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Ingeo Polylactic Acid (PLA) 4032D

    • Product Name: Ingeo Polylactic Acid (PLA) 4032D
    • Factroy Site: No. 100, Qinhuai Road, Jiangning District, Nanjing, Jiangsu, China
    • Price Inquiry: sales4@ascent-chem.com
    • Manufacturer: Boxa Chemical Group Ltd
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    Specifications
    HS Code 811796
    Productname Ingeo Polylactic Acid (PLA) 4032D
    Chemicalname Polylactic acid
    Casnumber 26100-51-6
    Meltingtemperature C 155-170
    Glasstransitiontemperature C 55-60

    As an accredited Ingeo Polylactic Acid (PLA) 4032D factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Ingeo PLA 4032D is typically packed in 25 kg moisture-barrier-lined paper bags, palletized and stretch-wrapped for industrial shipment.
    Container Loading (20′ FCL) Ingeo Polylactic Acid (PLA) 4032D loaded as palletized 25 kg bags, shrink-wrapped and secured in a dry 20′ FCL.
    Shipping Ingeo Polylactic Acid (PLA) 4032D is a non-hazardous, solid polymer supplied as pellets. It is normally shipped in sealed moisture-barrier bags, cartons, or supersacks on pallets. No UN number, hazard class, or transport placards are required. Keep dry and below recommended temperatures; avoid excessive heat and moisture.
    Storage Store Ingeo PLA 4032D in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid prolonged storage at elevated temperatures. Follow supplier recommendations, and dry the resin before melt processing if moisture exceeds specification.
    Shelf Life Shelf life is 12 months from manufacture if stored unopened below 50°C and 50% relative humidity, protected from moisture.
    Application of Ingeo Polylactic Acid (PLA) 4032D

    Sequential-stenter biaxial orientation of Ingeo 4032D begins with cast sheet quenched to an amorphous state on a polished roll stack maintained at 25–35°C. Raw polymer is pre-dried in desiccant hoppers at 80°C for 4 h to a moisture ceiling of ≤250 ppm because hydrolysis at melt temperatures 190–210°C reduces intrinsic viscosity and generates gel specks in the machine-direction orientation unit. Routine incoming-lot melt-flow qualification follows ASTM D1238 at 210°C/2.16 kg against the supplier specification, while cast sheet tensile is measured according to ISO 527-3. The sheet enters an MDO where infrared heaters raise the film surface to 65–75°C, and primary MD draw ratios are held between 2.8:1 and 3.2:1; transverse stretching on the tenter clips then applies a TD draw ratio of 3.0:1–4.0:1 at 70–85°C. Heat-setting follows at 120–140°C to raise crystallinity and control shrink. Formulation additions for BOPLA food-contact film are restricted by slip migration and seal-integrity concerns: the usual functional loadings are silica antiblock masterbatch at 0.8–1.2 wt% and erucamide-free polymeric slip at 0.5–1.5 wt% of the film layer, while inline corona treatment is set to 42–46 mN/m for lamination or print anchorage. Industry compliance for direct food contact in the EU is assessed under EU Regulation (EU) No 10/2011, with an overall migration limit of ≤10 mg/dm² depending on simulant; industrial compostability claims require EN 13432 certification, including 90% biodegradation within 180 days under aerobic composting conditions. The final laminate must be re-tested because barrier coatings and adhesives alter disintegration behaviour. Terminal product types produced from this route include clear window bread bags, fresh-cut salad overwrap, bakery box windows, and printed laminate outer webs where low haze and dead-fold are functional requirements.

    Table 1. Sequential-stenter BOPLA setpoint band and associated deviation signature for Ingeo 4032D
    ZoneSetpoint bandDeviation signature
    Cast roll quench25–35°CFilm above 35°C forms crystalline nuclei; surface below 20°C picks up condensation haze
    MDO preheat65–75°C±5°C variance creates longitudinal thickness bands and MD draw resonance
    TDO stretch70–85°C; draw 3.0:1–4.0:1Above 85°C web sags from clip; below 70°C stress-whitening and clip breaks increase
    Heat-set120–140°CBelow 110°C residual shrinkage rises; above 150°C surface degradation and plate-out occur

    Thermoformed Sheet Gauge Control and Trim Reincorporation

    Extruded sheet production for dairy and deli containers uses a single-screw extruder with L/D 36:1 and a general-purpose barrier screw, feeding a coat-hanger sheet die at melt temperature 200–215°C; melt pressure before the screen changer is maintained below 250 bar to avoid shear-induced viscosity loss. The melt enters a vertical three-roll calendering stack with roll temperatures 45–60°C top, 35–45°C middle, and 20–30°C bottom, producing sheet thickness from 300 µm to 900 µm. Formulation for thermoforming-grade sheet includes a non-phthalate impact modifier at 3–8 wt%, a nucleating agent masterbatch at 0.1–0.3 wt%, and antiblock at 0.2–0.5 wt%; plant regrind from skeletal scrap is reincorporated at ≤30 wt% of total feed because higher ratios increase gel counts and yellowness from multiple heat histories. The sheet is then fed to contact-heat pressure formers with plug assist; optimal sheet surface temperature is 85–105°C, measured by IR pyrometry, and plug temperature is held 10–15°C below the sheet set-point to reduce stick-slip marking. Production bottlenecks on rapid cycling lines involve sheet sag between oven zones and edge trim adhesion to the calendering stack; gauge variation is controlled by closed-loop die-bolt adjustment against a scanning beta gauge, with ±3% transverse gauge variance considered the upper limit for stable cutting and sealing. Compliance includes EU Regulation (EU) No 10/2011 for overall migration and, where the containers are marketed as compostable, EN 13432 disintegration and ecotoxicity testing; U.S. food-contact status for the formulated article is confirmed through the current Food Contact Notification inventory for the final resin/additive combination rather than by generic resin compliance. Terminal product types include refrigerated dairy cups, bakery clamshells, clear deli trays, and cold-food sample cups.

    Why Does Cast Film Web Stability Collapse Above 200°C?

    The primary instability in cast PLA web processing is not thermal degradation but the abrupt loss of melt elasticity when the melt stream exceeds 200°C; as the polymer exits the slot die onto a polished chill roll, high temperature lowers extensional viscosity and increases neck-in from the die lip, producing edge beads that later tear during slitting. A stable cast line for Ingeo 4032D therefore operates with adapter and die temperatures 185–200°C, chill roll temperature 15–25°C, and air-gap distance 10–20 mm; electrostatic pinning is applied at 2–4 kV across the web width to suppress frost-line movement and air entrapment. The base resin is compounded with a slip/antiblock masterbatch at 0.5–1.5 wt% and a processing aid at 0.2–0.5 wt% to reduce die-lip build-up, while optical clarity is maintained by avoiding high-crystallinity nucleants. Ink and coating systems must avoid strong amine carriers because alkaline species accelerate PLA ester hydrolysis at the film surface. Downstream production includes slitting and either solventless lamination or water-based printing; film thickness is typically 30–50 µm for label face stock and 50–90 µm for lamination webs. The compliance framework for these films is EU Regulation (EU) No 10/2011 with specific migration testing for lactic acid and any slip additive; for printed or laminated structures, the finished article must also comply with the appropriate national printing-ink regulations, and compostability claims require EN 13432. Terminal products include transparent label face stock, floral wrap, envelope windows, and non-food lamination carriers where high gloss and low heat-seal initiation are advantageous.

    After cast rollstock is slit to the sleeve printing width, the PLA web is passed through a heated transverse-direction stenter that stretches the film 3.5:1–4.5:1 in the TD axis while allowing 5–10% MD relaxation; the drawn web is then quenched below 45°C to freeze orientation. For sleeve substrates, the formulation differs from standard BOPLA because controlled shrink requires a low-crystallinity quenched precursor and a plasticizer content up to 5 wt%, typically a citric ester, to lower the shrink onset temperature to 60–70°C. The final sleeve exhibits TD shrink of 60–75% in a 70°C water bath, measured by immersion shrinkage testing according to ISO 11501:1995 or equivalent internal method; printed sleeves must maintain ink adhesion after steam tunnel recovery. Deep-dive control is required because excessive plasticizer levels above 6 wt% cause blocking on the unwind and registration drift in the seaming step, while insufficient plasticizer raises shrink onset above 75°C and prevents complete label recovery on cold-fill beverage bottles. Industrial compliance for sleeve film includes EU Regulation (EU) No 10/2011 for indirect food contact where the sleeve is removed before consumption, REACH SVHC screening for plasticizer and pigment substances, and brand-specific heavy-metal limits under the EU Packaging and Packaging Waste Directive 94/62/EC Article 11 limits for lead, cadmium, mercury, and hexavalent chromium totaling ≤100 ppm. Terminal product types include full-body shrink sleeves for beverage cans, tamper-evident neck bands, and promotional multi-pack bands.

    Stabilising Cell Morphology in Low-Density PLA Foam

    Low-density PLA foam for meat trays and cushioning is produced on a tandem extruder where the first stage melts and devolatilizes the Ingeo 4032D resin, and the second stage cools the melt to 150–165°C before injection of a physical blowing agent such as food-grade CO₂ at 3–5 wt%. Linear PLA has inadequate strain hardening to prevent cell wall rupture during pressure drop at the die; therefore, a chain-extension masterbatch based on an epoxy-functional styrene-acrylic oligomer is added at 0.3–0.7 wt%, and talc nucleation is introduced at 0.5–1.0 wt%. The die is a capillary or coat-hanger design with controlled pressure drop to produce open-cell or closed-cell morphology; nucleant particle size, blowing agent loading, and die temperature interact such that a die temperature increase of only 5°C shifts the foam from closed-cell plateau to open-cell collapse due to reduced melt strength. Products are annealed in a hot air tunnel at 100–120°C to crystallize the cell walls and raise the heat deflection temperature. The terminal parts include PLA foam meat trays, protective corner blocks, and short-distance transport cushioning; these applications are tested for compliance with EN 13432 if compostability is claimed, and food-contact compliance is assessed under EU Regulation (EU) No 10/2011 with attention to blowing-agent residuals and chain-extension degradation products. Published data for specific line configurations at high output are limited, so the stated ranges must be validated on the installed tandem extrusion line.

    When 4032D Replaces Fossil-Based PS in Blister Packaging

    When transparent blisters are converted from general-purpose polystyrene sheet to Ingeo 4032D sheet on the same thermoforming line, the first operational shift concerns the thermoforming temperature window; GPPS sheet can be formed at surface temperatures around 110–125°C, whereas PLA sheet requires 85–105°C, and the plug material must be changed from aluminium to syntactic polyamide or coated wood composite to avoid abrupt chill marks. A nucleated 4032D sheet formulation for blister packaging is compounded with impact modifier at 4–8 wt%, nucleant at 0.2–0.4 wt%, and antistatic masterbatch at 0.5–1.0 wt% for downstream automated dew of hinged packs. The sheet is extruded at 200–210°C and then pressure-formed with cavity pressure 4–6 bar, using plug assist to redistribute the sheet wall; corner radius limits are ≥0.5 mm to prevent stress-whitening, and sidewall draft angles are increased by 1–2° relative to PS to aid demolding. The resulting blisters are sealed to printed paperboard or RPET lidding with heat-seal coatings that activate at 90–100°C. Compliance for non-food consumer articles focuses on REACH SVHC screening, EN 71-3 migration of specific elements where the packaging may be accessed by children, and packaging heavy metal limits under 94/62/EC; food-contact blisters require EU Regulation (EU) No 10/2011 overall migration testing on the final lidding and sealant combination. Terminal products include transparent consumer-electronics blisters, personal-care sachet housings, stationery clamshells, and point-of-sale security packs.

    Table 2. Compliance verification matrix by downstream application
    ApplicationPrimary EU regulationAdditional standard/methodCritical test parameter
    BOPLA food filmEU Regulation (EU) No 10/2011EN 13432Overall migration ≤10 mg/dm²; disintegration 12 weeks; biodegradation 90% in 180 days
    Thermoformed dairy/deli sheetEU Regulation (EU) No 10/2011EN 13432Overall migration simulant D1; ecotoxicity after compost
    Cast film labels and laminationEU Regulation (EU) No 10/2011ISO 527-3Specific migration of lactic acid and slip additives; tensile after print
    Shrink sleeve labelEU Regulation (EU) No 10/2011ISO 11501:1995; 94/62/EC Article 11Shrink onset 60–70°C; heavy metals ≤100 ppm
    PLA foam cushioning and trayEU Regulation (EU) No 10/2011EN 13432Overall migration; foam density via ISO 845; biodegradation
    Blister packagingREACH; EU Regulation (EU) No 10/2011 for foodEN 71-3; 94/62/EC Article 11Specific element migration; heavy metals ≤100 ppm
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    Certification & Compliance
    More Introduction

    Ingeo Polylactic Acid (PLA) 4032D is a crystallizable poly(L-lactic acid) resin supplied for biaxially oriented film production, particularly twist-wrap, label, and lamination structures. The grade designation 4032D is associated with a D-lactide content of 2.0 mol%, a melt flow rate of 7 g/10 min at 210 °C/2.16 kg, and a specific gravity of 1.24. The D-lactide value is the principal chemical differentiator: it is lower than that of standard amorphous PLA grades and permits a higher attainable crystal fraction after orientation. Processing conditions must remain within a comparatively narrow temperature window because the resin crystallizes on hot surfaces above 100 °C and can block casting rolls if the quench temperature is too high.

    Composition, Rheology, and Thermal Transitions

    The D-lactide content of 2.0 mol% should be interpreted as a stereochemical defect concentration. At this level, the crystallization half-time is materially shorter than that of PLA grades containing 4.0 mol% D-lactide. The melt flow rate of 7 g/10 min represents a low-to-moderate viscosity for BOPLA casting, sufficient to maintain gauge uniformity when the die lip gap and cast roll speed are matched. The glass transition between 55 °C and 60 °C sets the lower boundary for orientation; below this range, stretching promotes crazing rather than strain-induced crystallization. The crystalline melt transition occurs in the 165 °C to 175 °C range and serves as the thermal stability limit during heat setting.

    PropertyTypical valueTest method
    Specific gravity1.24ASTM D792
    Melt flow rate7 g/10 min at 210 °C/2.16 kgASTM D1238
    D-lactide content2.0 mol%manufacturer chromatographic method
    Relative viscosity4.0 in chloroform at 25 °Cmanufacturer solution method
    Glass transition temperature55–60 °CASTM D3418
    Crystalline melt temperature165–175 °CASTM D3418

    Drying Protocols Are Not Optional for High-Gloss BOPLA Output

    Before melt processing, residual moisture is the primary source of molecular weight degradation in 4032D. PLA hydrolysis is autocatalytic; at melt temperatures above 190 °C, moisture contents above 250 ppm reduce intrinsic viscosity rapidly, producing edge trim brittleness and die-lip deposit formation. Drying in a desiccant-bed dryer with a dew point below -40 °C at 80 °C for 4 h to 6 h is recommended in manufacturer technical literature. The dry air flow rate should be maintained at 0.85 m³/h per kg/h of resin throughput. Hopper design should avoid bridging; 4032D pellets with specific gravity 1.24 and irregular cut surfaces can bridge in conical hoppers with angles shallower than 60°. Moisture analyzers operating on Karl Fischer titration or loss-on-drying at 120 °C should confirm the pellet moisture content before the first extruder barrel zone.

    On a twin-screw extruder with 30:1 L/D, a rising temperature profile from 180 °C in zone 1 to 220 °C at the adapter is typical for 4032D. Lower melt temperatures reduce thermal degradation but increase screw torque; higher temperatures reduce torque but accelerate lactide reformation. Barrel zone 1 is water-cooled on commercial lines to prevent premature pellet clumping in the feed throat. Screw designs with low-shear mixing elements are preferred over high-compression barrier screws because high shear heating can exceed the 230 °C degradation threshold. Back pressure is maintained below 100 bar to prevent excessive residence time in the melt pipe.

    What Limits High-Speed Biaxial Orientation of This Grade?

    At high line speeds, the limiting factor for 4032D is not the tenter speed but the relationship between cast roll quench rate and the subsequent MDO preheat. If the cast roll temperature is kept below 30 °C, the sheet remains amorphous and can be reheated to 65 °C to 75 °C for machine direction stretching at a draw ratio of 3.0:1 to 4.0:1; if the cast roll runs above 45 °C, spherulitic growth begins, and the MDO stretch can produce transverse gauge bands. Transverse direction stretching in the tenter is commonly conducted at 75 °C to 90 °C with a draw ratio of 3.5:1 to 5.0:1. The heat-set zone is maintained at 130 °C to 150 °C for 10 s to 20 s to stabilize the oriented crystal structure and reduce thermal shrinkage. Thermal shrinkage after 5 min at 100 °C can be measured using ISO 11501; line-specific values below 5% are reported by film converters when heat-set conditions are optimized.

    Film samples converted from 4032D on a tenter line are commonly tested for tensile modulus using ASTM D882, for Elmendorf tear using ASTM D1922, and for haze using ASTM D1003. Tensile modulus in the machine direction after MDO is typically higher than in the transverse direction unless tenter draw is increased; values depend on draw ratio and heat-set temperature. Haze below 2% is attainable on 20 µm film only when the cast roll surface is polished and the die lip is free of degraded resin. Edge tear resistance measured by ASTM D1922 is sensitive to trim blade sharpness and to residual moisture.

    When 4032D Replaces Cast PLA in a Cold-Temperature Packaging Line

    When 4032D is substituted for amorphous cast PLA in an existing line, the converter must account for the difference in quench behavior. The cast film process uses a polished chill roll at 20 °C to 30 °C; 4032D can be run under the same conditions, but the melt curtain stability requires the die lip to be set 10% to 15% wider than for a low-D-lactide grade with the same basis weight. The film will not seal at temperatures below 110 °C because of the crystalline phase; heat-sealable amorphous copolyester or low-D-lactide skin layers are required for packaging seals. Twist-wrap retention, by contrast, improves because the oriented crystal network acts as a physical crosslink. In a high-speed candy twist application, the film must be slit without cracking; slitting knives should be maintained with a shear gap below 5 µm and a rake angle between 20° and 25° to prevent microcracking along the cut edge.

    Comparative Melt Stability Against 4043D, 2003D, and 4060D on Single-Screw Extrusion

    On a single-screw extruder, 4032D shows lower melt stability than high-molecular-weight or high-melt-strength film grades because of its lower D-lactide content. The polymer melt is more Newtonian at shear rates below 100 s⁻¹; at shear rates above 500 s⁻¹, shear thinning is pronounced and die pressure is lower than that of a high-D-lactide grade with the same MFR. Compared with 2003D, which is supplied with a D-lactide content of approximately 4.0 mol%, 4032D crystallizes faster and develops higher modulus after orientation; however, it is less forgiving of thermal history. Compared with 4060D, an amorphous heat-sealable PLA, 4032D has a defined melt endotherm near 170 °C, and its seal initiation temperature is elevated because of the crystalline melt transition. 4043D is the closest commercial relative; published data for this specific configuration is limited, but the grade is directed toward high-speed biax orientation and coextruded films where its melt strength reduces edge sag in the tenter.

    Storage conditions before processing also affect 4032D; bags should remain sealed until the resin reaches room temperature to prevent condensation. Cold pellets transferred directly into a warm production hall can collect surface moisture in 30 min at 25 °C and 60% RH, exceeding the recommended moisture limit. The resin should be stored at 5 °C to 35 °C and protected from UV exposure, because prolonged UV exposure reduces molecular weight and yellows the film.

    Under food-contact regulations, the manufacturer’s compliance statement for 4032D references U.S. FDA Food Contact Notification FCN 000178 and European Union Regulation (EU) No 10/2011 for specific food simulants and use conditions. Compliance is not unconditional; films intended for hot-fill or retort applications must be tested under the intended temperature and contact time because PLA hydrolyzes above 60 °C in high-moisture environments. The resin should not be blended with amine-based antiblock or slip masterbatches that catalyze ester hydrolysis. Recycle of edge trim should be limited to 20 wt% unless the reprocessed flake is re-dried to below 200 ppm moisture, because hydrolysis-generated low-molecular-weight species migrate to the die lip and form deposits.