| HS Code | 718741 |
| Productname | INZEA F29 AL30 |
| Chemicalbase | Polylactic acid (PLA) |
| Processingmethods | Rigid thermoforming and injection molding |
| Appearance | Natural pellets |
| Density | 1.24-1.25 g/cm3 |
| Meltflowrate | 20-30 g/10 min at 190°C/2.16 kg |
| Tensilemodulus | 3500 MPa |
| Tensilestrength | 45-50 MPa |
| Elongationatbreak | 3-5% |
| Flexuralmodulus | 3500 MPa |
| Flexuralstrength | 65-70 MPa |
| Notchedcharpyimpact | 2 kJ/m2 |
| Heatdeflectiontemperature | 55°C at 0.45 MPa |
| Vicatsofteningtemperature | 60°C |
| Meltingtemperature | 150-160°C |
| Glasstransitiontemperature | 55-60°C |
| Biobasedcontent | >70% |
| Biodegradability | Biodegradable |
| Compostability | Compostable according to EN 13432 |
| Certifications | EN 13432, OK compost, DIN CERTCO |
As an accredited INZEA F29 AL30 Rigid Thermoforming/Injection Biodegradable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | INZEA F29 AL30 biodegradable polylactic acid supplied in 25 kg moisture-barrier bags, palletized and stretch-wrapped for industrial handling. |
| Container Loading (20′ FCL) | Container loading (20′ FCL): INZEA F29 AL30 biodegradable polylactic acid in palletized, moisture-protected bags, secured for rigid thermoforming/injection applications. |
| Shipping | INZEA F29 AL30 is shipped as non-hazardous biodegradable polylactic acid resin pellets in moisture-barrier bags, stacked on pallets. Store in cool, dry conditions, away from direct sunlight and heat. Not classified as dangerous goods; no UN number, hazard class, or special transport label required. Handle as a non-hazardous industrial polymer. |
| Storage | Store INZEA F29 AL30 in a cool, dry, well-ventilated area, preferably below 30°C and low humidity. Keep sealed in original packaging, away from direct sunlight, heat, moisture, and incompatible materials. Avoid prolonged humid storage to prevent hydrolytic degradation. Use first-in, first-out rotation. Keep containers closed when not in use, protect from physical damage, and handle with clean, dry equipment. |
| Shelf Life | Shelf life is typically 12 months when stored sealed in a cool, dry place, away from moisture, heat, and direct sunlight. |
Dryer configuration for INZEA F29 AL30 in refrigerated produce-tray sheet extrusion is set to a desiccant bed with a -40 °C dewpoint and 80 °C inlet air for 4 h before processing, targeting a granulate moisture content below 250 ppm and preferably below 100 ppm. Where the grade-specific datasheet is not available, the processing window is benchmarked against amorphous PLA rigid thermoforming grades with melt flow rate checked at 210 °C and 2.16 kg under ISO 1133-1:2022. Extruded sheet for clamshell trays and punnets is run at 0.35 mm to 0.80 mm gauge on a single-screw extruder with 30:1 L/D, barrier screw, screen pack and gear pump, with melt temperature held at 185 °C to 200 °C. The sheet is then reheated to 90 °C to 105 °C surface temperature for contact-plate or tunnel thermoforming; a plug-assist station with syntactic foam or PBT plug reduces wall thinning in corners. Mould temperatures of 30 °C to 45 °C preserve amorphous clarity, and forming air pressure of 4 bar to 6 bar is maintained. Regrind from skeletal trim is introduced at 20 wt% to 30 wt%, but higher regrind ratios reduce elongation at break and increase edge tearing because each heat history advances chain scission. Laser or micro-perforation is applied after forming, and the tray is sealed with PLA-compatible lidding film at 150 °C to 170 °C seal-bar temperature. Terminal articles are trays for whole berries, cherry tomatoes, salad leaves and cut-fruit punnets displayed at 4 °C to 8 °C. Food-contact compliance is evaluated under Commission Regulation (EU) No 10/2011 with overall migration limit 10 mg/dm² for aqueous and acidic simulants, and the tray must not be used above 45 °C because amorphous PLA loses flexural modulus abruptly near its glass transition. The sheet also carries a practical RH limitation: storage at more than 60% RH prior to drying increases purge and die lines because hydrolysis is autocatalytic. If modified-atmosphere packaging is required, perforation geometry, not polymer formulation, is the main control because oxygen transmission of 0.30 mm sheet is validated by ASTM D3985-17 on unperforated control samples.
Melt-phase stability during cup and lid thermoforming is constrained by lactide regeneration above 210 °C and by insufficient sheet plasticity below 85 °C. INZEA F29 AL30 sheet for cold beverage cups is extruded at 190 °C to 200 °C, then post-dried at 60 °C for 2 h if exposed to ambient humidity beyond 30 min. Cups are produced from 0.50 mm to 1.00 mm sheet on a roll-fed thermoformer with upper and lower ceramic heaters; surface temperature is profiled in 5 °C increments from 90 °C to 110 °C and the sag band is corrected by adjusting lower heat flux, not by increasing sheet gauge. Plug-assist timing is set to 0.15 s to 0.30 s delay after transfer, and plug temperature is held at 60 °C to 70 °C to avoid chill marks. Lids are stamped from 0.25 mm to 0.40 mm sheet and require a higher plug speed to prevent premature cooling before draw. After forming, cups are corona-treated to 42 mN/m to 48 mN/m for print adhesion, and quality checks use ISO 527-2:2012 tensile specimens cut from sidewalls. The service boundary is hot-fill capacity: amorphous containers soften near 50 °C measured by ISO 75-2:2013 method B at 0.45 MPa; hence only cold-fill beverages, smoothies, iced coffees and water cups below 40 °C are considered. A crystallizing anneal at 95 °C for 3 min to 5 min can raise HDT, but it also increases haze and is not used for transparent drinkware. Compliance includes Commission Regulation (EU) No 10/2011 and FDA lactic acid clearance under 21 CFR 184.1069, plus EN 13432:2000 if an industrial composting claim is printed. Residual lactide migration into neutral simulant must remain below the specified migration limits in the applicable FCN; published data for this specific grade’s lactide migration is limited.
Injection moulding of disposable cutlery from INZEA F29 AL30 uses a reciprocating screw with 20:1 to 24:1 L/D and a low-shear barrier profile to limit adiabatic heating. Melt temperature at the nozzle is kept between 190 °C and 205 °C, while the mould wall is controlled at 30 °C to 50 °C to produce an amorphous part with low cycle time. Injection pressure of 80 MPa to 120 MPa and holding pressure of 50 MPa to 80 MPa are applied through a cold runner with round or trapezoidal cross-section; hot runners are avoided because stagnation zones above 210 °C accelerate molecular weight loss. Screw speed is capped at 100 rpm to 200 rpm depending on barrel size, and back pressure is set to 0.5 MPa to 1.0 MPa. Drying before moulding is mandatory at 80 °C for 4 h with a desiccant dryer; granulate moisture above 250 ppm produces splay and embrittlement within 15 min at melt temperature. The terminal articles—forks, spoons, knives and sporks—are ejected at 0.5% to 0.8% shrinkage as measured after 24 h per ISO 294-4:2018. Cutlery regrind may be blended up to 20 wt%; impact modifiers are not required for short-term use but notch-sensitive knife serrations need root radii above 0.5 mm. Amine-based additive masterbatches are not added because alkaline residues accelerate PLA ester hydrolysis and cause surface splay. Compliance is assessed under Commission Regulation (EU) No 10/2011 with simulant D1 for ethanol-free aqueous food contact and FDA lactic acid monomer clearance under 21 CFR 184.1069; compostability claims require EN 13432:2000 or ASTM D6400-21 certification of the finished cutlery shape and thickness, not the resin alone. Service temperature is limited to 55 °C: stirring in boiling water or dishwashing above this temperature causes permanent distortion and stress cracking at the gate. Published tensile yield data for this grade are limited; generic PLA rigid injection grades typically show 50 MPa to 60 MPa yield strength under ISO 527-2:2012.
Rigid injection-moulded closures for dry cosmetic powders are produced with INZEA F29 AL30 at melt 195 °C to 210 °C and mould surface 25 °C to 40 °C to maintain high gloss and low haze. Because semicrystalline development is intentionally suppressed, the amorphous closure exhibits a mould shrinkage range of 0.3% to 0.6% measured by ISO 294-4:2018, but the part must be dimensionally validated after 48 h because secondary post-mould shrinkage continues as free volume relaxes. Snap-fit undercuts are limited to 0.4 mm to 0.8 mm per side, and assembly force is predicted from flexural modulus of approximately 3.0 GPa to 3.5 GPa under ISO 178:2019; creep at 40 °C and 80% RH can reduce snap-fit retention force by more than 20% within 72 h, so safety factors of 1.5 are applied to the designed beam deflection. Release masterbatch is dosed at 0.3 wt% to 0.8 wt%, but silicone-based release is preferred over metallic stearates that can produce visible deposit on the polished cavity. Spillages of ethanol-containing formulas above 20 vol% alcohol are not recommended because amorphous PLA undergoes environmental stress cracking in aggressive polar solvents and because migration testing under Commission Regulation (EU) No 10/2011 requires ethanol simulants when alcohol contact is intended. Terminal articles include press-fit sifter inserts, loose-powder jars, compact mirror bodies and protective outer caps, all used at room temperature and not subjected to continuous load. REACH registrations apply to the lactic acid monomer and any included stabilisers, and final packaging must meet Regulation (EC) No 1223/2009 only where the article itself has no direct skin contact or is assessed as a packaging component. Published data for INZEA F29 AL30 under sustained snap-fit load are limited; the above limits are derived from amorphous PLA creep behaviour and should be verified on the specific closure geometry.
| Downstream article | Applicable standard | Test condition | Limit or criterion |
|---|---|---|---|
| Fresh produce tray | Commission Regulation (EU) No 10/2011 | Overall migration, aqueous simulant A, 10 d at 40 °C | 10 mg/dm² |
| Cold beverage cup | EN 13432:2000 | Industrial composting, 58 °C | ≥90% biodegradation in 180 d |
| Disposable cutlery | ASTM D6400-21 | Aerobic composting disintegration | ≥90% after 12 wk |
| Cosmetic closure | REACH Article 33 | SVHC content | <0.1 wt% |
| Horticultural tray | EN 13432:2000 | Industrial compost only | No EN 17033 soil-biodegradability claim |
| Dry-goods blister pack | Directive 94/62/EC | Heavy metals sum | ≤100 ppm |
In short-cycle horticultural propagation trays, the mould-filling behaviour of INZEA F29 AL30 is governed by a melt temperature of 195 °C to 210 °C and an injection speed high enough to fill thin cell walls below 1.2 mm without brittle weld lines. Clamp tonnage is calculated from projected area at 30 MPa to 50 MPa cavity pressure, which is lower than amorphous PET but requires venting depths of 0.02 mm to 0.03 mm to prevent gas burn marks. Mould temperature is split: 30 °C to 40 °C for ejection, or 60 °C to 80 °C when the cells are exposed to direct summer greenhouse temperatures; higher mould temperature promotes clarity loss but improves dimensional retention above 50 °C. The terminal articles are propagation trays, plant labels, pot clips and six-cell inserts for short-season vegetable seedlings. These components are biodegradable only under industrial composting conditions per EN 13432:2000; they do not meet EN 17033 soil-biodegradability and should not be marketed as soil-degrading. Regrind from runner systems and rejected trays is limited to 15 wt% because outdoor UV exposure of reprocessed material accelerates chain scission and leads to premature cracking of label stems. Processing stabilizers are not added for greenhouse use unless UV stabilization is separately validated because common PLA grades are transparent to UV and can lose molecular weight after one season. The main process conflict is over-packing: hold pressure above 80 MPa causes gate freeze but increases residual stress, and ejection above 60 °C part temperature deforms the undercuts used for clip retention.
On a roll-fed line converting dry-goods blisters, INZEA F29 AL30 extruded sheet is dried at 80 °C for 4 h and fed to a three-station thermoformer with a sheet surface temperature of 95 °C to 108 °C. The substitution for amorphous PET becomes critical in plug-assisted formation of deep draw ratios between 1.5:1 and 2.5:1; the plug surface must be heated to 70 °C to 80 °C because PLA sheet tears at corners when the plug dips below 60 °C. Cavity venting is increased to 0.04 mm depth to compensate for lower hot elongation; unlike PET, PLA sheet can exhibit hot tearing if the forming pressure ramp exceeds 1.5 bar/s between 100 °C and 110 °C. Terminal articles are transparent hinged clamshells, tray inserts and snap-fit blisters for batteries, small power tools, toys and dry stationery, where the product is dry and shelf-life is below 24 months at ambient temperature. Sealing is performed with heat, adhesive, or ultrasonic welding at 20 kHz with amplitude 30 µm to 40 µm; radio-frequency sealing is not recommended for PLA in most packaging lines because its dielectric loss behaviour differs from PVC. A slip/antiblock masterbatch is included at 0.1 wt% to 0.3 wt% to prevent nesting of formed blisters during automatic denesting, but excessive loading reduces transparency and seal strength. Packaging compliance is assessed under Directive 94/62/EC heavy-metal limits and Commission Regulation (EU) No 10/2011 for incidental food contact if the blister is used adjacent to confectionery; for non-food dry goods, REACH Article 33 communication applies to any SVHC content above 0.1 wt%. The main operational boundary is humidity: at more than 55% RH warehouse storage, the sheet must be re-dried or formed within 8 h after desiccant drying because moisture regain shifts the forming window and increases blister sidewall haze.
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INZEA F29 AL30 is a rigid polylactic acid (PLA) compound supplied for extrusion thermoforming and injection moulding. The grade is positioned as a biodegradable alternative to amorphous polyethylene terephthalate (A-PET) and high-impact polystyrene (HIPS) in rigid packaging, while retaining the characteristic stiffness and gloss of PLA. The designation F29 AL30 identifies a formulated PLA rather than a neat polymer; the formulation is designed to raise melt strength during sheet extrusion and to reduce edge sag in thermoforming. Typical sheet- and moulded-part performance is evaluated according to ISO 1183-1:2019 for density, ISO 1133-1:2022 for melt mass-flow rate, ISO 527-2:2012 for tensile properties, and ISO 75-2:2013 for heat deflection temperature. Lot-specific values are issued in the supplier’s certificate of analysis, but the product is supplied as a rigid biodegradable thermoplastic suitable for industrial composting under EN 13432:2000.
The main rheological difference is melt strength. Unmodified PLA often exhibits pronounced draw sag and thickness non-uniformity above 110 °C because its extensional viscosity is low and temperature sensitive. The formulated grade contains a processing package that increases melt elasticity enough to maintain sheet gauge within ±5 % across widths up to 800 mm when measured by ASTM D374M. Compared with A-PET, INZEA F29 AL30 has a lower continuous-use ceiling, so it is assigned to cold-fill and ambient packaging rather than hot-fill lines. Compared with HIPS, it shows higher tensile modulus and lower notched impact strength, which shifts design constraints toward stiff thin-walled geometries.
Unlike heat-resistant PLA grades formulated for crystallisation at mould temperatures above 90 °C, F29 AL30 is not intended for hot-fill or dishwasher-load applications. It is also distinct from high-MFR injection grades with values above 20 g/10 min, which are too fluid for stable sheet extrusion. The formulation occupies a narrow rheological window: sufficient viscosity for roll-stack sheet formation and sufficient flow for injection moulding of thin-wall parts.
Published multiple-lot data for the exact F29 AL30 designation are limited in openly accessible literature; the ranges below are therefore class-typical for rigid PLA compounds and should be verified against the manufacturer’s certification for each batch.
| Property | Test method | INZEA F29 AL30 class-typical range | Unmodified PLA class-typical range | A-PET class-typical range |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.24–1.26 g/cm³ | 1.24–1.25 g/cm³ | 1.33–1.35 g/cm³ |
| Melt mass-flow rate | ISO 1133-1:2022 | 6–15 g/10 min at 190 °C/2.16 kg | 5–12 g/10 min | not applicable |
| Tensile modulus | ISO 527-2:2012 | 3000–3500 MPa | 3200–3600 MPa | 2000–2400 MPa |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2013 | 50–60 °C | 50–55 °C | 65–70 °C |
| Moisture limit at processing | ISO 15512:2019 | <250 ppm | <250 ppm | <50 ppm |
Capillary rheometry at 190 °C shows shear-thinning behaviour; representative linear PLA values are 800 Pa·s at 100 s⁻¹ declining to 200 Pa·s at 1000 s⁻¹ when measured in accordance with ISO 11443:2021. Melt strength measured by Rheotens test at 190 °C is typically 2–4 cN for formulated rigid PLA grades, although published data specific to F29 AL30 is limited.
Compounding of the formulation is typically performed on co-rotating twin-screw extruders with L/D ratios of 40:1 to 44:1, using vacuum devolatilisation at −0.08 MPa to remove residual volatiles. If the vent port is placed too close to the feed throat, PLA can hydrolyse before the melt seal is formed, producing black specks in translucent sheet. This failure mode is observed in production when the melt seal is below 60 % of screw fill or when the vacuum level is degraded by gasket wear.
Pre-drying is mandatory where ambient relative humidity exceeds 60 %. Moisture uptake in PLA compounds is sufficiently rapid that resins stored in open silos or hopper loaders in humid production halls may exceed 0.025 wt% residual moisture before melt processing. Hydrolytic chain scission during extrusion then becomes detectable as a reduction in melt strength and an increase in edge tear. Desiccant drying with a dew point of ≤ -40 °C and a residence time of 4 h at 80 °C is typically required to bring residual moisture below 250 ppm, as measured by ISO 15512:2019. Hot-air ovens are unsuitable because equilibrium moisture after overnight exposure at 60 % RH remains above the recommended threshold. Production-scale sheet extrusion lines fitted with closed-loop dryers have demonstrated that variance in pre-drying is the largest single contributor to lot-to-lot sheet brittleness.
Sheet extrusion for INZEA F29 AL30 is run on single-screw extruders with L/D ratios of 30:1 to 36:1 and barrier or Maddock mixing sections. Melt temperatures are maintained in the 190 °C to 210 °C range; exceeding 230 °C for more than 10 minutes accelerates thermal degradation and yellowing. The polished roll stack is typically held at 40 °C to 70 °C to reduce curling. Thermoforming sheet surface temperatures of 90 °C to 110 °C are used for plug-assisted positive forming; below 85 °C the sheet tears at corners, and above 120 °C it sags enough to create uneven wall sections. Aluminium or epoxy tooling with plug materials of syntactic foam gives the most consistent wall-thickness distribution in shallow trays. Deep-draw parts with draw ratios above 1.5:1 require heated female cavities at 40 °C to 50 °C to avoid early freezing. The narrow processing band of PLA means that sheet surface temperature should be controlled to ±5 °C across the forming area.
Thermoforming skeletons generate 30–50 wt% scrap; closed-loop regrind systems are therefore central to economic operation. Reintroduction of regrind at up to 20 wt% with virgin granules generally preserves tensile modulus within ±5 % of the virgin value when tested in accordance with ISO 527-2:2012. Above 20 wt%, the molecular weight reduction associated with repeated heat histories lowers elongation at break and shifts the brittle-ductile transition upward. At 50 wt% regrind, visible sheet gels and edge cracks may appear, especially if the regrind contains dust or partially hydrolysed edges from storage. Sieving through a 4 mm screen and direct re-extrusion without intermediate long-term storage minimises hydrolytic degradation. Regrind should not be blended with PET or PS flake in co-mingled recycling streams, as the different processing temperatures and melt viscosities generate delamination and weak knit lines.
Barrel profile for injection moulding of INZEA F29 AL30 is typically 180 °C, 195 °C, 205 °C, 205 °C, 205 °C from feed to nozzle, with a screw back pressure of 5–10 bar and injection speed adjusted to fill the cavity in 0.5–1.5 s. Mould temperatures between 25 °C and 40 °C produce adequate dimensional stability in thin-walled parts, but cycle times are longer than HIPS because of the low thermal diffusivity of PLA. Gates should be located at thick sections; pin gates smaller than 1.0 mm may freeze prematurely and cause sink marks. Mould shrinkage is typically 0.3–0.6 %, which is lower than polypropylene but higher than A-PET. Venting depth should not exceed 0.02 mm on the parting line to avoid flash at high injection speeds. Ejector pins should be larger than 6 mm because the rigid nature of PLA creates high ejection forces; thin-walled containers may require draft angles of 2–3° on cores. Hot-runner systems should be internally heated rather than externally heated to reduce residence time.
Moisture scavengers that rely on calcium oxide or other basic oxides can initiate chain scission under shear. Amine-based antistatic additives and certain metallic stearates can likewise shift the apparent pH of the melt and reduce molecular weight during compounding. The use of external release agents based on silicone is generally acceptable at 0.1–0.5 wt%, but fluoropolymer processing aids should not be assumed compatible without capillary rheometry trials. Masterbatch carriers should be PLA or a miscible biodegradable polyester; polyethylene-based masterbatches generate visible delamination in thin-wall sections.
The grade is evaluated against the following standards for compostability and regulatory compliance. Certification is lot- and formulation-specific; the table lists the standard, the acceptance criterion, and the packaging or material-use relevance.
| Standard | Acceptance criterion | Relevance |
|---|---|---|
| EN 13432:2000 | Disintegration ≤ 12 weeks; biodegradation ≥ 90 % after 180 days; ecotoxicity testing | Industrial compostability claim in the EU |
| ASTM D6400-21 | Aerobic composting specification for plastics | North American labelling |
| ISO 17088:2021 | Global specification for compostable plastics | International certification alignment |
| FDA 21 CFR 177.1520 | Food-contact olefin and certain polyester provisions; suitability depends on specific migration testing | US food-contact assessment |
| REACH and RoHS Directive 2011/65/EU | Substance restrictions | EU market access |
Industrial composting certification under EN 13432:2000 requires disintegration within 12 weeks and biodegradation ≥ 90 % after 180 days. These endpoints refer to industrial composting facilities at 58 °C; they do not imply degradation in soil, marine, or home-compost environments. Migration testing under EU Regulation 10/2011 may be required for specific food types; overall migration and specific migration of lactic acid and degradation products are evaluated with food simulants prescribed in Annex III. For packaging applications, the grade is not suitable for hot-fill above 60 °C unless the part is redesigned with ribs or a heat-resistant PLA grade is selected. Ultraviolet exposure causes yellowing and surface chalking; parts intended for outdoor use require UV stabilisation or an opaque masterbatch. Published data for the exact F29 AL30 grade under outdoor weathering or repeated microwave exposure is limited.