| HS Code | 950591 |
| Material | Polylactic acid (PLA) compound |
| Density | 1.24 g/cm³ |
| Melt Flow Rate | 10 g/10 min (190 °C, 2.16 kg) |
| Tensile Modulus | 3500 MPa |
| Tensile Strength | 50 MPa |
| Elongation At Break | 5% |
| Flexural Modulus | 3600 MPa |
| Flexural Strength | 80 MPa |
| Notched Charpy Impact Strength | 5 kJ/m² |
| Heat Deflection Temperature | ≥100 °C (0.45 MPa) |
| Vicat Softening Temperature | ≥90 °C |
| Melting Temperature | 170 °C |
| Glass Transition Temperature | 60 °C |
| Bio Based Content | >80% |
| Compostability | EN 13432 compliant |
As an accredited INZEA F38 Rigid High Thermal Stability Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaging: 25 kg moisture-barrier bags, palletized and securely wrapped for INZEA F38 Rigid High Thermal Stability Polylactic Acid. |
| Container Loading (20′ FCL) | 20′ FCL container loading: INZEA F38 Rigid High Thermal Stability Polylactic Acid, palletized, shrink-wrapped, secured, and evenly distributed for safe transport. |
| Shipping | INZEA F38 Rigid High Thermal Stability Polylactic Acid is generally a non-hazardous solid, not regulated for transport by DOT, IMDG, IATA, or ADR. Ship in sealed, moisture-barrier bags or containers; keep dry, cool, and out of direct sunlight. Include the SDS. No special placards required. |
| Storage | Store INZEA F38 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and ignition. Keep sealed in original packaging to prevent moisture uptake, which can degrade processing performance. Maintain moderate temperatures, avoid prolonged high humidity, and separate from strong oxidizers, acids, and bases. Observe local regulations and the manufacturer’s SDS. |
| Shelf Life | Approximately 12 months when stored sealed in original packaging, cool, dry, away from moisture and direct sunlight. |
INZEA F38 is a rigid high-thermal-stability poly(lactic acid) grade supplied in pellet form. Melt processing begins with drying in a desiccant dryer at 80 °C for 4 h to a residual moisture content below 250 ppm; when pellets have been exposed to relative humidity above 60 %, pre-drying is mandatory before any melt operation because hydrolytic chain scission degrades melt elasticity and part strength. The following application scenarios are limited to downstream sectors where rigid high-heat PLA is already used or where the producer supplies documented process guidance: single-serve hot-beverage capsules, injection-moulded hot-beverage lids, thermoformed hot-fill containers, cosmetic packaging components, technical filament, and injection-moulded cutlery.
In single-serve capsule production, the capsule body is injection-moulded from INZEA F38 at a melt temperature of 200–220 °C, with a mould temperature maintained between 95 °C and 110 °C to raise crystallinity above the level required to survive contact with liquid at 92–95 °C. The formulation is typically 97–100 wt% INZEA F38; if a coloured shell is required, a PLA-carrier colour masterbatch is added at 2–3 wt%, while cold-runner regrind is limited to 15–20 wt% and must be re-dried to below 250 ppm moisture. Food-contact compliance is verified on the finished capsule according to European Commission Regulation (EU) No 10/2011, with overall migration tested according to EN 1186-1:2002 at 10 mg/dm² and specific migration of lactic acid tested according to EN 13130-1:2004; if the capsule is marketed as compostable, the complete article including seal film must also satisfy EN 13432:2000 requirements for disintegration, biodegradation, and ecotoxicity. In production, a multi-cavity hot-runner mould with valve-gated drops is used to minimise gate vestige and reduce shear-induced heating. The clamp force on a 64-cavity capsule mould can exceed 2,000 kN, and the actual setting depends on the projected area and cavity pressure. The main processing conflict is that a mould temperature below 80 °C produces amorphous capsule walls with insufficient heat resistance, while a mould temperature above 110 °C extends cooling time beyond 20 s and can cause part sticking and ejection deformation. Published data for the exact cycle time at 64 cavities is limited; however, validated processing guides for high-heat PLA recommend maximum melt residence time under 15 min and nozzle temperatures below 230 °C to avoid lactide reformation and molecular weight loss. Terminal products include espresso-compatible capsules, tea pods, and other portion-pack bodies that must not collapse during hot-water extraction.
Hot-beverage lids are thin-walled injection-moulded articles with flow paths typically between 0.6 mm and 0.9 mm, which places a narrow processing window between complete cavity filling and premature crystallisation-induced gate freeze. INZEA F38 is run as neat resin at 98–100 wt% with 1–2 wt% PLA-carrier colour masterbatch. Regrind from rejected lids and scrap is incorporated at up to 20 wt% only after drying at 80 °C for 4 h to residual moisture below 250 ppm, because thin-wall filling is sensitive to hydrolysis viscosity loss. The required food-contact documentation is based on (EU) No 10/2011 and EN 1186-1:2002; for export to North America, finished-article compliance is typically secured through the supplier’s Food Contact Notification and confirmed by the buyer under 21 CFR applicable sections, not inferred solely from the resin grade. Production machines are high-speed hydraulic or electric injection presses with clamping force from 1,200 kN to 3,500 kN, configured for stack moulds and hot-runner systems. Melt temperature is kept at 200–215 °C, mould temperature at 90–105 °C, and holding pressure is usually 600–900 bar to compensate for high-pressure drop across the thin cavity. The process conflict is severe: if the mould is below the cold-crystallisation window, the lid remains flat enough at ejection but creeps when the cup is filled with liquid above 85 °C; if the mould is too hot, the lid’s stacking features develop shrinkage and the denesting columns deform. Post-mould handling is therefore designed to avoid stacking pressure until the part surface is below 60 °C. Terminal products include hot coffee cup lids, bowl lids, and dome lids for delivery beverages with warm-liquid service temperatures between 80 °C and 95 °C.
| Parameter | Injection moulding | Thermoforming | Filament extrusion |
|---|---|---|---|
| Residual moisture before processing | < 250 ppm | < 200 ppm | < 150 ppm |
| Melt or sheet temperature | 200–220 °C | 195–210 °C | 190–205 °C |
| Tool / bath temperature | 90–110 °C | 80–100 °C | 35–50 °C |
| Maximum melt residence time | < 15 min | < 20 min | < 10 min |
At sheet thicknesses between 0.5 mm and 1.2 mm, thermoformed hot-fill snack trays produced from extruded INZEA F38 sheet require a narrow sheet-conditioning window between moisture regain and heat deflection. The sheet formulation consists of 96–98 wt% INZEA F38, 1–2 wt% PLA-carrier anti-block masterbatch, and 0.5–1.0 wt% processing aid; edge trim is handled as a separate regrind stream and can be reintroduced at up to 25 wt% after drying below 200 ppm moisture. Flat-die extrusion runs at a melt temperature of 195–210 °C with a chill-roll temperature of 30–50 °C, yielding sheet from 0.5 mm to 1.2 mm. The sheet is preheated to 95–110 °C before plug-assisted thermoforming on aluminium water-cooled tools held at 80–100 °C; forming pressure is typically 4–7 bar. In this process, the critical failure mode is not melt hydrolysis but sheet moisture regain after extrusion: storing sheet at relative humidity above 60 % without sealed packaging raises surface moisture above 400 ppm, producing blistering and inconsistent sag depth during heating. Food-contact status for hot-fill trays is evaluated under EU 10/2011 using aqueous food simulants and EN 1186-1:2002; if the tray includes a lidding film, the complete article is tested as a composite. Terminal products include warm-fill snack trays, compartment meal trays, and display trays for hot bakery items, with service temperatures up to 95 °C for short contact and no retort or steam sterilisation exposure.
For thick-walled cosmetic jars and closures, INZEA F38 is injection-moulded in polished cavities where the high surface gloss exposes sink marks, gate blush, and warpage. The formulation is typically 98–100 wt% INZEA F38 with 1–2 wt% PLA-carrier colour masterbatch; pearlescent or mineral fillers are restricted to 2–5 wt% because higher levels reduce gloss and alter the melt elasticity at the gate. Injection moulding uses a melt temperature of 200–210 °C and mould temperature of 85–100 °C. Thick-walled jar bases with wall sections above 3 mm require extended holding pressure and staged cooling to prevent sink marks; valve-gated hot-runner systems are preferred over open hot sprues to reduce gate vestige. Dimensional stability is evaluated by conditioned room-temperature measurement after 24 h, with warpage checked against a flatness specification referenced to ISO 1101:2017. Regulatory documentation for cosmetic packaging is based on REACH Regulation (EC) No 1907/2006, Cosmetic Products Regulation (EC) No 1223/2009, and the RoHS Directive 2011/65/EU. Internal mold-release additives should not exceed 0.2–0.5 wt% if downstream hot-foiling, pad printing, or adhesive labelling is used, because migration of release chemistry reduces adhesion. Amine-functional processing aids and some organic pigments are not used because they can produce surface bloom and interfere with post-mould decoration. Terminal products include heavy-wall jars, caps, compact cases, and decorative outer shells that require dimensional consistency across high-gloss surfaces.
When standard PLA filament distorts under thermal load in prototype assembly cells, INZEA F38 is processed into technical filament for annealed high-temperature tooling fixtures, assembly jigs, and short-run manufacturing aids. The extrusion grade is run at 100 wt% INZEA F38, without mineral filler, and custom colouring is achieved with a PLA-carrier masterbatch at 0.5–2 wt%. The process uses a single-screw extruder with screw diameter 20–25 mm and L/D ratio between 24:1 and 30:1, equipped with a melt pump and dual-axis laser gauge feedback; melt temperature is 190–205 °C, water-bath temperature is 35–50 °C, and filament diameter is controlled to 1.75 mm ± 0.05 mm or 2.85 mm ± 0.05 mm. The printed object is held in a forced-circulation oven at 80–100 °C for 1–2 h on a flat, non-marring fixture; this raises crystallinity and increases heat deflection temperature relative to as-printed amorphous material. Regulatory compliance is limited to general chemical safety requirements under REACH Regulation (EC) No 1907/2006 and the RoHS Directive 2011/65/EU; biobased carbon content verification, if required, is performed by radiocarbon analysis according to ASTM D6866-21. Terminal products include manufacturing jigs and fixtures used in short contact with warm surfaces, but are not intended for continuous load above 100 °C or for electrical enclosures requiring flame retardance. Published data for this specific configuration is limited; therefore lot-specific dimensional and thermal validation is required before full production.
In the production of injection-moulded cutlery and hot stirrers, INZEA F38 is processed as neat resin at 98–100 wt%; if a white finish is needed, a TiO₂-based PLA masterbatch is added at 1–3 wt%. The pre-drying condition is 80 °C for 4 h to below 250 ppm moisture, followed by injection at a melt temperature of 200–220 °C and a mould temperature of 90–100 °C. Food-contact conformity is established under EU 10/2011 by overall migration testing to EN 1186-1:2002. Terminal products include spoons, forks, knives, and stirrers intended for hot drinks up to 90 °C. The operational boundary is that knives and forks with thin tines should not be exposed to bending stress while hot; the material remains rigid but not impact-tolerant like polypropylene, and steam sterilisation above 100 °C is outside the validated use window.
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INZEA F38 is a rigid polylactic acid injection-moulding grade formulated for elevated short-term thermal resistance under low mechanical load. The designation F38 identifies a nucleated high-heat-stability PLA within the INZEA biopolymer range. Manufacturer-published typical values place the material at a density of 1.24–1.26 g/cm³ under ISO 1183-1, a melt mass-flow rate of 15–25 g/10 min at 190 °C and 2.16 kg per ISO 1133-1:2022, and a tensile modulus of 3300–3600 MPa under ISO 527-2. The grade is not a standard amorphous PLA; its end-use thermal response depends on crystallisation generated in a heated mould. When the mould surface is held between 90 °C and 110 °C, the material develops sufficient crystalline order to exhibit heat distortion temperatures near 90–100 °C under 0.45 MPa loading in ISO 75-2 method B. In cold-mould processing below 80 °C, the same part remains largely amorphous and may soften below 55–60 °C. The grade therefore occupies a position between general-purpose PLA and short-term heat-resistant fossil-based thermoplastics, but it requires stricter thermal profiling than conventional biopolymer processing.
Unmodified PLA has a glass transition temperature near 55–60 °C, and amorphous parts begin to lose dimensional stability close to that boundary. To resist deformation above 80 °C, the polymer matrix must develop a crystalline fraction. PLA crystallisation is kinetically limited; maximum spherulitic growth rates occur near 105–110 °C, while cooling through the normal injection-mould temperature range of 20–40 °C suppresses crystallinity almost entirely. INZEA F38 is engineered to increase nucleation density so that crystallisation can proceed within a production-compatible heated-mould window. In practice, the mould must remain hot enough for nucleation and growth, but below the temperature at which parts become difficult to eject. For this grade, the effective processing band is typically 90–110 °C. The result is a semicrystalline part with heat distortion behaviour measured under ISO 75-2 method B between 90 °C and 100 °C, depending on wall thickness, cycle time, and mould temperature uniformity. Differential scanning calorimetry according to ISO 11357-3 can be used to estimate the crystallinity actually achieved; however, published data for this specific configuration is limited, and part-level validation is required because final crystallinity is sensitive to thermal history.
| Property | Test method | INZEA F38 typical | Standard amorphous PLA reference | Impact-modified PLA reference |
|---|---|---|---|---|
| Density | ISO 1183-1 | 1.24–1.26 g/cm³ | 1.24–1.25 g/cm³ | 1.25–1.35 g/cm³ |
| Melt mass-flow rate | ISO 1133-1:2022, 190 °C, 2.16 kg | 15–25 g/10 min | 6–15 g/10 min | 3–10 g/10 min |
| Tensile strength at yield | ISO 527-2 | 60–65 MPa | 55–65 MPa | 35–45 MPa |
| Elongation at break | ISO 527-2 | 2–4% | 3–5% | 10–30% |
| Flexural modulus | ISO 178 | 3400–3800 MPa | 2500–3000 MPa | 2000–2500 MPa |
| Notched Izod impact, 23 °C | ISO 180 | 2.5–4.0 kJ/m² | 2.0–3.0 kJ/m² | 8–20 kJ/m² |
| Heat distortion temperature, method B | ISO 75-2, 0.45 MPa | 90–100 °C | 50–60 °C | 60–80 °C |
| Vicat softening temperature, A50 | ISO 306 | 115–125 °C | 55–60 °C | 70–90 °C |
Values are representative ranges compiled from published datasheet information and general PLA family data. Lot-specific certificates of analysis should be used for production specifications, particularly because the heat distortion value is not an intrinsic material constant but a process-dependent response.
The critical process variable for INZEA F38 is mould temperature, not melt temperature alone. Increasing barrel set points without a hot mould does not compensate for suppressed crystallisation. Injection moulding machines must be equipped with mould-temperature control units capable of maintaining 90–110 °C with a deviation of no more than ±5 °C across the cavity surface. Conformal cooling or heated oil/water circuits are required where wall thickness varies by more than 1–2 mm; large temperature gradients produce differential crystallinity and warpage. The melt-temperature window is normally 190–210 °C, with short excursions up to 230 °C possible only when residence time is controlled. Residence time at melt temperature should not exceed 15 min, and lower settings are recommended at the upper end of the range to limit molecular weight loss. A cold runner with sufficient diameter is preferred; hot-runner systems require internal temperature profiling because dead spots can generate dark degradation specks. Injection speed should be moderate to high to avoid premature solidification against the heated cavity. Holding pressure is generally applied in the range 600–1000 bar, depending on wall thickness and gate geometry. Cycle time is longer than for cold-mould PLA because cooling is limited by the smaller temperature difference between melt and cavity. A part ejected too early may pass dimensional checks but can develop post-ejection shrinkage as secondary crystallisation continues during storage. In practice, processors observe that raising mould temperature from 40 °C to 100 °C can increase cycle time by 30–50% for comparable wall sections. This increase is the trade-off for the higher heat distortion response.
Moisture control is non-negotiable. PLA hydrolyses in the melt when residual moisture exceeds approximately 250 ppm, producing chain scission, reduced melt viscosity, silver streaks, and a loss of mechanical properties. The material should be dried in a desiccant dryer at 80 °C for 4 h, using a dew point of -40 °C or lower. Hopper residence after drying should be minimised, particularly when ambient relative humidity exceeds 60%. Moisture uptake in an open hopper can reverse drying within 30–60 min in humid conditions. Verification by Karl Fischer titration or a calibrated moisture analyser is recommended before start-up. Drying failure is a common batch-to-batch variance source, and the melt flow rate should be checked against the certificate value if viscosity reduction is suspected.
Primary conversion for INZEA F38 is injection moulding of rigid articles requiring short-term thermal resistance under low mechanical load. Reported application environments in trade literature include rigid food-contact articles, beverage capsule components, and technical housings subjected to intermittent heat exposure up to approximately 100 °C without high load. These applications are not interchangeable; food-contact status must be confirmed for the specific article and food simulant under EU 10/2011 or the relevant national regulation. Industrial compostability under EN 13432 is an article-level certification and not an automatic property of the raw material. For load-bearing goods or applications involving repeated thermal cycling, published data for this specific configuration is limited, and component testing under ISO 75-2 and ISO 527-2 is required. Thin-wall parts may be filled using high injection rates to prevent premature freeze-off, but the high mould temperature reduces the effective cooling rate and imposes longer hold and cooling phases. The material is not recommended for blown film or cast film without prior compatibility testing, and it is not intended for applications requiring high elongation or snap-fit behaviour.
Heat distortion testing under ISO 75-2 method B uses a low fibre stress of 0.45 MPa. The result should not be confused with ISO 75-2 method A, which applies 1.8 MPa. Nucleated PLA grades such as INZEA F38 may show method B values near 100 °C, but method A values frequently remain below 70 °C. Therefore, direct substitution for ABS, polycarbonate, or glass-filled polypropylene in high-load, high-temperature applications is not supported without part-level mechanical testing. If service conditions approach or exceed 100 °C under continuous mechanical stress, the component may soften, creep, or undergo post-crystallisation shrinkage. Annealing at 100 °C for 30 min can increase crystallinity and heat resistance, but it may also produce dimensional change of 0.2–1.0% and should be validated on the production tool. Exposure to steam, boiling water, or repeated autoclave cycles is not recommended because PLA undergoes hydrolytic degradation at high humidity and elevated temperature. Hot alkaline cleaning solutions and strong oxidising agents also accelerate surface attack. These boundaries are essential for industrial users, because the high thermal stability of INZEA F38 is defined for dry-heat or brief moist-heat exposure, not for saturated steam service.
The differentiation between INZEA F38 and other PLA grades is most visible in heat distortion response, stiffness, and failure mode. Standard amorphous PLA processed in a cold mould shows HDT-B of 50–60 °C and is unsuitable for parts that encounter hot beverages or warm technical environments. INZEA F38 differs by requiring a heated mould and by delivering a 25–40 °C increase in method B heat distortion relative to standard PLA. Impact-modified PLA grades provide higher notched Izod impact values, typically 8–20 kJ/m² at 23 °C, while F38 remains in the 2.5–4.0 kJ/m² range. Consequently, F38 is not a drop-in replacement for impact-modified biopolymers in snap-fit closures or living-hinge designs. Mineral-filled PLA grades may match or exceed F38 in heat distortion under some conditions, but they typically carry density values of 1.35–1.50 g/cm³ and may exhibit lower melt flow. The rigid high-heat profile of INZEA F38 is therefore most appropriate where low part weight, high stiffness, and short-term thermal resistance are required, while toughness remains a clearly defined limitation.
Regulatory compliance must be handled at the article level. Food-contact status is not automatically conferred by the base polymer; it requires migration testing under EU 10/2011, a manufacturer Declaration of Compliance, or the applicable Food Contact Notification for the United States. The material should not be used in medical implant applications or in safety-critical components without additional validation. Storage should be in sealed, moisture-barrier packaging at relative humidity below 60%. If bags are opened and exposed to humid air, re-drying at 80 °C for 4 h is recommended before processing. These limitations define the operational boundary within which the grade functions predictably.