| Код ТН ВЭД | 467685 |
Как аккредитованная фабрика RTP 2099 X 126216 B из стекловолокна с быстрым циклом цветной полимолачной кислоты, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
| Упаковка | RTP 2099 X 126216 B Glass Fiber Fast Cycle Colorable Polylactic Acid supplied in 25 kg sealed moisture-barrier bags, palletized, labeled. |
| Погрузка контейнера (20-футовый контейнер) | 20′ FCL: RTP 2099 X 126216 B Glass Fiber Fast Cycle Colorable Polylactic Acid, palletized, dry, ambient, secured, container loading. |
| Доставка | RTP 2099 X 126216 B Glass Fiber Fast Cycle Colorable Polylactic Acid typically ships as non-hazardous plastic molding pellets. Not DOT/IMDG/IATA regulated; no UN number, class, or packing group. Use sealed, labeled bags, drums, or octabins. Keep dry, cool, and contamination-free. Follow SDS and local transport rules. |
| Хранение | Store RTP 2099 X 126216 B Glass Fiber Fast Cycle Colorable Polylactic Acid in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep containers tightly sealed, preferably in original packaging with desiccant, to prevent hydrolytic degradation. Avoid contact with strong oxidizers. Maintain low humidity and ambient temperatures; rotate stock to ensure first-in, first-out use. |
| Срок годности | Typically 12 months from manufacture when stored unopened in a cool, dry area, protected from moisture, heat, and direct sunlight. |
Electronic enclosure molders evaluating RTP 2099 X 126216 B for e-reader back shells, smart speaker frames, router base plates, and handheld diagnostic device housings should first establish whether the part’s service temperature remains below the deflection threshold of the glass-filled PLA class. Published mechanical data for this exact compound is limited; tensile modulus, flexural modulus, and heat deflection values must be confirmed against the batch certificate and not inferred from general PLA glass-fiber literature. In thin-wall sections of 1.2 mm to 2.0 mm, velocity-controlled filling with a melt temperature of 190 °C to 215 °C and mold temperature of 25 °C to 40 °C is required to avoid gate freeze and downstream warpage caused by glass fiber orientation. Pre-drying is executed at 80 °C for 4 h in a desiccant dryer with a dew point at or below −40 °C, targeting a residual moisture content not exceeding 0.025% (250 ppm) as verified by ISO 15512:2019. Shop-floor formulation adjustment consists of adding 1.5–3.0 wt% PLA-carrier color masterbatch to the natural compound and blending 15–20 wt% clean, dried runner regrind; regrind fractions above 20 wt% correlate with reduced Charpy notched impact and increased gate blush in multi-cavity tools. The processing route is a reciprocating screw injection molding machine with a 20:1 to 22:1 L/D screw, a 2.5:1 compression ratio, and a shut-off nozzle to minimize drool between fast cycles. Cavity pressure should be held at 60–80 MPa during packing, and screw speed is limited to 50–100 rpm to protect glass fiber length; back pressure above 1.0 MPa raises melt temperature variability and is avoided. Compliance for these enclosures falls under RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006; non-flame-retarded PLA compounds of this class typically achieve UL 94 HB, and any V-2/V-0 requirement demands a separately formulated flame-retardant grade. Dimensional stability is checked according to ASTM D648-18 at 0.45 MPa and melt flow rate is verified by ISO 1133-1:2022. Terminal part types include network terminal housings, barcode scanner shells, e-reader back covers, and portable diagnostic device enclosures where peak internal air temperature is below 65 °C.
| Requirement | Standard / Directive | Assessment condition |
|---|---|---|
| Restricted substances | RoHS Directive 2011/65/EU | Supplier declaration per IEC 62321 |
| SVHC screening | REACH Regulation (EC) No 1907/2006 | Article 33 obligation |
| Flammability | UL 94 HB | Thickness 1.5 mm |
| Tensile properties | ASTM D638-14 | Type I specimen, 5 mm/min |
| Melt flow rate | ISO 1133-1:2022 | 210 °C, 2.16 kg |
| Heat deflection | ASTM D648-18 | 0.45 MPa |
Closure components and outer shells for cosmetic jars, compact cases, lipstick mechanisms, and deodorant stick barrels present a dual risk: cyclic thread loads and contact with esters, terpenes, aldehydes, and high-HLB surfactants present in fragrance oils and skin-care emulsions. RTP 2099 X 126216 B is not classified as a food-contact grade; any packaging claim under Regulation (EU) No 10/2011 requires migration testing on the finished article. For cosmetic packaging, formulators typically dilute the compound with 0.8–2.0 wt% PLA-carrier color masterbatch and hold clean regrind at or below 15 wt% because higher regrind fractions reduce gate-area gloss and enlarge the visible knit line on polished A-2 or A-3 mold surfaces. The production process uses cold-runner injection molds with vent depths of 0.01–0.02 mm and mold temperatures of 25–35 °C; fast-cycle settings reduce cycle time to 18–25 s for a 2.0 mm wall, but molding below 18 s is not advised because the central core remains above the glass transition and induces undercut distortion during ejection. Thread designs with marginal thread depth or unsupported lip geometry should be subjected to ASTM D638-14 tensile testing and ISO 178:2019 flexural testing before tool release. Resistance to cosmetic ingredients is evaluated by ISO 175:2010 immersion in ethanol/water and squalene, and stress cracking is assessed visually under polarized light after 72 h exposure. Terminal product types include jar closures, compact hinges, lipstick outer bodies, and deodorant stick barrels with mechanical snap features; packaging with continuous essential-oil contact may require an internal barrier liner or a different polymer class if mass loss exceeds 0.5% or visible crazing appears.
Room-temperature household appliance trim parts such as air purifier side panels, dehumidifier fascia frames, vacuum cleaner filter housings, and fan base covers are evaluated against the mechanical and thermal requirements of unattended use. The processing route is a hot-runner multi-cavity system with sequential valve gating; melt temperature is held at 195–215 °C, hot runner manifold temperature at 200–215 °C, and mold temperature at 25–40 °C. Fast cycle execution with a wall section of 2.5 mm runs on a 20–25 s cycle; cooling time below 12 s produces warpage at planar sealing surfaces. The compound is dried to 250 ppm maximum residual moisture per ISO 15512:2019 before processing; any regrind is limited to 15 wt% and must be dried under the same profile for 4 h at 80 °C. Color is introduced with 1.0–3.0 wt% PLA-carrier masterbatch or 0.5–1.5 wt% liquid color at the throat, but liquid color addition below 0.5 wt% results in visible swirl in high-gloss panels. Compliance is anchored to IEC 60335-1:2020 clause 30.2.3 for resistance to heat and fire; unmodified glass-filled PLA is not suitable for parts requiring 850 °C glow-wire flammability index without the addition of a flame-retardant package. UL 94 HB at 1.5 mm is the expected classification for the non-flame-retardant base compound, and any V-0 requirement must be confirmed on the specified color and wall thickness. Terminal parts include room-temperature appliance facias, filter housings, fan base covers, and low-load brackets that are not exposed to continuous service above 65 °C.
Glass-filled PLA carrier structures are limited to automotive interior components with continuous service temperatures below 65 °C and short excursions not exceeding 80 °C; parts above this boundary should be reassigned to ABS/PC or high-heat PLA/PA blends. Examples include HVAC louver vanes, seat side trim covers, cable guides, and console side panels. The injection molding process uses a reciprocating screw machine with a 22:1 L/D screw, 2.2:1 to 2.5:1 compression ratio, and mold temperature of 25–35 °C for rapid skin formation. Fast cycle time for a 2.0 mm wall is 20–28 s depending on gate size; valve-gated hot runners are preferred for balanced fill. Formulation at processing consists of 2 wt% black or neutral PLA masterbatch and 10–15 wt% clean regrind; regrind above 15 wt% decreases impact strength and raises volatile organic compound emissions. Flammability is tested per ISO 3795:1989 / FMVSS 302 with a burning rate not exceeding 100 mm/min, but several OEM specifications demand self-extinguishing behavior or 0 mm/min; the base non-flame-retarded PLA compound may require a flame-retardant variant to meet that criterion. Volatile emissions are screened with VDA 277:2018 with a total carbon emission ceiling often set at 50 µg C/g by OEM material specifications; low-gloss grained surfaces reduce visible scratches. Terminal product types include HVAC louver vanes, seat side trim, cable guides, and console side panels where grain-matched appearance and low load cycling are primary requirements.
For reusable office and home storage products such as desk organizers, pen trays, modular shelf bins, and drawer dividers, the critical failure mode is snap-latch fatigue at the hinge root, not peak mechanical strength. Molding trials on production-scale equipment show that glass fiber orientation in thin hinge sections is controlled by gate placement; edge gates placed along the flow axis reduce root stress concentrations compared with tab gates placed perpendicular to the hinge. The material is pre-dried at 80 °C for 4 h; mold temperature is held at 25–35 °C and melt temperature at 190–210 °C. Injection speed is profiled with an initial 30–50 mm/s through the hinge section and increased to 80–120 mm/s in the base area to avoid jetting. Color is added with 1.5–3.0 wt% PLA-carrier masterbatch; regrind is limited to 20 wt% for opaque colors and 10 wt% for translucent tint applications to minimize black specks and flow-line variation. Compliance for these articles follows REACH Regulation (EC) No 1907/2006 and, when marketed to children, EN 71-3:2019 migration of certain elements; child-use articles additionally require a small-parts assessment, and the glass-fiber surface must be encapsulated because protruding fibers are an exposure hazard. Dimensional checks use ASTM D648-18 for heat deflection and ISO 178:2019 for flexural modulus. Terminal products are modular storage bins, desk organizers, pen trays, and drawer dividers for room-temperature indoor use only; exposure to repeated alkaline cleaning solutions above pH 9 is not recommended unless compatibility testing per ISO 175:2010 is completed.
Laboratory enclosures such as pipette controller bodies, benchtop instrument front panels, centrifuge outer covers, and point-of-care diagnostic reader housings impose low outgassing and surface contamination constraints. RTP 2099 X 126216 B is selected where bio-based carbon content measured by ISO 16620-2:2019 is a specification requirement and where the service temperature remains below 65 °C. Processing is completed on a vertical or horizontal injection molding machine with a 20:1 L/D screw; mold temperatures of 25–35 °C are used to shorten cycle time, but fast cycle molding below 20 s for a 2.5 mm wall increases the risk of sink marks over bosses and ribs. The formulation addition on the floor consists of 1–2 wt% antistatic additive masterbatch when surface resistivity below 1012 Ω/sq is specified, plus 0.8–2.0 wt% color masterbatch; regrind is restricted to 10–15 wt% because antistatic package performance decays with multiple heat histories. Surface contamination is verified with total organic carbon or gravimetric methods; outgassing requirements are not covered by a single ISO enclosure standard and must be agreed with the end user. Compliance for electrical safety in laboratory equipment follows IEC 61010-1:2010/AMD1:2016, and restricted substances are controlled under RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006. Terminal product types include pipette controller housings, benchtop instrument front panels, centrifuge outer covers, and point-of-care reader enclosures where no direct patient fluid contact occurs.
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RTP 2099 X 126216 B is a glass-fiber-reinforced, fast-cycle, colorable polylactic acid compound within the RTP 2099 bio-based polyester series. The base resin is a semicrystalline poly(L-lactic acid) in which the D-isomer content is controlled to influence crystallization rate. The suffix X 126216 B identifies a custom formulation; the exact glass-fiber loading is not stated in open product literature and must be obtained from the supplier’s certificate of analysis. Published data for comparable short-glass PLA compounds place tensile modulus between 7 GPa and 12 GPa and flexural modulus between 6 GPa and 10 GPa when measured according to ISO 527-1:2019 and ISO 178:2019. Neat PLA typically exhibits tensile modulus of 3.0–3.8 GPa. The product is intended for injection molding applications in which renewable carbon content, reduced overall cycle time, and post-mold color matching are specified together. The presence of glass fiber eliminates the translucency of neat PLA and introduces anisotropic mold shrinkage, so gate location and fiber orientation must be considered before tool fabrication. The grade is supplied as pellet feedstock for standard reciprocating-screw molding machines and is not recommended for extrusion film or blow molding without separate validation because fiber orientation in those processes differs significantly from injection molding.
Fast-cycle behavior in this grade is not derived solely from the glass fiber. The formulation is designed with a controlled molecular weight distribution and nucleating package so that solidification occurs at shorter holding times without a proportional increase in molded-in stress. On a 120-ton hydraulic injection molding machine with a 30 mm screw, cycle-time reductions of 10–30% relative to an unmodified PLA of equivalent fiber loading have been reported in thin-wall tools with wall stock of 1.5–2.5 mm. The specific reduction for RTP 2099 X 126216 B must be confirmed on the target tool because gate size, cooling circuit design, and part ejection temperature dominate cycle time. The colorable designation means the base pellet is not pre-colored with carbon black or titanium dioxide. Color concentrates with a PLA carrier are preferred because non-PLA carriers can create interfacial defects around glass fibers. General-purpose glass-filled PLA often sacrifices cycle time for impact modification or heat resistance, while pre-colored grades cannot be used for broad color matching. The X 126216 B suffix therefore indicates a balance between process speed and post-mold color control rather than a simple increase in filler content.
Table 1. Representative literature ranges for short-glass PLA compounds compared with unreinforced PLA. Values are compiled from peer-reviewed and supplier technical literature; they do not constitute certified test results for RTP 2099 X 126216 B.
| Property | Test method | Neat PLA | PLA + 20 wt% short glass | PLA + 30 wt% short glass |
|---|---|---|---|---|
| Tensile modulus | ISO 527-1:2019 / ISO 527-2:2012 | 3.0–3.8 GPa | 6.5–9.0 GPa | 8.0–12.0 GPa |
| Tensile strength | ISO 527-2:2012 | 50–65 MPa | 70–100 MPa | 85–120 MPa |
| Flexural modulus | ISO 178:2019 | 3.5–4.5 GPa | 5.5–8.0 GPa | 7.5–11.0 GPa |
| Heat deflection temperature, 0.45 MPa | ISO 75-2:2013 | 55–65 °C | 90–140 °C | 140–160 °C |
Pre-drying is a boundary condition for all PLA compounds. Hydrolytic chain scission begins when moisture in the melt exceeds 0.025 wt% (250 ppm). Desiccant dryers with a dew point of -40 °C or lower and a drying temperature of 80 °C for 4 hours are typical for glass-filled PLA. Over-drying above 100 °C can anneal pellets and produce screw feeding instability. In production-scale trials, splay and weld-line strength loss are observed when the material is conveyed in open bins at ambient relative humidity above 60% for more than 1 hour. The material should be transferred directly from dryer to press hopper, and hopper residence time should not exceed 30 minutes under high-humidity conditions unless a dry-air blanket is maintained. Batch-to-batch moisture variation is a common failure mode on fast-cycle tools because moisture reduces melt viscosity and changes gate freeze time.
Glass fiber reinforcement increases heat deflection temperature by raising compound stiffness, but the PLA matrix itself can remain largely amorphous if the mold surface temperature is below the crystallization rate maximum. For this reason, a fast-cycle grade processed with mold temperatures of 20–35 °C may exhibit an HDT B below 70 °C, whereas the same material molded at 90–110 °C with longer cooling time can develop sufficient matrix crystallinity to exceed 140 °C under ASTM D648-18 or ISO 75-2:2013. This trade-off is critical: the fast-cycle designation applies to conditions where cycle time reduction is prioritized, and the heat resistance gain from glass fiber is primarily stiffness-related rather than crystallinity-related. For thin-wall parts, mold designers should specify cooling channel diameters and spacing to achieve a surface temperature variation of no more than ±5 °C. Wider variations produce differential shrinkage and anisotropic warpage in glass-fiber PLA. Published data for this specific configuration at high mold temperatures is limited; trials on a tool with conformal cooling are recommended before establishing production tolerances. Fast cycle processing is therefore not inherently low-temperature processing when high HDT is required.
Glass fiber length after plastication is a direct predictor of tensile modulus and impact resistance. In a general-purpose screw with a compression ratio of 2.5:1–3.0:1, fiber length can degrade to below 0.1 mm before the melt reaches the nozzle, reducing tensile modulus by up to 20% compared with a low-compression screw. For glass-filled PLA, a compression ratio of 1.8:1–2.2:1 and a check ring with a clearance of 2.5–3.0 mm are preferred. Shot volume should occupy 50–75% of machine barrel capacity to limit residence time. Residence time above 8 minutes at melt temperatures above 210 °C initiates thermal degradation of PLA, visible as brown streaking and increased melt flow index. The same degradation mechanism reduces fiber-matrix coupling because the sizing on the glass fiber is thermally stressed. A back pressure of 0.5–1.0 MPa is usually sufficient for color distribution and melt homogeneity; higher back pressure accelerates fiber breakage without improving dispersion. During compounding on a co-rotating twin-screw extruder with an L/D ratio of 40:1–48:1, glass fiber is typically introduced downstream at zone 6–8 of a 12-barrel configuration to preserve fiber length distributions with a mean length of 0.25–0.40 mm. Fiber attrition between compounding and molding should be monitored by ashing and optical microscopy, not by melt index alone.
Although the grade is colorable, not every pigment chemistry or masterbatch carrier is compatible. PLA is sensitive to moisture, acid, and residual monomer. Colorants with zinc-based or calcium-based carriers can catalyze hydrolytic degradation at processing temperatures. Pigment dispersions with a PLA carrier are specified for best fiber wetting and color uniformity. The recommended masterbatch let-down ratio is 2–4 wt% for standard colors; higher loadings can alter mold shrinkage by 0.05–0.15% and reduce tensile strength because particulate pigments act as stress concentrators, particularly at glass fiber ends. Liquid colorants above 0.5 wt% can plasticize the matrix and delay solidification, negating the fast-cycle advantage. Producers should verify that pigments have thermal stability at 220 °C for at least 5 minutes and do not contain amines or metallic stearates that affect the PLA ester linkage. Published data for this specific product color space is limited; color-matching trials should be performed on the target mold geometry because color perception is influenced by fiber orientation and surface finish. The same base resin may accept differently colored masterbatches, but the cooling rate and fiber orientation of each tool must be fixed before color match approval.
Relative to unreinforced PLA, RTP 2099 X 126216 B carries higher tensile and flexural modulus and reduced mold shrinkage, but lower elongation at break and notched impact strength remain expected limitations. Unreinforced PLA is preferred where transparency or deep-draw flow length is required. Impact-modified PLA grades use elastomeric modifiers to raise notched Izod values, but those modifiers lower heat deflection temperature and tensile strength compared with glass fiber. Mineral-filled PLA grades increase stiffness and reduce cost, but their density is higher and their tensile strength falls below glass-filled grades at equal filler weight. Compared with a standard glass-filled PLA, the fast-cycle designation indicates a narrower processing window for maximum cooling speed; mold temperatures above 100 °C are not needed for dimensional stability in thin sections, but such temperatures are required if crystalline HDT is targeted. The colorable designation distinguishes this product from pre-colored black glass-fiber grades, which may contain carbon black and cannot be matched to light or custom colors. Fiber orientation, weld-line location, and gate-induced anisotropy are shared across all glass-filled PLA compounds and are not eliminated by the colorable or fast-cycle formulation.
Typical downstream operations include high-volume consumer, cosmetic, and packaging components with wall thicknesses from 1.5 mm to 3.0 mm. The glass fiber level should be confirmed before tool cutting because lateral shrinkage can range from 0.2% to 0.5% in the glass orientation direction and up to 1.0% transverse, depending on gate geometry and fiber length retention. Mold-filling simulation with a fiber orientation solver is recommended to predict warpage. In operation, the compound is processed at melt temperatures of 190–215 °C, mold temperatures of 20–35 °C for fast cycles, injection speeds that maintain a melt front velocity above 100 mm/s to prevent hesitation lines, and a cushion of 3–5 mm to ensure consistent holding pressure. Hot runner systems are possible; open hot runner gates should be at least 1.5 mm in diameter because glass-filled PLA solidifies quickly in the gate. Repeated startup stops beyond 15 minutes require purging with a melt-stable PLA or lowering barrel temperatures to 160 °C to avoid hydrolytic degradation in the barrel.