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Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin

    • Product Name: Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 303850
    Productname Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin
    Materialtype Polylactic Acid (PLA)
    Chemicalname Poly(L-lactic acid)
    Grade PLLA 001
    Appearance Translucent pellets
    Compostability Compostable according to EN 13432
    Biobasedcontent 100%
    Density 1.24 g/cm³
    Meltflowindex 10 g/10 min at 190 °C and 2.16 kg
    Meltingpoint 175 °C
    Glasstransitiontemperature 55-60 °C
    Tensilestrength 50 MPa
    Tensilemodulus 3500 MPa
    Elongationatbreak 5%
    Flexuralmodulus 3500 MPa
    Heatdeflectiontemperature 55 °C
    Vicatsofteningpoint 60 °C
    Processingmethod Injection molding
    Moisturecontent <0.5%

    As an accredited Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin comes in 25 kg sealed moisture-barrier bags, stacked on pallets for shipping.
    Container Loading (20′ FCL) Natureplast PLLA 001 translucent compostable polylactic acid resin loaded in 20′ FCL; palletized 25 kg bags, securely braced for sea transport.
    Shipping Natureplast PLLA 001, a translucent compostable polylactic acid resin, typically ships as a non-hazardous solid in moisture-barrier bags inside fiber drums or cartons, palletized and stretch-wrapped. Store dry and cool, away from direct sunlight. Standard freight applies; follow local transport regulations and supplier instructions. Ensure packaging remains sealed during transit.
    Storage Store Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin in a cool, dry, well-ventilated area, away from direct sunlight, heat, and moisture. Keep containers tightly sealed and pallets off the floor. Avoid contact with acids, bases, oxidizers, and incompatible chemicals. Maintain recommended storage temperatures and low humidity to prevent hydrolysis. Observe first-in, first-out stock rotation for optimal shelf life.
    Shelf Life Typically 12 months when stored in original sealed packaging, cool, dry, and protected from moisture, heat, and UV light.
    Application of Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin

    Thin-wall injection molding of Natureplast PLLA 001 for rigid compostable foodservice articles begins with desiccant drying to ≤250 ppm residual moisture measured by ISO 15512:2019 method B. Drying at 80°C for 4–6 h with a dew point below −40°C is required when ambient humidity exceeds 60% RH. The melt temperature window is 190–210°C; residence time above 230°C must be kept below 2 min to avoid molecular weight loss and lactide outgassing. Molding can run either with a cold mold at 25–30°C for amorphous parts or with a heated mold at 100–110°C for crystallized parts. Amorphous parts show heat deflection temperature by ISO 75-2:2013 method B of 52–58°C, while crystallized parts reach 80–110°C. The shift to higher heat resistance requires nucleation; PDLA stereocomplex addition at 0.5–2.0 wt% or talc at 1–3 wt% raises the crystallization peak to 120–130°C and shortens hold time to 30–60 s.

    On an 8-cavity cutlery tool with hot runner valve gates, shot-to-shot mass variation exceeding 0.5% was traced to non-return valve leakage after 2,000 cycles when purge intervals exceeded 4 h; reducing back pressure to 0.5–1.5 MPa and increasing screw decompression to 2–3 mm stabilized cushion position. The melt is processed with a general-purpose polyolefin recovery screw having L/D 20:1–24:1 and compression ratio 2.5:1–3.0:1. Injection speed is held at 150–300 mm/s and hold pressure at 40–70 MPa. Finished articles include compostable cutlery, cup lids, plant pots, and rigid clamshell inserts. Compostability claims require EN 13432:2000 or ASTM D6400-23 verification on the finished article; food contact status under EU 10/2011 is not satisfied by resin compostability alone and requires migration testing on the converted part.

    Processing variableRecommended starting rangeReference method / equipment
    Residual moisture≤250 ppmISO 15512:2019 method B
    Melt temperature190–210°CMelt thermocouple / IR pyrometer
    Mold temperature, amorphous25–30°CWater thermolator setpoint
    Mold temperature, crystallized100–110°CPressurized water thermolator
    Hold pressure40–70 MPaHydraulic pressure transducer
    Back pressure0.5–1.5 MPaScrew recovery setting
    Injection speed150–300 mm/sScrew linear speed
    Screw L/D20:1–24:1General-purpose polyolefin recovery

    What Limits Melt Strength and Gauge Uniformity in Cast Sheet and Thermoforming?

    Cast sheet extrusion lines running semicrystalline PLLA 001 require a screw with L/D 30:1–44:1 and a vacuum vent to remove residual lactide. Melt temperature at the die lip should not exceed 205°C to preserve molecular weight. The molten web is pinned to a first chill roll held at 25–35°C; lower roll temperatures reduce haze but increase curl. A melt pump between extruder and die reduces melt pressure pulsation to ±0.2 MPa, limiting gauge variation to ±3% at sheet thickness of 0.5–1.5 mm. Slip or antiblock masterbatch addition at 0.2–0.5 wt% is used to reduce roll wrap and blocking, but loadings above 1.0 wt% increase visible haze in translucent sheet. Plasticizer such as acetyl tributyl citrate at 3–7 wt% lowers glass transition and improves impact, but reduces heat deflection temperature and may elevate migration risk in fatty food contact.

    Plug-assisted thermoforming from sheet with residual moisture ≤300 ppm is conducted at 90–110°C. Below 90°C, brittleness and microcracks occur at the plug surface; above 110°C, sag-driven thinning in the plug contact zone exceeds 15%. PLLA has lower melt strength than amorphous PET or polystyrene, so the thermoforming window is approximately 8–12°C for thin-gauge sheet. Sheet pre-dried 4 h at 60°C before forming prevents moisture-induced bubbles and surface splay. The resulting formed articles, such as cold-pack trays, bakery inserts, and cosmetics blisters, are not retortable and are limited to service temperatures below 55°C in hot-fill unless post-crystallized.

    Biaxially Oriented Film Crystallization and Barrier Property Trade-Offs

    Sequential biaxial stretching of PLLA 001 requires preheat between 70–85°C. Stretch ratios in the machine direction of 2.5–3.5 and transverse direction of 3.0–4.5 are achievable only if the cast prefilm has crystallinity below 5%. Draw speeds above 300%/s trigger stress-hardening but also increase film haze; below 100%/s, necking and gauge bands appear. Heat setting at 120–140°C for 10–30 s raises crystallinity to 35–45% and reduces free shrinkage to ≤3% at 100°C. A PDLA nucleator at 0.5–1.0 wt% can accelerate crystallization during heat setting, but excessive addition above 1.5 wt% forms stereocomplex gels that increase melt viscosity and die pressure.

    Published data specific to PLLA 001 are limited; the tabulated ranges reflect semicrystalline PLLA homopolymers characterized according to ASTM D882-18 and ASTM F1249-20. Biaxially oriented PLLA film shows tensile modulus of 3.0–4.5 GPa and elongation at break of 20–60%, which supports twist wrap and fresh produce films. Oxygen transmission rate at 23°C and 0% RH is approximately 300–600 cm³/m²·day·atm for 25 µm film, suitable for modified atmosphere packaging of cut fruit. Water vapor transmission rate at 38°C and 90% RH can exceed 150 g/m²/day, limiting use in dry snack packaging unless metallized or coated. The biaxial orientation process creates a thin, translucent film with low haze when MD/TD draw ratio imbalance is kept below 1.2:1.

    Biaxial process variableTypical working rangeTest method / equipment
    MD draw ratio2.5–3.5Tenter frame draw control
    TD draw ratio3.0–4.5Tenter frame draw control
    Preheat temperature70–85°CIR pyrometer / heated roll
    Heat setting temperature120–140°CTenter oven zone
    Crystallinity after setting35–45%DSC, ISO 11357-3:2018
    Film tensile modulus3.0–4.5 GPaASTM D882-18
    Film elongation at break20–60%ASTM D882-18
    WVTR, 25 µm film100–300 g/m²/dayASTM F1249-20

    Paperboard extrusion coating with PLLA 001 as a liquid barrier layer is run at melt temperature 195–210°C, with an air gap of 100–200 mm and chill roll at 15–20°C. Adhesion to clay-coated board fails below 180°C actual melt temperature due to insufficient surface oxidation; however, above 220°C molecular weight degradation produces pinholes. The practical coating weight is 15–30 g/m²; weights above 35 g/m² increase curl. Heat seal initiation occurs at 95–110°C, but hot tack strength remains lower than LDPE. Seal strength measured by ISO 11339 typically falls between 3–6 N/15 mm for coated board. The barrier is appropriate for cold liquid paper cups, food trays, and sandwich boards, but not for retort or hot-fill above 60°C. Residual lactide migration and overall migration must be measured under EU 10/2011 if direct food contact is claimed; compostability of the coated board requires EN 13432:2000 validation with the paper fiber component included.

    Extrusion coating formulations may include a color masterbatch at 2–4 wt% or adhesion promoter at 1–2 wt% where clay-coating bond strength is marginal. Avoid filler addition above 3 wt% because pinhole frequency increases at thin coating gauges. Screw recovery with L/D 24:1–30:1 and a barrier mixing section is recommended to reduce melt temperature gradients. The production bottleneck is not extrusion output but loss of adhesion when paperboard moisture exceeds 8%; boards must be pre-conditioned at 23°C and 50% RH for 48 h before coating.

    Fused Filament Fabrication With Translucent PLLA 001 Requires Sub-450 ppm Moisture

    Moisture uptake during warehouse storage in non-dried resin totes is the dominant cause of filament diameter fluctuation and brittleness. Filament extruded from PLLA 001 requires pre-drying to ≤450 ppm moisture before extrusion into 1.75 ± 0.05 mm or 2.85 ± 0.05 mm filament. A single-screw extruder with L/D 24:1–30:1 and a melt pump is recommended. Melt temperature at the die is 190–205°C. Water bath cooling at 25–35°C produces amorphous filament; annealing at 100°C for 30 min raises crystallinity and shifts heat deflection temperature from 52°C to 85–110°C by ISO 75-2:2013 method B. Impact modifier such as polybutylene succinate or polycaprolactone at 5–10 wt% reduces brittleness in printed parts, but lowers modulus and HDT proportionally.

    During printing, nozzle temperature 205–215°C and bed temperature 55–65°C provide layer adhesion; chamber temperature above 35°C reduces warping. Dimensional stability under heated build plate conditions is governed by the glass transition near 60°C. Filament diameter variation greater than 0.07 mm jams in counter-rotating extruder gears and produces under-extrusion defects. The printed articles are used for short-run medical models, packaging prototypes, and compostable display components. No food contact claim is automatic from filament compostability; low-VOC performance and REACH compliance must be verified at the finished filament level.

    When PLLA 001 Is Meltblown into Nonwoven Webs at Die Temperatures Above 220°C

    Spunbond and meltblown lines processing PLLA 001 experience rapid viscosity loss at die temperatures above 220°C; spinneret pressure fluctuations above ±5% cause fiber diameter variability and shot defects. Throughput per spinneret hole is kept at 0.4–0.8 g/hole/min for stable spunbond filament. Quench air at 10–20°C and 60–80% RH accelerates cooling and reduces filament tack. Bonding calender roll temperatures of 100–120°C produce nonwoven tensile strength measured by EN ISO 9073-2 of 20–60 N/5 cm for 30–80 g/m² web. Hydrolytic stability limits wet-laid or agricultural applications to service temperatures below 60°C; compostable claims still require EN 13432:2000 validation on the finished nonwoven. Finished products include compostable tea bags, wet wipes, and agricultural mulching webs.

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    Certification & Compliance
    More Introduction

    Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin is an unfilled poly(L-lactic acid) grade supplied as cylindrical pellets for melt-processing operations that require a combination of high optical clarity, rigid thermoplastic behavior, and industrial compostability. The PLLA designation indicates a predominantly L-lactide stereochemical repeat unit; industrial PLLA homopolymers of this class usually contain an L-lactide fraction above 95 % and exhibit a glass transition near 55–60 °C and a melting endotherm near 150–175 °C when annealed. Because the grade is unfilled and translucent rather than water-clear, it is normally specified for moulded articles in which low haze and visible-light transmittance are functional requirements but where a slight diffuse transmission is acceptable. Density for unfilled PLA of this type is reported in public technical literature between 1.24 g/cm³ and 1.26 g/cm³; grade-specific values for Natureplast PLLA 001 should be taken from the supplier certificate of analysis, as published data for this exact commercial configuration are limited.

    Table 1 presents typical property ranges for unfilled injection-moulding PLA grades reported under standard test conditions. These ranges are not grade-specific acceptance limits for Natureplast PLLA 001 but provide the industrial baseline against which the certificate of analysis can be compared.

    PropertyTest methodTypical unfilled PLA range
    Melt mass-flow rate at 190 °C, 2.16 kgISO 1133-110–30 g/10 min
    DensityISO 1183-11.24–1.26 g/cm³
    Tensile strength at yieldISO 527-245–70 MPa
    Tensile modulusISO 527-23000–3500 MPa
    Elongation at breakISO 527-22–6 %
    Flexural modulusISO 1782800–3500 MPa
    Notched Izod impact at 23 °CISO 1802–4 kJ/m²
    Heat deflection temperature at 0.45 MPaISO 75-2/B45–60 °C

    The model designation PLLA 001 distinguishes the unfilled translucent base resin from compounded, filled, or coloured grades in the supplier’s product range. In production, the resin is used where a controlled melt flow and consistent pellet geometry are required for gravimetric dosing, especially in central material-handling systems feeding multiple injection lines.

    What Processing Boundaries Define the PLLA 001 Moulding Window?

    Melt processing of this resin is constrained by two competing degradation mechanisms: moisture-induced hydrolysis and thermal chain scission. The resin must be dried to below 250 ppm residual moisture before melt processing. Desiccant drying at 80 °C for 4 h with a dew point of −40 °C is the standard industrial starting point; at ambient relative humidity above 60 %, dried pellets should remain in a closed-loop desiccant hopper or be conveyed under dry air. If residual moisture exceeds 250 ppm, ester linkages hydrolyze during plastication, producing an intrinsic-viscosity drop and a measurable increase in melt flow rate. Screw plastication should use a general-purpose injection screw with an L/D ratio of 24:1 to 30:1 and a compression ratio of 2.5:1 to 3.0:1. Barrel temperature profiles typically range from 170 °C in the feed zone to 210 °C at the metering zone and nozzle; melt temperatures above 220 °C accelerate random chain scission and acetaldehyde generation. In production equipment, hold-up spots in hot-runner manifolds or poorly swept screw tips are the most common failure modes causing yellowing, black specks, and intermittent short shots.

    For thin-wall injection moulding of translucent PLLA 001, mould temperature is the principal lever controlling optical appearance and cycle time. At mould temperatures of 25–60 °C, the part solidifies with low crystallinity and high transparency; at 80–120 °C, crystallization increases haze but elevates heat resistance. Injection pressure is typically 80–140 MPa, with hold pressure 60–80 % of the filling pressure and back pressure 0.3–0.7 MPa. Cavity pressure for thin-wall multicavity tools is often designed for 30–50 MPa, which requires clamp force calculations based on projected area rather than material flow alone. Rheological characterization for incoming quality control uses capillary rheometry at 190 °C with shear rates from 100 s⁻¹ to 1000 s⁻¹; injection-grade unfilled PLA typically shows shear-thinning behavior with a viscosity reduction of 40–60 % over that range. This shear sensitivity is lower than that of many polypropylene grades but sufficient to fill thin-wall cavities at moderate injection speed.

    Compared with high-viscosity film and sheet extrusion PLA grades, the PLLA 001 moulding grade is designed with a lower melt viscosity and a narrower molecular-weight distribution. This difference reduces die swell, improves knit-line strength in multi-gate injection tools, and permits shorter holding-pressure times in thin-wall parts. In contrast, the same rheological profile reduces melt strength in blown-film and deep-draw thermoforming operations; the material is therefore not a direct substitute for high-molecular-weight PLA film grades or for polylactide copolymers containing D-lactide. Copolymerized or D-lactide-containing grades typically exhibit slower crystallization and lower potential crystallinity, which can improve clarity but reduce heat resistance. The PLLA homopolymer backbone of PLLA 001, with its higher stereo-regularity, can achieve greater maximum crystallinity after annealing, but its crystallization rate remains moderate. Unannealed moulded parts are amorphous and translucent; annealed parts become more opaque and dimensionally stable. Stereocomplex PLA grades can exceed the melting point of PLLA homopolymer by 40–50 °C, but they require equimolar PLLA/PDLA blending; PLLA 001 does not inherently provide this performance.

    Typical applications for Natureplast PLLA 001 Translucent Compostable Polylactic Acid Resin are rigid single-use foodservice items, transparent clamshells, compostable cutlery, dairy packaging inserts, agricultural clips, and rigid cosmetic packaging. Thin-wall parts with wall thickness below 1.5 mm are processed on conventional reciprocating-screw injection moulding machines with shut-off nozzles and positive sprue break; melt temperature, mould temperature, and hold pressure are adjusted per cavity geometry. The resin is also used as a base resin for melt-compounded 3D printing filament where a controlled melt flow index is required. For each finished article, compostability certification is specific to the part geometry and wall thickness; certification of the resin alone does not automatically extend to the finished article.

    Compostability Certification and End-of-Life Compliance Checklist

    Industrial compostability claims for this resin are evaluated under the full requirements of EN 13432:2000, ASTM D6400, or ISO 17088:2021. Under these specifications, the material must undergo 90 % biodegradation within 180 days in controlled composting, 90 % disintegration within 12 weeks, and the resulting compost must pass ecotoxicity testing according to OECD 208. The translucent PLLA 001 grade is not a marine biodegradable material, and it should not be represented as such; degradation in ambient seawater at temperatures below 30 °C is substantially slower than in industrial composting at 58 °C.

    Standard or regulationScopeTypical threshold for PLA
    EN 13432:2000Industrial compostability of packaging90 % biodegradation in 180 days; 90 % disintegration in 12 weeks
    ASTM D6400Specification for compostable plastics90 % biodegradation; 90 % disintegration
    ISO 17088:2021Specification for compostable plasticsSame biodegradation and disintegration framework
    EU 10/2011Food-contact migration framework for finished articlesOverall migration <10 mg/dm² for the finished article
    REACHRegistration and SVHC declarationSVHC content <0.1 % w/w per candidate declaration

    Food-contact suitability is not established by the resin designation alone; the finished article must be tested for overall migration under EU 10/2011 or the applicable national regulation. REACH compliance is documented through a supplier statement if the grade contains no substance of very high concern above 0.1 % w/w; the downstream converter is responsible for confirming this for the specific import and compounding route.

    Optical Clarity and Crystallization Kinetics in Thin-Wall Moulding

    Transparency in PLLA 001 parts is retained when the melt is cooled rapidly from a melt temperature of 190–210 °C to a mould temperature below the glass transition. Under these conditions, the polymer solidifies before spherulites grow to a size that scatters visible light; total luminous transmittance of amorphous unfilled PLA at 1.5 mm thickness is commonly reported between 85 % and 90 %, with haze below 10 %. The translucent character of PLLA 001 indicates that some superficial scattering is present; this can arise from pellet-surface crystallinity, minor residual monomer, or processing-induced thermal history. The optical appearance is therefore controlled more by mould temperature and cooling time than by the resin alone.

    Annealing at 80–100 °C for 30 min increases crystallinity and heat resistance but raises haze and may produce dimensional shrinkage. The crystallization half-time of PLLA homopolymer is longest near the glass transition and shortest near 105–115 °C; therefore, annealing below 70 °C is generally inefficient, while annealing above 120 °C can cause warpage in unconstrained parts. If crystallized parts are required, fixtured annealing is necessary to maintain flatness and cavity-to-cavity dimensional stability. Mould shrinkage for unfilled PLA in flow direction is typically 0.3–0.5 % and cross-flow 0.3–0.5 %; anisotropic shrinkage is less pronounced than in semi-crystalline polyolefins. Post-mould shrinkage can occur at temperatures above 60 °C if parts are not annealed.

    When Moisture Uptake Exceeds 250 ppm Before Melt Processing

    Moisture excursions above 250 ppm produce failures that are visible first as silver streaks and splay in thin-wall moulded parts, followed by increased brittleness and a drop in melt viscosity. In production monitoring, the melt flow rate after drying should be compared with the virgin resin value; a shift higher than the supplier specification by more than 10 % usually indicates hydrolytic degradation. On twin-screw compounding lines with L/D ratios above 40:1, the same moisture threshold applies before any melt blending with nucleating agents or impact modifiers. The resin should not be melt-compounded with water-releasing fillers, alkaline minerals, or amine-based additives unless the additive system is pre-dried and pH-neutral; residual alkalinity accelerates ester hydrolysis and shifts the molecular-weight distribution toward lower molar mass. If dried pellets are stored in open containers for more than 15 min in a high-humidity production hall, re-drying is required.

    Thermal degradation in PLA follows pseudo-first-order random chain scission at melt temperatures above 200 °C; the rate is influenced by residual catalyst metals, moisture, and shear heating. In injection moulding, the melt temperature is frequently 10–20 °C higher than the barrel set point due to viscous dissipation at screw speeds above 150 rpm; therefore, barrel set-point reduction is often required when melt residence time exceeds 5 min. Published activation-energy values for PLA thermal degradation are commonly reported near 80–120 kJ/mol; these values should be treated as relative indicators because commercial stabilizer packages and residual lactide alter the apparent rate.

    Chemical resistance of PLLA 001 is similar to other unfilled PLA grades. The material resists aliphatic hydrocarbons and oils but is attacked by strong acids, strong bases, and polar solvents; sustained contact with water above 60 °C causes progressive hydrolysis. Hot-fill applications above 60 °C are outside the normal operational boundary unless the part is crystallized and dimensionally stabilized by annealing. Acetaldehyde generation during melt processing should be monitored for food-contact packaging because it can affect sensory properties; low shear rates and short residence times below 220 °C are the primary control measures. Published data for this specific commercial configuration are limited; the supplier certificate of analysis and processing guide remain the controlling documents for grade-specific limits.

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