| HS Code | 579581 |
| Manufacturer | RTP Company |
| Brand | RTP |
| Product Name | RTP 2099 X 131060 A |
| Material Type | Polylactic Acid (PLA) |
| Processing Method | Injection Molding |
| Flame Retardant | Yes |
| Form | Pellets |
| Density | 1.25 g/cm³ |
| Tensile Strength | 50 MPa |
| Flexural Modulus | 3500 MPa |
| Notched Izod Impact | 2.0 kJ/m² |
| Heat Deflection Temperature | 55°C at 1.8 MPa |
| Ul 94 Flame Rating | V-0 |
| Melt Flow Rate | 10 g/10 min |
| Drying Temperature | 80°C |
| Melt Temperature | 190-220°C |
| Mold Temperature | 25-55°C |
As an accredited RTP 2099 X 131060 A Flame Retardant Injection Molding Polylactic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | RTP 2099 X 131060 A supplied in 25 kg sealed moisture-barrier foil-lined bags, palletized for shipment to protect from moisture and contamination. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): RTP 2099 X 131060 A flame retardant injection molding polylactic acid, packaged in 25 kg bags. |
| Shipping | RTP 2099 X 131060 A Flame Retardant Injection Molding Polylactic Acid ships as non-hazardous polymer pellets. Proper shipping name: Not regulated. Hazard class: None. UN number: None. Packing group: None. No placards or labels required; follow SDS and carrier instructions. Store cool and dry. |
| Storage | Store RTP 2099 X 131060 A in a cool, dry, well-ventilated area away from heat, ignition sources, and direct sunlight. Keep containers tightly closed to prevent moisture absorption. Maintain recommended ambient temperature (e.g., 10–30°C) and low humidity. Do not store near incompatible chemicals. Use original packaging, follow first-in, first-out rotation, and protect from physical damage and water. |
| Shelf Life | Shelf life is typically twelve months when stored in cool, dry, sealed original packaging away from moisture and heat. |
In molded enclosures for smart-home sensors, USB charging adapters, and portable data terminals, this RTP 2099 X 131060 A compound is specified where fire enclosure criteria are required under IEC 62368-1 and where the manufacturer has committed to a non-halogenated formulation. The processing window starts with desiccant drying at 80 °C for 4 h to a dew point of -40 °C; moisture above 0.025 wt% hydrolyzes the PLA matrix during plastication and can reduce the number-average molecular weight sufficiently to alter knit-line strength and flame-retardant distribution. Barrel temperatures are typically profiled from 180 °C at the feed throat to 210 °C at the nozzle, with hot-runner manifold temperatures held at 195–205 °C. Mold temperature is set at 30–60 °C for amorphous parts, but higher mold temperatures of 80–100 °C are required when dimensional stability above 55 °C is specified. Regrind addition is limited to 15 wt% for fire enclosure surfaces because successive heat histories hydrolyze the ester backbone and the resulting viscosity reduction can allow the flame-retardant additive to migrate toward the surface during crystallization. Thin-wall sections of 1.2–1.5 mm should be gated with lands of 0.8–1.0 mm and vented at 0.02–0.03 mm to avoid burn marks caused by volatiles from the FR system. Finished component types include smart-home hub covers, sensor mounting bases, and miniature USB charger housings that require UL 94 V-0 at the part thickness listed in the resin supplier’s yellow card. RoHS 2011/65/EU and REACH SVHC declarations are typically required for these consumer-facing parts.
Internal carriers, motor shrouds, and terminal guard plates in unattended home appliances are tested as finished components under IEC 60695-2-11, and the selection of a PLA-based flame-retardant grade requires verification of glow wire ignition temperature and glow wire flammability index on the actual part. The addition of regrind at 15 wt% lowers the melt viscosity, shortens the shear heating contribution in the screw, and can produce a thinner flame-retardant char front at knit lines; processors therefore reduce regrind to 10 wt% when the part carries 850 °C glow wire test requirements. Melt temperature is held at the lower end of the range, 185–195 °C, to limit lactide reformation, and the injection profile uses a medium screw speed of 80–120 rpm with back pressure of 0.3–0.5 MPa to maintain dispersion without destroying the FR particle size. Mold temperature is elevated to 80–90 °C and cooling time is extended by 20–30% to build crystallinity; the crystalline fraction raises heat deflection temperature but also increases the risk of post-mold dimensional drift if ejection is premature. Terminal parts include motor end caps, relay mounting bases, and cordless appliance internal baffles. Compliance for unattended appliance use also requires IEC 60695-2-12 and IEC 60695-2-13 data when material substitution is filed with the appliance certifier.
For automotive cable clips, interior close-out panels, and HVAC actuator housings, the material represents a lower-temperature use boundary, with continuous exposure limited to 65 °C unless the part is annealed or crystallized and validated under the end-use temperature profile. The relevant interior flammability regulations are FMVSS 302 and ISO 3795, which require a burning rate not exceeding 100 mm/min; the material’s flame-retardant package can meet this standard at wall thicknesses down to 1.5 mm, but published data for this specific configuration is limited and molded sample verification is required. The recommended virgin-to-regrind ratio on automotive interior parts is 90:10 by weight, and no more than 2 wt% of a compatible color masterbatch should be added because the FR loading is close to the percolation threshold. Processing on a 120–180 ton press with a screw of 22:1 L/D and compression ratio of 2.5:1 provides adequate melting for shot weights between 10 g and 60 g; melt temperature is 195–205 °C and mold temperature is 80–95 °C to promote crystallinity and reduce post-mold warpage. The limiting boundary is not flammability but impact toughness: snap-fit geometries need minimum rib radii of 0.5 mm and gate positions placed away from snap fingers to prevent brittle fracture. Terminal products are HVAC blend door brackets, wiring harness clips, and interior trim retainers.
LED driver housings and luminaire connector shells require thermal endurance because internal driver components frequently operate at 85–95 °C in enclosed luminaires. This material can be considered only when the part is crystallized during molding and the wall thickness is kept above 1.6 mm; amorphous PLA parts will creep at these temperatures. The process is more demanding than consumer electronics molding: barrel temperature must not exceed 210 °C, and total melt residence time is limited to 300 s to avoid chain scission and FR additive decomposition. Mold temperature of 100–115 °C is required to achieve a crystallinity level sufficient for heat deflection under ASTM D648 Method B at 0.455 MPa; this high mold temperature lengthens cycle time by 35–50% relative to amorphous molding. Ratio control uses 100% virgin material for initial qualification, with regrind introduced at 5–10 wt% only after thermal aging at 85 °C for 500 h confirms retention of UL 94 V-0 and no surface exudation. The applicable luminaire standards are IEC 60598-1, IEC 61347-1, and UL 8750; flammability requirements are evaluated on the end product rather than on a plaque. Terminal products include linear LED driver boxes, emergency lighting power packs, and outdoor luminaire terminal covers. The boundary condition is the junction between the screw boss and the housing wall; bosses must be cored to maintain a wall thickness ratio of 1:1.5 to prevent sink marks that reduce creep resistance.
In office printer paper guides, scanner frames, and document feeder housings, this material has been evaluated as a replacement for PC/ABS because the PLA-based compound reduces the carbon footprint of the molded part while maintaining fire enclosure performance under IEC 62368-1. The substitution is not straightforward: PLA has a narrower processing window and lower practical heat resistance than PC/ABS, so the design cannot combine parts that operate near the fuser roller or power supply, where surface temperatures exceed 70 °C. Molding trials on a hot-runner tool with 8 cavities and shot weight of 45 g use a melt temperature of 195–205 °C, mold coolant temperature of 60–70 °C, and fill time of 1.2–1.5 s to prevent premature gate freeze-off. The ratio of flow length to wall thickness should remain below 150:1 for unreinforced FR PLA; attempting to fill a 1.0 mm wall beyond this ratio produces hesitations and burn marks at the flow front. Regrind ratio in office equipment housings is maintained at 10–15 wt%, and the material must be dried again whenever the plant operates in ambient relative humidity above 60% for more than 2 h before hopper loading. The fire enclosure path requires UL 94 V-0 at the minimum part thickness shown on the supplier’s yellow card, and the final assembly is tested to IEC 62368-1 clause 6.4 for combustibility. Terminal parts include scanner housings, ADF frames, and internal cable management troughs.
Because low-voltage connector bodies and terminal blocks are subjected to IEC 60112 comparative tracking index testing and IEC 60695-2-11 glow wire testing on the final assembled part, the processing conditions emphasize dispersion and char uniformity. The flame-retardant system in PLA can reduce the tracking index relative to non-flame-retardant PLA, so printed circuit board standoffs and connector insulation rated for CTI ≥ 250 V must be verified at the actual wall thickness. For connector bodies with multiple pin cavities, the recommended runner diameter is 4–5 mm and the sub-runner length is kept below 80 mm to avoid jetting. Processing uses a screw with a mixing section, 20:1 L/D, and back pressure of 0.2–0.4 MPa; melt temperature is 190–200 °C and mold temperature is 70–80 °C. The virgin-to-regrind ratio should not exceed 80:20 for non-safety connector parts, but is restricted to 90:10 when pins are insert-molded because contamination from metal insert preheating and oil residue can interfere with the FR char formation. Terminal products include appliance terminal housings, relay bases, and PCB connector bodies. The operational boundary is repeated high-humidity exposure: PLA connectors should be conditioned at 40 °C and 90% RH for 168 h and retested for tracking index if the application is in a condensing environment.
Handheld terminals, remote controls, and non-patient-contact portable device housings that contain lithium-ion cells require fire enclosure assessments under IEC 62368-1 clause B.4 or equivalent product safety standards. The PLA-based FR grade provides the required flame-retardant char when wall thickness is above 1.2 mm, but the drop-impact performance is the primary design constraint because neat PLA is more brittle than PC/ABS or polycarbonate. Thickness of screw bosses must not exceed 40% of the nominal wall thickness, and the ratio of wall thickness to rib thickness should be 1:0.5 or less to avoid sink and stress concentration. The molding process for drop-tested components uses a cold mold at 25–35 °C to produce an amorphous structure with higher impact resistance than a fully crystallized part; melt temperature remains 190–205 °C and hold pressure is set at 50–70% of the injection pressure to reduce molded-in stress. Only virgin material is used for the first shot qualification, and regrind is limited to 10 wt% after impact testing at -10 °C shows no brittle failure. Terminal products are battery-powered scanners, wall-mounted thermostat housings, and handheld data collectors. The limitation is prolonged contact with body oils and alcohols: the ester linkages in PLA are susceptible to environmental stress cracking when combined with sustained hoop stress around metal inserts.
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RTP 2099 X 131060 A Flame Retardant Injection Molding Polylactic Acid is an injection-moldable polylactic acid compound carrying a proprietary flame-retardant additive package. The X 131060 A suffix identifies the specific formulation, additive loading, and color state within the RTP 2099 PLA family; it is not a general-purpose PLA designation. Because published data for this specific configuration is limited, process and design qualification should begin with a supplier-controlled reference lot and should include lot-specific melt flow testing under ISO 1133-1:2022 at 210 °C/2.16 kg, tensile testing under ASTM D638-14 or ISO 527-2:2012, and vertical burn classification under UL 94 at the production wall thickness.
The grade is differentiated from unfilled PLA by its capacity to be evaluated for vertical burn classifications such as UL 94 V-0 at 1.5 mm nominal wall in properly gated and vented mold trials; unmodified PLA typically achieves only HB unless heavily modified. The flame-retardant package raises melt elasticity and can reduce impact strength compared with the base PLA; notched Charpy or Izod data must be reviewed before substituting this material for polycarbonate/acrylonitrile butadiene styrene in drop-impact applications. The compound is intended for injection molding of electrically non-functional insulating parts, housings, brackets, and enclosures where ignition resistance must coexist with a bio-based aliphatic polyester backbone.
Processors should not assume that this product handles like a standard unfilled PLA. The melt is more sensitive to residence time and shear heating because flame-retardant additives can accelerate ester bond degradation when thermal load exceeds the compound’s stable processing band. Incoming resin should be sealed and stored at <15 °C dew-point environment or in moisture-barrier packaging until drying; batch-to-batch variance in melt flow should be tracked against the compounder’s certificate of analysis and is recognized as a production control point on injection molding lines running hot-runner tooling.
Polylactic acid is an aliphatic polyester that undergoes random chain scission through hydrolysis of ester linkages. Moisture contents above 0.025 % by weight are sufficient to reduce molecular weight during plastication, lower melt viscosity, and produce splay, gas streaking, or reduced flame-retardant performance at the molded part surface. The material should be dried with a desiccant dryer delivering air at a dew point of −40 °C or lower. Drying at 80 °C for 3–4 h is a conservative starting point for PLA; however, the flame-retardant additive package may require a lower hopper residence time to prevent pellet bridging or tackification. The dry-air stream must not exceed 90 °C at the hopper inlet, because pellet softening and feed-throat blockage can occur before processing begins.
On production-scale hopper and conveying systems, the moisture balance is influenced by ambient relative humidity, regrind percentage, and the condition of desiccant bed regeneration. If regrind is added at rates above 20 % by weight, the regrind should be dried separately or blended before the hopper to avoid moisture stratification. Long dilute-phase conveying lines can generate fines from pellet attrition; fines consume additional additive stabilizer and create melt viscosity heterogeneity. A dedusting step or lower conveying velocity is preferable when lot-to-lot variation in melt flow exceeds ±10 % from the reference value.
| Parameter | Conservative starting range | Process basis |
|---|---|---|
| Desiccant dryer dew point | −40 °C to −50 °C | PLA hydrolysis control |
| Drying temperature | 80 °C for 3–4 h | Supplier-general PLA guidance |
| Residual moisture | <0.025 % by weight | Karl Fischer titration |
| Nozzle melt temperature | 195 °C to 215 °C | Reciprocating screw, L/D 20:1 or higher |
| Mold coolant temperature | 20 °C to 40 °C | Amorphous skin, dimensional control |
| Back pressure | 0.3 MPa to 0.7 MPa | Melt homogenization without shear overheat |
| Screw speed | 50 rpm to 100 rpm | Surface-speed dependent, <0.25 m/s on small screws |
| Cushion | 3 mm to 6 mm | Shot-size stability |
| Decompression | 2 mm to 5 mm | Nozzle drool control |
These values are starting-point conditions derived from general PLA injection-molding practice; they must be confirmed against the current supplier certificate of analysis for RTP 2099 X 131060 A. Mold-filling simulations should not use neat PLA viscosity data because the flame-retardant package alters the shear-thinning curve, particularly at shear rates below 100 s⁻¹.
Hot-runner systems introduce two process conflicts for flame-retardant PLA: extended residence time and stagnant melt zones. The gate should be thermally isolated from the manifold to prevent overheating of the gate seal. Direct-gated or valve-gated systems with minimum dead volume should be selected over open hot runners whenever possible. Screw-recovery time should be set so that total residence time in the barrel and hot runner remains below 8 min; temperatures above 220 °C at the manifold can generate acetic acid from PLA degradation, causing apparent viscosity loss, plate-out, and surface blush. Production-scale field observations on PLA compounds show that mold deposit accumulation becomes measurable after approximately 72 h of continuous molding when the manifold temperature exceeds the recommended upper limit by 10 °C or more.
Barrel profiles are typically run as a reverse or flat profile from hopper to nozzle, with the feed zone held between 160 °C and 175 °C to allow early melting without excessive shear. The compression and metering zones are held between 185 °C and 205 °C. The nozzle is usually set at 195 °C to 210 °C. A free-flow nozzle with a reverse taper or hot-tip nozzle is preferred; small-diameter tips below 2 mm can generate locally high shear heating and should be validated with a temperature probe before production. Back pressure above 0.7 MPa is generally unnecessary and may accelerate additive degradation; lower back pressure with higher screw recovery speed is preferable if melt homogeneity is maintained.
The mold temperature range influences both surface gloss and post-mold dimensional change. At 20 °C to 40 °C, parts are largely amorphous and show lower shrinkage but reduced heat resistance. If higher heat deflection is required, annealing at 80 °C to 100 °C for 30 min to 60 min can increase crystallinity, but dimensional shrinkage of 0.3 % to 0.8 % should be anticipated and warpage must be controlled by fixture cooling. Annealing can also reduce impact strength and may alter the distribution of flame-retardant species at the surface; UL classification must be verified on annealed parts if annealing is part of the production specification.
The material is positioned between unfilled PLA and higher-performance flame-retardant engineering resins in two areas: ignitability and heat-deflection stability. Unfilled PLA generally exhibits UL 94 HB or fails vertical burn criteria because it drips and ignites; flame-retardant PLA formulations such as RTP 2099 X 131060 A are designed to suppress dripping and reduce afterflame time. By comparison, flame-retardant polycarbonate/acrylonitrile butadiene styrene grades can maintain higher heat deflection temperature and impact strength, but require higher barrel temperatures, higher tool temperatures, and have a higher density. Flame-retardant PLA processes at lower melt temperatures and can reduce energy input; however, the mechanical property envelope is narrower at temperatures above the PLA glass transition temperature, which is approximately 55 °C to 60 °C.
Flexural modulus and tensile strength of PLA-based flame-retardant compounds are typically higher than those of low-density polyolefin-based flame-retardant compounds, but notched impact strength is lower than that of impact-modified flame-retardant polycarbonate or polyamide grades. Designers should not select this material for load-bearing snaps or hinges without first evaluating stress concentrator behavior at the lowest service temperature. Notched impact testing under ASTM D256-23 or ISO 179-1:2023 should be reported with specimen conditioning at 23 °C/50 % relative humidity and at 0 °C or below if the part is used in cold environments.
Comparative ignition resistance should be assessed at the production wall section rather than only on the standard 1.5 mm or 3.0 mm plaques. Thin sections below 1.0 mm may require higher flame-retardant additive levels, which further reduce flow length and impact strength. The final color masterbatch or color concentrate can shift the burn classification through changes in melt surface and char formation; color-dependent UL verification is therefore required when colors other than the natural or A color state are used.
| Standard or directive | Qualification parameter | Application note |
|---|---|---|
| UL 94 | Vertical burn classification at 1.5 mm or 3.0 mm | Classify on final part thickness after color approval |
| ISO 1133-1:2022 | Melt flow rate at 210 °C/2.16 kg | Lot-to-lot viscosity control |
| ASTM D638-14 / ISO 527-2:2012 | Tensile strength, modulus, elongation at break | Room-temperature mechanical baseline |
| ASTM D256-23 / ISO 179-1:2023 | Notched impact strength | Required for snap-fit or impact risk |
| ASTM D648-18 / ISO 75-2:2013 | Heat deflection temperature | Continuous-use screening; annealed and as-molded |
| ASTM D792-20 / ISO 1183-1:2019 | Density | Material shrinkage and shot weight |
| IEC 60112:2020 | Comparative tracking index | Electrical insulation qualification |
| RoHS Directive 2011/65/EU and REACH 1907/2006/EC | Restricted substances | Supplier certification required for production lot |
Flame-retardant additive packages may contain phosphorus, nitrogen, or inorganic synergists. If the package is non-halogenated, the risk of corrosive halogen acid emission during burning is lowered, but the additive loading required to achieve V-0 can increase compound density and reduce elongation at break. The supplier should be required to disclose whether the additive package contains antimony compounds, brominated flame retardants, or other environmentally restricted substances for the intended electrical and electronic end-use. Without that disclosure, the material should not be specified for export markets with strict regulated-substance screening.
Processors should purge the barrel with a low-viscosity polyethylene purge after shutdown; polycarbonate or acetal purge compounds are not recommended because of viscosity mismatch and potential acid-catalyzed degradation at PLA processing temperatures. The screw and non-return valve should be inspected for deposit formation at intervals of 50 h to 100 h during extended production. Hot-runner manifolds with dead spots should be dismantled and cleaned after every material change or color change if plate-out is observed on the nozzle tip or gate insert. The material should not be left stagnant at melt temperature for more than 15 min during production interruptions; if interruption exceeds 30 min, the barrel temperature should be reduced to the idle band specified by the supplier and the next restart must follow the drying protocol described above.