| HS Code | 746465 |
| Material Type | Biodegradable Polylactic Acid (PLA) |
| Processing Method | Rigid Injection Molding |
| Density | 1.24-1.25 g/cm³ |
| Melt Flow Rate | 10 g/10 min (190 °C, 2.16 kg) |
| Tensile Modulus | 3500-3600 MPa |
| Tensile Strength | 55-60 MPa |
| Elongation At Break | 3% |
| Flexural Modulus | 3500-3600 MPa |
| Flexural Strength | 80-90 MPa |
| Notched Charpy Impact Strength | 2.5 kJ/m² |
| Unnotched Charpy Impact Strength | 15 kJ/m² |
| Heat Deflection Temperature | 95-100 °C at 0.45 MPa |
| Vicat Softening Temperature | 100-110 °C |
| Biobased Content | 80-85% |
| Biodegradability | Compostable according to EN 13432 |
| Processing Temperature | 190-220 °C |
| Mold Temperature | 20-60 °C |
| Drying Temperature | 80 °C |
| Drying Time | 4 h |
As an accredited INZEA F29 HT 10 Rigid Injection Molding Biodegradable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg moisture-resistant paper bags, palletized and shrink-wrapped, for INZEA F29 HT 10 rigid injection molding biodegradable polylactic acid. |
| Container Loading (20′ FCL) | 20′ FCL loaded with INZEA F29 HT 10 rigid injection molding biodegradable polylactic acid resin in 25 kg palletized bags, stretch-wrapped. |
| Shipping | INZEA F29 HT 10 Rigid Injection Molding Biodegradable Polylactic Acid is shipped as non-hazardous, non-regulated solid resin pellets. Use sealed moisture-barrier bags or lined containers. Store/transport cool, dry, below 30°C/86°F, away from sunlight. No dangerous goods labels required. Not restricted by DOT, IMDG, IATA, or ADR. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly closed in original moisture-barrier packaging. Protect from humidity, water, and incompatible materials such as strong oxidizers, acids, and bases. Recommended storage temperature: below 30°C. Keep dry; PLA is moisture-sensitive. Use first-in, first-out rotation and reseal opened containers promptly. |
| Shelf Life | 12 months from date of manufacture when stored in unopened original packaging, in a cool, dry environment below 30°C. |
In thin-wall disposable cutlery production, INZEA F29 HT 10 is processed as the continuous matrix at 100 wt% in single-material injection runs, with post-industrial regrind from rejected sprues and runners added at ≤20 wt% only after verification of melt flow stability under ISO 1133-1:2022 at 210 °C and 2.16 kg. Color masterbatch is metered at 2–4 wt% with a gravimetric feeder; loading above 4 wt% can reduce the Vicat softening temperature measured per ISO 306/A50 by more than 2–4 °C. The compound must be dried to ≤250 ppm residual moisture using a desiccant dryer at 80–85 °C for 4–6 h, because hydrolytic chain scission at melt temperatures above 195 °C shifts the molecular weight distribution toward oligomers and causes short-shot defects in fork tine sections measuring 1.2–1.6 mm. Process conditions on 80–150 t hydraulic injection molding machines with general-purpose screws of 25–35 mm diameter and 20:1–24:1 L/D include melt temperature 195–215 °C, mold temperature 80–100 °C, injection speed 80–140 mm/s, and hold pressure 60–90 MPa; gate thickness should not fall below 0.8 mm in the tine-root transition zone. Compostability is assessed under EN 13432 and ASTM D6400, while food-contact safety is assessed under Regulation (EC) No 1935/2004 Article 3 and Commission Regulation (EU) No 10/2011 with overall migration limit 10 mg/dm². Terminal finished products include single-use forks, spoons, knives, dessert sporks, and hingeless disposable tasting spoons with wall sections between 1.0 mm and 2.4 mm.
For rigid single-serve coffee capsule bodies, the processing boundary is set by the need to retain hoop strength after steam exposure while avoiding brittle ejection fractures at the undercut ring. INZEA F29 HT 10 is introduced as the sole base polymer at 100 wt%; post-industrial capsule-skeleton regrind is limited to 10 wt% because higher fractions reduce melt strength at the hot-runner gate and increase the coefficient of variation in fill weight beyond ±2 % measured across 16-cavity stack molds. Release agent masterbatch is added at 0.2–0.5 wt% only when the masterbatch supplier certifies compliance with Commission Regulation (EU) No 10/2011; otherwise, coated mold surfaces with a demolding draft angle of 1.5–2.0° are used. Drying to ≤250 ppm moisture is mandatory, followed by processing at a melt temperature of 200–210 °C and a mold temperature of 90–100 °C to achieve the crystallinity regime required for dimensionally stable sealing flanges. Injection speed is held at 120–160 mm/s, hold pressure at 70–95 MPa, and cooling time at 8–12 s for wall sections of 0.5–0.9 mm; ejection force is monitored because a drop below 20 °C in mold temperature can increase ejection pin stress and produce microcracks at the capsule lip. Compostability certification for the finished capsule shell follows EN 13432, with disintegration testing under ISO 20200 and ecotoxicity assessment under OECD 208. Food-contact suitability is assessed per Regulation (EC) No 1935/2004 Article 3 and Commission Regulation (EU) No 10/2011. Terminal products include injection-molded capsule bodies and lids intended for use with compatible capsule machines; the shells are rigid, not flexible, and are not suitable for retort sterilization above 85 °C without additional thermal stabilizer validation.
Horticultural vine clips processed on single-cavity cold-runner tools demand a combination of flexural stiffness, hydrolytic resistance, and reliable mechanical release after gate freeze. INZEA F29 HT 10 is processed at 100 wt% as the base compound, with color masterbatch metered at 0.5–1.5 wt%; recycled material from rejected clips may be reintroduced at ≤25 wt% after drying to ≤250 ppm moisture and screening through a 1.0 mm sieve to remove degraded fines. The molds are typically single-cavity or 4–8-cavity cold-runner designs on 40–80 t injection machines. Melt temperature is set at 195–210 °C, mold temperature at 80–110 °C, injection pressure at 90–120 MPa, hold pressure at 50–80 MPa, and back pressure at 0.5–1.0 MPa; screw recovery is limited to 100–150 rpm to prevent adiabatic overheating in the compression zone. Clip flexural modulus is evaluated under ISO 178, tensile strength under ISO 527-2, and notched Izod impact under ISO 180/A; for greenhouse use, samples are conditioned at 23 °C and 50 % RH according to ISO 291 before mechanical testing. The grade is not a soil-biodegradation material; disposal is industrial composting under EN 13432 or ASTM D6400. Prolonged outdoor UV exposure causes chain scission and embrittlement, so service life beyond one season requires accelerated weathering data per ISO 4892-2. Terminal products include vine clips, plant-training clips, trellis fasteners, tree-tie holders, and rigid plant identification stakes with wall thickness generally between 1.2 mm and 3.0 mm.
When INZEA F29 HT 10 is substituted for ABS in cosmetic jars, caps, and compact cases, the critical differences are higher melt density, lower melt strength, and slower degradation of the high-shear zone inside the screw. The compound is run at 100 wt%, with pigment masterbatch at 1–3 wt%; regrind from rejected parts is restricted to ≤15 wt% because cosmetic surface gloss on mirror-polished mold surfaces degrades when regrind fraction exceeds this level. The material must be dried to ≤250 ppm residual moisture before processing. Melt temperature is controlled at 200–215 °C, while mold temperature is held at 90–110 °C to minimize flow marks and post-mold shrinkage. Injection speed is set at 90–130 mm/s for thick-walled jars with nominal wall thickness 2.0–3.5 mm, hold pressure at 60–85 MPa, and cooling time at 12–20 s; for caps with inner threads, the unscrewing core is rotated at 20–35 rpm and cooled to avoid thread deformation. Because PLA-based rigid compounds have a density near 1.25 g/cm³ under ISO 1183-1 compared with ABS at 1.04–1.07 g/cm³, cavities optimized for ABS yield heavier parts and may require adjusted packing profiles rather than geometry changes. Compliance is evaluated under REACH Annex XVII and the Packaging and Packaging Waste Directive 94/62/EC; dimensional stability is measured under ISO 294-4 after 24 h storage at 23 °C. Terminal products include injection-molded cosmetic jars, closure caps, compact bases, insert trays, and rigid refillable packaging components where impact strength requirements do not exceed the data obtained under ISO 180/A on conditioned samples. Published data for this specific configuration is limited; pilot tool trials are required before replacing ABS in existing tooling.
| Application cluster | Melt temperature (°C) | Mold temperature (°C) | Hold pressure (MPa) | Maximum regrind fraction (wt%) |
|---|---|---|---|---|
| Thin-wall cutlery | 195–215 | 80–100 | 60–90 | 20 |
| Coffee capsule shells | 200–210 | 90–100 | 70–95 | 10 |
| Horticultural clips | 195–210 | 80–110 | 50–80 | 25 |
| Cosmetic rigid packaging | 200–215 | 90–110 | 60–85 | 15 |
| Chilled ready-meal trays | 195–210 | 80–100 | 55–80 | 20 |
| Laboratory housings | 200–215 | 90–110 | 50–75 | 10 |
Chilled ready-meal tray denesting and post-consumer PLA reclaim streams impose constraints on melt stability, migration limits, and rim flatness under cold-chain storage. INZEA F29 HT 10 is introduced at 100 wt% as the base layer; post-industrial PLA regrind from thermoformed or injection-molded tray skeletons is added at ≤20 wt% only after melt-flow verification under ISO 1133-1:2022 and moisture control to ≤250 ppm. Pigment masterbatch is used at 2–4 wt%. Processing on 100–200 t injection molding machines with stack molds uses melt temperature 195–210 °C, mold temperature 80–100 °C, injection speed 100–150 mm/s, hold pressure 55–80 MPa, and cooling time 6–12 s for wall sections between 1.0 mm and 1.8 mm. Denesting is facilitated by sidewall draft angles of 1.0–1.5° and external release agents; excessive mold release spray can interfere with print adhesion and should be validated. Food-contact certification follows Regulation (EC) No 1935/2004 Article 3 and Commission Regulation (EU) No 10/2011 overall migration limit of 10 mg/dm²; compostability certification for the tray follows EN 13432, with disintegration under ISO 20200 and ecotoxicity under OECD 208. The trays are not intended for retort or oven use; sustained hot-fill temperatures above 85 °C require separate heat-resistance verification because thermal stress can induce warpage at the rim. Terminal products include chilled ready-meal trays, produce punnets, rigid deli containers, and bases for modified-atmosphere packages where the lidding film is applied after tray molding.
Rigid laboratory equipment housings that eliminate living hinges require snapping features, dimensional agreement with electronic inserts, and controlled residual stress after ejection. INZEA F29 HT 10 is processed as a neat resin at 100 wt%; if antistatic or color masterbatch is incorporated, it is limited to 2–5 wt% and must not reduce flexural modulus below the lower acceptance limit measured under ISO 178. Regrind from sprue and rejected housings is restricted to ≤10 wt% because higher levels decrease notched impact resistance under ISO 180/A and increase the rejection rate in snap-fit assembly features. Drying to ≤250 ppm residual moisture is required; processing employs a melt temperature of 200–215 °C, a mold temperature of 90–110 °C, injection pressure of 80–120 MPa, hold pressure of 50–75 MPa, and cooling time of 15–30 s for nominal wall thickness 2.5–4.0 mm. Tooling uses direct edge gates or hot-tip gates with a minimum diameter of 1.0 mm; tunnel gates are avoided at high regrind levels because the shear-induced temperature spike can cause local molecular weight loss. Dimensional stability is assessed under ISO 294-4, flexural properties under ISO 178, tensile properties under ISO 527-2, and heat deflection under ISO 75-2 with a load of 1.8 MPa. If the housing is part of electrical laboratory equipment, the molded article is evaluated under Directive 2011/65/EU (RoHS) and relevant REACH Annex XVII restrictions; for cleanroom use, outgassing and particulate shedding tests are product-specific and may require additional surface analysis. The material is not suitable for designs requiring repeated flexure or impact rebound; living-hinge geometries must be replaced with metal springs or multi-part mechanical joints. Terminal products include benchtop instrument covers, pipette stand housings, diagnostic cassette shells, sample rack bodies, and rigid transport cases for laboratory consumables.
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INZEA F29 HT 10 is a mineral-modified polylactic acid compound supplied as a rigid injection molding grade. The material is positioned within the INZEA F29 series as a high-thermal-resistance variant for semi-crystalline parts that must retain dimensional stability above the service range of unfilled amorphous PLA. The polymer matrix is compounded with a mineral nucleation and reinforcement system; the exact filler chemistry and loading are defined in the manufacturer technical datasheet and should be confirmed against the lot-specific certificate of analysis before production release. The grade is intended for processing on conventional reciprocating-screw injection molding machines with a desiccant drying system, closed-loop melt temperature control, and mold temperature capability sufficient to support crystallite development.
Published determination of melt flow index is performed in accordance with ISO 1133-1:2022 at 190 °C under 2.16 kg. Density is reported under ISO 1183-1. Tensile properties are measured on type 1A specimens per ISO 527-2, flexural properties per ISO 178, and heat deflection temperature under 0.45 MPa load per ISO 75-2/B. Reported values for this grade place melt flow index in the range of 10–15 g/10 min, density at 1.29–1.31 g/cm³, tensile yield stress at 44–48 MPa, tensile modulus at 3,800–4,200 MPa, flexural modulus at 4,300–4,700 MPa, and heat deflection temperature at 95–105 °C when molded under high mold temperature conditions. Charpy notched impact strength determined by ISO 179-1/1eA is typically 2.5–3.5 kJ/m². These values are lot-dependent and should be interpreted with specified specimen conditioning and mold temperature parameters.
The principal difference between INZEA F29 HT 10 and unfilled PLA grades lies in the mineral nucleation and stiffening system. This formulation shifts the failure mode of molded parts from a ductile, low-modulus response toward a more rigid, dimensionally stable response. The flexural modulus is higher than that of unfilled PLA by approximately 1,000–1,500 MPa, while tensile yield stress is slightly reduced. The mineral phase restricts molecular relaxation after ejection, lowering mold shrinkage from the 0.6–0.8% range typical of unfilled PLA to 0.3–0.5% when measured by ISO 294-4. This reduction is not uniform in all flow directions; orientation effects near the gate can produce anisotropic shrinkage, and the datasheet should be consulted for longitudinal and transverse values.
Compared with standard INZEA F29 grades, the HT 10 modification is derived from the same PLA backbone but incorporates a nucleating package that accelerates crystallization during mold residence. The effect is most visible in heat deflection temperature. Standard unfilled PLA injection grades frequently exhibit HDT-B values near 50–60 °C; INZEA F29 HT 10 reaches 95–105 °C when the mold surface temperature is sufficiently high to promote crystallinity. The trade-off is process-related rather than purely material-related: the elevated mold temperature required for full heat resistance increases cycle time and can complicate ejection in thin-wall sections.
The grade differs from petroleum-based rigid injection materials such as ABS and mineral-filled polypropylene in environmental degradation profile and thermal sensitivity. The PLA matrix is biodegradable under industrial composting conditions when the final article is assessed according to EN 13432 or ASTM D6400, though certification must be reconfirmed on the final part geometry and filler loading. In mechanical terms, the compound provides higher stiffness than many unfilled polyolefins, but lower notched impact toughness than ABS. Sharp internal corners, gate vestiges, and weld lines therefore require design review because the mineral-filled PLA matrix exhibits limited plastic deformation before crack initiation.
Before melt processing, the granulate must be dried to a moisture content below 0.025% by weight. A desiccant dryer with a dew point of -40 °C or lower is specified; drying at 80 °C for 4–6 hours is commonly used for PLA compounds. Moisture in excess of 0.05% produces hydrolysis, molecular weight reduction, increased melt flow index, lower melt strength, silver streaking, and inconsistent cavity filling. The drying hopper should maintain closed-loop air circulation, and material residence time in the hopper should not exceed 8 hours at drying temperature if production stops.
The melt processing window is narrower than that of many conventional thermoplastics. A barrel temperature profile of 180–210 °C from rear zone to nozzle is typically applied. Melt temperatures above 230 °C accelerate thermal degradation and should be avoided. The shot size should occupy 30–70% of the barrel capacity to limit residence time. Screw L/D ratios between 18:1 and 24:1 with low compression ratios and shallow metering sections are suitable for PLA compounds; excessive shear heating in high-compression screws can generate local temperature spikes at the melt film. Back pressure is maintained in the range of 0.5–1.0 MPa, and screw rotation speed is optimized to avoid over-shearing the mineral-filled melt.
Injection pressure requirements are geometry-dependent. Thin-wall sections below 1.5 mm may require hydraulic injection pressures above 120 MPa depending on flow length and gate design. On production lines with clamping force below 800 kN, the maximum shot weight must be evaluated against the available injection volume and the grade’s melt viscosity under actual melt temperature. Hold pressure is typically set at 50–80% of peak injection pressure and maintained until gate freeze. Premature hold release produces sink marks and increased post-molding shrinkage.
| Property | Test method | Typical value |
|---|---|---|
| Melt flow index | ISO 1133-1:2022, 190 °C, 2.16 kg | 10–15 g/10 min |
| Density | ISO 1183-1 | 1.29–1.31 g/cm³ |
| Tensile yield stress | ISO 527-2, type 1A | 44–48 MPa |
| Tensile modulus | ISO 527-2 | 3,800–4,200 MPa |
| Flexural modulus | ISO 178 | 4,300–4,700 MPa |
| Heat deflection temperature | ISO 75-2/B, 0.45 MPa | 95–105 °C |
| Charpy notched impact strength | ISO 179-1/1eA | 2.5–3.5 kJ/m² |
If the mold surface temperature is set to a conventional chilled-water range of 15–30 °C, the component will be ejected with a largely amorphous skin and incomplete crystallite development. In that condition, the heat deflection temperature may fall below 70 °C even though the material datasheet reports a value near 100 °C. The discrepancy is not a material failure but a processing condition effect: the mineral nucleating system cannot produce the crystalline morphology required for high-temperature dimensional stability if the cavity surface quenches the melt too rapidly. Mold trials on production equipment have shown that HDT-B values are maximized only when mold surface temperature is held at 90–110 °C, with sufficient hold time to allow crystal growth before ejection.
The use of high mold temperatures introduces ejection challenges. Mineral-filled PLA grades can exhibit increased ejection force and surface scuffing when the part remains too soft at the moment of mold opening. Core pins, ribbed sections, and textured surfaces require draft angles above 1°, and in some configurations above 2°, to prevent drag marks. Ejector timing should be coordinated with mold opening to avoid bending thin sections during demolding. In multi-cavity tools, cavity-to-cavity temperature variation should be kept within ±5 °C to maintain consistent shrinkage and dimensional repeatability.
The cycle-time penalty associated with high mold temperature is significant. For medium wall sections of 3–4 mm, the cooling time can increase by 20–40% compared with cold-mold processing of unfilled PLA. This is the central process conflict for the HT 10 grade: achieving the full heat resistance requires mold temperatures that extend the ejection window. If the application does not require service above 60 °C, standard unfilled PLA grades may be more economical. If the part requires dimensional stability in hot-fill, hot-air, or under-hood service conditions, the extended cycle time may be justified. The production decision should be based on molded-part HDT testing rather than datasheet values alone.
In food-contact and consumer-durable applications, the compound must be evaluated on the final article rather than on the granulate. The base PLA matrix is generally covered by food-contact frameworks such as FDA 21 CFR 177.1520 and EU Regulation 10/2011, but the mineral filler and nucleating additives require migration testing under the intended food simulant and contact temperature. Industrial compostability certification is valid only for a defined article thickness and surface-to-volume ratio; fragments thicker than the tested reference or parts with metallic inserts are excluded from standard compostability claims. Restricted substance compliance is documented under REACH and RoHS through the manufacturer’s technical dossier.
| Assessment area | Standard or regulation | Verification requirement |
|---|---|---|
| Industrial compostability of PLA matrix | EN 13432, ASTM D6400 | Final article certification required |
| Biobased carbon content | ASTM D6866 | Manufacturer-documented for PLA resin |
| Food-contact suitability | FDA 21 CFR 177.1520, EU 10/2011 | Application-specific migration testing required |
| Restricted substances | REACH, RoHS directive | Supplier declaration and batch records |
In direct-gated technical parts, gate blush and jetting are controlled by reducing injection velocity in the first filling phase and by positioning the gate against a wall or pin to break the melt stream. For multi-cavity food packaging lids and closures, hot runner systems with externally heated manifolds are preferred over cold runners because the mineral-filled compound can produce cold-slug ejection problems in tunnel gates below 1.2 mm diameter. Weld-line strength is lower than that of the bulk material; knit lines should be located in low-stress areas and verified by short-shot studies and burst or flexural tests on molded articles. The compound is not recommended for combination with amine-based processing aids or colorants that accelerate PLA hydrolysis. Only mineral-compatible masterbatches with a PLA carrier resin should be used to avoid phase separation and delamination.