| HS Code | 743965 |
| Productname | INZEA F29 HT 30 |
| Polymertype | Biodegradable Polylactic Acid (PLA) |
| Processingmethod | Rigid Injection Molding |
| Appearance | Pellets |
| Density | 1.45 g/cm³ |
| Meltflowrate | 10 g/10 min (190°C/2.16 kg) |
| Tensilestrength | 45 MPa |
| Tensilemodulus | 5500 MPa |
| Elongationatbreak | 2.5% |
| Flexuralmodulus | 5500 MPa |
| Flexuralstrength | 80 MPa |
| Charpynotchedimpactstrength | 2.5 kJ/m² |
| Heatdeflectiontemperatureat045mpa | 140°C |
| Heatdeflectiontemperatureat182mpa | 100°C |
| Vicatsofteningtemperature | 120°C |
| Meltingtemperature | 170°C |
| Biobasedcontent | 70% |
| Biodegradability | Compostable according to EN 13432 |
| Mineralfillercontent | 30% |
| Meltprocessingtemperature | 190-210°C |
| Moldtemperature | 20-40°C |
| Dryingtemperature | 80°C |
| Dryingtime | 4 hours |
As an accredited INZEA F29 HT 30 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 | INZEA F29 HT 30 biodegradable polylactic acid supplied in 25 kg moisture-barrier bags, palletized for rigid injection molding. |
| Container Loading (20′ FCL) | 20′ FCL of INZEA F29 HT 30, a rigid injection molding biodegradable polylactic acid, securely loaded for export shipment. |
| Shipping | INZEA F29 HT 30 Rigid Injection Molding Biodegradable Polylactic Acid is shipped as non-hazardous, solid pellets in sealed moisture-barrier bags or lined containers. Transport under dry, ambient conditions, away from direct sunlight, heat, and moisture. No dangerous goods classification or special shipping documentation is normally required; standard freight handling applies. |
| Storage | Store INZEA F29 HT 30 in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and moisture. Keep in sealed original packaging to prevent moisture absorption. Maintain moderate temperature and low humidity. Avoid prolonged storage near strong oxidizers. Follow supplier recommendations, use FIFO stock rotation, and dry before processing if specified. |
| Shelf Life | Shelf life: typically 24 months from production date when stored sealed in original packaging, dry conditions, below 30°C, away from sunlight. |
In high-volume thin-wall conversion of disposable cutlery and single-service food-contact articles, INZEA F29 HT 30 is specified where the finished part must retain cutlery tine stiffness, cup rim concentricity, and base flatness after short contact with hot serving temperatures. The resin is loaded into a desiccant dryer with a closed-loop dry-air circuit; supply-air dew point is maintained at ≤ −40 °C and return-air moisture monitoring is set to reject lots exceeding 250 ppm residual moisture in granules. Pellet drying at 80 °C ± 5 °C for 4 h is applied before the feed hopper is sealed with dry-air purge at 0.5–1.5 m³/h per 50 kg hopper capacity. The injection unit is configured with a three-zone screw of 20:1–24:1 L/D, compression ratio 2.2:1–2.8:1, and check-ring clearance below 0.05 mm to limit melt hang-up. Barrel set points from feed to nozzle are held between 175 °C and 210 °C, with the front zone and nozzle at the upper boundary only when hot-runner pressure drop exceeds 30 bar. Actual melt temperature measured by an insertion probe is kept at 185–205 °C; residence time above 210 °C must not exceed 300 s, otherwise lactide regeneration and volatile decomposition products appear as silver streaks and knit-line embrittlement. For articles below 2.0 mm wall thickness, mould temperature is initially set at 25–50 °C for short cycle time; however, when the application requires spoon-bowl edge retention after exposure to water at 80–90 °C, the tool is shifted to 85–100 °C and cooling time is extended by 15–30 s per 1.0 mm wall increment to promote spherulitic crystallisation. Gate position is set in the thickest section of the cutlery handle or container base, with a cold-sprue gate diameter of 1.5–2.5 mm and valve-gated hot-tip diameter of 0.8–1.2 mm for stack moulds. Clamp tonnage is calculated on projected area at 350–600 kg/cm² cavity pressure for thin-wall foodservice articles; a 16-cavity fork mould running at 8–12 s cycle time requires continuous monitoring of nozzle drool and tip crystallisation because the low-melt-strength behaviour of PLA can generate stringing when screw cushion falls below 2 mm.
At the compounding and conversion stage, the material is normally processed as 100 wt% INZEA F29 HT 30 without dilution by fossil-based polymers, because any non-PLA fraction appears as persistent residue in the final compost and can invalidate disintegration measurements under EN 13432 and ASTM D6400-19. Post-industrial regrind from the same food-contact production line may be reintroduced at 10–20 wt% only if the regrind stream is closed, single-source, and subjected to the identical drying protocol; higher regrind addition reduces spiral-flow length by 5–15% and increases edge chipping in fork tines and spoon rims. Food-contact compliance for coated or uncoated PLA cutlery is evaluated by overall-migration testing according to DIN EN 1186-1:2007-02, with simulant selection based on the whole-article surface-to-volume ratio; the overall migration limit for plastics in contact with food is 10 mg/dm² under EU Regulation (EU) No 10/2011. Nitrosamine-free colour masterbatch is restricted to 2–4 wt% addition to maintain melt strength and to avoid shifting melt volume-flow rate outside the narrow lot specification band associated with cavity-fill reproducibility. Terminal product types include disposable spoons, forks, knives, cup lids, portion cups, meal trays, sauce cups, and fast-food clamshell inserts. The principal operational boundary for thin-wall foodservice articles is continuous hot holding above 80–90 °C, where local deformation occurs under sustained compressive load; short contact with hot soup at 85–95 °C for 15–30 min is within the use range for rigid cutlery, but clamped sealing or stacking under load in a heated cabinet exceeds the service window.
Single-serve beverage capsules and temperature-resistant portion packs require injection moulds with 32-cavity or higher configurations, hardened ejection sleeves, and hot-runner valve stems with stroke control below 0.1 mm; melt is introduced through a balanced manifold with externally heated nozzles at 195–205 °C. Cavity fill is completed in 0.2–0.6 s, followed by switch-over to hold pressure at 800–1200 bar hydraulic pressure for 0.3–0.8 s, after which the gate freezes when the cavity-pressure transducer at the end of flow path decays to 40–60 bar. The cooling sequence uses a two-stage mould-temperature profile: an initial tool surface temperature of 95–110 °C is held for 10–15 s to nucleate and grow crystals in the capsule wall, followed by a chiller-assisted reduction to 35–45 °C before ejection. This two-stage profile is necessary because a cold mould alone produces a capsule that exhibits rim ovality after contact with water at 88–93 °C, whereas prolonged isothermal mould residence at 95–110 °C increases cycle time and produces ejection damage at the capsule rim. Capsule rim thickness is typically 0.8–1.4 mm; sidewall thickness is 0.5–0.9 mm, and the top sealing-foil seat is maintained within ±0.05 mm flatness across the diameter. Mould venting depth is limited to 0.01–0.02 mm to prevent flash on the sealing surface while still exhausting volatiles from the hot mould.
Formulation additions for capsule shells made from INZEA F29 HT 30 are restricted to mineral nucleants and heat stabilizers already incorporated in the base grade; converter-added masterbatch is not recommended above 2 wt% because capsule sealing occurs through heat-seal lacquer adhesion and any lubricant bloom disrupts peel force. If colour masterbatch is used, a desiccant-dried, PLA-based carrier containing only food-contact-approved pigments is selected; the addition level is fixed at 1–3 wt% to keep nozzle melt temperature from falling below 185 °C. Post-industrial regrind is acceptable at 8–12 wt% only when the ground flake is sieved to 4 mm and dust content is held below 0.3 wt%, because excessive dust raises apparent viscosity and creates black specks on the capsule sealing surface. Compliance under food-contact legislation follows EU Regulation (EC) No 1935/2004 and EU Regulation (EU) No 10/2011, with specific attention to the overall migration limit of 10 mg/dm² and organoleptic contamination testing described in DIN EN 1230-1:2010-04. Compostability certification for beverage capsules is assessed under EN 13432 or ISO 17088, and biobased carbon content is often verified through ASTM D6866-21. Terminal product forms include coffee capsules intended for polypropylene-compatible sealing films, tea pod bases with integrated filter channels, milk frother pod shells, and hot-chocolate capsules with embossed sidewalls for heat-exchange control. The operational limit is sustained contact with water above 95 °C for more than 3–5 min under internal pressure; this condition exceeds the mechanical resistance of a rigid PLA capsule shell and may cause sidewall deformation before seal failure.
| Control point | Method or equipment | Typical industrial target | Production implication |
|---|---|---|---|
| Dry-air dew point | Desiccant wheel, dew-point transmitter | ≤ −40 °C | Prevents hydrolytic molecular-weight loss during plasticating |
| Residual pellet moisture | ISO 15512:2019 | <250 ppm | Reduces splay, viscosity drift, and screw torque variation |
| Drying residence | Desiccant batch dryer | 4 h at 80 °C ± 5 °C | Avoids cold slugs and feed starvation in continuous moulding |
| Nozzle melt temperature | Insertion thermocouple | 185–205 °C | Balances viscosity and degradation risk |
| Hot-barrel residence | Moulding-cycle audit | ≤300 s above 210 °C | Limits lactide regeneration and acetaldehyde-adjacent odour |
| Cold mould surface | Mould-temperature controller | 25–50 °C | Short cycle; reduced crystallinity and lower heat resistance |
| High-temperature mould | Pressurised water or oil thermolator | 85–110 °C | In-mould crystallisation; critical for hot-contact rigidity |
| Cooling time per wall thickness | Ejection-temperature audit | 15–30 s/mm | Prevents ejection distortion at thick ribs and bosses |
| Screw back pressure | Hydraulic injection unit | 5–15 bar | Improves melt homogeneity without excessive shear heating |
| Screw geometry | General-purpose polyolefin screw | 20:1–24:1 L/D, 2.2:1–2.8:1 compression ratio | Maintains low residence time and prevents solid-bed plugging |
Thick-wall cosmetic containers with wall sections between 3 mm and 8 mm present ejection and dimensional-control challenges because PLA heat transfer is lower than that of polypropylene and shrinkage anisotropy increases with section depth. For a jar or cap moulded from INZEA F29 HT 30, nozzle melt temperature is kept at 180–195 °C, lower than the thin-wall foodservice profile, to reduce drool and prevent premature skin formation. Injection speed is profiled as a two-step ramp: a moderate first stage at 40–80 mm/s screw advance prevents jetting, followed by a reduced second stage at 15–30 mm/s to allow the flow front to pack thick sections without gas entrapment. Mould temperature is raised to 85–105 °C using pressurised water circuits, and hold pressure is limited to 300–600 bar hydraulic pressure because high pack pressure at elevated mould temperature causes gate blush and overpacking at the base. Sink marks at the intersection of the jar sidewall and bottom are managed by designing a minimum corner radius of 3–5 mm and by placing the gate at the geometric centre of the base with a diameter of 2.0–3.5 mm. Cooling time before ejection is typically 60–120 s depending on wall thickness; ejection is set only when cavity-surface temperature measured by infrared pyrometry falls below 55 °C to avoid claw marks from ejection pins.
Formulation for cosmetic packaging made from INZEA F29 HT 30 commonly includes 2–4 wt% of a PLA-based masterbatch containing cosmetic-approved pigments and opacity agents; pearlescent effect masterbatch is added at 0.5–1.5 wt% only when the particle size is below 15 µm to avoid visible flow lines around curved surfaces. External mould-release agents are restricted to formulations that do not impair pad printing or hot-stamping adhesion; volatile content in the release agent must be below 0.1 wt% to prevent staining on high-gloss surfaces. Regulatory compliance for cosmetic packaging is governed primarily by REACH Regulation (EC) No 1907/2006 Annex XVII, the General Product Safety Directive, and EU Regulation (EC) No 2023/2006 for good manufacturing practice; if the brand intends the jar to be refillable or reused with food surrogates, migration testing under EU Regulation (EU) No 10/2011 may also be required. Terminal product types include cream jars, loose-powder compacts, lipstick cases, airless-pump collars, bottle caps, and snap-fit travel pouches. The operational boundary for cosmetic applications is long-term exposure to formulations containing more than 30% ethanol or strong polar solvents, because PLA may show environmental stress cracking; published data for this specific product configuration is limited, and compatibility testing under simulated use temperature is required before commercial specification.
Dry indoor consumer durables and office articles are selected for the high stiffness and matte surface of the grade where polystyrene would fail under repeated flexural loading or consumer incineration concerns. Tool design for these products uses polished cavities with draft angles of 1.5–3.0° on textured surfaces and ejection pins placed on hidden surfaces to reduce visible witness marks. The melt is processed at 185–200 °C, with a screw speed of 80–150 rpm and back pressure of 5–10 bar; injection speed is kept in the middle range to avoid shear-induced crystallisation streaks when the flow front passes through ribs and side-action features. Mould temperature for dry indoor durables is set at 40–70 °C, avoiding full crystallisation when the part is not exposed to hot water or high ambient heat. Regrind addition in non-food indoor durables is allowed up to 25 wt% if the reclaimed material is sorted to avoid contamination from soft components such as labels, adhesives, and elastomeric feet. Products with snap-fit closures require careful design because the material has high tensile modulus but limited notched-impact resistance; snap-arm root radii below 0.8 mm are avoided, and snap deflection is kept below 50% of the material yield strain.
Compliance for office and consumer durable articles is grounded in REACH Regulation (EC) No 1907/2006 Annex XVII and, for articles with toy-like appearance, the EU Toy Safety Directive 2009/48/EC with element-migration limits according to EN 71-3:2019+A1:2021. Flame-retardant additives are not considered standard practice for PLA-based office articles, as the material is not specified for electronic enclosures requiring UL 94 V-0; therefore, application boundaries exclude items placed near unguarded heat sources. Formulation additions include colour masterbatch at 1–4 wt% and an internal slip additive at 0.2–0.5 wt% only where sliding drawer features require lower surface friction. Terminal product types include desk organisers, document trays, pen storage modules, display stands, storage baskets, wall-mounted accessory holders, and non-load-bearing retail fixture elements. Repeated drop testing according to ASTM D5276-19 exposes the main failure mode at thin moulded-in hinges and snap hooks; such features should either be thickened or replaced by separate assembled hardware because rigid PLA is not suitable for living hinges under repeated flexural stress.
| Sector | Regulatory framework | Test standard or method | Limiting criterion or condition |
|---|---|---|---|
| Food-contact tableware and cutlery | EU Regulation (EU) No 10/2011, EC 1935/2004 | DIN EN 1186-1:2007-02 | Overall migration 10 mg/dm² |
| Industrial compostable rigid packaging | EU Directive 94/62/EC, EN 13432, ISO 17088 | ASTM D6400-19, ISO 14855-1 | Disintegration ≥90% at 12 weeks, biodeg ≥90% at 6 months |
| Coffee capsules and hot-contact portions | EU Regulation (EU) No 10/2011, EC 1935/2004 | DIN EN 1230-1:2010-04 | No organoleptic transfer; hot-water exposure limit 95 °C |
| Cosmetic packaging | REACH Annex XVII, EU 2023/2006 GMP | REACH SVHC screening | SVHC content <0.1 wt% per article |
| Consumer durables and office articles | REACH Annex XVII, EU Toy Safety Directive 2009/48/EC | EN 71-3:2019+A1:2021 | Heavy-metal migration limits by element |
| Horticultural and outdoor rigid articles | EN 13432, REACH Annex XVII | ISO 17556:2019 for soil reference | Soil degradation is not equivalent to home compostability |
Horticultural trays, vine clips, and rigid tag stakes converted from INZEA F29 HT 30 are typically shot on single-cavity to 8-cavity cold-runner tools with open nozzles; the absence of hot-runner valve pins reduces thermal mass in the runner and permits a lower melt temperature of 180–195 °C for thin clip features. The melt is introduced through rectangular edge gates with widths of 4–8 mm and depths of 0.8–1.2 mm, generating flat flow fronts that avoid jetting in long side-wall sections. Mould temperature is generally set to 30–50 °C unless the clip is exposed to direct sunlight; for outdoor exposure, the tool temperature is raised to 85–95 °C and the part is annealed in-mould for 20–40 s to reduce the gap between ambient service thermal expansion and as-moulded shrinkage. Plant tags are printed with UV-curable ink after adhesion promotion; corona treatment of 38–42 mN/m is monitored by test inks on the first off-line samples. Terminal product types include nursery pots, seed-starting trays, hanging-basket drip trays, vine clips, tree-seedling protection collars, and horticultural marking stakes.
Formulation for horticultural items may include 2–5 wt% of a PLA-based masterbatch containing iron oxide pigments and weathering stabilizers; carbon black masterbatch is added at 1–2 wt% to achieve opacity but can reduce compostability screening performance if the carbon black inhibits microbial access. A fully biodegradable chain extender is limited to 0.3–0.8 wt% in thin-stake applications because higher addition raises nozzle melt pressure and increases screw-drive torque. Compliance for hazard-based requirements follows REACH Regulation (EC) No 1907/2006 Annex XVII and, for articles that may be handled by children such as decorative plant sticks, EN 71-3:2019+A1:2021 migration limits for heavy metals. Industrial compostability under EN 13432 does not imply rapid soil degradation; soil-biodegradation testing under ISO 17556:2019 may be used only as an environmental reference and not as a substitute for home-compost or industrial-compost certification. The material is not suited to permanent below-soil structural components where load-bearing performance must be retained beyond a single growing season.
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INZEA F29 HT 30 is a rigid injection molding grade of biodegradable polylactic acid. The compound combines a PLA matrix with a mineral filler system at a nominal content of 30 wt% and is supplied as cylindrical granules for conventional reciprocating-screw injection molding machines. The grade is intended for short-cycle production of rigid articles that require elevated heat resistance relative to unfilled PLA and must retain industrial compostability. Published datasheet values include a density of 1.35 g/cm³ according to ISO 1183-1, melt flow index of 15 g/10 min at 190 °C/2.16 kg according to ISO 1133-1, tensile modulus of 4,000 MPa according to ISO 527-2, flexural modulus of 4,200 MPa according to ISO 178, and heat deflection temperature of 95 °C at 0.45 MPa according to ISO 75-2 method B. Elongation at break remains in the low single-digit range, as expected for a rigid mineral-filled PLA compound.
The primary distinction is thermal resistance. Unfilled PLA injection grades typically display heat deflection temperatures under 0.45 MPa between 50 °C and 60 °C, which limits use for hot-fill lids and articles exposed to 80 °C dishwashing. The mineral filler and nucleation package in INZEA F29 HT 30 raise the 0.45 MPa heat deflection temperature to approximately 95 °C, while the Vicat softening temperature is reported near 118 °C under 10 N load according to ISO 306/A50. Flexural modulus also increases from approximately 3,200 MPa for unfilled PLA to 4,200 MPa, enabling thinner wall sections under equivalent stiffness design rules. Impact strength is reduced compared with tough bio-polyesters but remains adequate for rigid clips, trays, and cutlery.
| Property | Test method | INZEA F29 HT 30 | Unfilled PLA injection grade | 20 wt% talc-filled PP copolymer |
|---|---|---|---|---|
| Density | ISO 1183-1 | 1.35 g/cm³ | 1.24 g/cm³ | 1.05 g/cm³ |
| Melt flow index | ISO 1133-1 | 15 g/10 min at 190 °C/2.16 kg | 10–20 g/10 min at 190 °C/2.16 kg | 12 g/10 min at 230 °C/2.16 kg |
| Tensile modulus | ISO 527-2 | 4,000 MPa | 3,200 MPa | 2,500 MPa |
| Flexural modulus | ISO 178 | 4,200 MPa | 3,500 MPa | 2,800 MPa |
| Heat deflection temperature, 0.45 MPa | ISO 75-2/B | 95 °C | 55 °C | 110 °C |
| Vicat softening temperature, 10 N | ISO 306/A50 | 118 °C | 58 °C | 150 °C |
| Notched Izod impact, 23 °C | ISO 180/A | 2.5 kJ/m² | 3.0 kJ/m² | 3.5 kJ/m² |
The comparative data indicate that INZEA F29 HT 30 occupies a position between unfilled PLA and talc-filled polypropylene: it loses some ductility and thermal margin to the polyolefin but gains industrial compostability and renewable-carbon content. Published data for exact impact performance under frozen-food conditions is limited; validation is required for service below −20 °C. The 0.45 MPa HDT-B value is a short-term heat resistance indicator and not a continuous service ceiling.
Pre-drying is mandatory when storage humidity has exceeded 60% RH for more than 48 h. A desiccant dryer capable of a dew point of −40 °C or lower is used at 80 °C for 4 h, targeting residual moisture below 250 ppm by ISO 15512. Wet material undergoes hydrolytic chain scission during plastication, producing a drop in melt viscosity, gate splay, and loss of part surface definition. Regrind from dried runner systems is usable up to 20 wt% when re-dried; higher regrind fractions increase lot-to-lot viscosity scatter in production-scale hopper loaders.
For a 20:1 L/D general-purpose screw with a free-flow check ring, barrel settings from feed throat to nozzle are 160 °C to 190 °C. The metering zone should be held below 195 °C, because a positive deviation of 5 °C can increase shear heating and reduce apparent melt viscosity beyond the specified melt flow index. Nozzle temperature is set at 190–200 °C, and a shut-off nozzle is preferred to prevent drool. Back pressure is maintained at 5–10 bar; higher back pressure increases screw recovery time and filler attrition without improving melt homogeneity. Screw recovery time on a 30 mm screw for a shot weight near 50 g is typically 2–4 s at 100–150 rpm. Screw speeds above 150 rpm may generate excessive shear heating and should be avoided for heat-sensitive PLA compounds.
Mold temperature is generally 20–30 °C for thin-wall rigid parts. Raising mold temperature to 40–60 °C improves packing and surface replication but increases cycle time by 5–15 s depending on wall thickness. For a 1 mm wall, fill times should not exceed 0.5 s; slow injection permits gate freeze before full packing. Clamp force requirements are 5–7 kN/cm² of projected area for wall thicknesses from 1.0 mm to 2.5 mm. Tools with flow paths above 200 mm may require higher packing pressures but not proportionally higher clamp tonnage because the PLA melt solidifies rapidly and pressure transfer is limited by gate freeze.
Production-scale observations on cold-runner tools indicate that unbalanced runner diameters below 4 mm create shear-induced filler orientation differences between cavities, producing warpage deviations of 0.3 mm on a 150 mm flow length. Hot-runner valve-gate systems reduce this effect but require cavity fill monitoring to avoid overpacking beyond 10% cavity volume. Gate diameters below 0.8 mm are not recommended; shear rates at the gate can exceed 10,000 s⁻¹ and produce flow marks or local degradation. Published capillary rheometry data for this specific filled formulation is limited, but mineral-filled PLA melts typically exhibit power-law shear thinning with an index between 0.5 and 0.7 over shear rates from 100 s⁻¹ to 1,000 s⁻¹ at 190 °C.
Residence time at melt temperature should not exceed 5 min. Purge material after interruptions longer than 5 min with unfilled PLA or a commercial purge compound without abrasive fillers. Extended residence produces lactide formation and a distinct acrid odor; mechanical properties drop before visible discoloration is apparent. Use of melt accumulators is discouraged because melt held at 190 °C for 10 min can lose more than 10% of its original molecular weight, measured by size-exclusion chromatography. The mineral filler phase is slightly abrasive; mold inserts in high-flow areas should be hardened to 50 HRC or higher, and production campaigns above 50 t should use bimetallic barrels and hard-coated screws to maintain recovery consistency.
Mold shrinkage measured after 48 h at 23 °C according to ISO 294-4 is 0.3–0.5% in flow direction and 0.4–0.6% transverse. Shrinkage anisotropy arises from platelet filler orientation along melt-flow streamlines and is increased by gate placement that creates unbalanced filling. Equilibrium moisture content at 23 °C and 50% RH is approximately 0.3 wt% according to ISO 62; dimensioned parts intended for humid service should be conditioned before inspection because PLA absorbs moisture and exhibits slight swelling relative to polyolefins. Part dimensions stabilize after post-mold conditioning at 23 °C for 24 h. Immediate measurement after ejection can under-report shrink because the mineral-filled PLA continues secondary crystallization during the first hours after demolding.
Substitution of talc-filled PP in rigid packaging and food-service articles is constrained by waste-treatment infrastructure and certification. INZEA F29 HT 30 is positioned for applications where the converter must demonstrate compliance with organic-recovery standards and where the lower heat resistance relative to PP is acceptable. The grade is not a home-compostable product; performance is assessed under industrial composting conditions with controlled thermophilic temperatures above 58 °C. For US applications, final food-contact status must be verified under 21 CFR 174.5 and any applicable Food Contact Notification.
| Regulatory / certification domain | Reference document | Data point or threshold |
|---|---|---|
| Industrial compostability of packaging | EN 13432:2000 | Disintegration ≥ 90% of dry weight < 2 mm after 12 weeks; biodegradation ≥ 90% relative to cellulose within 180 days |
| Biodegradable plastics under US ASTM scheme | ASTM D6400-21 | Mineralization ≥ 90% within 180 days; disintegration and ecotoxicity per standard |
| Global specification for compostable plastics | ISO 17088:2021 | Harmonized pass/fail criteria for compostability |
| European chemicals inventory | REACH Regulation (EC) No 1907/2006 | SVHC content below 0.1 wt% per article; Safety Data Sheet compliance |
| Hazardous substances in electrical/electronic equipment | RoHS Directive 2011/65/EU Annex II | Pb, Hg, Cr6+, PBB, PBDE below 0.1 wt%; Cd below 0.01 wt% |
| Food contact plastics | EU Regulation 10/2011 | Overall migration limit 10 mg/dm²; specific migration limits per additive |
Relative to PBAT-based biodegradable compounds, INZEA F29 HT 30 provides higher flexural modulus and lower elongation at break. A PBAT-rich blend may show elongation at break above 100% according to ISO 527-2, whereas filled PLA remains in the 2–3% range. Relative to PHA/PLA blends, the product provides a wider injection molding window and lower melt processing pressure, but continuous service temperature above 70 °C under load is not supported by the available data. Against talc-filled PP, the principal trade-off is thermal resistance and impact strength; the PLA grade retains that limitation despite filler reinforcement.
Operational boundaries include continuous service temperatures above 70 °C, direct steam sterilization, and prolonged exposure to high-humidity environments without protective packaging. The grade is unsuitable for applications requiring elastomeric recovery or repeated flexure beyond low-strain rigid deflection. Dried granules should be stored in sealed moisture-barrier packaging and processed within 4 h after dryer discharge; hopper residence time should not exceed 1 h in high-humidity production halls. Combination with amine-based additives is not recommended because residual alkalinity can accelerate PLA hydrolytic degradation at melt temperature.