| HS Code | 139227 |
| Material Type | Polylactic Acid (PLA) |
| Polymer Family | Bio-Based Thermoplastic Polyester |
| Bio Based Content | 80% |
| Impact Modification | Impact Modified |
| Optical Property | Transparent |
| Specific Gravity | 1.24 |
| Melt Flow Rate | 10-15 g/10 min |
| Tensile Strength | 5,500-6,000 psi |
| Tensile Elongation | 150-200% |
| Flexural Modulus | 300,000-350,000 psi |
| Notched Izod Impact | 2.0 ft-lb/in |
| Unnotched Izod Impact | No Break |
| Heat Deflection Temperature | 115-120 °F at 66 psi |
| Vicat Softening Temperature | 135-140 °F |
| Mold Shrinkage | 0.004-0.006 in/in |
| Processing Method | Injection Molding |
| Form | Pellets |
| Color | Natural |
As an accredited RTP 2099 X 124789 D Impact Modified Transparent Bio-Based Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | RTP 2099 X 124789 D Impact Modified Transparent Bio-Based Polylactic Acid supplied in 25 kg foil-lined bags, palletized, labeled per regulations. |
| Container Loading (20′ FCL) | 20′ FCL container loading: RTP 2099 X 124789 D Impact Modified Transparent Bio-Based Polylactic Acid, palletized, shrink-wrapped, and secured cargo. |
| Shipping | RTP 2099 X 124789 D Impact Modified Transparent Bio-Based Polylactic Acid is shipped as solid pellets in sealed bags, drums, or octabins. It is typically not regulated as hazardous for transport unless the SDS states otherwise. Keep containers closed, dry, and away from excessive heat. No special placards are normally required. |
| Storage | Store in a cool, dry, well-ventilated area in tightly sealed containers or moisture-barrier bags. Protect from direct sunlight, heat, flames, and moisture, as the material is hygroscopic. Keep away from strong oxidizers. Maintain ambient temperatures, preferably below 30°C, and low humidity. Use clean handling to avoid dust and contamination. Rotate stock and dry before processing. Keep containers closed when not in use. |
| Shelf Life | RTP 2099 X 124789 D PLA compound: store sealed, cool, dry; typical shelf life is 12 months from manufacture if unopened and moisture-protected. |
In cold-chain retail operations where refrigerated display cabinets maintain product temperatures at or below 4 °C, the thermoformed tray-and-lid segment is an established downstream route for RTP 2099 X 124789 D Impact Modified Transparent Bio-Based Polylactic Acid. The material is introduced at 100 wt% of the sheet-extrusion feedstock, while closed-loop thermoforming skeleton and edge-trim regrind may be metered back into the virgin pellet stream at a maximum of 20 wt% only when the flake is dried to a residual moisture level below 250 ppm and optically sorted to exclude label contamination. Food-contact compliance is anchored to Regulation (EC) No 1935/2004, Commission Regulation (EU) No 10/2011 as amended by Regulation (EU) 2016/1416, and the supplier’s FDA food-contact substance dossier; the overall migration limit applied to the finished article is 10 mg/dm² under the food simulant and time-temperature conditions selected according to Annex III and Annex V of Regulation (EU) No 10/2011. For converters making compostability or organic-recovery claims, formed articles must be assessed against EN 13432 for disintegration, biodegradation, and ecotoxicity rather than inferred from the bio-based carbon content, which is measured separately by ASTM D6866-22 Method B. Production employs a single-screw sheet extrusion line with a 36:1 L/D barrier screw, fine-mesh screen changer, and melt pump feeding a flat die set between 190 °C and 205 °C; roll-stack temperatures are maintained between 25 °C and 40 °C to minimize uncontrolled crystallinity and haze. Thermoforming follows as a plug-assisted, pressure-assisted process using aluminum tooling conditioned between 30 °C and 45 °C, with hinge regions designed to exceed 0.5 mm post-form thickness because the maximum failure risk occurs at stress-whitened hinge lines after repeated opening. Terminal article types include hinged berry punnets, chilled salad containers, deli-lid domes, and cold-chain clamshells; the operational boundary is strictly non-hot-fill and non-pasteurization use because the heat distortion temperature of PLA remains below 60 °C under load, and exposure to dishwashing or microwaving is outside the validated process window.
Because the impact-modified PLA phase cannot fully re-entangle across a frozen weld line when cavity steel is run below approximately 20 °C, weld-line integrity in transparent cosmetic closures and jar bases becomes the controlling variable when a sequential valve-gated hot runner delivers melt fronts around a core pin. The downstream formula is a ready-molding grade presented at 100 wt%; in-house regrind is limited to 15 wt% because multiple heat histories in PLA accelerate molecular weight reduction and shift yellowness index upward, while transparent oil-soluble dyes are introduced at 0.01–0.05 wt% only through a gravimetric liquid-color feed. Packaging compliance is controlled by Regulation (EC) No 1223/2009 for cosmetics packaging compatibility, Directive 94/62/EC Article 11 for heavy-metal concentration in packaging where the summed lead, cadmium, mercury, and hexavalent chromium content must remain below 100 mg/kg, and REACH Annex XVII for restricted substances. The injection molding line should run a three-zone screw with compression ratio at or below 2.0:1, barrel profile from 185 °C to 200 °C, hot-runner manifold set at 190 °C, and mold steel at 25–40 °C; injection speed is set to fill the part in 0.8–1.5 s, while holding pressure is adjusted between 40 MPa and 70 MPa to sink-mark-free packing. The known process conflict is that raising mold temperature to improve weld-line strength increases cycle time and can create post-molding crystallinity that reduces transparency; lowering mold temperature preserves haze but produces notch-sensitive weld lines measured according to ISO 179-1:2010 Charpy notched impact or ASTM D256 Izod. Terminal parts include transparent jar bases, lipstick outer shells, overcap collars, and airless-pump housings. Compatibility testing must exclude ethanol-based formulations above approximately 30 % concentration and strongly ketone-based fragrances because PLA stress-cracking occurs in highly polar solvent environments; published data for the specific grade under particular fragrance compositions is limited and requires storage testing at 45 °C for 28 days before production release.
Filament manufacturers serving the additive-manufacturing market require a closed-loop dimensional control strategy because the melt viscosity difference between the PLA matrix and the impact-modifier domain can produce short-term diameter oscillation if the extruder is run in open-loop mode. The resin is used at 100 wt% pellet feed, with spool-edge and start-up regrind limited to 20 wt% and re-dried to below 250 ppm moisture; opaque or colored masterbatch is restricted to 2–4 wt% for non-optical applications because higher let-down ratios reduce light transmission and increase haze beyond the transparent filament specification. A barrier-screw extruder with 24:1–30:1 L/D, a screen pack of 100/80/100 mesh, and a gear pump is used to feed a 1.75 mm or 2.85 mm die; the melt temperature is held between 195 °C and 205 °C, and the first water bath is maintained at 30–40 °C to prevent coolant quenching that introduces axial shrinkage. Dual-axis laser gauges measure diameter at 200 Hz, and the haul-off speed is adjusted to maintain a tolerance of ±0.05 mm for 1.75 mm filament and ±0.08 mm for 2.85 mm filament. Ovality, expressed as the difference between maximum and minimum diameter, is held below 0.03 mm for 1.75 mm filament because larger ovality causes drive-gear slippage in Bowden-type extruders. Printed part mechanical properties are characterized by ISO 527-2:2012 for tensile strength and elongation at break, ISO 180 for notched impact, and ASTM D1003-21 for haze on printed plaques; published comparative datasheets indicate that impact-modified PLA trades approximately 10–15 % of tensile modulus relative to unmodified PLA while improving notched impact and reducing brittle fracture in snap-fit prototypes. Downstream printing conditions for this material class are typically a nozzle set point of 200–220 °C, a bed temperature of 50–60 °C, and closed-chamber ambient below 30 °C. Filament spools should be dried at 60 °C for 4 h before printing if exposed to relative humidity above 60 %, because hydrolysis reduces interlayer adhesion. Terminal product types include transparent prototypes, light-guide mock-ups, anatomical teaching models, assembly fixtures, and packaging mock-ups; the material is not recommended for continuous service above 55 °C or load-bearing under UV exposure without accelerated weathering data according to ASTM G154.
For backlit point-of-sale lenses and decorative diffuser panels where LED board temperatures remain below 45 °C, the impact-modified transparent bio-based PLA is converted through flat-sheet extrusion, laser cutting, and low-force thermoforming to create transparent parts that must not warp under edge-clamping stress. The sheet feedstock uses 100 wt% as-supplied pellets; edge trim from in-line slitting may be reintroduced at 15–25 wt% if the regrind particle size distribution passes a 3 mm screen and the moisture content is below 250 ppm. Compliance is governed by Directive 2011/65/EU for RoHS, Regulation (EC) No 1907/2006 for REACH, and IEC 60598-1:2020 for luminaire construction when the diffuser is mounted inside a luminaire assembly; flame performance is evaluated according to UL 94 at 1.5 mm thickness, where PLA is typically rated HB and should not be used as an enclosure for uninsulated live parts. The sheet line runs a twin-screw or single-screw configuration with a melt pump and a polished three-roll stack controlled between 30 °C and 45 °C, producing thicknesses from 0.8 mm to 2.0 mm; thermoforming is conducted with plug-assisted pressure forming and tooling at 35–45 °C, with part draw ratios kept below 1.5:1 to avoid local thickness reduction below 0.4 mm. Screen printing and UV-curable inks should be qualified for adhesion because the low surface energy of PLA requires corona or plasma pre-treatment at 38–42 mN/m dyne level before decoration. Terminal products include edge-lit point-of-sale sign lenses, LED diffuser covers, decorative light guide plates, and display trim; the operational boundary excludes high-brightness LED arrays that generate heatsink temperatures above 55 °C and outdoor exposure without UV stabilizer qualification.
The limiting process variable in thin-wall diagnostic enclosure molding is not injection pressure but residence-time control, because PLA subjected to prolonged barrel residence above 200 °C generates lactide and oligomers that create plate-out, splay, and optical defects on transparent diagnostic windows. The material is introduced at 100 wt% as a ready-to-mold pellet; regrind from sprues and runners is restricted to 10 wt% and only for non-patient-contact internal components because the biocompatibility evaluation of the finished device applies to the exact formulation, and increasing recycled content changes the leachable profile. The regulatory framework includes ISO 13485:2016 for quality management, ISO 14971:2019 for risk management, IEC 61010-1:2010/AMD1:2016 for electrical test equipment housings, and ISO 10993-5:2009 plus ISO 10993-10:2021 for cytotoxicity, irritation, and sensitization testing on the final device; the RTP grade is not an implantable grade, and published data for this specific compound under all intended sterilization modalities is limited. Injection molding uses a shot-size-controlled 30–40 mm screw with a non-return valve designed for low shear, barrel profile 185–200 °C, hot-runner manifold 190 °C, and mold steel at 25–35 °C; cushion is held at 2–4 mm to prevent screw bottoming and to control hold pressure decay. The process window should keep total material residence time below 5 min at melt temperature, and the machine should be purged with a bio-based PLA purging compound after any ABS, PC, or PVC material change to avoid contamination-induced haze. Terminal products include point-of-care analyzer housings, benchtop diagnostic enclosures, lateral-flow cassette windows, and transparent sample observation lids. The documented operational boundary is that autoclave sterilization at 121 °C is not feasible due to heat-deflection limits, and gamma irradiation or ethylene oxide exposure must be evaluated for yellowing and mechanical degradation on molded plaques before release.
In the toy and educational model segment, transparent window shells and display covers require impact-modified PLA because the notch-sensitive behavior of unmodified PLA frequently causes hinge and snap-fit fractures during assembly and play. The compound is fed at 100 wt% in injection molding; sprues and runners may be reground at up to 10–15 wt% only when the regrind is lot-controlled and used in non-transparent internal components, because multi-pass heat history raises haze and decreases impact consistency. Toy safety compliance is established by Directive 2009/48/EC on the safety of toys, EN 71-3:2019+A1:2021 for migration of certain elements, and ASTM F963-23 for U.S. toy-market testing; REACH Annex XVII and Regulation (EC) No 1272/2008 apply to hazardous substances in the plastic matrix. The production process uses a general-purpose screw with 20:1 L/D and a mold temperature between 25 °C and 40 °C, with injection speed high enough to fill thin transparent windows in 0.6–1.2 s but low enough to prevent shear splay at the gate; hot-tip gate diameters of 1.0–2.0 mm are preferred over tunnel gates because the impact-modified melt is more shear sensitive than unfilled PLA. Terminal product types include transparent sorting-block windows, plush-toy eye shells, educational model display covers, and transparent assembly playsets. The limitation is that repeated mechanical abuse at sub-zero temperatures below 0 °C should be avoided because impact resistance decreases with temperature, and the finished toys should not be subjected to dishwasher washing at temperatures above 55 °C.
Competitive RTP 2099 X 124789 D Impact Modified Transparent Bio-Based Polylactic Acid prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
RTP 2099 X 124789 D is a compounded impact-modified transparent bio-based polylactic acid (PLA) supplied by RTP Company. The 2099 prefix identifies the bio-based PLA compound series, while the X 124789 D suffix denotes the specific formulated product and color/identification code assigned by the manufacturer. The material is intended for injection molding and sheet extrusion applications where renewable feedstock content and optical clarity are required simultaneously with improved impact resistance relative to unmodified PLA. Publicly released specification limits for this exact suffix are limited; therefore, representative numerical values cited here are based on RTP 2099 series technical communications and are not final lot acceptance criteria. The compound is not a dry blend of pellets and impact modifier. It is produced by melt compounding PLA resin with an impact-modifier package selected to limit refractive index mismatch against the PLA matrix. If the dispersed modifier domain size is excessive or the refractive index difference is too large, total luminous transmittance falls and haze increases because light scattering is induced. Typical transparent grades of this class retain total luminous transmittance above 85 % and haze below 20 % on a 2.0 mm plaque tested according to ASTM D1003-21.
| Property | Test Method | RTP 2099 X 124789 D Representative Range | Neat Transparent PLA | Opaque Impact-Modified PLA |
|---|---|---|---|---|
| Specific gravity | ASTM D792-20 | 1.23–1.27 g/cm³ | 1.24 g/cm³ | 1.22–1.26 g/cm³ |
| Tensile strength at yield | ASTM D638-14 Type I, 5 mm/min | 35–50 MPa | 60 MPa | 25–40 MPa |
| Elongation at break | ASTM D638-14 | 15–100 % | 2–5 % | 50–300 % |
| Flexural modulus | ASTM D790-17 | 1800–2400 MPa | 2800–3500 MPa | 1200–1800 MPa |
| Notched Izod impact, 23 °C | ASTM D256-23 | 80–160 J/m | 20–30 J/m | 100–300 J/m |
| Haze, 2.0 mm plaque | ASTM D1003-21 | 5–20 % | 2–5 % | Opaque |
| Heat deflection temperature at 0.46 MPa | ASTM D648-18 | 50–65 °C | 50–60 °C | 45–60 °C |
These values illustrate the central trade-off in this product category. The impact-modified transparent compound retains sufficient optical character for light-diffusing and transparent rigid packaging, but its flexural modulus is lower than that of neat PLA by approximately 20–35 %. Compared with an opaque impact-modified PLA, the transparent grade may sacrifice some low-temperature toughness because the impact-modifier package must also maintain refractive index compatibility. Notched Izod data at −20 °C are not consistently published for this specific suffix; cold-impact decisions should be based on a separate ASTM D256-23 lot test at the application temperature.
Impact modification in transparent PLA does not function as simple plasticization. The modifier must form a dispersed phase with a refractive index close to the PLA matrix. If the modifier is miscible with the matrix, the glass transition temperature and heat deflection temperature may be reduced. If the modifier is immiscible but not refractive-index matched, haze increases because scattering intensity scales with the square of the refractive index difference and with the sixth power of the dispersed particle radius. For a transparent compound, the modifier particle size is typically maintained below approximately 200 nm to avoid visible scattering. That constraint limits the maximum notched Izod attainable because particle cavitation and shear yielding are controlled by modifier domain size. In a production twin-screw extruder with 40:1 L/D and high-shear mixing sections, dispersion depends on barrel temperature profile, screw speed, and feed location. Published data for this specific suffix under controlled shear history are limited; therefore, compounding reproducibility must be verified by in-line melt viscosity monitoring and off-line ASTM D1003-21 plaque testing.
Application evaluations for RTP 2099 X 124789 D generally include rigid cosmetic packaging, compact components, consumer electronics cover lenses, point-of-sale display frames, and light-diffusing panels. In these applications, the material is typically injection molded in wall thicknesses from 1.0 mm to 3.2 mm. Production-scale experience on an all-electric injection molding machine with a 30 mm diameter reciprocating screw and 22:1 L/D ratio indicates that a flat melt temperature profile between 185 °C and 200 °C is required. At melt temperatures below 170 °C, thin-wall sections show short shots and weld-line opacity. At temperatures above 210 °C, residence times longer than 5 min produce molecular weight loss, reduced notched Izod, and measurable yellowing according to ASTM E313-20.
The compound must be dried before processing. A desiccant-bed dryer delivering air with a dew point of −40 °C or lower is required. Drying at 80 °C for 4 h reduces moisture content to below 0.025 % by weight when verified according to ISO 15512:2019 or equivalent Karl Fischer titration. If ambient relative humidity exceeds 60 %, dried material should not remain in an open machine hopper for more than 30 min. Hydrolytic degradation is first observed as a reduction in melt viscosity. A melt flow-rate increase beyond the lot control limit indicates unacceptable molecular weight loss. Melt flow-rate is measured according to ASTM D1238-20 at 210 °C with 2.16 kg; representative values for the RTP 2099 series range from 6 to 20 g/10 min. Nozzle melt temperature should not exceed 205 °C, and barrel residence time should be minimized when screw recovery time is extended.
Mold temperature is normally controlled between 15 °C and 40 °C. Lower mold temperatures reduce cycle time but increase molded-in residual stress, which is visible as photoelastic fringe patterns in transparent parts. Higher mold temperatures improve surface gloss and reduce stress whitening at weld lines but extend cooling time. Back pressure is maintained in the range of 0.3–0.7 MPa to ensure melt homogeneity without excessive shear heating. Low back pressure can leave unmelted impact-modifier domains that appear as visible gels or fisheyes in the molded part.
Component designs requiring notched Izod values above 80 J/m at 23 °C should be evaluated against actual lot data rather than representative ranges. The representative range for this class is 80–160 J/m, but the distribution depends on modifier loading and processing history. High-speed loading conditions are better assessed by instrumented puncture resistance according to ASTM D3763-20 than by notched Izod alone. Impact-modified PLA may show ductile puncture behavior at 23 °C, but the transition to brittle failure occurs at a higher temperature than in polycarbonate. Compared with transparent polycarbonate, the bio-based PLA compound offers a lower melt processing temperature and higher bio-based carbon content, but lower continuous use temperature and lower impact at sub-zero exposure. Compared with PETG, the PLA compound may show lower heat deflection temperature. PETG typical heat deflection temperature at 0.46 MPa is approximately 70–75 °C, whereas the impact-modified PLA representative range is 50–65 °C. Heat sterilization is therefore not appropriate for this material.
Snap-fit designs should not rely solely on flexural modulus. The lower flexural modulus relative to neat PLA requires deeper undercuts or shorter engagement lengths. Creep behavior under sustained load should be confirmed according to ISO 899-1:2017 or ASTM D2990-17 because short-term tensile data do not predict time-dependent deflection in transparent PLA compounds. Gate design also influences impact performance: edge gates in thin-wall parts can create molecular orientation that reduces notched Izod perpendicular to flow. A tab gate or fan gate with a gradual land thickness transition is preferred when impact-critical sections are located away from the gate.
The bio-based carbon content of the base PLA polymer can be verified according to ASTM D6866-22 Method B. Typical PLA polymers contain a bio-based carbon fraction above 90 %. However, impact modifiers, colorants, and processing stabilizers may reduce the total bio-based carbon content of the compounded pellet. Renewable feedstock content should not be equated with industrial compostability. Compostability requires independent certification under EN 13432:2000 or ASTM D6400-23. Published data for compostability of this specific impact-modified formulation are limited; the presence of non-PLA impact modifiers may prevent the compostability claims permitted for unmodified PLA.
For food-contact uses, the compounded grade must be evaluated under the applicable regulatory pathway. In the United States, 21 CFR 177.1500 covers PLA for certain food-contact conditions, but the specific additive and color package requires confirmation through the supplier’s letter of guarantee. In the European Union, EU Regulation 10/2011 requires migration testing according to EN 1186-1:2002 before a food-contact declaration can be made. RoHS documentation is typically limited to the absence of intentionally added substances listed in Directive 2011/65/EU Annex II. REACH compliance under EC 1907/2006 should be confirmed by the supplier for each specific suffix and production batch.
| Regulatory or Standard Reference | Scope | Required Verification |
|---|---|---|
| ASTM D6866-22 Method B | Bio-based carbon fraction | Base resin above 90 %; compounded pellet to be lot-verified |
| EN 13432:2000 / ASTM D6400-23 | Industrial compostability | Limited data for impact-modified formulation |
| 21 CFR 177.1500 | U.S. food contact | Additive and color package must be confirmed |
| EU Regulation 10/2011 | European Union food contact | Migration testing per EN 1186-1:2002 required |
| Directive 2011/65/EU Annex II | RoHS restricted substances | No intentionally added restricted substances; batch documentation required |
| EC 1907/2006 | REACH SVHC | Supplier confirmation required for specific suffix |