Products

Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound

    • Product Name: Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 789290
    Product Name Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound
    Material Type Polylactic Acid (PLA) compound
    Grade Premium ductile compostable
    Appearance Natural pellets
    Density 1.24 g/cm³
    Melt Flow Rate 10-20 g/10 min (190°C/2.16 kg)
    Tensile Strength 50 MPa
    Tensile Modulus 3.5 GPa
    Elongation At Break 120%
    Notched Izod Impact Strength 20 kJ/m²
    Heat Deflection Temperature 55°C
    Vicat Softening Point 60°C
    Melting Point 150-170°C
    Glass Transition Temperature 55-60°C
    Bio Based Content 100%
    Compostability EN 13432, ASTM D6400
    Processing Method Injection molding, extrusion, 3D printing

    As an accredited Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg moisture-barrier multiwall paper bags with polyethylene liners, palletized and shrink-wrapped for safe storage and transport.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized 25 kg bags of Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound, securely strapped and shrink-wrapped.
    Shipping Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound is shipped as a non-hazardous solid in sealed moisture-barrier bags, drums, or supersacks. Keep dry, below 50°C, away from UV and contamination. No UN dangerous-goods classification; include SDS. Follow local regulations and preserve packaging integrity during transport.
    Storage Store in a cool, dry, well-ventilated area in tightly sealed original packaging. Keep away from direct sunlight, heat sources, moisture, and strong oxidizing agents. Maintain below 30°C and low humidity to prevent hydrolysis, clumping, or degradation. Protect from physical damage, keep containers closed when not in use, and practice stock rotation for optimum shelf life.
    Shelf Life Shelf life is typically 12–24 months when stored cool, dry, sealed, away from moisture, heat, and UV; retest after expiration.
    Application of Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound

    High-cavity injection molding of Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound on a 100–180 t hybrid press produces compostable cutlery, lids, and thin-wall containers with part mass from 4 g to 18 g. Residual moisture must be reduced to <250 ppm in a desiccant dryer with a -40 °C dew point at 80 °C for 4–6 h; open storage above 60% RH for more than 30 min before the feed throat reintroduces surface moisture sufficient to produce splay and embrittlement. A reverse barrel profile from 180 °C at the feed zone to 210 °C at the nozzle keeps the melt viscosity in a shear-thinning window that fills 4–16 cavities without excessive gate blush. The screw should use a compression ratio of 2.5:1 and a low-shear metering zone; recovery time typically lengthens when back pressure exceeds 5 MPa, while screw speeds above 150 rpm can generate frictional heat beyond 230 °C, initiating lactide reformation and black speck formation. Injection speeds of 120–180 mm/s with holding pressure 30–60 MPa produce acceptable gate sealing; slower speeds create flow lines at the melt front, and faster speeds cause jetting at pin gates smaller than 0.8 mm. Mold surface temperature is maintained at 25–35 °C to freeze the amorphous morphology and allow ejection at 45–55 °C; part warpage increases when the demolding surface temperature exceeds 60 °C. On molded plaques tested at 23 °C and 50% RH according to ISO 527-2:2012 at 5 mm/min, tensile elongation at break falls between 15% and 60%, while unmodified PLA typically exhibits 3–6%. Notched Izod impact under ISO 180:2023 ranges from 6 kJ/m² to 12 kJ/m²; when moisture content exceeds 400 ppm, impact strength falls below 4 kJ/m² due to hydrolytic chain scission in the barrel. Finished cutlery meets disintegration requirements of EN 13432:2000 only in industrial aerobic composting at 58±2 °C; no claim should be made for marine or home compost unless separately certified under a home compost certification scheme.

    What Thermoforming Conditions Prevent Sheet Sag and Webbing in the Ductile PLA Grade?

    Roll-fed thermoforming of extruded sheet at 0.5–1.2 mm thickness uses ceramic infrared heaters to raise the sheet surface to 95–110 °C and the core to 80–90 °C before plug-assisted forming. The allowable surface temperature range is ±5 °C; below 95 °C the sheet tears at the corners, and above 110 °C gravity sag and webbing become severe. The mold body temperature is held at 100–110 °C to allow partial crystallization while the sheet is in contact with the tool; this reduces post-forming shrinkage above the PLA glass transition at 58–60 °C but increases cycle time because the part must be quenched to 50–60 °C before trimming. A heated syntactic foam plug at 100–110 °C with plug speed 200–300 mm/s distributes material into the base corners; draw ratios above 2.5:1 produce corner thinning greater than 60% of the original sheet thickness, as measured by cross-section microscopy. If a clear amorphous tray is required, the mold is dropped to 20–30 °C, but the final part will distort if exposed above 55 °C during transport or reheating. Crystalline hot-mold parts show higher haze due to spherulitic growth; haze is quantified according to ASTM D1003-21. The sheet must be dried to <250 ppm moisture before extrusion, and re-drying at 60 °C for 2 h is recommended if rolls are stored outside vapor barrier film at >60% RH. Post-trim annealing at 80 °C for 30 min may improve dimensional stability but is not always practical on high-output lines. Scrap reclaim rates up to 30 wt% have been run without significant loss of dart impact in trays, although repeated heat histories increase melt flow rate by 10–20% per pass and narrow the forming window. The trays are suitable for cold and ambient food contact under EU 10/2011 overall migration limits and are tested according to EN 1186-1:2002; fatty food contact above 40 °C requires specific migration analysis for the impact-modifier phase.

    In blown film extrusion, the ductile PLA compound is processed on a 45 mm single-screw extruder with L/D 30:1 and a 100 mm spiral mandrel die with die gap 1.0–1.5 mm. Melt temperature is held at 170–190 °C; operation above 200 °C promotes bubble instability and lactide volatilisation, which condenses on the air ring as a white deposit. A dual-lip air ring with air temperature 15–25 °C and blow-up ratio 2.0:1 to 2.5:1 stabilises the bubble, and the frost line height is kept between 15 cm and 25 cm. At film thickness 15–40 µm, gauge variation measured by ISO 4591:2000 remains within ±8% when melt pressure before the die is 18–25 MPa. Below 15 µm, draw resonance and edge flutter produce gauge bands and a loss of dart impact; blown film lines with automated gauge control can compensate but cannot fully remove the melt strength limitation of the PLA matrix. The impact-modifier phase raises machine-direction and transverse-direction elongation to 100–200% under ISO 527-3:2018, but Elmendorf tear strength under ASTM D1922-23 remains lower than that of LDPE of equivalent thickness. Compostable produce bags and liners from this film are certified under EN 13432:2000; after industrial composting at 58±2 °C, the film disintegrates within 12 weeks. For agricultural mulch film, soil burial at 25 °C is significantly slower, and published field data for this specific ductile compound are limited; therefore regulatory claims for soil biodegradation must be supported by a separate ISO 17556:2019 study.

    Table 1. Melt processing parameter ranges by downstream converting method
    Processing methodMelt or sheet temperatureResidual moisture targetTooling or roll temperatureMaximum recommended residence time
    Injection molding185–210 °C<250 ppm25–35 °C≤8 min
    Thermoforming95–110 °C sheet surface<250 ppm100–110 °C mold10–30 s IR dwell
    Blown film170–190 °C<250 ppm25–35 °C air ring≤6 min
    Extrusion coating210–230 °C<200 ppm15–25 °C chill roll≤15 min
    FFF filament200–220 °C<250 ppm50–60 °C bed≤5 min in hot end

    When Seal Initiation Temperature and Blocking Resistance Govern Flexible Compostable Laminates

    Heat sealability of the ductile PLA compound is measured on a laboratory hot-tack frame and a gradient sealer. Seal initiation begins at 85–95 °C, and the peelable seal window extends to 115 °C; above 120 °C the film shrinks and the seal becomes brittle. Jaw pressure of 0.3–0.6 MPa with dwell 0.5–1.5 s produces seal strength 4–12 N/15 mm in ASTM F88/F88M-21. Hot tack strength under ASTM F1921-18 at 90–110 °C is typically 2–5 N/15 mm, sufficient for vertical form-fill-seal lines but below metallocene PE thresholds; line speed must be reduced when package mass exceeds 250 g. Blocking resistance is evaluated at 50 °C and 0.1 MPa for 24 h; films with high surface tack require anti-block masterbatch at 0.5–2.0 wt% to prevent roll block during storage. The addition of anti-block changes surface energy and may reduce seal strength by 10–20%. Flexible compostable laminates made with this compound are intended for industrial composting after use; if printed with nitrocellulose inks, the heavy-metal limits of EN 13432:2000 must be met, and the laminate must be tested for disintegration as a complete structure, not as individual layers. For food-contact lamination, EU 10/2011 overall migration testing is performed with aqueous, acidic, and fatty simulants, and the seal layer must not transfer the impact-modifier phase above the specific migration limit.

    Extrusion Coating on Cellulosic Substrates and Die Deposit Stability

    The compound can be applied as a coating weight of 10–25 g/m² onto corona-treated paper or paperboard using a 90 mm single-screw extruder with L/D 30:1 and a T-slot die with 0.5 mm lip opening. Melt temperature at the die is 210–230 °C; below 210 °C the melt curtain tears, and above 230 °C lactide monomers deposit on the die lips and transfer to the coating as oval defects. The air gap is maintained at 100–200 mm, and the chill roll is held at 15–25 °C with a water contact time of 0.5–1.5 s. Neck-in at 200 m/min is approximately 10–15%, and line speeds above 300 m/min exceed the melt strength of the ductile grade, causing edge weave. Adhesion to paper depends on substrate porosity and surface treatment; a dyne level of 42–46 mN/m is required, and adhesion is checked by ASTM F904-16. For paper cups, the PLA coating provides liquid holdout but has oxygen barrier inferior to EVOH or PVDC; therefore it is not suitable for extended shelf-life without additional barrier layers. The compostability certification is based on EN 13432:2000 or ASTM D6400-23, but the paper substrate must also meet the same criteria before the final article can be labelled compostable. Die deposit rates after 4–6 h of continuous coating are observed as amber edges; purging with low-melt-index polyolefin may remove some deposits, but complete cleaning requires shutdown and copper-wool wiping. The use of reactive purge compounds containing amine-based modifiers is not recommended because they can accelerate polycondensation residues and create gel specks in the next PLA run.

    Filament made from the ductile PLA compound is extruded on a 25 mm single-screw extruder with L/D 24:1 and a melt pump, followed by a water trough at 40–50 °C. The diameter target is 1.75±0.05 mm with roundness within 0.03 mm; continuous laser gauging with feedback to the melt pump is required because the ductile modifier phase increases die swell relative to unmodified PLA. Fused filament fabrication with this filament uses a nozzle temperature of 200–220 °C, a bed temperature of 50–60 °C, and a chamber temperature below 35 °C for open-frame printers. Print speed of 40–80 mm/s with layer height 0.12–0.20 mm yields tensile strength in the print direction of 35–50 MPa under ISO 527-2:2012; perpendicular to the build direction, tensile strength is 20–30% lower due to interlayer fusion limits. Part cooling fans should run at 50–100% after the first layer to prevent sagging in walls thicker than 3 mm. Shrinkage of amorphous printed parts is 0.3–0.5%, and bed adhesion improves on glass with polyvinyl alcohol adhesive at 60 °C. Printed parts demonstrate notched impact values lower than injection molded parts because the interlayer weld acts as a flaw; users must not assume that the compound’s ductile molded properties transfer directly to FFF parts. Compostability of FFF parts follows EN 13432:2000 only in industrial composting; disassembly from metal inserts is required because metals are not compostable. For prototypes used in food-contact contexts, the printed part must comply with EU 10/2011, but the typical FFF surface porosity and layer-line roughness complicate cleaning and may retain food residues; therefore printed parts are generally limited to non-food contact or single-use contact with aqueous foods below 40 °C.

    Table 2. Compliance matrix for the ductile PLA compound across downstream applications
    Standard/regulationScopeTest methodTypical requirement
    EN 13432:2000Industrial compostability of packagingISO 14855-1:2012; ISO 16929:2021≥90% biodegradation in 180 days; ≤10% residue > 2 mm after 12 weeks
    ASTM D6400-23Compostable plastics in municipal and industrial aerobic facilitiesASTM D5338-15≥90% mineralization of organic carbon within 180 days
    EU 10/2011Plastic food contact materialsEN 1186-1:2002; EN 13130-1:2004Overall migration < 10 mg/dm²
    FDA 21 CFR 175.300Resinous and polymeric coatings for food contact, including extrusion coating on paperboardFDA extraction cellExtractives limits as appropriate for food type
    Regulation (EC) No 1907/2006 Annex XVIIChemical safety in EU marketDeclaration and analytical screeningNo restricted substance above specified concentration
    Free Quote

    Competitive Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound 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

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Bioplastic PLA-Premium Ductile Compostable Polylactic Acid Compound is supplied as a dried and sealed pelletized grade with bulk density 0.75–0.85 g/cm³ and pellet diameter 2.5–3.5 mm. The product model is identified in documentation as PLA-Premium Ductile; no additional subgrade designation appears on the certificate. The formulation is based on polylactic acid modified with non-aromatic biodegradable copolyester and ester-based processing modifiers to reduce low-strain brittle fracture while maintaining compostability under EN 13432:2000 and ASTM D6400-23. The grade is intended for extrusion, coextrusion, thermoforming, and injection molding where higher elongation and impact resistance than unmodified PLA are required but where PBAT-rich compounds exhibit insufficient modulus or low heat resistance. Stress–strain response is shifted from the brittle tensile yield of standard PLA, typically 5–10 % elongation, to a ductile necking and drawing region exceeding 150 % elongation when tested to ISO 527-2 at 23 °C and 50 % RH.

    What Processing Constraints Apply to Ductile PLA Melt Conversion?

    Before melt processing, pellet moisture must be reduced to 0.025 % (250 ppm) or lower. A desiccant dryer with a dew point no higher than -40 °C and a drying temperature of 80 °C for 4–6 h is specified. Hopper residence time above 8 h at temperature can accelerate ester interchange and shift melt viscosity. The melt flow index under ISO 1133-1:2022 at 190 °C and 2.16 kg is specified in the range 4.0–8.0 g/10 min. In a corotating twin-screw extruder with L/D 40:1, the barrel profile from feed to die is maintained at 160 °C, 180 °C, 190 °C, 195 °C, 195 °C, 190 °C; the die head is held at 190 °C. The melt temperature window is narrow, with a setpoint deviation of no more than ±5 °C in downstream zones. Residence time above 220 °C accelerates lactide reformation and causes molecular weight reduction; viscosity loss can exceed 20 % within 5 min of elevated-temperature exposure. Screw speed is maintained at 300–450 rpm and specific mechanical energy at 0.18–0.25 kWh/kg; a vacuum vent of -0.08 MPa is applied at the metering zone to remove residual monomer and moisture. Published data for this specific configuration is limited; the settings represent typical production conditions for PLA-copolyester compounds reported in processing literature.

    On single-screw cast film and sheet lines with L/D 30:1 to 36:1, the compound is processed with a barrier screw and a screen pack of 60/100/60 mesh. Back pressure is held at 80–120 bar. The die gap for cast film is set at 0.5–0.8 mm with an air gap of 80–120 mm to limit neck-in. Viscoelastic response differs from polyolefins; shear viscosity at 190 °C and 100 s⁻¹ is in the range 300–800 Pa·s. Because the compound is hygroscopic, edge trim regrind must be predried before reintroduction and is limited to 15 wt% for film to preserve gel count and compostability.

    Process stability at the die is further constrained by the narrow difference between PLA crystalline melt temperature and thermal degradation onset. A melt temperature above 210 °C reduces apparent viscosity by more than 15 % and can cause die-lip build-up from low-molecular-weight fractions. Periodic die-lip cleaning every 6 h is standard on production lines. Melt fracture may appear as sharkskin at shear rates above 1,000 s⁻¹; for the ductile grade, the critical shear rate at 190 °C is lower than that of unmodified PLA due to the reduced melt strength of the copolyester phase. Stable cast film is obtained when the draw-down ratio is kept below 20:1 and the frost line distance is 60–120 mm from the die.

    Mechanical Specification Sheet and Test Methodology

    The following release specifications apply after 40 h conditioning at 23 °C and 50 % RH. Tensile testing is performed on 1A dog-bone specimens at 5 mm/min; impact testing uses notched 80 mm × 10 mm × 4 mm specimens.

    PropertyUnitSpecificationTest Method
    Melt flow indexg/10 min4.0–8.0ISO 1133-1:2022
    Tensile strength at breakMPa≥ 35ISO 527-2
    Elongation at break%≥ 150ISO 527-2
    Flexural modulusMPa900–1400ISO 178
    Charpy notched impact at 23 °CkJ/m²≥ 20ISO 179-1/1eA
    Vicat softening temperature°C55–65ISO 306/B50
    Densityg/cm³1.24–1.28ISO 1183-1
    Moisture content%≤ 0.025ISO 15512

    The 900–1400 MPa flexural modulus is lower than unreinforced PLA, which is typically 3000–3500 MPa, but higher than PBAT-rich compounds at 40–120 MPa. The Charpy notched impact value above 20 kJ/m² changes the failure mode from brittle crack propagation to ductile deformation under notched or punctured service conditions. The Vicat softening temperature of 55–65 °C limits continuous service in hot-fill applications above 60 °C; the compound is not suitable for microwave or dishwasher sterilization. The moisture content specification is critical because retained water in the pellet hydrolyzes PLA during melting.

    ParameterStandard PLAPLA-Premium DuctilePBAT-rich compound
    Elongation at break, ISO 527-25–10 %≥ 150 %400–800 %
    Flexural modulus, ISO 1783000–3500 MPa900–1400 MPa40–120 MPa
    Vicat softening temperature, ISO 30655–60 °C55–65 °C< 30 °C
    Charpy notched impact, ISO 179-1/1eA2–3 kJ/m²≥ 20 kJ/m²no break
    Compostability frameworkEN 13432EN 13432EN 13432

    Compared with standard PLA, the compound reduces flexural modulus by approximately 60 % while increasing elongation at break from 5–10 % to no less than 150 %. Compared with PBAT-dominant compounds, retention of a continuous PLA phase preserves a Vicat softening temperature above 50 °C, whereas PBAT-dominant films may distort below 30 °C. The biodegradable copolyester content is not disclosed in the supplied documentation; published data for this specific formulation is limited. The grade is intended for applications requiring a balance of ductility, stiffness, and compostability, but it does not match the low-temperature flexibility or elastic recovery of PBAT- or PBS-dominant compounds.

    Thermal analysis of the compound shows a glass transition at 55–60 °C, cold crystallization onset at 95–105 °C, and melting endotherm at 150–165 °C. The crystalline melt enthalpy is below 30 J/g. Annealing at 80 °C for 30 min raises the heat deflection temperature by 10–15 °C and reduces post-mold shrinkage. These values are typical for PLA-copolyester systems; product-specific data for the exact modification are limited.

    When the Compound Replaces Standard PLA in Thermoformed Packaging

    Sheet produced from the compound is heated to 85–100 °C prior to forming; temperature uniformity across the sheet must be within ±3 °C to prevent localized thinning. Plug-assisted thermoforming with acetal or syntactic foam plugs at 70–80 °C and a plug-assist ratio of 0.45:1 permits draw ratios up to 3.5:1 without flange cracking. In production-scale trials on a shuttle thermoformer with 600 mm × 400 mm tooling, a 0.5 mm initial sheet yielded wall thickness distribution from 0.28 mm to 0.42 mm. Standard PLA sheet at the same draw depth exhibits corner cracking; the ductile compound accommodates corner radii of 2 mm without fracture. Cycle time is 8–12 s including cooling; mold surfaces are maintained at 30–50 °C to balance crystallization and demolding. Post-mold shrinkage after 24 h at 23 °C is specified below 1.5 %. This comparison is based on production line data reported for PLA-copolyester compounds; site-specific results vary with tooling geometry and heating efficiency.

    On injection molding machines with clamp force between 800 kN and 2,500 kN, the compound is processed with barrel zones from 175 °C to 195 °C and a nozzle temperature of 190 °C. Mold temperature is set at 25–40 °C. Injection speed is 30–60 mm/s and back pressure 20–50 bar. Screw decompression after plasticating is limited to 3–5 mm to avoid air entrapment. For thin-wall cutlery with wall stock of 2.0 mm, packing pressure of 400–600 bar applied for 3 s minimizes sink marks. The short-shot response is more shear-sensitive than unmodified PLA; increasing melt temperature by 5 °C improves fill more than increasing injection speed by 20 mm/s. Gate diameters below 1.0 mm are avoided because shear heating can exceed 10 °C and cause local degradation. These parameters are drawn from production-scale technical literature and require machine-specific confirmation.

    Compostability Is Certified Only Within a Narrow Boundary of Thickness, Temperature, and Moisture

    The compostability certificate covers industrial composting conditions only. Disintegration under ISO 16929 must demonstrate fragmentation with sieve retention below 10 % on a 2 mm sieve after 12 weeks. Biodegradation under ISO 14855-1 must reach 90 % conversion to CO₂ within 180 days relative to a positive reference. Ecotoxicity testing per EN 13432 requires germination rate and plant biomass no less than 90 % of the control. The compound contains no intentionally added per- and polyfluoroalkyl substances and is compliant with EU Regulation (EC) No 1907/2006 REACH and Directive 2011/65/EU RoHS for lead, cadmium, mercury, and hexavalent chromium. Food-contact suitability is not certified by the pellet alone; each finished article must be tested under 21 CFR 175.300 or EU Regulation (EU) No 10/2011 with migration tests specific to the intended food simulant. Compostability must not be interpreted as marine, freshwater, or soil biodegradability; no claim is made under ISO 22766 for microplastic formation.

    Additive incompatibility exists with primary and secondary amines, which catalyze hydrolytic degradation and shift melt viscosity. The compound is incompatible with polyolefins, polystyrene, and aromatic polyesters; contamination above 2 wt% may cause delamination and loss of compostability. Storage below 30 °C and below 60 % RH is specified to prevent moisture uptake. Unopened bags maintain moisture below 0.025 % for 12 months from date of manufacture. Opened bags should be used within 24 h or resealed with desiccant. Regrind addition is limited to 20 wt% for injection molding and 15 wt% for film and sheet, after verification of melt flow index and moisture content.

    Top