| HS Code | 760470 |
| Material Type | Polylactic acid (PLA) nano-composite |
| Appearance | Semi-opaque |
| Form | Pellets |
| Color | Natural/off-white |
| Biodegradability | Compostable |
| Compostability Standard | EN 13432 / ASTM D6400 (typical) |
| Processing Method | Injection molding |
| Melt Temperature Range C | 180-220 |
| Mold Temperature Range C | 20-50 |
As an accredited EcolGreen EGP-104 Semi-Opaque Nano-Composite Biodegradable Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | EcolGreen EGP-104 is supplied in 25 kg sealed, moisture-barrier foil-lined bags on 500 kg pallets with UV-resistant identification labels. |
| Container Loading (20′ FCL) | EcolGreen EGP-104 Semi-Opaque Nano-Composite Biodegradable Polylactic Acid loaded into 20′ FCL, palletized bags, shrink-wrapped and secured for ocean shipment. |
| Shipping | EcolGreen EGP-104 ships as non-hazardous solid pellets/resin in sealed, moisture-barrier bags or fiber drums. Store and transport in a cool, dry, ventilated area away from direct sunlight, heat, and ignition sources. Maintain package integrity; follow applicable local, national, and international transport regulations. Handle with standard industrial hygiene; avoid dust generation. |
| Storage | Store EcolGreen EGP-104 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep containers tightly closed to prevent moisture uptake and contamination. Protect from UV light and oxidizing agents. Maintain stable ambient temperature; avoid extreme heat or freezing. Use appropriate secondary containment, label clearly, and follow manufacturer/SDS guidance for safe handling and shelf life. |
| Shelf Life | Store in a cool, dry place; shelf life is 12 months from manufacture when kept in unopened original packaging. |
Thermoformed rigid packaging produced from EcolGreen EGP-104 imposes a simultaneous constraint on melt strength, sheet haze, and food-contact compliance because the semi-opaque nano-composite polylactic acid sheet must retain a forming window between the glass transition onset and the cold crystallisation peak. On production lines configured with a 75 mm single-screw extruder with an L/D 30:1 barrier screw, a melt pump, and a flexible lip flat die of 900 mm working width, the material is typically compounded at 4.0 wt% to 8.0 wt% into PLA grades such as NatureWorks 4043D or TotalEnergies Luminy LX175 to produce sheet in the 350–800 µm thickness range. The loading band is selected to move haze from the 4–9% range characteristic of unfilled PLA to a semi-opaque band of 62–78% when measured at 500 µm according to ASTM D1003, while preserving melt strength sufficient to prevent web sag in the die-to-chill-roll air gap. Chill roll temperatures are held at 32–48°C, the polishing nip pressure is adjusted to suppress surface micro-pitting, and sheet take-off speed is constrained by the nucleation-rate increase generated by the nano-composite phase; operators report that barrel zone temperatures above 210°C accelerate lactide reformation, causing acrid vapour generation and yellowing of the sheet edge trim. Pre-drying at 75°C for 4–6 h with a desiccant-bed dew point below -40°C is required when ambient relative humidity exceeds 50%, because residual moisture produces splay, surface hydrolysis, and loss of drawability in the thermoforming step. Industry compliance for food-contact articles is established under EU 10/2011/EC as amended by Regulation (EU) 2020/1245, with overall migration testing performed in food simulants D1, B, and A according to the intended food type; in the United States, the formed article is evaluated under FDA FCN 000543 where the PLA base grade holds food-contact authorisation, with the additional requirement that the nano-composite additive possess independent regulatory clearance or be demonstrated as non-migrating at detectable levels. Terminal finished product types include cold-fill dairy dessert cups, bakery clamshells, fruit punnets, and deli trays with peelable lidding films, and the formed parts are checked for dimensional stability using ASTM D648-18 at 0.45 MPa because the practical continuous service ceiling remains near 55–65°C. Regrind incorporation is limited to 20 wt% because repeated heat histories reduce the onset of cold crystallisation and embrittle the corner sections of deep-draw thermoformed articles.
Filament feedstock for fused filament fabrication requires a tight balance between melt viscosity, ovality control, and the interlayer adhesion that determines tensile anisotropy in the final printed part. When EGP-104 is processed as a filament-grade compound on a single-screw extruder with L/D 24:1 to L/D 30:1, a breaker plate screen pack of 40/80/120 mesh, and a water trough held at 38–52°C, the diameter of 1.75 mm and 2.85 mm filaments is maintained within ±0.03 mm using a three-axis laser gauge. Deposition via a nozzle temperature of 195–215°C and a build plate temperature of 50–60°C reduces warping while preventing excessive cold crystallisation on the part base; the nano-composite filler decreases die swell and improves filament dimensional stability but raises apparent melt pressure in nozzle systems with prolonged residence time, so retraction distances above 2 mm at 40 mm/s are typically avoided because the reheated semi-opaque compound can crystallise at the melt zone boundary and produce nozzle clogging. The addition ratio in extrusion formulations is either 100 wt% EGP-104 as a ready-to-run filament resin or a 50–70 wt% let-down into unfilled PLA/PHA blend where thinner walls require lower haze or higher elongation before break. Tensile validation is performed according to ASTM D638-14 Type IV specimens, flexural modulus according to ISO 178:2019, and melt flow stability according to ISO 1133-1:2022 at 210°C/2.16 kg; the melt flow index of the undiluted grade is reported in the 6–12 g/10 min range on the supplier certificate of analysis, while published data for this specific configuration is limited and should be confirmed against the supplier technical file. General-purpose regulatory compliance is anchored to REACH 1907/2006 Annex XVII, RoHS 2011/65/EU Annex II, and California Proposition 65 where applicable. Terminal printed products include compostable retail display fixtures, architectural scale models, electronics production jigs, and short-run packaging mock-ups; medical or implantable applications are outside the demonstrated use envelope because the nano-composite grade is not characterised for prolonged physiological contact.
Agricultural mulch films must combine soil tear resistance, UV weathering resistance, and a controlled opacity window that suppresses weed emergence while retaining sufficient light transmission for crop development. In blown film configurations using a three-layer die with a 1.2 mm to 2.0 mm die gap and a blow-up ratio of 2.5:1 to 3.2:1, EGP-104 is added at 5.0 wt% to 12.0 wt% into a PBAT/PLA base resin blend to produce finished film at 12–25 µm thickness with visible light transmission reduced to 40–60%. Melt temperature at the die is limited to 155–175°C because PLA undergoes chain scission above this envelope, while the PBAT phase loses bubble stability above 185°C; internal bubble cooling is adjusted to hold the frost line height between 1.5 m and 2.0 m, and slit rolls are cured at ambient temperature for 24 h before winding to allow secondary crystallisation and film flatness stabilisation. Compliance for biodegradable mulch film is defined by EN 17033:2018 and ISO 23517:2021, with soil disintegration testing according to ISO 20200:2015 or ASTM D5988-18, and ecotoxicity evaluation according to OECD 208; industrial compostability of the base polymer system is separately confirmed by ASTM D6400-23 or EN 13432:2000/AC:2005. Terminal products include in-field mulch films for tomato, pepper, melon, and strawberry systems, particularly where the semi-opaque finish allows reduced herbicide use under high weed pressure. A documented operational boundary is moisture sensitivity during storage: at warehouse relative humidity above 65%, pre-drying at 50°C for 2–4 h is required before extrusion to prevent hydrolysis and gel speck formation in the blown film.
Cosmetic packaging produced from biodegradable PLA requires an injection moulding window that preserves surface gloss and dimensional stability while avoiding the abrasive wear on mould steel associated with coarse mineral fillers. EGP-104 is processed as a pre-compounded pellet after drying at 70°C for 5–7 h to a moisture content below 250 ppm, with a barrel profile from 165°C rear zone to 195°C nozzle and a mould temperature of 25–40°C. The formulation ratio in the finished moulded article is either 100 wt% EGP-104 for stiff thin-wall components or 20–40 wt% EGP-104 compounded into a PLA/PBS base resin where snap-fit closures require higher elongation before break. On a 120-tonne hydraulic machine producing a 2.5 mm wall jar with a single hot-runner valve gate, cycle time is generally 18–25 s and the gate freezing time is controlled by the cold crystallisation rate of the nano-composite rather than by cooling-water temperature alone. Mechanical validation for injection moulded components uses ASTM D638-14 for tensile properties, ASTM D256-10 for Izod impact, and ISO 306:2022 for Vicat softening temperature. Global market compliance is anchored to REACH 1907/2006, RoHS 2011/65/EU Annex II, and EU 1223/2009 insofar as the finished package must not transfer prohibited substances to the cosmetic formulation even though the package itself is not classified as a cosmetic product. Terminal product types include eyeshadow compacts, lipstick tubes, airless pump housings, and single-use sample jars. The material is not suitable for continuous service above 55°C or for dishwashing cycles above 45°C because the heat deflection temperature of the PLA matrix produces thread deformation and closure loosening under sustained load.
Extrusion coating lines processing polylactic acid for paperboard barrier applications encounter a narrow adhesion window between the melt curtain and corona-treated board because PLA exhibits higher surface tension sensitivity than branched polyolefins. When EGP-104 is incorporated at 4.0 wt% to 7.0 wt% into a coating-grade PLA such as NatureWorks 4044D on a 90 mm single-screw extruder with a 900 mm flat die, a 200 mm air gap, and a chill roll held at 15–25°C, the semi-opaque nano-composite modifies melt drawing behaviour and reduces pinhole formation in a coating layer of 15–25 g/m². Line speed is typically constrained to 80–180 m/min depending on board weight and chill roll capacity; melt temperature at the die lip is kept below 220°C because polylactic acid degrades through lactide reformation at higher temperatures. Board surface treatment is maintained to a minimum wetting tension of 42 mN/m before coating by corona discharge, with the treated surface checked according to ASTM D2578-23, because failure to sustain this level produces adhesive delamination at the board–polymer interface. Food-contact compliance for the coated paperboard is assessed under FDA 21 CFR 176.170 for components of paper and paperboard in contact with aqueous and fatty foods, and under EU 10/2011/EC for the plastic layer with overall migration testing in food simulants A, B, and D1 according to the intended contact ratio. Terminal finished products include cold beverage cup sidewalls, frozen food board trays, sandwich boxes, and bakery board bases where a semi-opaque PLA layer replaces mineral-filled film or a conventional polyolefin coating layer. The operational boundary is moisture sensitivity: the coated board should be converted within 12 weeks at 20–25°C and 40–60% RH, and if board moisture exceeds 7.0 wt%, the coating layer can exhibit steam blisters during heat sealing of the finished pack.
Meltblowing of PLA-based nonwovens is constrained by a narrow viscosity window between melt fracture at high shear and fibre breakage at low draw, and the semi-opaque nano-composite grade is run on meltblown pilot lines with extruder zones set between 175°C and 210°C and a hot air plenum at 240–270°C. EGP-104 is let down at 2.0 wt% to 5.0 wt% into a PLA meltblown resin to increase web opacity and substrate hiding power without generating the shot defects associated with coarse mineral opacifiers; spinneret holes of 0.20–0.40 mm diameter are used at a throughput of 0.30–0.60 g/hole/min, and the collector distance is adjusted to 150–300 mm to balance fibre attenuation and thermal bonding. Fibre diameter distribution is measured according to EDANA NWSP 070.4.R1 (15), and fabric basis weight is determined according to ISO 9073-1:1989; the resulting web is thermally point-bonded or through-air bonded at 90–110°C to maintain biodegradation potential while improving tensile strength. Compliance for compostable nonwoven products is established under EN 13432:2000/AC:2005 and ASTM D6400-23 where industrial compostability claims are made; for hygiene and personal care applications, additional skin sensitisation testing according to OECD 439 or ISO 10993-10:2021 may be required depending on the regulatory route. Terminal products include biodegradable tea bag materials, coffee filter nonwovens, agricultural crop covers, and compostable wipes; the semi-opaque character is critical for wipe applications where substrate masking is specified. A documented operational incompatibility exists with cationic antistatic systems containing primary amines, which accelerate melt instability and cause brittle fusion bonds in the nonwoven web; non-ionic antistatic additives are therefore specified for all hygiene-grade runs.
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EcolGreen EGP-104 is a semi-opaque nano-composite biodegradable polylactic acid compound supplied as cylindrical pellets with a bulk density of 0.78 g/cm³ and packaged moisture below 400 ppm. The formulation combines a PLA matrix with a biodegradable aliphatic-aromatic copolyester impact modifier and a dispersed organically modified mineral nucleant at 1.5 wt% to 3.0 wt%; the supplier reports the nucleant median particle size D50 below 500 nm. The product is intended for injection molding, sheet extrusion, and thermoforming where faster crystallization, higher heat deflection temperature, and semi-opaque appearance are required, and where full transparency is not the primary specification.
The manufacturer’s technical data sheet lists a melt volume-flow rate of 6.0 cm³/10 min at 210°C and 2.16 kg under ISO 1133-1:2022. Density is 1.26 g/cm³ under ISO 1183-1:2019. On injection-molded Type 1A specimens tested according to ISO 527-2:2012, tensile yield strength is 48 MPa and tensile modulus is 3.1 GPa. Notched Izod impact at 23°C is 4.5 kJ/m² under ISO 180:2023, while unnotched Charpy impact at 23°C is 18 kJ/m² under ISO 179-1:2023. Total luminous transmittance at 1.0 mm thickness is 62% measured according to ISO 13468-1:2019.
| Property | Test method | Value |
|---|---|---|
| Melt volume-flow rate | ISO 1133-1:2022, 210°C, 2.16 kg | 6.0 cm³/10 min |
| Density | ISO 1183-1:2019 | 1.26 g/cm³ |
| Tensile yield strength | ISO 527-2:2012, Type 1A | 48 MPa |
| Tensile modulus | ISO 527-2:2012 | 3.1 GPa |
| Notched Izod impact, 23°C | ISO 180:2023 | 4.5 kJ/m² |
| Unnotched Charpy impact, 23°C | ISO 179-1:2023 | 18 kJ/m² |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2013, Method B | 78°C |
| Vicat softening temperature, A50 | ISO 306:2022 | 82°C |
| Total luminous transmittance, 1.0 mm | ISO 13468-1:2019 | 62% |
Pre-drying is mandatory. The supplier specifies desiccant drying at 80°C for 4 h with a dew point of -40°C or lower, targeting residual moisture below 250 ppm. If pellets are exposed to ambient air at relative humidity above 60%, drying should be extended to 6 h. Hydrolytic degradation during processing becomes measurable at residual moisture above 500 ppm, producing viscosity loss, silver streaking, and reduced notched impact strength.
Melt processing occurs within a narrow thermal window. Recommended barrel set-points are 180°C to 195°C, with melt temperature not exceeding 200°C. Capillary rheometry on a 25 mm single-screw extruder equipped with a slit die indicates that residence time at 200°C beyond 5 min reduces melt viscosity by approximately 12% relative to fresh material. At 210°C, the same residence time produces a viscosity drop above 20% and a shift in tan δ associated with molecular weight reduction of the PLA backbone. The practical processing window is therefore approximately ±5°C around the recommended melt temperature.
Compounding and masterbatch dilution on a co-rotating twin-screw extruder with 40:1 L/D and vacuum venting at -0.08 MPa should use screw speed 250 min⁻¹ to 350 min⁻¹ and specific mechanical energy input of 0.18 kWh/kg to 0.22 kWh/kg. Higher energy input causes local shear heating above 195°C and nucleant agglomerate formation, visible as surface micro-gels in extruded sheet. On a 120-ton hydraulic injection molding machine with a 25 mm general-purpose screw and 20:1 L/D, injection pressures of 70 MPa to 90 MPa and mold temperatures of 25°C to 30°C are suitable for thin-wall parts of 1.0 mm nominal wall thickness. Crystallization onset is reported at 112°C by ISO 11357-3:2018 at 10 K/min, allowing cycle-time reductions of approximately 20% compared with unfilled PLA. Gates below 0.8 mm require injection velocities above 100 mm/s to prevent premature freeze-off.
Unmodified PLA homopolymer typically crystallizes slowly and has low notched impact strength. Under ISO 180:2023, notched Izod values for unfilled PLA are often below 3.0 kJ/m². EGP-104 increases that value to 4.5 kJ/m² while maintaining a tensile modulus of 3.1 GPa. The nucleant raises crystallinity after injection molding to 35% to 40%, measured by density gradient column according to ISO 1183-2:2019; annealed unfilled PLA under identical thermal history reaches 20% to 25%.
Relative to talc-filled PLA at 5 wt%, EGP-104 retains higher total luminous transmittance. At 1.0 mm thickness, talc-filled PLA often falls below 45% under ISO 13468-1:2019, whereas EGP-104 remains at 62%. The semi-opaque nano-composite architecture therefore preserves more visible-light transmission than micron-scale mineral fillers while still providing heterogeneous nucleation.
Compared with PLA/PBAT blends at 75/25 weight ratio, EGP-104 has lower Elmendorf tear strength under ISO 6383-1:2015, at 18 N/mm, versus values that can exceed 35 N/mm for PBAT-rich systems. In return, EGP-104 retains tensile modulus near 3.1 GPa, whereas a 75/25 PLA/PBAT blend may fall to 2.0 GPa. The grade is therefore positioned between brittle transparent PLA and high-elongation opaque PLA/PBAT compounds.
Biodegradation and compostability must be verified on the final article geometry. PLA is recognised as industrially compostable under EN 13432:2000 and ASTM D6400-23 when formulation additives do not exceed threshold concentrations. In controlled composting at 58°C and 50% moisture, standard PLA achieves 90% biodegradation within 180 days under ISO 14855-1:2012. For EGP-104, published data for this specific configuration is limited; the manufacturer should provide third-party certification for final packaging or single-use articles before industrial compostability claims are made. Disintegration of 1.0 mm injection-molded plaques under ISO 16929:2021 is reported to exceed 90% after 84 days, but this value is geometry-dependent.
| Standard or regulation | Scope | Condition or limit |
|---|---|---|
| EU 10/2011 | Plastic food-contact materials and articles | Overall migration below 10 mg/dm² |
| EN 13432:2000 | Industrial compostability of packaging | Pass, article-dependent, third-party certification required |
| ASTM D6400-23 | Aerobic composting specification for plastics | Complies when final article certification is available |
| ISO 14855-1:2012 | Ultimate aerobic biodegradation under controlled composting | ≥90% in 180 days for PLA matrix; grade-specific data limited |
| REACH EC 1907/2006 | Registration, evaluation, authorisation and restriction of chemicals | No SVHC above 0.1 wt% |
| RoHS 2011/65/EU | Heavy metal and brominated flame retardant restrictions | Below maximum concentration values |
Application contexts for EGP-104 include food-contact trays, disposable cutlery, cosmetic closures, and horticultural clips. In food-contact trays with 1.0 mm wall thickness, mold temperature of 25°C to 30°C and cooling time of 8 s to 12 s are achievable on hydraulic injection molding machines with clamp force above 120 tons. The heat deflection temperature of 78°C under ISO 75-2:2013, Method B, permits short-term exposure to hot-fill liquids up to 70°C, but continuous service above 45°C is not recommended due to hydrolytic degradation.
In sheet extrusion for thermoformed cups, EGP-104 can be extruded at die temperatures of 185°C to 195°C with polished roll temperatures of 40°C to 50°C. The semi-opaque sheet has a haze level that conceals minor regrind-induced colour variation but still allows transmitted light. Thermoforming requires sheet surface temperature of 90°C to 100°C; below 90°C the sheet is prone to stress whitening, and above 105°C sag increases significantly.
Incompatibilities and boundary conditions include avoidance of amine-based stabilizers and alkaline fillers because residual basic species accelerate transesterification and molecular weight reduction. Aqueous service above 45°C produces progressive hydrolysis, with significant embrittlement within 30 days at 60°C water immersion. Contact with oxidizing acids or chlorinated solvents is not recommended. On a 300-ton injection molding machine running a 4-cavity cutlery tool, pack-and-hold pressure of 55 MPa for 1.5 s yielded consistent part weight within 0.4%, but screw recovery delay increased when back pressure exceeded 5 MPa due to the shear-thinning profile of the compound.