| HS Code | 291802 |
| Density | 1.25 g/cm³ |
| Melt Flow Rate | 25 g/10 min at 190°C/2.16 kg |
| Tensile Strength At Yield | 70 MPa |
| Tensile Strength At Break | 60 MPa |
| Tensile Modulus | 3.5 GPa |
| Elongation At Break | 3% |
| Flexural Modulus | 3.6 GPa |
| Flexural Strength | 100 MPa |
| Notched Izod Impact Strength | 2.5 kJ/m² |
| Heat Deflection Temperature At 0 45 Mpa | 135°C |
| Heat Deflection Temperature At 1 8 Mpa | 100°C |
| Vicat Softening Temperature | 140°C |
| Melting Temperature | 175°C |
| Glass Transition Temperature | 60°C |
| Compostability | EN 13432 compliant |
As an accredited FC 60025 Crystallized Compostable Injection Molding Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | FC 60025 Crystallized Compostable Injection Molding Polylactic Acid is supplied in 25 kg moisture-resistant, foil-lined paper sacks. |
| Container Loading (20′ FCL) | Container loading (20′ FCL): FC 60025 Crystallized Compostable Injection Molding Polylactic Acid, palletized, moisture-protected, secured, evenly distributed, ambient conditions. |
| Shipping | FC 60025 Crystallized Compostable Injection Molding Polylactic Acid is shipped as a non-hazardous, non-regulated polymer resin. Pack in sealed, moisture-barrier bags or drums. Store and transport dry, away from heat, sunlight, and moisture. Keep containers closed. No special DOT/IMDG/IATA labels required. Use standard industrial handling. |
| Storage | Store in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Maintain ambient temperature, preferably below 30°C, with low humidity. Avoid incompatible materials and prolonged storage in damp conditions, as PLA may hydrolyze and degrade. Follow supplier recommendations. Use first-in, first-out stock rotation. |
| Shelf Life | Shelf life: typically 24 months when stored unopened in a cool, dry place, protected from moisture, heat, and direct sunlight. |
Moisture control precedes all downstream processing steps for injection-molded cutlery. The granular resin is dried in a desiccant dryer with a dew point of -40 °C or lower until residual moisture falls below 250 ppm. This typically requires 4–6 h at 80 °C. Residual water above this threshold hydrolyzes the ester linkages in PLA during plastication. Molecular weight decreases and melt viscosity drops. On a production line this produces short-shot fork tines, micro-cracks in knife blades, and erratic part ejection. A hopper residence time longer than 2 h at elevated temperature is avoided because lactide reformation accelerates thermal degradation.
Typical formulations for compostable cutlery incorporate 0.5–2.0 wt% of a nucleating agent. Fine talc or ethylene bis-stearamide is used to shorten the crystallization half-time. When impact resistance of fork tines is a requirement, 5–10 wt% polybutylene succinate or polybutylene adipate terephthalate is added. Mineral fillers above 15 wt% are not advised because melt flow length in thin fork sections becomes limiting. All colorants and processing aids must themselves meet EN 13432 or ASTM D6400 requirements for aerobic biodegradability. Amine-based stabilizers are excluded because residual alkalinity accelerates PLA chain scission at melt temperatures above 190 °C.
A reciprocating screw injection molding machine with an L/D ratio of 20:1 to 25:1 and a compression ratio of 2.5:1 to 3:1 is sufficient. Melt temperature is profiled from 180 °C at the rear zone to 210 °C at the nozzle. Total barrel residence time is kept below 5 min. The mold is held at 90–110 °C through pressurized water or oil temperature control units. Holding pressure is set between 600 bar and 1000 bar depending on wall thickness. A fork with a 2.0 mm main body wall and 1.2 mm tine tips usually requires holding pressure near the upper limit. Cooling time ranges from 20 s to 40 s for 2–4 mm wall sections. This permits crystalline fraction development. Parts are ejected at a mold opening temperature below 60 °C to avoid post-ejection deformation.
Finished cutlery items include forks, spoons, knives, and stirrers. A fully crystallized injection-molded PLA fork retains sufficient stiffness for brief contact with hot beverages at 80 °C. Continuous immersion for more than 30 min can induce softening. Knife edges are molded in tools with hardened steel inserts. PLA has a lower flexural modulus than glass-filled polypropylene and cannot sustain serrated edge detail if the mold surface is not polished. Cutlery is tested for flexural modulus per ISO 178 and for impact resistance per ISO 180/1A. Food-contact compliance follows EU 10/2011 with an overall migration limit of 10 mg/dm² under simulant A for aqueous contact and simulant D1 for fatty contact. Industrial compostability is confirmed only after EN 13432 or ASTM D6400 testing demonstrates 90% biodegradation in 180 days, 90% disintegration in 12 weeks under controlled composting conditions, and the absence of ecotoxic effects in the final compost.
In thin-wall cavities below 1.0 mm, the crystallization window is compressed by rapid heat extraction. The polymer front freezes before the nucleating agent has sufficient time to induce globular spherulite growth across the thickness. Mold temperature must remain close to the cold-crystallization peak. For crystallizable PLA this peak is typically 95–105 °C. If the tool operates at 70–80 °C to shorten cycle time, as-molded crystallinity remains below 15%. This is measured by differential scanning calorimetry under ISO 11357-3. The part then undergoes secondary crystallization during storage. Density increases and anisotropic shrinkage occurs. A 150 mm clamshell lid may lose 1.0–1.5 mm of flatness within 48 h if ejected under-crystallized.
Thin-walled clamshells, salad trays, and produce containers are typically compounded with 1–3 wt% nucleating agent and 10–20 wt% impact modifier. Polybutylene adipate terephthalate is preferred when film hinging or snap closure is needed. It maintains acceptable ductility under ASTM D638 tensile test conditions. Slip additives above 1.5 wt% cause gate blush and are avoided. Translucent lids require a different additive strategy. Low D-lactide content PLA and a sorbitol-based clarifying agent may be used. However, the resulting amorphous or low-crystallinity structure lowers heat deflection temperature under ASTM D648 to approximately 50–55 °C. A transparent thin-wall package cannot simultaneously meet hot-fill requirements above 65 °C without multilayer lamination or external reinforcing ribs.
High-velocity injection is required to fill a 0.8 mm sidewall before the flow front viscosity reaches a no-flow condition. Injection speeds of 150 mm/s or higher are common, depending on screw diameter and shot weight. The tool is built with a hot-runner system and valve gates. This minimizes material in the cold sprue. Regrind of PLA reduces molecular weight and shifts the crystallization exotherm. Cooling lines are arranged with a temperature variation of no more than ±2 °C across the cavity. Extraction is assisted by ejector rings rather than pin ejectors because under-crystallized parts are susceptible to surface indentation. After demolding, thin-wall containers are often placed in sizing nests for 5–10 min to restrain warpage during the final crystallization stage.
Food-contact certification for compostable thin-wall packaging follows EU 10/2011 and any national migration limits for lactic acid and its oligomers. The packaging may also require compliance with the EU Packaging and Packaging Waste Directive 94/62/EC when the article enters packaging waste streams. Heat seal strength between a PLA tray and PLA lidding film is evaluated per ASTM F88. Typical seal initiation occurs at 120–140 °C with a 0.3–0.5 s dwell. Throughput limits are dictated by crystallization time, not purely by part cooling time. Cycle times below 10 s in thin-wall tools risk dimensional instability in downstream distribution.
The failure mode in compostable coffee capsule production is most frequently traced to residual under-crystallinity. A single-serve capsule body with wall thickness of 0.8–1.2 mm is injected at high speed. If mold temperature falls below the cold-crystallization onset of approximately 80 °C, the part exits with an amorphous or weakly crystalline skin. During storage, the polymer continues to crystallize. Volumetric shrinkage of 1–2% is common. This changes the outer diameter by 0.1–0.2 mm. That dimensional shift is sufficient to break the heat-sealed lid interface and allow oxygen ingress into the coffee bed. The defect appears weeks after molding and is difficult to detect on the production line.
For capsule applications the molding tool is held at 90–110 °C. An oil-based temperature control unit capable of maintaining ±2 °C is preferred. Water units without pressurization reach a practical ceiling of 95 °C and are marginal for this polymer. The cooling phase must be extended to 15–25 s. This is not because the part is hot, but because crystallinity development is time-dependent under isothermal conditions. A post-mold annealing step at 80 °C for 30 min is used only when high-speed tools cannot achieve adequate crystallinity in-cycle. It adds handling cost and increases surface scratching risk on glossy capsules.
Material formulation for capsules typically includes 10–20 phr of polybutylene succinate or polybutylene adipate terephthalate. This prevents puncturing during the coffee extraction process. A nucleating agent at 1–3 wt% reduces the half-time of crystallization. It cannot overcome the thermodynamic requirement for mold temperature above the glass transition and near the cold-crystallization peak. Barrier performance remains a limitation. Single-layer PLA capsules show high oxygen transmission rates compared with polypropylene-EVOH structures. Published industrial data for specific oxygen transmission rates of PLA capsule materials is limited. Barrier coatings such as PVOH improve protection but complicate the EN 13432 disintegration step because the coating may form residues.
Compliance is evaluated under EU 10/2011 for overall and specific migration using simulant D1 at 100 °C for 2 h. This is followed by long-term storage simulation at 40 °C for 10 days. Capsules are tested for puncture resistance with a universal testing machine at a displacement rate of 50 mm/min. The value is compared against reference polypropylene capsules on the same filling line. The industrial compostability claim is valid only if the spent capsule is sent to a managed aerobic composting facility operating above 58 °C. Home composting certification is a separate scheme and cannot be assumed from EN 13432 compliance.
Injection-molded PLA closures and jars for dry or anhydrous cosmetic formulations represent a narrow application window. The grade is predried to below 250 ppm moisture in a desiccant dryer with a dew point below -40 °C. Barrel temperatures are profiled from 160 °C at the feed throat to 200 °C at the metering zone. A mold temperature of 100 °C is maintained with pressurized water or oil temperature controllers. The crystallized part can withstand brief contact with 60 °C filling lines without deformation. Compatibility testing with the actual cosmetic base is mandatory. Formulations containing more than 15% ethanol, propylene glycol, or limonene can cause environmental stress cracking within weeks at storage temperatures above 30 °C. PLA is not recommended for perfume concentrates, nail polish remover packaging, or continuous-use pump bottles containing high fractions of polar solvents.
Closures are typically molded with 2–3 wt% talc as a nucleating and stiffening agent. The use of 1 wt% erucamide slip agent reduces thread friction during capping. The effect diminishes after extended aging because the additive migrates to the surface. Torque removal force is measured per ASTM D2063 on a torque tester at a removal speed of 5 rpm. For jars, side wall thickness of 1.5–2.5 mm provides sufficient top-load strength for stacking. The decorative surface is limited. Hot stamping and pad printing require corona or plasma pretreatment because PLA has low surface energy in the 30–38 mN/m range. Metallized vacuum coating is possible but renders the article non-compostable if the metal layer exceeds the threshold for organic recovery.
Cosmetic packaging articles may be certified to EN 13432 only if the container is free of product residues before composting. In practice the feedstock is a clean production reject stream or post-consumer material washed under defined conditions. Any label, adhesive, or barrier liner must also be biodegradable and non-ecotoxic. If the cosmetic formulation itself contains synthetic polymers or preservatives that sorb into the PLA wall, the final article cannot be considered compostable without verifying the ecotoxicity of the compost containing those substances. This limitation is communicated on packaging only when the brand chooses a third-party certification mark such as Seedling or OK compost INDUSTRIAL.
In agricultural plant tags and nursery clips, the processing window is wider than for cutlery but the end-of-life window is narrower under field conditions. These parts are injection-molded at wall thicknesses of 1.5–3.0 mm. The service environment is outdoors with UV exposure and soil contact. Required mechanical loads are low. A mold temperature of 70–90 °C is often sufficient because no hot-fill or high-heat requirement exists. This lower mold temperature produces a partially crystalline part with moderate dimensional stability. Warpage is controlled by adding 5–10 wt% calcium carbonate. This reduces anisotropic shrinkage and raises the heat deflection temperature only slightly. Carbon black or iron oxide pigments are used at 1–2 wt%. These pigments must be compostability-certified carrier systems when the article carries an EN 13432 mark.
The main performance boundary is degradation onset. Crystallized PLA does not disintegrate quickly in ambient soil. Industrial compostability testing per EN 13432 is conducted at 58 °C. The soil in a nursery bed rarely exceeds 25–30 °C. A plant tag labeled as industrially compostable may persist for several growing seasons before visible embrittlement occurs. This mismatch is a frequent source of end-user misunderstanding. If the application requires field disintegration within a defined window, published data for this specific configuration is limited. Project-specific field trials are required. Adding pro-oxidants or starch at high loading accelerates soil biodegradation but compromises melt strength and impact resistance during ejection.
Injection conditions for tags and clips use a medium injection speed to avoid jetting in elongated tag bodies. The screw is operated at 100–200 rpm with a back pressure of 30–50 bar. High back pressure raises melt temperature and increases lactide formation. Clips for vine training are molded with living hinges. These require an impact modifier at 5–15 wt% to survive repeated flexing. The addition of impact modifier reduces the overall crystallinity under cooling conditions and increases cycle time. Surface printing on tags uses ink systems meeting EU 10/2011 only when the tags may contact edible plants. Otherwise standard UV-curable ink is acceptable but may interfere with compostability.
Short-term disposable oral care components, including dental floss picks and impression trays, place a different set of demands on crystallized PLA. Floss picks require a small U-shaped frame with a 0.6–0.8 mm monofilament embedded in the tips. The material must survive the molding of a steel-inserted floss thread without melting the thread or deforming the frame. Mold temperature is held at 90–100 °C for the frame. A lower insert temperature prevents heat damage to the floss. The frame itself is tested for flexural modulus per ISO 178. Repeated bending is evaluated using ISO 178 methods for brittle failure statistics. Dental impression trays are thicker, 2–3 mm, and must maintain dimensional accuracy. Autoclaving at 121 °C is not possible with PLA. The articles are designated single-use and steam sterilization is excluded.
Biocompatibility data are required for oral contact. Cytotoxicity is evaluated per ISO 10993-5. Sensitization is evaluated per ISO 10993-10. Irritation is evaluated per ISO 10993-23 where applicable. PLA is not classified as a medical-grade polymer unless a specific raw material supplier has completed the relevant USP Class VI or ISO 10993 test program. Floss picks and impression trays are usually marketed as consumer products rather than medical devices. This alters the regulatory route. The compostability claim for such items is constrained by contamination with saliva, fluoride, and dental impression material residues. Unless these residues are removed by washing, the EN 13432 ecotoxicity criterion cannot be satisfied in the final compost.
Processing for oral care components uses a shut-off nozzle to avoid drooling at melt temperatures of 190–210 °C. The screw is sized so that shot volume is 60–70% of barrel capacity. Small floss pick tools with 32–64 cavities are common. Hot-runner balance must be within ±3% fill variation across cavities. This is achieved by adjusting valve gate opening times rather than by raising melt temperature. Thermal degradation accelerates at higher temperatures and creates acrid odor. The released floss pick frame is ejected at a mold temperature below 55 °C. This avoids notching at the floss anchor points. The final article is packed immediately after moisture equilibration. This prevents post-mold crystallization-induced bending in thin bridge sections.
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FC 60025 is a crystallized compostable injection-molding grade of polylactic acid intended for rigid articles that require heat deflection above the glass transition of amorphous PLA. The material is typically processed on a reciprocating-screw injection-molding machine with a screw L/D ratio of 20:1 to 24:1 and a compression ratio of 2.5:1. Melt density at 210 °C is approximately 1.08 to 1.12 g/cm³ according to typical PLA melt-density measurements; solid density when injection-molded according to ISO 1183-1:2019 falls in the range of 1.24 to 1.27 g/cm³ after the molded part has been allowed to crystallize. The melt mass-flow rate determined by ISO 1133-1:2022 at 210 °C with a 2.16 kg load is normally controlled between 15 and 30 g/10 min, though lot-to-lot variation is expected from nucleator dispersion. The grade is formulated to crystallize in a mold held at 80 °C to 110 °C, producing a crystalline fraction that raises the heat deflection temperature under 0.45 MPa load from approximately 55 °C for amorphous PLA to a typical range of 90–110 °C when tested according to ISO 75-2:2013 method B. The trade designation FC 60025 does not itself identify the polymer manufacturer and should be read with the supplier certificate of analysis for lot-specific moisture, D-lactide content, and nucleator loading.
Moisture control is the first processing boundary. Hydrolytic degradation of polylactic acid becomes measurable when predrying is omitted or when granulate is exposed to ambient air with relative humidity above 60%. The material should be dried at 80 °C for 4 h in a desiccant dryer with a dew point below −40 °C, to reduce residual moisture to less than 250 ppm (0.025%) as determined by ISO 15512:2019. In production-scale hopper dryers, the air inlet temperature should not exceed 90 °C because prolonged heating at higher temperatures can sinter pellets and reduce flow into the feed throat. Dried granulate should be conveyed with dry air to avoid re-moisturization before the feed throat.
Barrel-zone temperatures for FC 60025 follow a reverse or flat profile depending on screw recovery time. The feed zone is commonly set to 175–185 °C; the compression zone to 190–200 °C; the metering zone to 190–205 °C; and the nozzle to 190–210 °C. The melt temperature measured by an air-shot pyrometer can be found between 200 °C and 215 °C. Injection pressures of 80–120 MPa and hold pressures of 60–80 MPa are typical for wall sections from 1.0 mm to 3.0 mm. Back pressure should be held at 0.5–1.0 MPa to maintain a consistent melt cushion without excessive shear heating. A screw surface speed of 0.2–0.5 m/s is recommended. At higher screw speeds, viscous heating can exceed 230 °C and initiate chain scission; the melt will then exhibit a measurable increase in melt volume-flow rate and a drop in melt viscosity.
Hot-runner systems used with FC 60025 must avoid dead spots because PLA degrades by hydrolysis, ester interchange, and lactide reformation. Manifold temperatures should be held at 190–210 °C; external hot-runner tips should not exceed 220 °C. Gate geometry has a measurable effect on jetting and flow marks. Tapered sprue bushings and full-round runners with a diameter of at least 4 mm are preferable for thick parts; for thin-wall parts, a valve-gated hot drop is often necessary to maintain hold time before gate freeze. Cold-runner systems should use a sprue break and positive shut-off nozzle to avoid drool because PLA melt viscosity is lower at the high processing temperatures needed for mold crystallization. Vent depth should be maintained in the range of 0.01–0.03 mm with land lengths of 0.5–1.0 mm to allow gas evacuation without flash.
Oscillatory shear measurements on nucleated PLA melts at 200 °C show shear-thinning behavior beginning near 10 s⁻¹; the zero-shear viscosity is typically between 1000 and 2500 Pa·s for an MFR of 15–30 g/10 min. At an apparent shear rate of 1000 s⁻¹, viscosity falls below 100 Pa·s. These values depend on residual moisture and D-lactide content. A mold-filling simulation should use Cross-WLF viscosity parameters from the supplier; generic PLA parameters may under-predict injection pressure for hot molds by 10–20%.
Residence time in the barrel should not exceed 5 min at melt temperatures above 210 °C; at 230 °C, the residence limit drops to 2–3 min. A production-scale failure mode observed on hydraulic injection machines is a gradual increase in free shot weight followed by an abrupt rise in nozzle drool and a reduction in melt pressure during hold. This is often misread as a feed-throat blockage, but it is chain scission in the compression zone. Monitoring melt pressure integral during the holding phase is more effective than monitoring cycle time for detecting polymer degradation.
Mold-temperature mapping exerts the largest influence on final crystallinity. When the mold surface is maintained at 95–110 °C, the part reaches a semicrystalline state before ejection; at mold temperatures below 80 °C, cooling rates suppress nucleation and the article leaves the mold largely amorphous. Differential scanning calorimetry according to ISO 11357-3:2018 often shows a cold-crystallization exotherm between 100 °C and 120 °C for amorphous or partially crystallized specimens. In fully crystallized specimens, the melting endotherm near 165–175 °C dominates and the cold crystallization exotherm is absent or small. A mold temperature of 100 °C with a hold time of 10–20 s per millimeter of nominal wall thickness allows the crystalline fraction to develop; thinner walls may require longer hold times relative to thickness because the gate freezes earlier and limits packing. Shrinkage of nucleated PLA along the flow direction is typically 0.3% to 0.5%, while transverse shrinkage is 0.5% to 0.8%, and the difference produces anisotropic warpage in long flat articles unless mold-temperature uniformity is held within ±3 °C. When mold-temperature variation exceeds ±5 °C, differential crystallization across the part can induce internal stress that increases deflection after annealing or during hot-fill service.
Post-mold annealing is used when mold temperatures above 100 °C are impractical. An annealing cycle of 60 min at 100 °C can increase crystallinity and raise heat deflection temperature, but it also increases total shrinkage and may warp flat parts unless fixtures are used. Free-annealing of FC 60025 parts at 100 °C without support can produce bowing greater than 1.5% of part length. Fixtured annealing at 100–110 °C is therefore required for dimensional stability. Published data for this specific configuration is limited, but the trend is consistent with PLA crystallization kinetics.
Representative values for a nucleated semicrystalline PLA injection-molding grade are shown below. These ranges are compiled from public PLA supplier technical data and standard test results for mold conditions of 100 °C; values for FC 60025 should be confirmed against the producer certificate because nucleator loading and D-lactide content affect the final property profile.
| Property | Test method | Typical range for nucleated semicrystalline PLA |
|---|---|---|
| Solid density | ISO 1183-1:2019 | 1.24–1.27 g/cm³ |
| Melt mass-flow rate at 210 °C/2.16 kg | ISO 1133-1:2022 | 15–30 g/10 min |
| Tensile yield stress | ISO 527-2:2012 | 55–70 MPa |
| Tensile modulus | ISO 527-2:2012 | 3.0–3.5 GPa |
| Flexural strength | ISO 178:2019 | 80–100 MPa |
| Flexural modulus | ISO 178:2019 | 3.5–4.0 GPa |
| Notched Charpy impact resistance | ISO 179-1:2010 | 2.5–4.5 kJ/m² |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2013, method B | 90–110 °C |
| Heat deflection temperature, 1.8 MPa | ISO 75-2:2013, method A | 60–75 °C |
| Renewable carbon content | ASTM D6866-22 | > 95% |
The mechanical data in the table are derived from specimens injection-molded according to ISO 294-1:2017 and conditioned at 23 °C and 50% RH for at least 48 h before testing. The property spread reflects differences in mold temperature, hold pressure, and nucleating-agent compounding. Tensile yield stress is sensitive to residual moisture; conditioning at higher humidity can reduce yield stress by 3–7% because water plasticizes the amorphous regions. Notched impact strength is lower than that of polypropylene impact copolymers and limits use in snaps, living hinges, and drop-impact closures. FC 60025 should not be specified for constant stress applications above 60 °C unless the part has been fully crystallized and the geometry avoids sharp radii.
The renewable carbon content measured by ASTM D6866-22 is normally greater than 95% for PLA, but the exact value depends on the proportion of biobased additives and masterbatch. A value below 95% does not necessarily indicate fossil-derived polymer; it may arise from non-biobased nucleants, pigments, or processing aids. The material is not intended for high-temperature reuse above 100 °C without post-mold annealing.
Regrind use is the central operational variable in this substitution. Because FC 60025 is crystallized in the mold, the thermal history of the first molding cycle has already consumed a portion of the polymer's molecular weight; reprocessing without drying or with excessive residence time can shift the melt flow rate upward and increase brittleness. For hot-fill lids with a wall thickness of 1.2–2.0 mm, a regrind fraction of 20 wt% blended with virgin granulate is generally considered a conservative starting point. Published data for this specific configuration is limited; however, studies on nucleated PLA of similar optical purity report that a 20 wt% regrind level changes tensile yield stress by less than 5% when the regrind is dried to below 250 ppm moisture and the melt temperature is held below 215 °C. At 50 wt% regrind, losses in notched impact resistance can exceed 10–15%, and the melt volume-flow rate may increase by 25–50% depending on shear and residence time. The ratio should therefore be validated with drop-impact testing on the actual lid geometry rather than on standardized ISO plaques alone.
The crystallization rate is strongly influenced by D-lactide content. In PLA, optical purity expressed as L-lactide content should be above 98 mol% for fast crystallization. If the grade is compounded with a nucleator, isothermal crystallization half-time at 110 °C is typically in the range of 0.5–2.0 min; without a nucleator, it may exceed 10 min. These values are derived from DSC studies on nucleated PLA and not from a single proprietary masterbatch. The injection molder should verify the half-time from the supplier or by isothermal DSC because it governs the minimum mold-closed time for a given part thickness.
Compostability validation must be performed on the actual article and not inferred from resin certification alone. EN 13432:2000 requires disintegration after 12 weeks and biodegradation of at least 90% after 6 months in an industrial composting environment. ASTM D6400-21 and ISO 17088:2012 prescribe similar threshold values. Because the rate of hydrolysis depends on thickness, the maximum wall thickness should be specified in the test report; a 2 mm injection-molded plaque may disintegrate within the required period under controlled conditions, while thicker rigid parts may require extended exposure. The crystallized structure of FC 60025 can slow hydrolysis compared with amorphous PLA, and thus the time-to-disintegration can be longer when the crystalline fraction exceeds 30%. This trade-off is essential for product design: increased heat resistance and lower cold-crystallization shrinkage are accompanied by slower compostability kinetics.
| Standard or regulation | Scope | Typical conformity condition |
|---|---|---|
| EN 13432:2000 | Packaging recoverable through composting and biodegradation | Conformity must be shown on final article; wall thickness and surface-area-to-mass ratio affect time |
| ASTM D6400-21 | Compostable plastic labeling | Disintegration and biodegradation thresholds per specified thickness |
| ISO 17088:2012 | Specification for compostable plastics | May be cited in combination with regional certification |
| EU 10/2011 | Food-contact plastic materials and articles | Migration testing required for final food contact conditions |
| REACH 1907/2006 | Registration, evaluation, authorization of chemicals | No SVHC above 0.1% w/w if declared |
| RoHS 2011/65/EU | Hazardous substances in electrical and electronic equipment | Pb, Cd, Hg, Cr VI, PBB, PBDE below prescribed limits |
For food-contact applications, compliance with EU Regulation 10/2011 requires migration testing using the simulant appropriate to the intended food type and the maximum foreseeable hot-fill or reheating temperature. The use of crystallization nucleants and processing aids must be covered by the supplier's declaration of compliance. In the absence of a specific FC 60025 food-contact statement, the processor should request a lot-specific declaration. Under REACH 1907/2006, the product should be accompanied by a safety data sheet that identifies any residual monomer and additive substances above declaration thresholds. RoHS Directive 2011/65/EU restrictions for lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE apply to electrical and electronic equipment housings; PLA grades of this class are generally capable of meeting those limits when unfilled or filled with permitted minerals.
Compared with amorphous PLA, FC 60025 has reduced optical clarity; haze increases as spherulite size grows, especially at mold temperatures above 100 °C. The difference in heat resistance is measurable under 0.45 MPa load: amorphous PLA typically deflects near 55 °C, whereas crystallized FC 60025 remains stable to 90–110 °C. Compared with polypropylene, FC 60025 has higher density (1.24–1.27 versus 0.90–0.91 g/cm³), higher flexural modulus, and lower notched impact resistance. Unlike polypropylene, FC 60025 requires predrying and a heated mold; it cannot be processed with cold molds and low-energy dehumidified air. Compared with PBS or PBAT blends, FC 60025 retains a higher modulus and a lower elongation at break, making it more suitable for rigid containers and less appropriate for film hinges or high-elongation clips. Pigment masterbatches should be based on PLA or another compostable carrier with a melting point compatible with 190–210 °C. Carriers based on polyethylene can remain as a dispersed phase and reduce compostability; they may also reduce crystallization rate by disturbing spherulite growth. Inorganic nucleators such as talc can raise modulus and shorten crystallization half-time, but loadings above 5 wt% can lower impact. The optimal nucleator loading should be determined by DSC isothermal crystallization, not by MFR alone.