| HS Code | 497860 |
| Productname | INZEA F28 HT |
| Materialfamily | Polylactic Acid (PLA) |
| Materialtype | Rigid compostable biopolymer compound |
| Renewablecontent | 80% |
| Compostability | Compostable according to EN 13432 |
| Density | 1.25 g/cm3 |
| Meltflowrate | 10 g/10 min at 190°C/2.16 kg |
| Tensilemodulus | 3500 MPa |
| Tensilestrength | 50 MPa |
| Elongationatbreak | 3% |
| Flexuralmodulus | 3800 MPa |
| Flexuralstrength | 80 MPa |
| Heatdeflectiontemperature | 85°C at 1.8 MPa |
| Vicatsofteningtemperature | 120°C |
| Processingmethod | Injection molding |
| Meltprocessingtemperature | 190-220°C |
| Moldtemperature | 20-60°C |
| Dryingtemperature | 80°C |
| Dryingtime | 4 hours |
| Shrinkage | 0.5-0.8% |
As an accredited INZEA F28 HT Rigid 80% Renewable Compostable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INZEA F28 HT Rigid 80% Renewable Compostable Polylactic Acid is packaged in 25 kg moisture-resistant paper sacks, palletized for shipping. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): INZEA F28 HT Rigid, 80% renewable compostable polylactic acid, and securely palletized for safe chemical transport. |
| Shipping | Typically shipped as non-hazardous, compostable PLA pellets in sealed moisture-barrier bags or foil-lined cartons, palletized and stretch-wrapped. Not regulated by DOT, ADR, IMDG, or IATA. Keep dry, cool, and protected from heat, UV, and contamination. Standard freight is suitable. |
| Storage | Store INZEA F28 HT in its original, sealed packaging in a cool, dry, well-ventilated warehouse. Protect from moisture, direct sunlight, heat sources, and strong odors. Recommended conditions: 10–25 °C and relative humidity below 50%. Keep containers closed, away from incompatible materials and ignition sources. Use within the stated shelf life; avoid prolonged humid or hot storage to prevent degradation. |
| Shelf Life | Shelf life: approximately 12 months when stored sealed in a cool, dry place, away from moisture, heat, and direct sunlight. |
On a 16-cavity hot-runner cutlery stack, injection molding of single-use forks, spoons, knives, and stirring sticks from INZEA F28 HT Rigid 80% renewable compostable polylactic acid compound is run on electrically driven reciprocating-screw machines with L/D 20:1–24:1 and reverse-taper nozzle shut-off. The formulation at line start consists of 100 wt% pre-dried compound; closed-loop regrind from sprue and cold-runner scrap is incorporated at 10–20 wt% only after the regrind fraction has been re-dried to <200 ppm moisture and its melt flow index shift is below 2.0 g/10 min at 210°C/2.16 kg. A 2–4 wt% commercial PLA-based masterbatch is dosed at the throat for colour, not a polyolefin carrier, to preserve EN 13432:2000 disintegration performance. Drying uses a desiccant-bed dryer with dew point −40°C, 80°C for 4 h, hopper residence time not exceeding 6 h. Melt temperature measured at the nozzle stays within 200–210°C; barrel zone set points from feed to nozzle are 180°C, 195°C, 200°C, 205°C, and 210°C. Mold temperature is controlled at 90–100°C via pressurized water or oil thermolators; below 85°C crystallinity development is incomplete and heat resistance collapses on contact with hot food above 70°C. Clamp force is calculated at 4.8 kN/cm² projected cavity area; the 16-cavity family tool with heated sprue bushing operates with 55–65 t clamp force. Injection velocity is profiled 30–45 cm³/s to avoid jetting; holding pressure 60–80 MPa for 1.5–2.5 s; cooling time 12–18 s depends on wall thickness 2.0–3.0 mm. The terminal articles are certified to EN 13432:2000 and, for food contact, EU Regulation 10/2011 with overall migration below 10 mg/dm² under simulant D1 and D2. ASTM D6400-21 applies for North American compostability claims; renewable carbon content is verified by ASTM D6866 Method B.
Roll-fed thermoforming of INZEA F28 HT Rigid sheet for deli trays uses a sheet formulation of 100 wt% virgin compound with 15–25 wt% internal edge-trim regrind, with the regrind fraction not exceeding 25 wt% because repeated extrusion lowers intrinsic viscosity and reduces puncture resistance under ISO 6603-2 instrumented impact testing; the sheet is extruded to 0.8–1.2 mm gauge on a single-screw line of L/D 28:1–32:1 with a gear pump and flexible-lip flat die at melt temperature 190–205°C, then conveyed through a three-roll stack set at 40–60°C. The roll-fed thermoformer uses contact heater surface temperatures of 100–120°C, plug-assist temperature 80–100°C, and forming mold temperature 60–80°C; plug material is thermally stable syntactic foam, and plug speed is reduced to 20–25 mm/s to prevent chill marks on tray bottoms. Corners are designed with radius not below 2 mm and draft angle 3–5° to reduce oriented stress that later manifests as edge cracking during distribution. Compliance for the finished deli trays, produce punnets, and tray lids includes EN 13432:2000, ISO 17088:2021, EU Regulation 10/2011, and ASTM D6400-21 where North American claims are made.
Because residual lactide gas evolution affects high-gloss cosmetic surfaces, tooling for cosmetic jars, compacts, and lipstick bases is configured with polished A2 steel inserts, valve-gated hot runners, and parting-line venting. The formulation at the press is 100 wt% INZEA F28 HT Rigid; internal cold-runner regrind is capped at 10 wt% because flow-line visibility on high-gloss surfaces becomes detectable above that threshold, and no post-consumer regrind is used for traceability and batch documentation. Drying before molding uses a desiccant-bed dryer at 80°C for 4–6 h to reach <250 ppm moisture. Melt temperature is maintained at 200–215°C, with mold temperature at 95–105°C to promote crystallization and dimensional stability in warm retail or bathroom environments. After ejection, parts are annealed at 70–80°C for 30–60 min; unannealed jars show post-mould shrinkage up to 0.35 % within 24 h, measured according to ISO 294-4. The compliance framework includes REACH Regulation (EC) No 1907/2006, EN 13432:2000 for industrial compostability, and natural-origin index calculation under ISO 16128-1:2016.
| Application category | Compostability standard | Food-contact framework | Renewable carbon method | Chemical safety framework |
|---|---|---|---|---|
| Injection-moulded cutlery | EN 13432:2000, ASTM D6400-21 | EU Regulation 10/2011 | ASTM D6866 Method B | REACH Regulation (EC) No 1907/2006 |
| Thermoformed food trays | EN 13432:2000, ISO 17088:2021 | EU Regulation 10/2011 | ASTM D6866 Method B | REACH |
| Cosmetic packaging | EN 13432:2000 | Not food-contact | ISO 16128-1:2016 calculation | REACH Regulation (EC) No 1907/2006 |
| Nursery pots and seedling trays | EN 13432:2000, ISO 17088:2021 | Not food-contact | ASTM D6866 Method B if claim made | REACH |
| Hot beverage lids | EN 13432:2000, ASTM D6400-21 | EU Regulation 10/2011; FDA FCN | ASTM D6866 Method B | REACH |
| Electronics packaging | EN 13432:2000 | Not food-contact | ASTM D6866 Method B if claim made | REACH, RoHS Directive 2011/65/EU Annex II |
For nursery pots and seedling trays converted from this compound, extruded sheet at 185–205°C and 0.5–0.8 mm gauge is thermoformed with 10–20 wt% post-industrial edge-trim regrind added only after verifying ISO 179-1 Charpy notched impact remains above 6 kJ/m²; the finished 10–15 cm pots and 72-cell seedling trays are certified to EN 13432:2000 and ISO 17088:2021 for industrial composting only, not for direct soil biodegradation.
The hot-runner cold-runner mix ratio is treated as a critical parameter in coffee cup lid molding because the thin-wall flow path of 0.8–1.2 mm amplifies viscosity shifts. At line start, the compound is used at 100 wt%; closed-loop regrind is added at 10–15 wt% and must not exceed 20 wt% without verifying that spiral-flow length at 205°C remains within ±10 % of virgin compound. Drying with a desiccant-bed dryer at 80°C for 4 h to <200 ppm moisture is mandatory before each molding run. Melt temperature is kept at 200–210°C; mold temperature is controlled at 95–105°C to achieve the heat-deflection performance required for lids in contact with 90°C beverages. Hot-runner manifold and nozzle temperatures are set 5–10°C above the nozzle melt temperature, with sequential valve-gate opening to avoid weld-line brittleness. Clamp force on a 12-cavity lid stack is typically 80–100 t, with injection pressure 90–120 MPa and holding pressure 50–70 MPa for 1.0–1.8 s. Contact compliance is governed by EU Regulation 10/2011 with overall migration below 10 mg/dm², EN 13432:2000 for industrial compostability, and FDA food-contact status must be established through a food-contact substance notification applicable to the specific compound; ASTM D6400-21 supports compostability claims in North America. Terminal parts are hot-beverage lids and sipper caps.
| Converting line | Melt/stock temperature | Mold/forming temperature | Moisture target | Regrind boundary |
|---|---|---|---|---|
| Injection molding cutlery | 200–210°C | 90–100°C | <250 ppm | 10–20 wt% |
| Thermoformed deli trays | 190–205°C | 60–80°C | <250 ppm | 15–25 wt% |
| Cosmetic jar molding | 200–215°C | 95–105°C | <250 ppm | 10 wt% |
| Nursery pot thermoforming | 185–205°C | 60–80°C | <250 ppm | 10–20 wt% |
| Hot beverage lid molding | 200–210°C | 95–105°C | <200 ppm | 10–15 wt% |
| Electronics clamshell thermoforming | 190–210°C | 100–120°C | <250 ppm | 10 wt% |
Although published data for electronics packaging in this specific configuration is limited, consumer electronics clamshells and insert trays formed from this compound use 100 wt% INZEA F28 HT Rigid with regrind limited to 10 wt% because point-of-sale optical clarity and surface finish on 0.7–1.0 mm clamshells decline at higher recycled content; sheet extrusion at 190–210°C and thermoforming at 100–120°C produce the clamshells, and the downstream articles are assessed under REACH Regulation (EC) No 1907/2006, RoHS Directive 2011/65/EU Annex II, and EN 13432:2000 for industrial compostability. The stated set points are derived from industrial PLA sheet extrusion and should be qualified by inline DSC crystallinity measurement.
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INZEA F28 HT Rigid 80% Renewable Compostable Polylactic Acid is produced under the INZEA brand as a rigid polylactic acid compound. The grade designation F28 HT separates this material from flexible film grades and from standard amorphous PLA: the HT suffix indicates a heat-resistant formulation, while the 80 % renewable carbon claim refers to the biogenic fraction of total organic carbon rather than to a mechanical property. Polylactic acid is a linear aliphatic polyester obtained by ring-opening polymerisation of lactide derived from fermented plant starch or sugar. The final behaviour of the compound depends on stereochemical composition, nucleating agents, filler content, and melt-processing history. Because additive load and molecular weight vary within manufacturing tolerance, lot-specific data should be taken from the certificate of analysis rather than from generic PLA literature.
The renewable carbon content and compostability of INZEA F28 HT are regulated by separate standards. Renewable carbon is normally measured by ASTM D6866 or EN 16640, both of which distinguish modern biogenic carbon from fossil carbon by isotopic analysis. Compostability is certified under EN 13432 for packaging or ASTM D6400 for plastics intended for aerobic municipal or industrial composting. Certification may impose limits on part thickness, pigmentation, and lamination. These limits are relevant for heat-resistant PLA grades because nucleating agents and mineral fillers can change disintegration kinetics. A formulation that meets the disintegration requirement at 1.5 mm thickness may not automatically meet it at 5 mm wall thickness.
The principal difference is crystallisation behaviour. Standard amorphous PLA parts are usually limited to a heat deflection temperature near 55 °C under ISO 75-2 Method B because the glass transition temperature of PLA is approximately 55–60 °C. High-heat PLA compounds are formulated to develop measurable crystallinity during moulding or annealing, which can raise heat deflection temperature into the approximate class range of 80–110 °C depending on filler content and part geometry. In rigid high-heat PLA, tensile modulus measured by ISO 527-2 typically falls between 3000 MPa and 4200 MPa, while elongation at break remains below 5 %. This is a stiff, low-elongation response. Compared with standard PLA, the processing window narrows because nucleation accelerates solidification. For the F28 HT designation, published data for this specific configuration is limited; the values below represent a class envelope rather than a lot-specific guarantee.
| Property | Test method | Typical class range |
|---|---|---|
| Renewable carbon content | ASTM D6866 / EN 16640 | 80 % nominal |
| Tensile modulus | ISO 527-2 / ASTM D638 | 3000–4200 MPa |
| Heat deflection temperature | ISO 75-2 / ASTM D648 | 80–110 °C |
| Melt mass-flow rate | ISO 1133-1 at 190 °C/2.16 kg | 3–15 g/10 min |
In twin-screw compounding lines with 40:1 L/D and vacuum venting, moisture ingress is the dominant source of batch-to-batch variation. PLA undergoes hydrolytic chain scission at melt-processing temperatures when residual moisture exceeds approximately 250 ppm. Production-scale desiccant dryers should maintain a dew point of -40 °C or lower. A common drying profile is 80 °C for 4 h, but the actual condition must be validated for the specific dryer bed depth and air flow. Residual moisture is measured before extrusion by Karl Fischer titration under ISO 15512. Inadequate drying is observed on the line as screw torque fluctuation, die-lip build-up, splay, and reduced melt strength. These symptoms cannot be corrected by raising barrel temperature because thermal degradation then competes with hydrolysis and further reduces molecular weight.
Injection moulding of rigid HT PLA grades is controlled more by mould-temperature strategy than by melt temperature alone. Barrel profiles from 180 °C to 210 °C are commonly used, with the nozzle held below 220 °C to limit molecular weight loss. Cold-mould cycles at approximately 25 °C are suitable for thin-walled amorphous parts with short cycle targets, but the resulting heat deflection temperature remains close to the glass transition. Hot-mould cycles at 90–110 °C induce crystallisation during filling and packing, raising heat resistance at the cost of longer cycle time and higher mould maintenance. Clamp force requirements follow standard PLA viscosity. A hydraulic injection pressure of 80–120 MPa is typical for rigid PLA compounds, but the exact value depends on gate geometry, wall thickness, and flow length. Hydrocarbon-based mould release agents are generally compatible. Amine-based release agents and amine-containing additives should be avoided because they can accelerate degradation through aminolysis.
The 80 % renewable carbon figure is a supply-chain claim, not a mechanical specification. Under ASTM D6866, the result is reported as the fraction of modern carbon in total organic carbon. Under EN 16640, the result is expressed as biogenic carbon content. These methods rely on isotope ratio measurements and do not identify trace additives or inorganic fillers unless sample preparation accounts for total carbon. Audit documentation should therefore include the certification scope, sample identification, and the exact standard and method used. In European packaging applications, a renewable carbon measurement does not replace conformity to EN 13432 or the applicable compostability certificate. If food-contact use is claimed, migration testing under Regulation (EU) No 10/2011 is also required. The final article must be tested in its actual thickness, surface-to-volume ratio, and intended contact conditions because lactic acid and additive migration depend on the finished part rather than on the polymer resin alone.
Certification bodies such as DIN CERTCO and TÜV Austria operate certification schemes under the relevant compostability standards. The supplier’s certificate number should be verified against the specific product grade and production site. A general brand certificate is insufficient because different INZEA grades can carry different additives, fillers, and thickness limits. The renewable content certificate should also be current: feedstock changes, mass-balance allocation choices, and production location can affect the audit result even if the nominal biobased carbon fraction remains at 80 %.
Compostability under EN 13432 requires four measurable properties: chemical characterisation for regulated metals and hazardous substances; aerobic biodegradation of at least 90 % relative to a reference within 180 days at 58 °C; disintegration with no more than 10 % residue retained on a 2 mm sieve after 12 weeks; and absence of negative effects in ecotoxicity tests specified by the standard. For high-heat PLA compounds, the filler package can slow disintegration if the mineral content is high or if the part thickness exceeds the certification boundary. Similar criteria apply under ASTM D6400, but the test environment and inoculum are defined by that standard. Industrial compost operators may impose shorter residence times than the laboratory test maximum, so passing the standard does not guarantee acceptance at every facility. Compostability does not imply home compostability or anaerobic digestion compatibility unless a separate certification exists. The property also disappears if the material is commingled with conventional plastics, placed in landfill, or incinerated.
In high-humidity storage, PLA compounds absorb moisture from ambient air. At relative humidity above 60 %, pre-drying is mandatory before melt processing. Storage should be in sealed moisture-barrier packaging, and opened bags should be consumed within one shift or re-dried before use. The material is incompatible with prolonged contact with hot alkaline solutions, strong acids, and certain amine-based additives. For extrusion lines, purging with a suitable PLA purge compound before and after processing is recommended to avoid cross-contamination with polyolefin stock. Residual polyolefin domains reduce impact resistance and create visible delamination at part surfaces. The F28 HT grade should not be specified for continuous service above 100 °C unless the part has been crystallised and tested under the actual service load and environment. Heat deflection data are short-term results; they do not guarantee creep resistance at elevated temperature. Where sustained load-bearing performance is required, creep testing under ISO 899-2 or the relevant application standard should be performed.