| HS Code | 573333 |
| Density | 1.24 g/cm³ |
| Meltflowrate | 14 g/10 min (210°C, 2.16 kg) |
| Tensilestrengthatyield | 48 MPa |
| Tensileelongationatbreak | 2.5% |
| Tensilemodulus | 3500 MPa |
| Flexuralmodulus | 3500 MPa |
| Flexuralstrength | 80 MPa |
| Notchedizodimpact | 2.5 kJ/m² |
| Glasstransitiontemperature | 55-60°C |
| Meltingtemperature | 145-155°C |
| Heatdeflectiontemperature | 50°C at 1.82 MPa |
| Vicatsofteningtemperature | 55°C |
| Renewablecarboncontent | 100% |
| Compostability | Certified compostable (ASTM D6400, EN 13432) |
| Clarity | Transparent |
As an accredited Ingeo Polylactic Acid (PLA) 3052D factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Ingeo PLA 3052D is packaged in 25 kg moisture-resistant foil-lined bags, palletized and stretch-wrapped for transport. |
| Container Loading (20′ FCL) | Ingeo PLA 3052D loaded in a 20′ FCL container, palletized bags, kept dry and secured against shifting during transport. |
| Shipping | Shipping description: Ingeo Polylactic Acid (PLA) 3052D, non-hazardous solid resin pellets. Not regulated for transport; no UN number, hazard class, or packing group. Supplied in moisture-barrier bags, boxes, or octabins. Keep dry, avoid excessive heat, and ensure packaging remains sealed. Use standard industrial handling precautions. Store under cool, dry conditions. |
| Storage | Store Ingeo Polylactic Acid (PLA) 3052D in a cool, dry, well-ventilated area away from direct sunlight and heat. Keep containers tightly sealed in original moisture-barrier packaging. Recommended conditions are below 30°C and below 50% relative humidity. Protect from moisture pickup, which can hydrolyze the resin. Use first-in, first-out stock rotation and avoid strong oxidizers. Do not store near ignition sources. |
| Shelf Life | Shelf life: approximately 12 months from manufacture when stored unopened in original packaging in a cool, dry place. |
On a 32-cavity hot-runner stack mold producing 22 g forks, Ingeo 3052D is processed at a melt temperature of 195–210°C and a mold temperature of 28–32°C. The low mold temperature suppresses spherulitic crystallisation, retaining the amorphous clarity that is lost when mold-wall temperatures exceed 45°C. At 80–120 mm/s injection velocity, apparent melt viscosity at the gate falls below 30 Pa·s at 10,000 s⁻¹, but dead spots in the hot runner increase residence time and generate lactide, shifting the melt flow index from 14 g/10 min to 18–22 g/10 min after 15 min of interrupted cycling. Pre-drying at 80°C for 4 h in a desiccant dryer with a dew point below -40°C is enforced before start-up; residual moisture above 250 ppm produces splay on the tine surfaces and reduces tensile yield strength to 51–54 MPa. The production formulation is kept at 100.0 wt% 3052D for food-contact clarity; if a standard color masterbatch is required, it is limited to 0.5–2.0 wt% and selected from PLA-carrier concentrates with EU 10/2011 migration compliance. Nucleating agents are omitted because the resulting crystallinity raises haze and reduces notched Izod impact below 12 J/m. Terminal articles include injection-molded forks, spoons, and knives. They meet material requirements of EN 13432 industrial compostability when wall thickness is 2.5 mm or less, with disintegration testing at 58°C for up to 12 weeks, but they are not suited to prolonged contact with food above 55°C because the heat deflection temperature at 0.45 MPa is 55°C per ASTM D648.
On the same line, ejection force is monitored at 8–12 kN per stack half; insufficient cooling below 9 s leaves the fork hinge area above the glass transition temperature of 55–60°C, causing punch-mark deformation on ejector pins. A semi-crystalline skin 0.1–0.3 mm thick forms only when mold temperature is raised to 50°C; this raises the heat deflection temperature at 0.45 MPa to 65–70°C but increases cycle time to 45–55 s and produces opacity at the gate seal. The notch-sensitive geometry at the tine root has an as-molded notched Izod impact of 16 J/m per ASTM D256; regrind is limited to 10–15 wt% because higher regrind raises the melt flow index by 4–6 g/10 min and reduces fill consistency. Published data for this specific stack-mold configuration is limited to line trials; therefore these values are reported as observed ranges rather than universal limits.
When transparent jar bases are gated through a single 0.8 mm valve gate, cavity pressure transducers demonstrate that the 3052D melt freezes at the gate after 3.5–4.5 s at 200°C, making packing beyond 80 MPa ineffective and raising sink-mark depth on the outer wall above 0.02 mm. The accepted cosmetic-packaging formulation is 99.5–100.0 wt% 3052D; a migrating slip additive is avoided, while a non-migrating processing aid at 0.2–0.5 wt% is used only when screw recovery time exceeds 4.0 s. The material for jar bases and 15–50 mL cream jars is pre-dried at 80°C for 4 h to 250 ppm moisture or lower, then injection molded at 190–205°C melt temperature and 25–30°C mold temperature with a hold pressure of 60–80 MPa for 4.0–5.5 s. Wall thickness is maintained between 2.5 mm and 4.0 mm; below 2.5 mm, gate blush appears at the injection point, and above 4.0 mm, cycle time rises beyond 35 s and cooling becomes the rate-limiting step. Under Regulation (EC) No 1907/2006 Annex XVII and Regulation (EC) No 1223/2009 Article 17, the PLA compound is supplied with absence declarations for substances listed in Annex II of 1223/2009; migration of monomers and process aides into the cosmetic matrix is assessed case-by-case after storage at 45°C for 28 days, because published data for leave-on cream formulations in contact with PLA is limited. Terminal product types include injection-molded jar bases, compact bases, and low-torque threaded closures, but not transparent over-caps used with alcohol-based perfumes, since the amorphous 3052D surface develops solvent stress cracking when exposed to ethanol concentrations above 20% in continuous contact.
Rim-wall thickness variation in a 300 mL injection-molded dairy cup absorbs more than 60% of the total process window because the 3052D melt exhibits power-law shear thinning at gate shear rates above 10,000 s⁻¹ and transitions to plug-like flow in the 0.6 mm rim channels. For chilled dairy and deli applications, the formulation is 100.0 wt% 3052D for the cup body; antifog additive concentrate is added at 0.3–0.8 wt% only in lids, where water condensation on the inner surface must be suppressed without reducing transparency below 12% haze on a 2 mm plaque per ISO 14782. The production process uses a two-platen stack mold with 8+8 cavities and hot-cold valve gating; melt temperature is 195–200°C, mold temperature 25–28°C, cooling time 10–12 s, and total cycle time 18–24 s. Compliance for food contact is established under Regulation (EU) No 10/2011, with overall migration below 10 mg/dm² after 10 days at 40°C in food simulant A (10% ethanol) and food simulant C (20% ethanol), as appropriate for chilled milk and low-fat deli emulsions. Terminal products are 200–500 mL cups, deli containers, and transparent lids for chilled distribution below 5°C; they are not designed for microwave reheating or hot-fill above 55°C, because the heat deflection temperature at 0.45 MPa is 55°C per ASTM D648.
Processing bottlenecks occur at the rim gate land: shear rates above 80,000 s⁻¹ at the land cause local melt temperature rise to 215°C, which accelerates lactide formation and creates an acetone-like volatile plume at mold opening. To limit this, the valve gate is opened in two stages and the rim wall is tapered from 1.2 mm to 0.6 mm over 5 mm. Measured melt flow index drift under normal production remains below 2 g/10 min over 8 h; if drift exceeds 3 g/10 min, material residence time is reduced by lowering screw rotation speed from 80 rpm to 55 rpm.
| Parameter | Disposable cutlery | Cosmetic jar base | Dairy cup/lid |
|---|---|---|---|
| Melt temperature | 195–210°C | 190–205°C | 195–200°C |
| Mold temperature | 28–32°C | 25–30°C | 25–28°C |
| Injection velocity | 80–120 mm/s | 30–50 mm/s | 100–140 mm/s |
| Hold pressure | 70–90 MPa | 60–80 MPa | 50–70 MPa |
| Total cycle time | 16–22 s | 30–38 s | 18–24 s |
| Pre-drying | 80°C / 4 h | 80°C / 4 h | 80°C / 4 h |
Transparent pen barrels with 0.8–1.0 mm nominal wall are molded from 100.0 wt% 3052D; a low-dust colorless masterbatch is used at 0.5–1.0 wt% only when UV-stabilised grades are required for point-of-sale display, but the addition shifts the melt flow index by +1 to +2 g/10 min and requires a 5°C reduction in melt temperature to avoid drool at the 0.6 mm pin gate. Barrel concentricity is maintained by a two-stage injection profile with initial fill velocity of 90–110 mm/s, deceleration to 30–40 mm/s before volumetric switchover at 95–98% fill, and packing at 45–60 MPa for 2.5–3.5 s. The mold temperature is held at 28–32°C; higher temperatures create a semi-crystalline surface layer that reduces light transmission and produces visible gate-ring marks. Because the notched Izod impact of 3052D is 12–18 J/m per ASTM D256, snap-fit features in the cap and tip threads require a root radius above 0.5 mm to avoid crack initiation during assembly. Toxicological compliance for writing implements marketed as child-attractive is evaluated under EN 71-3:2019+A1:2021 for element migration; REACH Regulation (EC) No 1907/2006 Annex II safety data sheet obligations apply to the resin and masterbatch suppliers. Terminal product types include transparent fountain-pen barrels, rollerball ink tubes, and cap sleeves, where the amorphous 3052D can replace SAN only when the service temperature remains below 50°C and the ink solvent is not a strong ester or ketone.
When a transparent sorting-tray window is transferred from SAN to 3052D, the cold-runner tool must be rebalanced because PLA has a narrower processing window and a melt residence time above 10 min at 195°C initiates chain scission that lowers the tensile yield strength from 60 MPa to 48–52 MPa without a visible color shift. The toy formulation is adjusted to 92.0–95.0 wt% 3052D with 5.0–8.0 wt% biodegradable impact modifier to meet drop-test requirements of ASTM F963-23; the modifier raises notched Izod impact from 12–18 J/m to 25–35 J/m but increases haze to 15–25% and reduces tensile modulus to 2.7–3.0 GPa. Injection molding is performed with melt temperature 190–200°C, mold temperature 30°C, injection velocity 60–80 mm/s, and packing pressure 40–55 MPa; the lower melt temperature is mandatory because the impact modifier phase elongates at shear rates above 5,000 s⁻¹ and causes surface streaking at higher velocities. Compliance is assessed under EN 71-3:2019+A1:2021 for element migration and under REACH Annex XVII for child-attractive plasticised material; no phthalate plasticisers are used in 3052D, so phthalate-specific limits are met by design rather than by migration testing. Terminal product types include transparent sorting trays, construction-set windows, and non-mouth-contact puzzle bases; mouth-contact toy components are excluded unless the specific formulation is tested under EU 10/2011 because the impact modifier package may alter overall migration values.
Biaxially oriented PLA films are not produced from 3052D, but injection-molded retail display components such as 2 mm hinged clamshell inserts and tool trays exploit the resin’s amorphous clarity at low service temperatures. The formulation is 100.0 wt% 3052D; antistatic masterbatch may be added at 0.5–1.0 wt% for electronics accessory trays, but the addition reduces clarity and is limited to non-food retail inserts. Processing uses a hydraulic injection machine with a 24:1 L/D barrier screw, melt temperature 185–195°C, mold temperature 25°C, and back pressure 3–5 MPa. The lower melt temperature is used because thin-wall 1.5 mm retail inserts have short flow length but high gate shear, and melt temperatures above 200°C produce acetone-tinged volatiles and gate-stringing. Compliance for non-food retail packaging is governed by REACH Regulation (EC) No 1907/2006 and by Directive 94/62/EC on packaging and packaging waste, with the sum of lead, cadmium, mercury, and hexavalent chromium below 100 mg/kg in the packaging material. Terminal product types are hinged retail inserts, electronics accessory tool trays, and low-load display clips with service temperatures not exceeding 45°C and continuous load below 0.2 MPa to avoid creep beyond 1% after 1,000 h at 23°C per ISO 899-2.
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Ingeo polylactic acid 3052D is a high-flow PLA grade directed primarily at injection molding operations where thin-wall filling, reduced cycle time, and moderate heat resistance must be balanced against the thermal sensitivity of the polyester backbone. The resin is not an extrusion-grade PLA: its melt mass-flow rate, reported in manufacturer technical literature as 10–25 g/10 min at 210 °C and 2.16 kg under ISO 1133-1:2022, exceeds general-purpose sheet and profile grades and reduces nozzle pressure during fast mold filling. Solid-state density is approximately 1.24 g/cm³ by ISO 1183-1:2019, and tensile yield strength is commonly cited near 60 MPa when tested to ISO 527-2:2012 on type 1A bars. Reported flexural strength is near 83 MPa under ISO 178:2019, while notched Izod impact is typically cited at 16 J/m under ISO 180:2019. These values place 3052D in the semicrystalline PLA family, but process capability is governed less by ambient mechanical data than by moisture content, melt residence time, screw plastication behavior, and mold-temperature history.
On a 1200 kN hydraulic clamp injection molding machine equipped with a general-purpose screw at 20:1 L/D, a reverse barrel-temperature profile is typically specified from rear zone 170–180 °C, middle zone 185–195 °C, front zone 195–205 °C, and nozzle 200–210 °C. Screw rotation of 50–100 rpm and back pressure of 0.5–1.0 MPa are cited in processing guides as starting conditions, although published data for this exact machine configuration are limited. Mold temperatures between 15 °C and 25 °C preserve amorphous clarity and reduce cooling time, but the resulting parts remain constrained by heat deflection temperatures near 55 °C at 0.45 MPa. Mold temperatures in the 80–100 °C range induce cold crystallization and elevate heat resistance, yet longer cooling cycles and ejection sticking become common when the cooling time is insufficient or when draft angles are below 1°. Short shots are most frequently observed in sections below 0.8 mm at flow-length-to-wall-thickness ratios above 150:1; raising the melt temperature to 220–230 °C can improve filling, but prolonged exposure above 230 °C accelerates chain scission and should be avoided.
Melt residence time should remain below 20 min when the barrel set point is above 200 °C. Beyond this boundary, hydrolytic and thermal degradation mechanisms reduce molecular weight, and molded specimens subsequently show lower notched Izod impact and reduced tensile elongation. Quantitative molecular weight loss data for this exact 3052D residence-time window are not fully published; however, the general mechanism of polyester chain scission under hot, moisture-containing melt conditions is well documented. Screw recovery behavior on older injection units may exhibit stalling if the rear zone is set below 170 °C, because pellet plastication is incomplete before feed-zone compression. The use of a general-purpose screw without a mixing section is acceptable for unmodified 3052D, but masterbatch dispersion at high letdown ratios may require a dispersion gate or a shearing zone in the metering section because the resin’s melt viscosity is too low to generate high shear stress in the screw channel alone.
Where 3052D diverges from extrusion-grade PLA is most evident in melt strength and screw recovery pressure. The higher melt flow index permits lower injection pressure and faster filling in multicavity tools, but the same flow characteristic produces thin-web melt curtains that are difficult to maintain in extrusion blow molding or cast-film drawing without neck-in. In a 25 mm single-screw extruder with 24:1 L/D, the resin can be processed as a compounding carrier only if the screw contains sufficient compression; low melt viscosity may cause surging and poor pellet wetting at rear-zone temperatures above 180 °C. These differences should be evaluated against the specific downstream conversion step rather than assumed from PLA as a single material class.
Compared with extrusion-grade Ingeo 2003D, 3052D typically exhibits lower zero-shear viscosity and lower elongational viscosity under uniaxial extension. The practical consequence is that injection-molded tensile bars of 3052D often show slightly lower elongation at break than 2003D when both are tested under ISO 527-2:2012; typical elongation at break for 3052D is cited near 2.5–6%, while lower-flow PLA may lie at the upper end of this range or above depending on annealing state. Notched Izod impact strength for 3052D is reported near 16 J/m by ASTM D256-10, which is moderate for unmodified PLA and lower than toughened PLA blends. This positions 3052D for rigid housings, disposable cutlery, and other stiff parts rather than snap-fit closures requiring high post-yield ductility. Melt-flow stability after single-pass regrind is acceptable, but regrind addition above 20 wt% tends to increase brittleness and melt-flow deviation; the blended melt mass-flow rate should be checked under ISO 1133-1:2022 on dried pellets.
| Property | Test method | Reported value | Condition |
|---|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | 10–25 g/10 min | 210 °C, 2.16 kg, dried pellet |
| Density | ISO 1183-1:2019 | 1.24 g/cm³ | Amorphous injection-molded plaque |
| Tensile yield strength | ISO 527-2:2012 | 60 MPa | Type 1A, 50 mm/min |
| Tensile modulus | ISO 527-2:2012 | 3.5 GPa | Secant modulus, 1 mm/min |
| Flexural strength | ISO 178:2019 | 83 MPa | 2 mm/min, 80×10×4 mm bar |
| Notched Izod impact | ISO 180:2019 | 16 J/m | 23 °C, edgewise, type 1 notch |
| Heat deflection temperature | ISO 75-2:2013 | 55 °C | Method B, 0.45 MPa, flatwise |
Moisture management is not a peripheral issue for 3052D because PLA hydrolysis kinetics are autocatalytic and become significant when pellet moisture exceeds 0.025 wt%. Pre-drying in a desiccant dryer at 80 °C for 4 h is the standard starting condition, with dryer inlet dew point held below -40 °C. Hopper-to-throat relative humidity should remain below 60%, because virgin pellets and regrind can re-acquire surface moisture in under 30 min in humid production halls. Visual inspection cannot detect the 0.025 wt% threshold; Karl Fischer titration or a coulometric moisture analyzer is required. When hydrolysis has occurred, molded parts may show reduced notched Izod impact, surface splay, and lower melt viscosity, but the molecular weight loss is not recoverable by additional drying. Avoid combination with amine-based additives, residual peroxides from compatibilizers, and high-free-fatty-acid metal stearates, all of which can accelerate chain scission and widen the melt-flow distribution during compounding.
Amorphous moldings of 3052D typically exhibit a heat deflection temperature near 55 °C under 0.45 MPa load by ISO 75-2:2013, which restricts hot-fill applications above 60 °C. When service conditions require dimensional stability at 80–100 °C, the part must be crystallized by annealing at 90–100 °C. Cycle length scales with part wall thickness; a 3 mm plaque may require 20–30 min at temperature, but published data for this exact 3052D plaque geometry are limited. Annealing causes shrinkage of roughly 0.5–1.5% in the primary plane and increases brittleness; parts should be fixtured to control warpage. The choice between high mold temperature and post-mold annealing depends on tool thermal design: high mold temperature above 80 °C can reduce post-mold operations but may cause ejection damage if the part contains deep ribs with insufficient draft. Thin-wall packaging applications operating below 50 °C can often retain the amorphous structure without annealing, while rigid food-service items exposed to hot beverages require crystallization to avoid deformation.
Capillary rheometry at 220 °C and apparent shear rates from 100 s⁻¹ to 1000 s⁻¹ demonstrates pseudoplastic behavior with a power-law index below 0.8 in published PLA curves. This shear-thinning characteristic allows filling of thin sections but also lowers pressure transmission in long channels; tool designers should maintain gate diameters above 1.0 mm and runner lengths below 100 mm to avoid premature freeze-off. In a 4-cavity cold-runner tool producing rectangular lids with wall thickness 1.0 mm, mold filling is typically stable when the injection speed is profiled to avoid jetting and when the melt cushion is held at 3–5 mm. Published data for this specific 3052D tool configuration are limited, and cycle-time optimization should be confirmed by short-shot studies on the production press rather than transferred from laboratory spiral-flow data.
Compliance under European chemical safety frameworks is not a function of melt flow but of resin composition, supply-chain documentation, and final-article testing. The matrix below lists assessment categories, not blanket certifications. For food-contact use, the final packaging article must be tested for overall migration and specific migration limits because the polymer alone does not define food-contact compliance. US FDA status for PLA is typically product-specific and should be confirmed against the applicable food-contact notification or effective FCS clearance; no blanket 21 CFR Part 177 listing should be assumed for all PLA grades.
| Framework | Designation | Typical assessment | Verification requirement |
|---|---|---|---|
| EU RoHS Directive | 2011/65/EU | No homogeneous-material restricted substance above threshold declared in manufacturer safety data sheet | Supplier certificate; XRF screening of final assembly |
| EU REACH | (EC) No 1907/2006 | No SVHC above 0.1 wt% in current manufacturer declaration | Safety data sheet and Annex XIV candidate list check |
| EU food-contact plastics | (EC) No 10/2011 | Compliance is article-specific and requires migration testing | Overall and specific migration tests on final package |
| US FDA indirect additive status | 21 CFR Part 177 | Product-specific food-contact notification may apply; no blanket resin clearance is assumed | Regulatory counsel review of applicable FCN or clearance |
Storage life for unopened, moisture-barrier packaging is generally 12 months from production when kept below 40 °C, but opened containers should be consumed within 8 h in an atmosphere above 60% RH unless a hopper dryer is in service. Recycling of post-industrial scrap is operationally feasible if the scrap is kept clean and dry, but post-consumer PLA streams introduce variable crystallinity and contamination that can shift melt-flow behavior and reduce notched impact strength. When post-consumer recycled PLA is blended with 3052D, the blend should be characterized for melt mass-flow rate under ISO 1133-1:2022 and for tensile yield strength under ISO 527-2:2012 before the material is released to production, because published data for this specific recycled-content configuration is limited.