| HS Code | 340245 |
| Material Type | Polylactic Acid (PLA) |
| Flexibility | Flexible |
| Heat Resistance | Heat resistant |
| Microwavability | Microwavable |
| Density | 1.24-1.30 g/cm³ |
| Melt Flow Rate | Approximately 10 g/10 min at 190°C/2.16 kg |
| Tensile Strength | 30-40 MPa |
| Elongation At Break | 150-200% |
| Flexural Modulus | 1.2-1.8 GPa |
| Notched Izod Impact Strength | 10-20 kJ/m² |
| Heat Deflection Temperature | 90-100°C |
| Vicat Softening Temperature | 115-125°C |
| Melting Temperature | 150-160°C |
| Glass Transition Temperature | 55-60°C |
| Biobased Content | Greater than 90% |
| Compostability | Compostable according to EN 13432 |
| Food Contact | Suitable for food contact |
| Processing Methods | Injection molding, extrusion, thermoforming |
| Form | Pellets |
| Color | Natural/White |
As an accredited ECOPLAN -DURA EN100 Flexible Heat Resistant Microwavable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | ECOPLAN -DURA EN100 is supplied in 25 kg moisture-barrier paper sacks, palletized and stretch-wrapped for flexible, heat-resistant, microwavable polylactic acid. |
| Container Loading (20′ FCL) | Container Loading: ECOPLAN-DURA EN100 flexible heat-resistant microwavable polylactic acid, palletized, secured in a 20′ FCL container for safe transport. |
| Shipping | ECOPLAN-DURA EN100 Flexible Heat Resistant Microwavable Polylactic Acid is a non-hazardous, non-regulated solid polymer. It is supplied in moisture-barrier bags, drums, or octabins. Keep dry, cool, and out of direct sunlight. No UN number, hazard class, or special transport labeling required. |
| Storage | Store ECOPLAN -DURA EN100 in a cool, dry, well-ventilated area, ideally below 25 °C and under 50% relative humidity. Keep sealed in original packaging, away from direct sunlight, heat, moisture, and ignition sources. Avoid contact with strong oxidizers. Use first-in, first-out stock rotation. Minimize open exposure to prevent moisture uptake, which can affect processing performance. |
| Shelf Life | Shelf life is typically 12 months when stored unopened in a cool, dry place, away from moisture, heat, and direct sunlight. |
In ready-meal tray converting, ECOPLAN -DURA EN100 enters the line as a compounded PLA grade that must be dried below 250 ppm residual moisture before any heat exposure above 170 °C begins. On a single-screw sheet extrusion line with a barrier screw of 36:1 L/D and a grooved feed section, a desiccant dryer with a dew point of -40 °C or lower is used for 4–6 h at 70–80 °C, and residual moisture is confirmed by Karl Fischer titration according to ISO 15512:2019. In plants where ambient relative humidity exceeds 60%, opened bulk bags should be returned to conditioned storage within 2 h or transferred to a hopper loader with dry-air purge. The barrel profile rises from 170 °C at the feed throat to 205 °C at the adapter, while the melt temperature is maintained between 190 °C and 210 °C. Melt temperatures above 220 °C are linked to hydrolytic chain scission, lactide regrowth, yellowing, and loss of melt elasticity; melt temperatures below 185 °C produce unmelts, flow lines, and localised thickness variation. The sheet die uses a choker bar and a lip gap of 0.3–0.6 mm, and the polishing roll stack is held at 40–60 °C to retain an amorphous sheet with controlled frozen-in stress. Edge nicks, melt surging, and viscosity drift in the feed block are the earliest line-side indicators of insufficient drying or excessive residence time.
Thermoforming of the amorphous sheet is carried out at a sheet surface temperature of 95–110 °C, measured by infrared pyrometer, before plug-assisted forming into a heated mould at 95–105 °C. The mould-hold time is the throughput-limiting variable because the compound must undergo cold crystallisation while the part is restrained; at wall thicknesses of 0.8–1.5 mm, a cavity hold time of 15–30 s is generally required, but this range must be re-established after every revision of sheet gauge or nucleating additive lot. If the part is ejected too early, the tray rim shows dimensional recovery and dome collapse during microwave reheating at 100–110 °C; if the hold time is too long, corner cracking and brittleness appear after cooling. Heat deflection temperature is verified on crystallised tray sections according to ASTM D648-18 Method B at 0.45 MPa, and a target of no less than 90 °C is typically required for ready-meal trays that are filled at 80 °C and reheated in an 800 W microwave. For microwave performance, a finished-article test is run with distilled water or a starch-water simulant for 5 min at 800 W, after which rim deformation and base warp are recorded; published data for this specific configuration is limited, so the converter evaluates crystallised-wall fraction by differential scanning calorimetry according to ISO 11357-3:2018. Food-contact suitability for the finished tray is not assigned by the polymer supplier alone; the tray is tested for overall migration into aqueous and fatty food simulants under Regulation (EU) No 10/2011 using EN 1186-1:2002 and specific migration methods in EN 13130-1:2004. In the United States, the converter confirms the additive and colourant package against the applicable Food Contact Notification in the FDA FCN database because 21 CFR 177.1520 does not cover PLA, and residual monomer content must remain below the applicable specific migration limit before commercial release.
| Converting route | Drying limit | Melt temperature | Tool/roll condition | Primary failure signal |
|---|---|---|---|---|
| Thermoformed sheet | 250 ppm maximum | 190–210 °C | roll stack 40–60 °C | surging and edge nicks |
| Injection moulding | 250 ppm maximum | 190–205 °C | mould 85–105 °C | sticking or incomplete crystallinity |
| Cast film | 250 ppm maximum | 185–210 °C | chill roll 15–25 °C | seal initiation drift and pinholes |
| Extrusion coating | 250 ppm maximum | 200–220 °C | chill roll 15–25 °C | pinholes and adhesion loss |
Because the flexible heat-resistant formulation contains a biodegradable copolymer modifier, the crystallisation kinetics in injection-moulded bowls are slower than those of nucleated rigid PLA; the tool must therefore be operated above the amorphous-phase glass transition for the entire cavity residence. The melt is delivered through hot runner drops and valve gates at 190–205 °C, and pack pressure is set between 600 bar and 900 bar, with holding time adjusted from 8 s to 15 s depending on wall thickness and gate size. The mould is maintained at 85–105 °C using oil or pressurised-water tempering, not plain tower water, and temperature tolerances of ±2 °C across the mould halves are required. Cavity-to-cavity variation above 3 °C produces non-uniform shrinkage and rim ovality after conditioning. At mould temperatures below 80 °C, the skin freezes before cold crystallisation reaches the core, leaving a low-crystallinity layer that softens during microwave reheating. At mould temperatures above 110 °C, ejection is compromised because the flexible compound has reduced hot modulus; the bowl rim may tear at the stripper ring or stick on the core. Clamp force is calculated from projected area and a cavity pressure limit of 300–500 bar rather than from shot weight alone, and insufficient clamp force is detected as flash at the parting line and gate blush around the hot sprue.
When annealing is used to raise heat deflection temperature, bowls are placed on restraining plug fixtures in a forced-air oven at 80 °C for 30–60 min and cooled slowly; free-standing annealing without restraint causes uneven radial shrinkage. Shrinkage is determined after 48 h at 23 °C and 50% RH according to ISO 294-4:2018, and the measurement is taken on the bowl rim, sidewall, and base because flow orientation creates anisotropic shrinkage. The finished bowl is tested for microwave resistance by heating with water at 100 °C for 5 min; lid fit, rim flatness, and inner-wall surface crazing are recorded, and the bowl is re-checked for heat deflection temperature according to ASTM D648-18 Method B at 0.45 MPa. Migration kinetics of the additive package are temperature-dependent and must be evaluated by specific migration testing on the moulded article under Regulation (EU) No 10/2011; in the United States, the converter confirms food-contact status through the applicable FCN for the additive and colourant package, as PLA itself is not covered by 21 CFR 177.1520.
Steam-in-bag lidding produced from ECOPLAN -DURA EN100 requires a different thermal history than rigid thermoforming; the film is purposely quenched rather than crystallised so that a low seal initiation temperature remains available on vertical form-fill-seal machines. Cast film extrusion is performed at a melt temperature of 185–210 °C and a chill-roll temperature of 15–25 °C. This thermal history suppresses the crystalline fraction and permits heat-seal initiation near 85–95 °C, provided jaw pressure and dwell are adjusted for film gauge. On a VFFS line, seal strength is measured according to ASTM F88/F88M-21; a typical acceptance limit for a 25 µm lidding film is 8 N/25 mm after a 0.5 s dwell at 120 °C and 2 bar jaw pressure, but the converter must revalidate after each gauge change because seal strength does not scale linearly with thickness for plasticised PLA compounds. If the film is not quenched quickly enough, the seal layer develops haze and the seal initiation rises above 100 °C, which then damages the substrate tray during sealing. Amine-based antifog masterbatches should not be assumed compatible; amine migration can accelerate ester hydrolysis and premature film embrittlement, so the additive must be verified by oven-ageing at 50 °C for 7 days before line trials.
Blown-film processing of the same compound for pouches is performed with a die gap of 0.8–1.2 mm, a blow-up ratio of 2.0:1–3.0:1, and a frost-line height of 4–6 die diameters. The bubble is susceptible to draw resonance when melt strength is depleted by excess moisture; the same 250 ppm moisture limit applies, and dryer uptime becomes a direct production metric. Pinholes are evaluated with a water-bath leak test under internal pressure, and oxygen transmission is measured according to ASTM D3985-05 at 23 °C and 0% RH; PLA films are not high-barrier structures, so steam-in-bag formats usually require an additional barrier coating or lamination layer. Water vapour transmission is measured according to ASTM F1249-20 at 38 °C and 90% RH, and the result is used to determine shelf life for frozen or chilled products. Compostability claims are verified separately under EN 13432 or ASTM D6400-21.
In clamshell foam extrusion, the processing window narrows because the gas-loaded PLA melt has lower elongational viscosity than talc-filled polypropylene. The line is configured as a tandem extruder with a 36:1 L/D primary screw and a 28:1 L/D cooling screw; physical blowing agent injection, typically carbon dioxide or nitrogen, is located after the melt seal at approximately 24:1 L/D on the primary barrel. Melt temperature must be maintained between 180 °C and 200 °C at the die, which is 10–20 °C lower than the melt temperature used for dense sheet; above 205 °C, cell coalescence and prefoaming inside the die produce surface defects and density variation. Below 175 °C, the gas-laden melt exhibits high head pressure and melt fracture at the die lips. The die gap is set between 0.2 mm and 0.5 mm, and the forming temperature is maintained in a narrow band of ±3 °C across the sheet because the flexible PLA compound has a lower cold-crystallisation onset than rigid PLA and therefore a narrower thermoforming plateau. Density reduction is verified according to ASTM D792-20, and foam cell size is measured according to ASTM D3576-15.
Post-extrusion trim and guillotine cutting are more sensitive to blade temperature; ambient slitting of PLA foam at speeds above 20 m/min can generate microcracks along the hinge area. Clamshell hinges made from foam are the main failure zone during repeated microwave reheating; a hinge flex test after 10 open/close cycles at 23 °C and after heating at 100 °C for 3 min identifies crack initiation. Published data for this specific configuration is limited, so converters should generate a fractional factorial design including melt temperature, gas injection rate, and cooling roll temperature before committing to long-run production. Food-contact evaluation follows Regulation (EU) No 10/2011 and applicable FDA FCN requirements, with particular attention to blowing-agent residuals and print adhesion.
Extrusion coating of ECOPLAN -DURA EN100 onto paperboard for microwavable cups and bowls creates a failure mode that is not visible at the coating line but appears after steam pressure is generated under the PLA layer during reheating. The melt curtain is delivered from a slot die at 200–220 °C and drawn into a nip at 80–120 m/min. If the paperboard contains more than 9% moisture at the nip, the vaporising water disrupts the melt web and leaves latent pinholes. Paperboard is conditioned to 7–9% moisture and the chill roll is held at 15–25 °C to freeze the amorphous PLA surface before crystallisation can produce pinholes or adhesion loss. Coating thickness below 12 µm is not recommended for microwave steam release because pinhole probability increases as the melt web is drawn to lower thickness; 15–25 µm is the typical product window. Adhesion is checked by a 90° peel test after 24 h conditioning, and pinholes are detected with a solvent-based dye penetrant test before and after microwave reheating.
The second source of pinhole failure is melt-temperature drift at the die lip. If the die lip temperature falls below 195 °C, the melt curtain develops edge thickening and folds, creating air entrapment at the web edges; if the die lip temperature exceeds 225 °C, oxidative degradation at the lip increases and the coating surface becomes turbid. These defects are monitored by recording die lip temperature at 6 points across the width and by measuring the coating weight profile with a beta gauge before the chill roll. For cups and bowls, the coated paperboard is die-cut, folded, and heat-sealed; the seal area is tested according to ASTM F88/F88M-21 after being filled with water and heated in a microwave at 800 W for 5 min. Food-contact verification of the finished cup is performed under Regulation (EU) No 10/2011 using EN 1186 and EN 13130 test protocols, and the converter confirms that the paperboard, coating, and printing system are covered by the applicable FDA FCN or 21 CFR section for the complete construction.
| Property or hazard | Method | Condition |
|---|---|---|
| Tensile strength | ISO 527-2:2012 / ASTM D638-14 | 23 °C, 50% RH |
| Heat deflection temperature | ASTM D648-18 Method B | 0.45 MPa |
| Melt flow rate | ISO 1133-1:2022 | 210 °C, 2.16 kg |
| Density | ASTM D792-20 | 23 °C |
| Seal strength | ASTM F88/F88M-21 | 120 °C, 0.5 s, 2 bar |
| Oxygen transmission | ASTM D3985-05 | 23 °C, 0% RH |
| Water vapour transmission | ASTM F1249-20 | 38 °C, 90% RH |
| Overall migration | EN 1186-1:2002 | EU food simulants |
| Residual moisture | ISO 15512:2019 | pellets before extrusion |
| Compostability | EN 13432 / ASTM D6400-21 | finished article |
A separate class of application is the direct food-contact pouch for frozen vegetables that is transferred from freezer storage at -18 °C to microwave reheating at 100 °C steam. Flex-crack resistance at -18 °C is evaluated according to ISO 527-2:2012 after conditioning the film for 48 h at 23 °C and 50% RH, then chilling for 24 h at -18 °C. The compound's flexible modifier shifts the low-temperature brittle point downward relative to unmodified PLA, but the exact value depends on the additive lot; converters should therefore run a gel permeation chromatography check of molecular weight before converting return regrind above 15% because hydrolytic degradation caused by residual moisture concentrates in film scrap. At the blown-film die, a die gap of 0.8–1.2 mm, a blow-up ratio of 2.0:1–3.0:1, and a frost-line height of 4–6 die diameters are used to balance machine-direction and transverse-direction tear resistance; the bubble is run with a collapsing frame that is pre-heated to 30–40 °C to reduce blocking and wrinkle writing. Seal initiation is measured on a gradient sealing jig according to ASTM F88/F88M-21, and the heat-seal window is defined as the range between the minimum seal strength of 8 N/25 mm and the temperature at which the film shrinks or wrinkles on the tray flange.
After the pouch is sealed, a steam-in-bag test is conducted with frozen food simulant or vegetable mix; the seal is inspected for channel leaks, and the film is visually rated for whitening, delamination, and pinholing after 5 min at 800 W. Because the polymer is not a high-barrier material, the package design uses a laminated or coated structure when oxygen-sensitive vegetables are packed, and the oxygen transmission rate is measured according to ASTM D3985-05 at 23 °C and 0% RH. Compostability claims for the finished pouch are verified separately under EN 13432 or ASTM D6400-21 and are not granted by the PLA resin supplier without complete article testing. The film handler must also confirm that the antifog and slip additives used in the formulation do not raise water vapour transmission beyond the limit set for frozen-to-microwave use, which is measured according to ASTM F1249-20 at 38 °C and 90% RH.
Competitive ECOPLAN -DURA EN100 Flexible Heat Resistant Microwavable Polylactic Acid prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
ECOPLAN -DURA EN100 Flexible Heat Resistant Microwavable Polylactic Acid is a poly(lactic acid)-based thermoplastic compound supplied for injection moulding, sheet extrusion, and thermoforming of food-contact packaging that must tolerate short microwave reheating. The grade is formulated to reduce the brittleness of standard PLA and to shift the thermal service limit above the range at which amorphous PLA begins to creep under load. It is not a polyolefin drop-in; successful conversion requires adjustment of drying, mould temperature, runner geometry, and wall thickness. The EN100 identifier positions the product within the supplier’s durability and heat-resistance series, but the exact heat deflection temperature, elongation at break, and melt flow rate are batch-specific and must be obtained from the supplier’s certificate of analysis. The processing and performance data presented below are compiled from published PLA compound behaviour and from production-scale moulding and extrusion experience; they do not replace the grade-specific technical data sheet.
Standard amorphous PLA homopolymer has a glass transition near 55–60°C and a heat deflection temperature under ISO 75-2:2013 at 0.45 MPa in the same range. That thermal profile is inadequate when a lid or tray carries a hot food load above 70°C. Heat-resistant PLA compounds are produced by nucleation, stereocomplex blending, or post-mould annealing to increase crystalline content and raise the Vicat softening point measured under ISO 306:2022. The EN100 suffix indicates a heat-resistant flexible grade; however, published data for this specific configuration is limited, and design release values should be taken from the supplier’s technical data sheet.
Differential scanning calorimetry under ISO 11357-1:2016 and ISO 11357-3:2018 is used to characterise the glass transition, cold-crystallisation exotherm, and melting endotherm. A low cold-crystallisation onset indicates that hot mould temperatures will be required during injection moulding to develop the intended crystalline network. In microwave reheating, the polymer is heated mainly by conduction and convection from the food rather than by direct dielectric absorption. Localised oil and sugar pockets can exceed 100°C while the bulk aqueous phase remains below boiling. Qualification therefore requires instrumented food simulant tests that record maximum part surface temperature, deformation under lid load, and migration after repeated cycles. Heat distortion testing alone is not sufficient to certify a microwavable part.
Flexibility modification in PLA compounds is usually achieved with biodegradable aliphatic-aromatic copolyester impact modifiers or citrate/ester plasticisers. The tensile modulus under ISO 527-2 declines relative to unmodified PLA by a factor that depends on modifier loading. Notched Izod impact under ISO 180:2019 may increase from the brittle regime below 5 kJ/m² to a ductile regime above 10 kJ/m², but the exact change for EN100 is supplier-specific. The flexible phase can also reduce the concentration of crystalline regions at the surface if mould temperatures are too low; therefore, the heat-resistance claim is coupled to processing conditions rather than to the resin alone.
Moisture control is the primary processing constraint. PLA undergoes hydrolytic chain scission in the melt if residual moisture exceeds approximately 250 ppm. Pellets must be pre-dried in a desiccant dryer at 80°C for 4–6 h or dried in-line to a dew point below -40°C. At factory relative humidity above 60%, machine hoppers and open gaylords should be blanketed with dried air or nitrogen. Residual moisture should be confirmed before start-up by Karl Fischer titration or a calibrated online moisture analyser.
On a co-rotating twin-screw extruder with an L/D ratio of 28:1–40:1, barrel zone set points typically range from 160°C to 200°C. Melt temperature at the die should not exceed 210–220°C for normal cycles; excursions above 230°C accelerate lactide formation and discolouration. For injection moulding, a low-compression screw with a compression ratio of 2.5:1–3:1 and a back pressure of 5–15 bar is appropriate. Shot size should be kept between 30% and 70% of barrel capacity. Thin-wall parts with flow length-to-wall thickness ratios approaching 150:1 may require hot mould temperatures of 80–110°C to promote crystallization and maintain ejection rigidity. Mould temperatures below 40°C tend to freeze an amorphous skin, reduce heat resistance, and increase warp after demoulding. Cavity pressure sensors are recommended in multi-cavity tools because melt-viscosity variation among flexible PLA batches can shift fill balance and produce dimensional drift in microwave lids.
If the material is converted as a pre-compound, incoming pellet uniformity should be checked by melt flow rate under ISO 1133-1:2022 at 190°C/2.16 kg or 210°C/2.16 kg. Values must not be compared across different temperature and load conditions. Batch-to-batch MFR variability greater than 15% can indicate hydrolytic degradation or modifier dispersion faults. Production-scale extrusion lines with vacuum venting below 50 mbar absolute are used to strip residual moisture and lactide; loss of vent vacuum produces surface splay and gas bubbles in sheet or moulded parts.
| Parameter | Typical setting / envelope | Control method |
|---|---|---|
| Pre-drying temperature | 80°C | Desiccant dryer, dew point below -40°C |
| Pre-drying time | 4–6 h | Residual moisture below 250 ppm, Karl Fischer or online analyser |
| Barrel zone temperature | 160–200°C | Profile thermocouples |
| Melt temperature limit | 210–220°C maximum 230°C | Melt probe |
| Screw compression ratio | 2.5:1–3:1 | Injection moulding screw specification |
| Back pressure | 5–15 bar | Hydraulic or electric injection unit |
| Mould temperature for heat resistance | 80–110°C | Mould temperature control unit |
| Residence time at melt temperature | Less than 2 min | Process log and shot-to-shot recovery |
Food-contact status for ECOPLAN -DURA EN100 is not a universal property. Compliance is established through the supplier’s United States Food Contact Notification, the EU Declaration of Compliance under Commission Regulation (EU) No 10/2011, and applicable national food-contact standards such as GB 9685 in China. Overall migration must not exceed 10 mg/dm² or 60 mg/kg under the prescribed simulants and test conditions. Because PLA is hydrolytically sensitive in aqueous simulants at elevated temperature, migration testing should be performed at the intended time–temperature profile rather than only the standard 10-day 40°C condition. Industrial compostability is evaluated under EN 13432:2000, ASTM D6400-19, and ISO 17088:2021; these standards do not confer home compostability or marine biodegradation. The microwave-use designation is a thermal fitness claim, not a food-contact clearance. It must be supported by final-part tests with representative food simulants and by hot-spot mapping at the intended microwave power output.
Migration kinetics in polymer matrices depend on molecular mobility near the glass transition. In flexible PLA grades, impact modifiers and plasticisers can raise the diffusion coefficient for low-molecular-weight additives at temperatures above 60°C. Therefore, compliance certificates for microwave service should be reviewed for the specific additive package, and new tool surface or regrind ratios above 20% should be revalidated because regrind may alter migration behaviour and heat resistance.
Polypropylene is the incumbent material for microwave lids and trays because it typically exhibits a heat deflection temperature of 90–110°C at 0.45 MPa under ISO 75-2:2013, tensile elongation above 100% under ISO 527-2, and very low moisture sensitivity. ECOPLAN -DURA EN100 is selected where the part owner requires a PLA-based, compostable or bio-based alternative and accepts a narrower thermal and mechanical operating window. The replacement is not a simple resin swap.
Standard polypropylene living hinges with a thickness of 0.25–0.4 mm generally do not transfer directly to PLA-based compounds. Hinge thickness should be increased to 0.4–0.6 mm, the hinge radius enlarged, and repeated flex testing performed at the intended microwave exit temperature. Flow length-to-wall thickness ratios should be lowered below 150:1 because PLA melt strength and thermal conductivity differ from polypropylene. Hot mould temperatures required for crystallisation increase cooling time and may raise cycle time by 15–30% relative to PP. Dimensional stability in thin-wall parts should be validated with injection-compression moulding or in-mould annealing to control warp. Clamp force requirements should be estimated from cavity pressure measurements rather than from PP historical data because lower melt thermal diffusivity can alter solidification rate and peak injection pressure.
Microwave service should also account for the lid or tray thickness distribution. In PLA compounds, chilled amorphous skins can develop at the mould surface while the core crystallises; this skin–core structure produces differential shrinkage and can warp after reheating. Annealing fixtures or post-mould crystallisation at 80–100°C for 10–30 min may be required to stabilise geometry before microwave testing. The annealing step is not required for polypropylene and represents an additional cost.
| Material class | Heat distortion at 0.45 MPa (ISO 75-2:2013) | Tensile elongation at break (ISO 527-2) | Moisture sensitivity | Short microwave suitability |
|---|---|---|---|---|
| ECOPLAN -DURA EN100 | Higher than standard PLA; supplier release value required | Flexible PLA class; supplier release value required | High; pre-drying under 250 ppm moisture required | Designed for short aqueous reheat; validate local hot spots |
| Standard amorphous PLA | 55–60°C | 2–5% | High | Not suitable above 70°C |
| Nucleated heat-resistant PLA | 80–120°C | 3–10% | Moderate to high | Possible for low-load short heat; validate part geometry |
| PLA/PBAT blend | Below 50°C | Greater than 200% | Moderate | Not suitable for hot-fill or microwave reheating |
| Polypropylene | 90–110°C | Greater than 100% | Low | Suitable but not compostable |
Operational boundaries for ECOPLAN -DURA EN100 must be stated. The material is not intended for continuous oven use, retort, steam sterilisation, or dishwasher cycles unless the finished part has been validated at the corresponding temperature–time profile. The compound should not be processed with amine-based additives or strongly alkaline concentrates because these species can accelerate polymer degradation and reduce heat resistance. Storage should be in sealed moisture-barrier packaging at relative humidity below 60%; opened packaging exposed for more than 8 h should be re-dried before moulding. Equipment should be purged with a low-melt-index polyolefin or a commercial purge compound before shutdown to avoid stagnant melt zones above 200°C. Regrind levels should be limited to 20–30% or the supplier’s validated maximum; higher regrind addition can lower melt viscosity and heat distortion. These limitations are class-level boundaries for flexible heat-resistant PLA compounds; the manufacturer’s grade-specific technical data sheet and application test report form the binding specification for any commercial part.