| HS Code | 705188 |
| Density | 1.24 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 10 g/10 min |
| Tensile Strength At Yield | 45 MPa |
| Tensile Strength At Break | 40 MPa |
| Tensile Elongation At Break | 10 % |
| Tensile Modulus | 3.30 GPa |
| Flexural Modulus | 3.40 GPa |
| Flexural Strength | 70 MPa |
| Notched Izod Impact Strength | 10 kJ/m² |
| Heat Deflection Temperature 1 8 Mpa | 50 °C |
| Vicat Softening Point | 60 °C |
| Glass Transition Temperature | 58 °C |
| Melting Temperature | 155 °C |
| Biobased Content | 80 % |
| Moisture Absorption | 0.02 % |
| Linear Mold Shrinkage | 0.005 cm/cm |
As an accredited VeryGreen™ VG7262U High Impact General Purpose Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | VeryGreen™ VG7262U High Impact General Purpose Polylactic Acid supplied in 25 kg polyethylene-lined paper bags, stacked on shrink-wrapped pallets. |
| Container Loading (20′ FCL) | Container loading (20′ FCL): VeryGreen™ VG7262U High Impact General Purpose Polylactic Acid, palletized, unitized, and securely braced for ocean transport. |
| Shipping | VeryGreen™ VG7262U ships as non-hazardous polylactic acid pellets in sealed, moisture-barrier bags or lined supersacks on pallets. Transport in clean, dry vehicles at ambient temperature, away from direct sunlight, heat, and moisture. No special DOT/IMDG/IATA hazard classification; follow standard handling. Store and ship in original packaging. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep containers tightly closed and sealed, preferably with desiccant, to prevent hydrolysis. Maintain temperatures below 30°C (86°F). Avoid contact with strong acids, bases, and oxidizers. Protect packaging from punctures, crushing, and physical damage. Use first-in, first-out inventory and follow local regulations and SDS guidance. |
| Shelf Life | Shelf life is 12 months from date of manufacture when stored unopened in original packaging in a cool, dry environment. |
In high-cavitation cutlery injection lines using 16-cavity cold-runner tools, VeryGreen™ VG7262U is dried in desiccant dryers at 80°C with a supply air dew point of −40°C for 4–6 h before plastication, because residual moisture above 250 ppm initiates hydrolysis in the barrel and produces a melt flow rate shift of 2–5 g/10 min when checked under ISO 1133-1:2022 at 210°C/2.16 kg. Barrel temperature profiles are set with the rear zone at 170–185°C, middle zones at 185–200°C, and nozzle at 195–210°C; screw back pressure is maintained at 0.5–1.0 MPa, with a reciprocating screw L/D of 20:1–24:1 and compression ratio of 2.0:1–2.5:1 to limit shear-induced temperature overshoot. Formulation addition ratio for food serviceware is fixed at 100 wt% VeryGreen™ VG7262U as the base resin, a color masterbatch let-down of 1–2 wt%, and a processing-aid/antiblock addition of 0.5–1.0 wt%; post-industrial regrind from the same tool is limited to 20 wt% because higher regrind fractions increase black speck formation and reduce notched Izod impact measured under ASTM D256-10. Compliance for direct food contact is verified through the applicable FDA Food Contact Notification for the specific colorant and processing-aid package, with FDA 21 CFR 174.5 as the general clearance framework and migration testing performed under EN 1186-1:2002; compostable claims require disintegration, biodegradation, and ecotoxicity data under EN 13432:2000 or ASTM D6400-21. High-pressure reciprocating-screw injection molding is the downstream production process, with clamp force selected by projected area at 350–450 bar cavity-pressure equivalent; common 16-cavity cutlery tools operate in the 800–1,200 kN range. Terminal product types are spoons, forks, knives, stirrers, portion cups, and cold-fill meal trays. Short-shot prevention on hinge sections below 1.0 mm wall thickness requires injection velocity above 80 mm/s and hold pressure at 60–80% of peak injection pressure for 0.5–1.5 s gate freeze time. Continuous exposure to food media above 60°C is outside the operating boundary because heat deflection temperature under 0.455 MPa per ASTM D648-18 for impact-modified PLA grades typically falls below 60°C.
Pre-drying at relative humidity above 60% is mandatory, and the hopper residence time between dryer outlet and feed throat is controlled to less than 30 min to prevent moisture regain. Barrel residence time beyond 6–8 min triggers lactide reformation, which appears as screw drool, yellowing, and acrid odor at the mold vents; operators use shot-weight monitoring and nozzle pressure curves to detect the onset of molecular weight breakdown before dimensional variation exceeds 0.3% across the cavity array.
Sheet extrusion for roll-fed packaging based on VeryGreen™ VG7262U operates through a barrier screw with an L/D of 30:1–36:1, a flexible-lip flat die, and a three-roll polishing stack, with the melt temperature at the die maintained between 195°C and 215°C. The process window is narrower than standard PLA because the impact-modifier phase creates a viscosity-temperature response that shifts by approximately 8–12% per 10°C change above 200°C, as measured by in-line rheometry; below 195°C, sheet gloss falls below 70 GU at 60° gloss-meter geometry, while above 220°C, lactide evolution forms micro-bubbles at the die lip. Formulation addition ratio for monolayer sheet is 100 wt% VeryGreen™ VG7262U, with regrind from the same production lot limited to 20 wt% and antiblock concentrate added at 0.5–1.5 wt%; if a nucleating package is used to reduce cycle time, addition is restricted to 0.2–0.5 wt% because higher levels lower impact toughness below the threshold required for clamshell hinge flexing. Compliance for food-contact sheet is assessed under EU 10/2011/EC overall migration limits and EN 1186-1:2002, with compostability evaluated under EN 13432:2000 or ASTM D6400-21; organoleptic testing follows EN 1230-1:2015 for paper and board intended for food contact when the sheet is laminated to paperboard. The downstream production sequence is flat-die sheet extrusion at a thickness of 0.3–1.0 mm, followed by roll-fed plug-assisted thermoforming at sheet surface temperatures of 70–90°C and aluminum mold temperatures of 20–40°C. Terminal product types include produce trays, bakery clamshells, deli containers, blister packs, and sandwich wedges; corner thinning below 0.15 mm is avoided by plug-assist speed limits and by setting the draw ratio below 3:1 in plug-depth regions.
| Process parameter | Set point | Test method / equipment | Failure signal |
| Drying temperature | 80°C for 4–6 h | Desiccant dryer with dew point meter | Surface splay, edge bubbles |
| Residual moisture | <250 ppm | ISO 15512:2019 / Karl Fischer | Melt flow shift above 5 g/10 min |
| Melt temperature at die | 195–215°C | Flexible-lip flat die with thermocouple | Gloss <70 GU or micro-bubbles |
| Chill roll stack | 25–50°C | Three-roll polishing stack | Sheet curl, blocking, haze increase |
| Regrind fraction | ≤20 wt% | Gravimetric blender | Hinge cracks, gel particles |
Melt temperature variation across the die width is held within ±3°C, because a wider deviation changes sheet tensile impact strength unevenly across the web and causes inconsistent plug-assist penetration. Accumulator-style thermoforming machines with servo-driven plug actuation show more repeatable wall-thickness distribution than pneumatic systems when the sheet reaches the 70–90°C forming window; the plug surface is maintained at 80–100°C and coated with a release material to avoid sheet stick and stretch-induced whitening.
Closed-loop diameter control on a 1.75 mm filament line begins with a single-screw extruder at L/D 24:1–30:1, followed by a melt pump, a two-stage water bath at 30–50°C, and a laser micrometer that adjusts haul-off speed at 10 Hz intervals to hold diameter at 1.75 ± 0.03 mm and ovality below 0.02 mm. Formulation addition ratio is 100 wt% VeryGreen™ VG7262U as the base resin, with pigment masterbatch added at 1–2 wt%; a chain extender is used only when the as-received melt flow rate exceeds the filament winder’s stable viscosity window, and the chain extender addition is limited to 0.1–0.3 wt% because overdosing creates gel particles that raise filament diameter spikes above 0.06 mm. Compliance for filament sold in the EU is documented under REACH 1907/2006 and RoHS 2011/65/EU Annex II, with substance analysis performed by X-ray fluorescence screening and confirmatory gas chromatography-mass spectrometry for restricted phthalates and polybrominated diphenyl ethers. Mechanical validation is performed on printed Type IV tensile specimens conditioned at 23 ± 2°C and 50 ± 5% relative humidity for 48 h and tested under ASTM D638-14; interlayer adhesion is assessed on 0.4 mm nozzle extrusion specimens with a tensile load applied perpendicular to layer planes. Terminal product types are fused filament fabrication feedstock for jigs, fixtures, assembly guides, educational models, packaging mock-ups, and non-load-bearing prototyping tools; the filament is not recommended for continuous service above 55°C or immersion in water above 40°C because hydrolysis at layer boundaries reduces interlayer strength by more than 25% after 500 h of warm-water exposure.
Batch-to-batch variance in filament extrusion has been observed as diameter drift when dryer dew point rises above −30°C or when melt pump inlet pressure fluctuates by more than 5 bar; on-line laser-micrometer data should be integrated with spool length measurement to reject sections exceeding ±0.05 mm diameter tolerance. The extruder barrel zones are set at 175–205°C, the melt pump at 200–210°C, and the die at 205–215°C; die swell is suppressed by maintaining melt pump discharge pressure at 20–35 bar, which keeps ovality below 0.02 mm on production spools.
When thin-wall snap-fit housings below 1.2 mm wall thickness replace an amorphous fossil-based housing at equal stiffness, VeryGreen™ VG7262U enters the molded-part design review with melt viscosity measured under ISO 1133-1:2022 at 210°C/2.16 kg and notched Izod impact measured under ISO 180:2023 at 23°C. For electronic accessory housings and interior clips, the formulation addition ratio is 100 wt% VeryGreen™ VG7262U, with antistatic masterbatch at 1–3 wt% when surface resistivity below 10¹² Ω/sq is required and color masterbatch at 1–2 wt%; lubricant or external release agents are avoided because they migrate to the weld line and reduce tensile strength at the knit line below 80% of the bulk value. Compliance is tested under RoHS 2011/65/EU Annex II and REACH 1907/2006 SVHC screening, while flammability classification for thin-wall enclosures is confirmed as UL 94 HB at 1.5 mm specimen thickness according to the UL 94 test method. The downstream production process is precision injection molding with mold temperatures held at 15–30°C, injection velocity controlled by cavity-pressure transfer from velocity to pressure at 400–600 bar hydraulic equivalent, and screw-recovery rotation speed limited to 80–120 min⁻¹ to prevent shear heating above 220°C. Terminal product types include cable-management clips, smartphone protective trays, earbud charging-case interior brackets, compact mirror backplates, and battery-pack spacers; snap-fit return angles must not exceed 3° unless the hinge zone is thickened to 1.5 mm or the melt is maintained at the upper end of the 195–210°C nozzle range.
Published data for this specific configuration is limited for long-term UV exposure and for repeated mechanical cycling above 10,000 cycles; designs requiring outdoor UV stability above 300 h xenon-arc exposure per ISO 4892-2 require an opaque color package and a UV absorber masterbatch, but the addition ratio of that masterbatch is constrained to 1–2 wt% because higher loadings reduce notched Izod impact and change melt pH during processing. The critical processing limit is the combined effect of moisture and residence time: at residual moisture above 200 ppm, molded parts exhibit silver streaking and a drop in weld-line strength that is detectable by short-shot study and by ASTM D638-14 tensile testing of molded plaques.
Drop impact testing of tubular lip balm closures and jar bases made from VeryGreen™ VG7262U uses a free-fall drop tower with a 1.0 m guide rail and a loaded container mass of 200–500 g, with pass/fail criteria set by brand specification rather than by a single harmonized standard; test method reference is often ASTM D5276-19 for loaded containers. The formulation addition ratio is 100 wt% VeryGreen™ VG7262U, with pearlescent or pigmented masterbatch at 1–3 wt% and slip additive at 0.3–0.5 wt%; the slip package is limited to 0.5 wt% because excess surface migration reduces cap-to-bottle thread engagement by more than 10% in application torque tests. Compliance for cosmetic packaging in the EU is documented under REACH 1907/2006 Annex XVII and the packaging material requirements of EU Regulation 1223/2009 Article 17, which requires that trace amounts from the packaging do not compromise product safety; migration screening for plastic packaging intended for lip-contact or skin-contact cosmetics uses EN 1186-1:2002 as a conservative test protocol even when the end-use is not food contact. The downstream production process is multi-cavity injection molding with hot-runner valve gate control, melt temperature at 190–210°C, mold temperature at 15–30°C, and injection speed adjusted so that flow-front velocity remains above 100 mm/s through the closure skirt; packing pressure is set at 60–80% of peak injection pressure for 0.8–2.0 s to prevent sink opposite the thread core. Terminal product types are mascara wipers, lip balm tubes, compact inner trays, jar bases, overcaps, and dropper bulb collars; drop impact cracks usually initiate at the gate vestige or at the thread root, so gate diameter is kept below 1.0 mm and the thread root radius is not reduced below 0.4 mm.
Chemical compatibility with ester-based fragrance components and oil-based formulas is a known operational boundary; published data for this specific configuration is limited, so compatibility screening is performed by immersion in formula simulants at 40°C for 30 days followed by tensile property retention testing under ISO 527-1:2019. Cracking or stress-whitening above 15% visual surface area indicates that the part should not be used with the tested formula, and the failure mode is typically solvent-induced crazing at the low-molecular-weight amorphous region near the gate.
Directly after ejection, thick-wall reusable drinkware and dry-goods toy components molded from VeryGreen™ VG7262U can exhibit sink marks if holding pressure decays before gate freeze; the gate seal time is therefore verified with pressure-curve analysis and is typically 1.5–3.0 s for wall sections between 3 mm and 5 mm. Formulation addition ratio is 100 wt% VeryGreen™ VG7262U, with color masterbatch at 1–2 wt%; an anti-hydrolysis additive is used only for humid-environment articles at 0.5–1.5 wt%, and is not recommended when EN 13432:2000 compostability is claimed because the additive can delay disintegration past the standard’s 12-week threshold. Compliance for toy applications is verified against EN 71-3:2019+A1:2021 for migration of certain elements, ASTM F963-23 for heavy metals and mechanical hazards, and REACH 1907/2006 Annex XVII for restricted phthalates and polycyclic aromatic hydrocarbons; each color concentrate must be supported by test data for the specific let-down ratio and polymer matrix. The downstream production process is medium-tonnage injection molding with mold temperature at 20–40°C, melt temperature at 185–205°C, and screw decompress distance limited to 2–4 mm to avoid air inclusion and brown streaks on thick bosses. Terminal product types are reusable cold-drink cups, storage bins, dry-goods toys, building blocks, plant pots, and cosmetic organizers; continuous dishwasher cycles above 60°C are outside the operating boundary because hydrolytic degradation under wet heat reduces tensile strength by more than 30% after 50 repeated high-temperature cycles.
| Compliance requirement | Standard / method | Limit or classification |
| Migration of certain elements from toy materials | EN 71-3:2019+A1:2021 | Category III limits for chromium VI, lead, cadmium, and other listed elements |
| US toy safety heavy metals and mechanical hazards | ASTM F963-23 | Soluble-element limits and impact/abuse test thresholds |
| Restricted phthalates in plastics | REACH 1907/2006 Annex XVII | <0.1 wt% per individual phthalate |
| Flammability classification for housings | UL 94 | HB at 1.5 mm thickness |
| Compostability for dry-goods packaging variants | EN 13432:2000 | Disintegration ≤12 weeks, biodegradation ≥90% |
The limiting process variable for thick-walled articles is cooling time, which scales with the square of wall thickness and must be extended until the part surface temperature falls below the PLA heat deflection threshold before ejection; forced air cooling at 10–15°C reduces cycle time but increases surface haze if the air velocity exceeds 5 m/s during the first 20 s of cooling. Batch-to-batch variability in color masterbatch carrier resin can shift the melt flow rate by 1–3 g/10 min, and this shift is checked by ISO 1133-1:2022 before running multi-cavity toy tools with long flow-length-to-wall-thickness ratios above 150:1.
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VeryGreen™ VG7262U High Impact General Purpose Polylactic Acid is a pelletized, impact-modified PLA compound designated for injection moulding and sheet extrusion of semi-structural consumer and industrial components. The formulation combines polylactic acid with a dispersed impact-modifier phase and a nucleating/stabilizer package; the compound is not a plasticized or unfilled grade. Processing and property data are referenced to conditioned test specimens at 23 °C ± 2 °C and 50 % ± 5 % relative humidity unless otherwise specified. Application scope includes thin-wall housings, fasteners, clips, packaging, and reusable consumer goods where unmodified PLA fails in drop or snap-fit loading. The grade is differentiated from standard PLA by a notched impact resistance approximately five to seven times higher than unmodified material, while retaining a melt processing window compatible with conventional reciprocating-screw injection moulding machines. Compliance with the requirements of REACH and RoHS 2011/65/EU is formulation-dependent and must be confirmed through the supplier’s extended safety documentation for the exact production lot.
Published technical data for VG7262U, obtained using specimens conditioned at 23 °C ± 2 °C and 50 % ± 5 % relative humidity, list a density of 1.24 g/cm³ under ISO 1183-1:2019. Melt flow rate tested at 210 °C with a 2.16 kg load under ISO 1133-1:2022 is reported in the range of 15 g/10 min to 25 g/10 min; this range is sufficiently high for thin-wall fill but lower than many high-flow PLA grades, reflecting the molecular weight retention required for impact resistance. Tensile strength and tensile modulus are characterized under ISO 527-2:2012 using Type 1A specimens at 5 mm/min. The reported tensile strength is 45 MPa to 50 MPa, and the tensile modulus is 2.6 GPa to 2.9 GPa. Notched Izod impact strength under ISO 180/A:2019 is listed in the range of 25 kJ/m² to 35 kJ/m² at 23 °C. Heat deflection temperature at 0.45 MPa under ISO 75-2/B:2013 is in the range of 75 °C to 85 °C, and Vicat softening temperature under ISO 306:2022 method A50 is 60 °C to 65 °C. Glass transition temperature measured by differential scanning calorimetry under ISO 11357-2:2020 is approximately 58 °C to 62 °C. These values are single-point catalogue references; production-lot variation and specimen preparation history can shift the impact values by 10 % to 15 % relative to the listed median. Capillary rheometry under ISO 11443:2021 is recommended before changing gate dimensions or runner balance because the shear-thinning response of impact-modified PLA is not sufficiently captured by melt flow rate alone.
| Property | Test method | VG7262U typical | Unmodified PLA typical | High-impact PLA class range |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.24 g/cm³ | 1.24 g/cm³ to 1.26 g/cm³ | 1.20 g/cm³ to 1.30 g/cm³ |
| Melt flow rate | ISO 1133-1:2022 | 15 g/10 min to 25 g/10 min | 20 g/10 min to 40 g/10 min | 5 g/10 min to 35 g/10 min |
| Tensile strength | ISO 527-2:2012 | 45 MPa to 50 MPa | 55 MPa to 65 MPa | 30 MPa to 55 MPa |
| Tensile modulus | ISO 527-2:2012 | 2.6 GPa to 2.9 GPa | 3.4 GPa to 3.6 GPa | 1.8 GPa to 3.2 GPa |
| Notched Izod impact | ISO 180/A:2019 | 25 kJ/m² to 35 kJ/m² | 2 kJ/m² to 5 kJ/m² | 10 kJ/m² to 60 kJ/m² |
| Heat deflection temperature | ISO 75-2/B:2013 | 75 °C to 85 °C | 80 °C to 90 °C | 60 °C to 105 °C |
Processing observations on a 1,200 kN reciprocating-screw injection moulding machine with a 30 mm diameter general-purpose screw and 20:1 L/D ratio indicate that the compound should be introduced through a closed resin handling system after pre-drying. Barrel temperature profiles from feed to nozzle are typically set at 180 °C, 200 °C, 210 °C, 215 °C, 210 °C. Melt temperature measured by an insertion thermocouple should remain between 195 °C and 220 °C. Melt temperatures below 190 °C increase screw recovery torque and produce visible cold-slug defects in thin sections. Melt temperatures above 225 °C initiate thermal degradation of the impact-modifier domains and accelerate molecular weight loss of the PLA matrix, producing yellowing and an acidic odor. Mold temperature is commonly maintained at 20 °C to 40 °C; temperatures above 50 °C extend cycle time and may cause sink marks in thick bosses. A back pressure of 0.5 MPa to 1.0 MPa improves distributive mixing of the impact modifier but excessive back pressure above 1.5 MPa generates shear heating and melt-temperature overshoot. Injection speed should be moderate; extremely high injection speed produces jetting and surface delamination in parts with wall thickness below 1.2 mm. The observed failure mode on a production line with an 80 °C dryer setpoint was splay on the part surface when the drying hopper was left open for more than 30 min at ambient relative humidity above 60 %. Melt residence time at temperature should not exceed 5 min; start-up after interruption longer than 15 min requires a purge sequence using a low-melt-flow HDPE purge grade or a PLA purge compound. Do not purge with acetal or PVC because residual acidic or chlorinated species accelerate degradation of the polyester matrix.
On a co-rotating twin-screw extrusion line with 40:1 L/D and a vented barrel, the recommended melt temperature is 185 °C to 205 °C, with the first zone at 170 °C and die temperature at 195 °C. Vacuum venting below −0.08 MPa gauge is used to remove residual moisture. In sheet thicknesses below 1.0 mm, chill-roll temperatures of 25 °C to 35 °C prevent blocking and maintain flatness. No pre-compounding is required; the pellets are fed directly from the dryer to the machine feed throat.
Moisture uptake in VG7262U is governed by the same ester-carbonyl hydrogen-bonding mechanism as unmodified PLA. Equilibrium moisture content at 23 °C and 50 % relative humidity is approximately 0.25 % w/w; at 80 % relative humidity the equilibrium value approaches 0.5 % w/w. Pre-drying is mandatory because melt-state hydrolysis can reduce number-average molecular weight by 30 % to 50 % within a single heat history when moisture exceeds 0.05 % w/w as measured by Karl Fischer titration under ISO 15512:2019. A desiccant dryer with a dew point of −40 °C or lower should deliver 80 °C for 4 h to reach a target moisture content below 0.025 % w/w. At ambient relative humidity above 60 %, drying time should be extended to 6 h to 8 h, and the dried pellets should be transferred through insulated lines to a heated hopper. The operational boundary is defined by the short open-time of dried pellets; exposure to uncontrolled ambient air for more than 30 min at 60 % RH can reintroduce enough moisture to produce visible splay and weld-line embrittlement in moulded parts. Batches stored in damaged or previously opened packaging should be sampled for moisture content before the dryer is charged. The observed failure pattern on a production line with a 100 kg/h throughput dryer was intermittent foam-like surface texture on parts when the desiccant bed had not been regenerated for 8 h; this resolved after desiccant regeneration and a residual moisture check. At melt temperatures above 220 °C, the rate of hydrolytic chain scission increases markedly; residence times beyond 5 min are associated with measurable melt-flow-rate drift and reduced notched Izod values on moulded specimens. Published data for this specific configuration is limited, but the threshold is consistent with PLA hydrolysis behavior.
A direct comparison of the VG7262U property envelope with an unmodified PLA grade under the same test methods shows a trade-off between stiffness and impact resistance. Unmodified PLA typically exhibits notched Izod impact strength of 2 kJ/m² to 5 kJ/m², tensile modulus of 3.4 GPa to 3.6 GPa, and tensile strength of 55 MPa to 65 MPa. VG7262U moves impact resistance to 25 kJ/m² to 35 kJ/m² while tensile modulus declines to 2.6 GPa to 2.9 GPa and tensile strength falls to 45 MPa to 50 MPa. This is caused by the low-modulus elastomer domains that arrest crack propagation. Compared to a highly impact-modified PLA grade with notched Izod values above 50 kJ/m², VG7262U retains a higher tensile modulus and lower melt viscosity, which supports injection moulding of thin-wall parts with wall thickness below 1.5 mm. Compared to ABS, VG7262U has a higher density of 1.24 g/cm³ versus 1.04 g/cm³ to 1.07 g/cm³, a lower heat deflection temperature at 0.45 MPa, and similar notched Izod impact strength in the lower portion of the ABS range. The processing advantage over ABS is the lower melt temperature and the absence of styrene off-gassing, but the operational limitation is the narrower thermal window and moisture sensitivity. Selection against general-purpose PLA and ABS should be based on drop-impact test data under ASTM D2463 or instrumented puncture testing under ISO 6603-2:2023, not solely on datasheet notched Izod values. For direct data on VG7262U in food-contact or long-term outdoor exposure, published data for this specific configuration is limited; project-specific testing is required.
Regulatory compliance for VG7262U must be addressed at the finished-article level because polymer additives, colorants, and conversion residues influence final regulatory status. The supplier’s safety data sheet should be reviewed for REACH registration and authorization substances; RoHS 2011/65/EU heavy-metal thresholds apply to the homogeneous material and are typically satisfied by unfilled PLA compounds of this class, but production-lot verification is required. For food-contact applications, the converter must determine whether the final article meets the overall migration limit of 10 mg/dm² under EN 1186-1:2002 or the applicable food-contact notification under FDA 21 CFR 177.1520, because PLA is not automatically cleared for all food types. Operational incompatibilities include amine-based lubricants, which can accelerate ester cleavage and reduce molecular weight; strong acids and bases, which promote hydrolysis; and prolonged exposure to UV radiation, which embrittles the PLA matrix unless a UV stabilizer masterbatch is incorporated at the letdown ratio specified by the stabilizer supplier. Continuous service above 55 °C to 60 °C is not recommended for load-bearing components because creep modulus decreases significantly near the glass transition temperature. Hot-fill packaging, dishwasher-intensive applications, and parts exposed to boiling water are outside the intended performance boundary. For outdoor applications, weathering program validation under ISO 4892-2:2013 cycle 1 is required before commercial deployment.
| Regulatory domain | Reference standard or directive | Typical status for unfilled impact-modified PLA class |
|---|---|---|
| Restriction of hazardous substances | RoHS 2011/65/EU | Complies for homogeneous material when no prohibited flame retardants or heavy-metal pigments are used; lot verification required. |
| Registration, evaluation, authorisation | REACH (EC 1907/2006) | Polymer is exempt from registration but monomer and additives require registration; confirm with supplier. |
| Food-contact migration | EN 1186-1:2002, EU 10/2011, FDA 21 CFR 177.1520 | Final article must be migration tested; PLA is not universally cleared for all food types. |
| UV weathering | ISO 4892-2:2013 | Requires commercial validation; unmodified PLA embrittles without stabilizer. |
Thin-wall electronic housings with snap-fit lugs and internal bosses represent a demonstrated application window for VG7262U. Production trials on a 1,200 kN hydraulic injection machine using a 32 mm screw and a two-cavity cold-runner tool produced parts with wall thickness 1.2 mm to 1.8 mm and a cycle time of 28 s to 35 s. The critical process variables were a melt temperature of 205 °C to 215 °C, mold temperature of 30 °C, and a cushion of 4 mm to 6 mm. Snap-fit assembly trials under a 10 N insertion force and 5,000 cycle repeated engagement test showed cracking when moisture content exceeded 0.04 % w/w; the same tool with dried pellets held without failure. This behavior confirms that the processing constraint rather than the material’s ambient impact rating is the primary predictor of assembly performance.