Tensile elongation at break below 3 % indicates excessive molecular weight loss; lots with MFR above 8 g/10 min may fail to maintain die-melt strength during sheet extrusion and may suffer torn trim edges or sagging across the die. Light transmittance of 85–90 % at 2 mm is sufficient for many clear packaging applications, but it is lower than the 90–95 % transmittance typical of virgin PLA; crystal nucleation from residual additives or contamination further reduces transparency. These results are sensitive to plaque preparation conditions under ISO 293:2004; visual inspection should be performed against a sealed reference plaque because surface scratches and flow marks can be misread as optical property failures.
Certification of PLRE 002 under EN 13432:2000 or ASTM D6400-23 does not automatically confer food-contact approval. Industrial compostability requires ≥ 90 % biodegradation within 180 days under 58 ± 2 °C aerobic composting conditions, disintegration of the final article within 12 weeks, and absence of negative effects on compost quality and plant germination. The organic recovery claim applies to industrial composting facilities only; the material should not be described as home compostable unless the supplier provides a specific certification such as TÜV Austria OK compost Home or NFT 51-800 compliance. For food-contact applications, the finished article must be evaluated under EU Regulation 10/2011 or US FDA 21 CFR conditions of use; recycled feedstock can introduce non-intentionally added substances that require migration testing under EN 1186-1:2002 and EN 13130-1:2004. Where articles are exported, REACH and RoHS compliance must be verified against the specific lot and supplier safety data sheet. Published data for this specific recycled configuration’s food-contact status is limited; a migration test plan is therefore recommended before commercial use. This compliance boundary distinguishes PLRE 002 from some virgin PLA grades that carry clearer food-contact documentation. In addition, the industrial compostability certificate does not imply aerobic or anaerobic degradation in marine, freshwater, or soil environments unless separate testing under ISO 17556:2019, ISO 14851:2019, or equivalent has been performed.
Substitution of virgin PLA with PLRE 002 in clear serviceware and packaging reduces virgin polymer demand but changes optical, mechanical, and processing trade-offs. Compared with virgin PLA, the recycled grade may exhibit a 10–20 % reduction in tensile strength and a 5–15 % increase in haze, depending on feedstock quality and extrusion history. This does not necessarily disqualify the material from packaging use, but it requires wider incoming QC limits and may require higher wall thickness to compensate for reduced tensile elongation. Compared with recycled poly(ethylene terephthalate) (rPET), PLRE 002 is industrially compostable under EN 13432:2000, whereas rPET is not. However, rPET offers higher heat deflection temperature, typically 70–85 °C at 0.45 MPa, and lower oxygen transmission. PLA articles soften near 55–60 °C and are unsuitable for hot-fill above 60 °C unless they are crystallized, which reduces transparency. Compared with PBAT or PBS biodegradable polyesters, PLRE 002 is stiff: tensile modulus is approximately 3,000–3,500 MPa, whereas PBAT grades often fall below 100 MPa with elongation at break above 400 %. PLRE 002 is therefore selected for rigid transparent applications, not flexible film. Within the recycled PLA range, transparent grades such as PLRE 002 differ from opaque recyclates because they require a cleaner feedstock; black or colored pellets, metal fragments, and crosslinked gel particles are more apparent in the final article. This feedstock constraint raises cost and sorting complexity but enables use in see-through lids, trays, and blister packs. Operators replacing virgin PLA with PLRE 002 may need to reduce the draw ratio in sheet extrusion or increase melt temperature by 5–10 °C within the 190–210 °C band to compensate for lower melt strength.
Moisture uptake follows Fickian diffusion kinetics in PLA; pellets stored in opened bags at 23 °C and 50 % RH can reach moisture levels above 250 ppm within 24–48 h. At 80 % RH, the time to reach this limit shortens substantially, and drying before processing becomes non-negotiable. Unopened bags should be stored below 30 °C and protected from direct UV exposure. Under those conditions, PLA recyclates generally retain processability for 12 months; however, the recycled fraction may exhibit greater acid number and lower thermal stability than virgin PLA after prolonged storage. Incoming QC should include moisture by ISO 15512:2019, melt flow index by ISO 1133-1:2022, and visual haze on a 2 mm compression-molded plaque under ISO 293:2004. Lot acceptance limits should be based on the supplier’s certificate of analysis and internal process capability. Where MFR exceeds the upper control limit, the lot may be restricted to lower-shear extrusion applications rather than injection molding. Conversely, lots with MFR at the low end may require a 5–10 °C increase in melt temperature, within the 190–210 °C band, to achieve adequate fill. Recycled feedstock variability means that a single set of processing parameters cannot be assumed stable across all production campaigns; process adjustments should be driven by measured melt viscosity and not solely by barrel set points. Blending of multiple recycled lots may be necessary to stabilize melt flow and color; however, blending should be performed before drying and with documented lot traceability to maintain compliance with organic recovery certifications.