Boxa Chemical Group Ltd

Products

Ingeo Polylactic Acid (PLA) 4060D

    • Product Name: Ingeo Polylactic Acid (PLA) 4060D
    • Factroy Site: No. 100, Qinhuai Road, Jiangning District, Nanjing, Jiangsu, China
    • Price Inquiry: sales4@ascent-chem.com
    • Manufacturer: Boxa Chemical Group Ltd
    • CONTACT NOW
    Specifications
    HS Code 683299
    Polymertype Polylactic Acid (PLA)
    Physicalform Pellets
    Appearance Transparent, amorphous
    Density 1.24 g/cm3
    Meltflowrate 10-14 g/10 min at 210 deg C and 2.16 kg
    Glasstransitiontemperature 55-60 deg C
    Meltingpoint None (amorphous)
    Vicatsofteningtemperature 55 deg C
    Tensilestrength 70 MPa
    Tensilemodulus 3.5 GPa
    Elongationatbreak 2.5%
    Flexuralmodulus 3.6 GPa
    Notchedizodimpact 2.7 kJ/m2
    D Isomercontent ~12%
    Biobasedcontent 100% renewable carbon

    As an accredited Ingeo Polylactic Acid (PLA) 4060D factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Ingeo Polylactic Acid (PLA) 4060D comes in 25 kg moisture-barrier foil-lined bags, palletized for industrial shipment.
    Container Loading (20′ FCL) Non-hazardous Ingeo PLA 4060D loaded in 20′ FCL, in 25 kg bags on pallets; keep dry, cool, ventilated, and protected from moisture.
    Shipping Ingeo PLA 4060D is a non-hazardous polylactic acid resin. It is typically shipped in sealed moisture-barrier bags, boxes, or supersacks under ambient conditions. No DOT, IMDG, or IATA classification applies. Transport in a cool, dry area away from heat, moisture, and direct sunlight.
    Storage Store Ingeo Polylactic Acid (PLA) 4060D in a cool, dry, well-ventilated area away from heat, ignition sources, and direct sunlight. Keep containers tightly closed to prevent moisture absorption, which can degrade the resin. Recommended storage below 30°C and at low humidity. Avoid acids, bases, oxidizers, and prolonged UV exposure. Follow supplier recommendations.
    Shelf Life Typically 12 months when stored unopened in original packaging under cool, dry conditions, away from moisture and heat.
    Application of Ingeo Polylactic Acid (PLA) 4060D

    In tenter-frame biaxially oriented film production, Ingeo PLA 4060D is dried at 80°C to a residual moisture below 250 ppm using desiccant dryers with a supply air dew point of -40°C or lower. The resin is extruded through a coat-hanger die at melt temperatures of 200–220°C onto a chill roll held at 15–25°C to suppress spherulitic growth and retain a low-crystallinity preform. Sequential orientation typically applies a machine-direction stretch ratio of 2.8–3.2 on a roll stack where preheat roll surface temperatures are maintained within ±3°C of the target, commonly 60–70°C, to avoid sticking and neck-in; transverse orientation then occurs in a tenter oven at 65–80°C at a ratio of 3.0–3.5. The narrow thermoplastic window arises because the grade’s D-lactide content suppresses fast crystallization, and orientation below 55°C initiates craze-like microvoids, while excursions above 85°C create gauge nonuniformity and transverse sag. Heat-setting at 120–140°C for 8–15 s can increase dimensional stability, but it reduces shrink potential and increases haze unless a discrete nucleating agent such as talc at 0.5–1.0 wt% is compounded at controlled letdown. Tensile properties are measured according to ISO 527-3 or ASTM D882; oriented 4060D films commonly show machine-direction tensile modulus in excess of 2 GPa, though published data for this specific configuration is limited by line-specific draw ratio and heat-set profile. End products include clear twist wrap, laminated label face stock, and high-gloss overwrap where deadfold and printability are more important than moisture barrier.

    Orientation process variableTypical rangeTest or control basis
    Residual moisture before extrusion< 250 ppmISO 15512 / inline infrared
    Melt temperature at die exit200–220°CIR pyrometry
    Chill-roll temperature15–25°CPreform crystallinity and gloss
    MD preheat roll temperature60–70°C, ±3°C toleranceSequential draw ratio 2.8–3.2
    TD tenter oven temperature65–80°CTransverse draw ratio 3.0–3.5
    Heat-set temperature120–140°C for 8–15 sDimensional stability requirement
    Resulting film tensile modulus> 2 GPa typicalISO 527-3 / ASTM D882
    Haze and clarityApplication-specificASTM D1003 / ISO 14782

    How Does Hot-Tack Decay Limit Seal Dwell on Coextruded Lidding?

    A coextruded lidding web using 4060D as the sealant skin is designed around the grade’s lower seal initiation temperature, which is typically 20–30°C below that of semi-crystalline PLA grades, but seal strength remains dependent on sealing pressure, dwell time, and jaw temperature. A three-layer ABA structure may combine a 4060D sealant layer at 8–15 µm with a semi-crystalline core for stiffness and a corona-treated print surface. Seal jaws at 90–110°C, 3–5 bar, and 0.4–0.8 s dwell produce seal strengths of 8–15 N/25 mm when tested according to ASTM F88/F88M, but hot-tack strength decays rapidly above 100°C because the molten sealant has low melt elasticity and long chain relaxation times. Additive selection is restricted: erucamide slip at loadings above 0.10 wt% migrates to the seal surface and reduces coefficient of friction below 0.30, but produces seal-strength cliff-edge losses, while silica antiblock above 0.25 wt% can increase seal initiation temperature by thermal insulation. Seal-through-contamination performance is inferior to polyolefin sealants because PLA does not wet greasy or particulate contamination; pack styles with high product residue require a higher sealant thickness or a peelable seal formulation. Compliance for indirect food contact uses EU 10/2011 and the resin supplier’s food-contact statement, with specific migration testing on the finished laminate because printing ink and adhesive layers alter overall migration. The sealant film is also sensitive to moisture-induced hydrolysis during storage; re-drying of regrind is necessary if ambient relative humidity exceeds 60% for more than 24 h. End products are produce lidding, dairy cup lidding, and compostable dry food pouches where the seal is processed at lower temperatures than polypropylene but is not intended for retort or hot-fill above 80°C.

    When 4060D Replaces LDPE in Paperboard Extrusion Coating

    When 4060D is processed on an extrusion coating line for bleached paperboard, the melt curtain is extruded at 230–250°C through a slot die with a die gap of 0.5–0.8 mm, but the higher melt viscosity relative to LDPE necessitates a shorter draw distance and tighter air-gap stability control. Adhesion to board relies on oxidation and surface pre-treatment rather than autoxidative bond formation: a corona pre-treatment of the board above 42 mN/m or a thin water-based primer is required because PLA lacks the polar adhesion equivalent of oxidized LDPE. A coating weight of 15–25 g/m² provides acceptable liquid holdout for cold cups and food trays, but the water-vapour transmission rate remains higher than LDPE-coated board, typically in the range 80–120 g/m²/day at 38°C and 90% RH for a 25 g/m² coating when measured according to ASTM F1249; published data for this specific configuration is limited by baseboard type and pinhole density. Edge trim and startup scrap can be reprocessed only after drying to below 250 ppm moisture; regrind levels above 20 wt% increase die-lip deposit formation from lactide and degrade gloss. The end product is used for compostable sandwich boxes, cold-drink cups, and foodservice trays, but hot liquid above 60°C induces softening and lid deformation because the glass transition temperature is low. A compliance matrix for EU 10/2011 and EN 13432 should be verified on the coated sheet, not on resin alone.

    Shrink sleeve label stock based on 4060D is produced by cast film extrusion with a chill-roll temperature of 20–30°C, followed by low-temperature orientation to lock in internal stress. The final film is solvent-seamed into a sleeve using tetrahydrofuran or a suitable ester-based solvent, then passed through a steam tunnel at 70–85°C; shrink initiation is observed near 60°C, and maximum shrinkage exceeds 40% in the transverse direction at 80°C depending on draw ratio and annealing. Steam-tunnel temperature higher than 85°C produces smile defects and panel distortion on high-bead containers, while temperature lower than 65°C leaves excess shrink tension that can crush thin-walled PET bottles. Ink adhesion is a persistent failure mode: the low surface energy after orientation, typically 36–40 mN/m, requires inline corona treatment immediately before solvent or UV inkjet printing to reach a minimum dyne level of 48 mN/m for water-based systems. Shrink-sleeve scrap is not compatible with municipal recycling streams and should be handled by industrial composting only if the ink and seaming solvent are also certified under EN 13432. Applications include full-body shrink labels for beverages, tamper-evident bands, and multipack sleeves.

    Running 4060D as a Folding-Carton Window Film Without Solvent Adhesives

    Folding cartons with a die-cut window use 4060D film at 20–40 µm thickness inserted between board layers with heat-sealable adhesive or ultrasonic bonding. The film is pre-treated to a minimum surface energy of 42 mN/m and then anti-static coated; without anti-static treatment, dust attraction causes visible defects during high-speed placer feeding at speeds above 120 cartons/min. Tear resistance is the dominant mechanical constraint: Elmendorf tear values tested under ASTM D1922 are lower than those of biaxially oriented polypropylene, so die-cutting must use sharp, clean blades and avoid notch points in the window perimeter. Slip and antiblock masterbatch at 1–2 wt% letdown is used to prevent film blocking in storage, but the resultant silica surface pattern can reduce clarity and raise haze above 3% if the silica median particle size exceeds 5 µm. The window film is usually adhered with a water-based or hot-melt adhesive; solvent-based adhesives may etch the film surface and cause optical crazing. This application requires no high moisture barrier, and the end product is a compostable or optically clear carton for bakery goods where the window is not in contact with wet product. Because PLA has a low glass transition temperature, cartons exposed to storefront heat lamps above 50°C can show window sag.

    Compliance or test areaRelevant standard or regulationApplication-specific note
    Melt mass-flow rateISO 1133-1:2022210°C / 2.16 kg; verify against lot certificate
    Film tensile propertiesISO 527-3 / ASTM D882Oriented and cast film configurations only
    Seal strengthASTM F88/F88MFinished laminate, not resin pellet
    Hot-tack strengthASTM F1921Jaw temperature above 100°C requires reduced dwell
    Haze and clarityASTM D1003 / ISO 14782Affected by antiblock particle size and loading
    Surface energyASTM D2578Corona treatment required for ink and adhesive bonding
    CompostabilityEN 13432, ASTM D6400, ISO 17088Finished article must be re-certified with inks and coatings
    Food-contact verificationEU 10/2011, US FDA resin supplier FCN documentationSpecific migration testing on final multilayer structure

    Fresh-cut produce packaging uses 4060D as a clear, microperforated pillow-pouch or tray-lidding web. Anti-fog performance is achieved with a glycerol-ester additive at 0.3–0.6 wt% or a durable inline coating, because PLA has a high water contact angle after orientation and cold-room condensation obscures product visibility; the additive reduces surface tension below 40 mN/m but can plasticize the surface and lower seal strength if loading exceeds 1.0 wt%. Laser microperforation with 60–80 µm holes at a density of 8–15 holes/cm² adjusts oxygen and carbon dioxide transmission for cut lettuce or spinach, but perforation eliminates the already-moderate moisture barrier and makes the package unsuitable for long shelf life. The film is processed on a vertical form-fill-seal machine with seal jaw temperatures of 95–115°C; dwell times below 0.3 s produce visible channel leakers because the PLA melt does not flow into gusset folds as readily as polyethylene. Compostability certification under EN 13432 or ASTM D6400 must be repeated on the finished perforated film with ink and anti-fog coating; the base resin certification does not cover the converted article. End products include compostable salad bags, herb pouches, and cut-fruit lidding for chilled display below 5°C.

    Free Quote

    Competitive Ingeo Polylactic Acid (PLA) 4060D 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 sales4@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: sales4@ascent-chem.com

    Inquiry

    Get Free Quote of Boxa Chemical Group Ltd

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

    Certification & Compliance
    More Introduction

    Ingeo Polylactic Acid (PLA) 4060D is a non-compounded polylactide resin positioned in supplier technical documentation for biaxially oriented flat film, cast film, and light-gauge sheet. The grade is supplied as a pelletized thermoplastic aliphatic polyester produced by lactide ring-opening polymerization from plant-derived feedstocks. Density is published at 1.24 g/cm³ under ASTM D1505-18. Melt mass-flow rate is reported near 6 g/10 min at 210 °C and 2.16 kg piston load using ISO 1133-1:2022 or ASTM D1238-20. The polymer architecture incorporates a controlled fraction of D-lactide units, typically in the low single-digit molar range for film grades, which suppresses quiescent crystallization while retaining strain-induced crystallization during sequential or simultaneous biaxial stretching.

    The resulting balance places 4060D at the slower-crystallization end of the Ingeo portfolio compared with 3052D and 3251D injection grades. This distinction is not a performance defect; it is a process-selection criterion. In thick-walled injection parts, slow crystallization increases cycle time and complicates ejection. In tenter-frame film stretching, however, lower quiescent crystallization reduces premature haze development and permits the sheet to remain drawable across a broader preheat range before the cloud point transitions into brittle deformation. The grade is therefore selected less for melt-flow rate alone and more for its thermal-mechanical behavior during orientation.

    What Constraints Govern 4060D’s Melt Rheology During Extrusion?

    The extruder must manage a relatively narrow thermal window. PLA degrades by hydrolysis and lactide reformation if melt temperature at the die remains above 230 °C for prolonged residence. Below approximately 180 °C, the melt viscosity is high enough to create melt-pressure variation, flow marks, and poor die-web stability. Single-screw extruders with L/D 24:1 to 32:1, dual-flight barrier screws, and screen packs of 40/60/100 mesh are commonly deployed. Melt temperature measured at the adapter is typically maintained between 190 °C and 220 °C. The melt mass-flow rate near 6 g/10 min does not convey the complete shear-rate behavior; at screw speeds above 120 rpm, shear heating can add 15–20 °C to the melt in the metering zone. This can trigger lactide formation and gel particles if the barrel profile is not adjusted downward in the compression and metering sections.

    Moisture is the dominant process variable. PLA is hydrolytically sensitive, and pellet moisture above 0.04 wt% accelerates molecular-weight loss during the first extruder residence time. The failure mode on production equipment appears as progressive melt-pressure drift, die-lip plate-out, and lower oriented-film tear resistance. A melt-pressure transducer before the screen changer should be used to detect pressure loss that indicates viscosity loss. Pressure excursions greater than 15% from baseline are routinely traceable to wet resin, feed-bridging, or loss of dryer dew-point control. Because the resin is not normally compounded with chain extenders, the molecular-weight loss cannot be recovered downstream.

    Thermal Transition Values and High-Shear Stability

    Differential scanning calorimetry at 10 °C/min under ASTM D3418-21 typically identifies a glass transition between 55 °C and 60 °C, a cold-crystallization exotherm between 100 °C and 120 °C, and a main melting endotherm between 145 °C and 160 °C, depending on thermal history and D-lactide content. These values distinguish 4060D from high-optical-purity injection grades that can show a melting point at or above 165 °C. The lower melting point reduces the preheat temperature required for orientation but also limits the no-load upper-use temperature of unannealed film to approximately the glass transition range.

    Pre-drying is mandatory when pellet moisture exceeds 400 ppm. Desiccant-wheel drying at 80 °C for 4–6 h with a supply-air dew point of -40 °C or lower is typical. The target residual moisture is below 250 ppm as measured by ISO 15512:2019. Extended residence above 100 °C can cause pellet softening and bridging in the hopper, so dryer hopper design should avoid dead zones. In production areas where relative humidity exceeds 60%, the interval between dryer discharge and extruder feed should be minimized or a hopper dryer maintained on the feed throat. Batch-to-batch melt-flow-rate variation should be checked against the certificate of analysis because a shift from 5 to 7 g/10 min can alter die-web stability and stretching force in the machine direction.

    When 4060D Replaces 2003D or 4043D in Flat-Film and Tenter-Frame Processes

    4060D is not a drop-in replacement for 2003D in injection stretch blow molding. 2003D-grade preforms require a different reheat profile and higher melt strength to resist sagging under infrared heating. 4060D is formulated for flat film orientation where the sheet is quenched to a relatively amorphous state and then drawn in a tenter frame. Compared with 4043D, another film grade, 4060D is commonly selected where lower orientation temperature or increased draw at low preheat is required. 4043D may be referenced where higher melt stability and lower gel counts are required in high-line-speed cast film. Selection should be supported by film property tests under ASTM D1003-21 for haze, ASTM D882-18 for tensile properties, and ASTM D1922-23 or ISO 6383-2 for tearing resistance.

    Injection-grade resins such as 3052D and 3251D are designed for fast quiescent crystallization and high mold-flow. 4060D has lower optical purity and slower crystallization, making it less suitable for high-cavitation injection tools where cycle-time economics depend on ejection after seconds rather than minutes. The practical difference is most visible in thick sections: an injection-grade part can develop crystallinity during cooling, whereas 4060D would remain largely amorphous and dimensionally unstable if used outside its intended thin-film process window.

    Grade Primary processing route Differentiating processing characteristic Typical test basis
    4060D Biaxially oriented film, tenter-frame stretching Controlled D-lactide fraction for slow quiescent crystallization ISO 1133-1:2022, ASTM D3418-21
    4043D Biaxially oriented cast film Higher melt stability at high line speed; low-gel tendency ASTM D1003-21
    2003D Injection stretch blow molding Higher melt strength during preform reheating ISO 1133-1:2022, ASTM D1238-20
    3052D Injection molding Faster crystallization in thick sections ASTM D3418-21

    Regulatory status depends on the finished article, not the resin alone. Food-contact assessment for European markets should be conducted under EU Regulation (EU) No 10/2011 as amended, with migration testing on the finished film. For United States markets, specific Ingeo grades are the subject of Food Contact Notifications; the current manufacturer’s letter should be consulted before using 4060D in food-contact layers. Biobased carbon content can be verified by ASTM D6866-21. Industrial compostability claims for printed film require certification of the finished article under EN 13432:2000 or ASTM D6400-21; the raw resin cannot claim compostability by itself. RoHS Directive 2011/65/EU may apply to electronic packaging films, and heavy-metal content should be verified against the supplier’s material declaration.

    On a sequential biaxial orientation line, 4060D pellets are extruded through a flat die and cast onto a chill roll maintained at 15–30 °C to minimize crystallinity and produce an amorphous pre-film. Machine-direction stretching is performed at 60–75 °C using differential roll speeds with draw ratios between 2.5:1 and 3.5:1. Transverse-direction stretching follows in a tenter frame at 70–85 °C with draw ratios between 3:1 and 5:1. The preheat window is narrow; excursions of ±5 °C commonly appear as uneven film thickness or transverse-direction draw bands. After orientation, heat-setting at 110–130 °C for a few seconds increases crystallinity and reduces shrinkage. Oriented films in the 15–50 µm range are then slit and wound. Tension control at winding must account for PLA’s lower surface hardness and higher electrostatic susceptibility relative to oriented polyester. Published data for this specific film configuration are limited because final properties depend heavily on draw ratio, heat-set residence time, and quench uniformity.