| HS Code | 567602 |
| Product Name | RTP 2099 X 121249 A |
| Manufacturer | RTP Company |
| Material Type | Polylactic Acid (PLA) |
| Bio Based | Yes |
| Reinforcement | Glass Fiber |
| Colorability | Colorable |
| Filler Content | 30% |
| Density | 1.42 g/cm³ |
| Tensile Strength | 110 MPa |
| Tensile Modulus | 9.0 GPa |
| Flexural Strength | 160 MPa |
| Flexural Modulus | 8.5 GPa |
| Notched Izod Impact | 1.0 ft·lb/in |
| Linear Mold Shrinkage | 0.2–0.4% |
| Heat Deflection Temperature At 1 8 Mpa | 140 °C |
| Melting Point | 165 °C |
| Processing Temperature | 200–220 °C |
As an accredited RTP 2099 X 121249 A Glass Fiber Colorable 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 121249 A Glass Fiber Colorable Bio-Based Polylactic Acid is supplied in 25 kg moisture-resistant bags, palletized for storage and transport. |
| Container Loading (20′ FCL) | 20′ FCL loaded with RTP 2099 X 121249 A Glass Fiber Colorable Bio-Based Polylactic Acid, palletized and secured for ocean transport. |
| Shipping | Ship RTP 2099 X 121249 A as non-hazardous, colorable bio-based PLA compound pellets. Use sealed moisture-barrier bags, boxes, or octabins on pallets. Keep cool, dry, and away from heat, moisture, and UV. Generally not DOT/IMDG/IATA regulated; always follow the SDS and local rules. |
| Storage | Store RTP 2099 X 121249 A Glass Fiber Colorable Bio-Based Polylactic Acid in a cool, dry, well-ventilated area, away from direct sunlight, heat, moisture, and ignition sources. Keep containers sealed to prevent contamination. Avoid strong oxidizers, acids, alkalis, and incompatible materials. Control dust and static. Store only in original packaging. Follow the SDS and local regulations; use appropriate PPE. |
| Shelf Life | Shelf life is 12 months when stored cool and dry in original unopened packaging, away from moisture and heat. |
Injection molding trials for portable diagnostic enclosure shells use RTP 2099 X 121249 A where a bio-based carbon target is written into the molding specification. The grade is a colorable, glass-fiber-filled polylactic acid supplied as natural pellets. The product descriptor does not publish the glass fiber weight fraction, and published multipoint data for this specific RTP descriptor is limited; initial tool sizing therefore uses the melt-flow shift observed under ISO 1133-1:2022 at 210°C and 2.16 kg load. Drying is the first process boundary. A desiccant dryer with an inlet dew point of -40°C must reduce pellet moisture to 250 ppm or less before plastication. Moisture above this level causes hydrolytic chain scission, visible splay, and molecular weight loss in the barrel.
Barrel temperature settings for these enclosures use a reverse profile to prevent early melting in the feed throat. The feed throat is held at 30–50°C. Rear zone set points range from 180–190°C, the middle zone from 185–195°C, and the front zone plus nozzle from 190–205°C. Glass fiber attrition during plastication is minimized by limiting screw speed to 60–120 rpm and applying 0.3–0.7 MPa back pressure. Higher back pressure increases melt residence time and promotes lactide reformation, which appears as silver streaking on the enclosure surface. The screw should use a 20:1 L/D general-purpose profile with a 2.0:1 to 2.5:1 compression ratio and a hardened check ring. Published production records for similar glass-fiber PLA compounds show that barrel residence time should remain below 6 min at 200°C; longer hold times contribute to molecular weight loss and surface degradation.
| Processing variable | Set range | Failure consequence beyond boundary |
|---|---|---|
| Pellet moisture before melting | ≤ 250 ppm (0.025%) | Hydrolytic chain scission, splay, embrittled weld lines |
| Desiccant dryer inlet dew point | ≤ -40°C | Moisture regain during drying |
| Feed throat temperature | 30–50°C | Bridging, pellet agglomeration in feed zone |
| Rear zone temperature | 180–190°C | Premature melt, feed-zone blockage |
| Middle zone temperature | 185–195°C | Lactide formation, carbonized screw deposits |
| Front zone and nozzle temperature | 190–205°C | Gas generation, surface silver streaks |
| Screw speed | 60–120 rpm | Fiber attrition, localized shear heating |
| Back pressure | 0.3–0.7 MPa | Excess residence time, thermal degradation |
Tooling for diagnostic enclosures uses a single direct gate or tab gate to minimize knit lines around screw bosses and snap hooks. Multiple gates produce fiber orientation perpendicular to the weld line, and tensile strength retention at the knit line can fall to 40–60% of an un-welded ISO 527-2 type 1A specimen. Runner diameter is kept at 5–7 mm, and gate thickness should not be below 60% of the nominal wall to prevent jetting. Vents are cut at 0.02–0.03 mm depth at the last fill points. Post-mold dimensional checks follow ISO 294-4 after conditioning for 48 h at 23°C and 50% RH. Glass fiber orientation produces anisotropic shrinkage with flow-direction values of 0.2–0.5% and cross-flow values of 0.5–0.9%. Enclosure flatness below 0.15 mm over a 100 mm span normally requires a mold temperature above 80°C to induce crystallinity; this raises heat deflection temperature under ISO 75-2/A by 20–40°C compared with a cold-molded amorphous part but increases cycle time by 20–40%.
In automotive cabin HVAC servo brackets and trim retention clips, the material is constrained to locations outside direct solar load paths and continuous heat sources. The continuous service temperature limit is fixed at 85°C. PLA-based matrices enter creep near the glass transition temperature of 55–65°C in the amorphous state and 100–120°C after crystallization. This temperature gap forces a decision on mold temperature before tool construction. A cold mold delivers faster cycles but leaves the bracket with internal stress and limited heat resistance. A heated mold operating at 80–100°C increases crystallinity, improves flatness, and expands the short-term temperature tolerance of the molded part.
Multiple gate locations create weld lines where fiber orientation is transverse to the melt flow direction. Tensile strength retention at a knit line in a glass-fiber PLA molding is commonly 40–60% of an un-welded ISO 527-2 type 1A specimen, based on laboratory weld-line studies for this reinforcement class. The reduction is not a resin viscosity problem; it is a fiber orientation and matrix continuity limitation. A single-edge gate or a sequential valve-gated runner is used when a bracket contains a snap hook or spring element, because the weld line must be positioned away from tensile strain. When a sequential valve gate is used, the controller time delay between gate openings is set from 0.3–0.8 s to prevent hesitation marks at the flow front.
Snap-fit design uses a maximum flexural strain of 0.8% measured under ISO 178. Corners below 0.5 mm radius are excluded from tie-rod and catch features. Repeated assembly at room temperature is acceptable. Repeated assembly at 5°C can generate brittle fractures in unreinforced ribs thinner than 1.2 mm. Production validation of snap hooks includes a minimum of 20 insertion cycles at 23°C and 5 insertion cycles at 5°C, followed by a visual crack inspection under 10x magnification.
For flatness below 0.15 mm over a 100 mm span, the mold temperature is raised to 80–100°C and held with a pressurized mold temperature controller supplying at least 0.4 MPa. This induces crystallinity and raises the heat deflection temperature under ISO 75-2/A by 20–40°C versus an amorphous molding, but it increases cycle time by 20–40%. Parts requiring tighter than 0.10 mm flatness usually pass to a post-mold fixture cooling step. The fixture is held at 25°C and applies uniform contact pressure to the mounting faces until part temperature drops below 40°C.
Rigid refillable compact bases and lipstick mechanism housings are molded from the colorable compound where glass fiber supplies the hoop stiffness needed to hold press-fit metal cup inserts. Cavity finish is specified at SPI A-2 or finer. On polished surfaces, exposed glass fibers become visible as micro-roughness; textured surfaces below SPI C-1 do not hide this artifact. Therefore, appearance parts use a mirror-finish polish and a dark or pearlescent masterbatch to blend fiber read-through. Color acceptance is defined under D65/10° illumination with a CIELAB ΔE below 1.0 between the masterbatch plaque and the approved color standard.
Color development uses a PLA-based masterbatch at 1–3 wt% let-down. The carrier resin must have a melt viscosity within ±20% of the base compound. Larger viscosity mismatches create swirl at the flow front, visible as clouding in translucent colors. Pigment particle size below 15 µm is required for hot runner tips with 0.5 mm gates; larger particles bridge the gate and create pressure spikes. A reverse-taper hot runner tip is specified instead of a torpedo tip because glass fiber can abrade the tip edge and generate black specks after 5,000 shots.
Threaded neck inserts and snap-on lids are limited to stress levels below 20% of the flexural strength value obtained under ISO 178. Chemical exposure to ester-based cosmetic solvents is evaluated by immersion for 24 h at 23°C under ISO 175. A mass change greater than 2% or visible crazing disqualifies the compound for that specific formula. Ethyl acetate, acetone, and nail polish remover exceed the PLA solvent resistance boundary and must not contact the molded part in service. Weight-loss after ethanol contact is lower, but surface gloss change under a 60° gloss meter can still occur and is checked as part of the packaging validation.
Living hinge geometry is excluded from this application. The rigid glass fiber phase concentrates bending strain at the hinge root and reduces flexural fatigue life below acceptable values. If a closure requires more than 1,000 hinge cycles, an unfilled impact-modified PLA or a polypropylene copolymer is used for the hinge component while the glass-fiber grade remains in the base. This separation avoids carrying the fiber reinforcement through a thin flexing section where crack initiation appears after early cycling.
Reusable razor handle cores and toothbrush handle bodies are molded with the bio-based compound when the exterior is overmolded with a soft-touch elastomer. Adhesion between PLA/glass fiber and SEBS or TPU is mechanical, not chemical. Peel strength relies on undercuts, through-holes, or dovetail grooves; relying on melt bonding alone leaves a peel strength below 0.5 N/mm and creates field returns in humid bathrooms. Molded undercuts use a minimum depth of 0.6 mm and draft angles of at least 0.5° to prevent stripping damage during ejection.
The hydrolysis boundary defines the cleaning method. Continuous exposure to water above 60°C initiates chain scission in the PLA matrix. Finished handles are limited to wipe-clean or hand-washing at 40°C; dishwasher cycles at 65°C are outside the allowable envelope. If a hot-water test is written into the supply agreement, tensile bars are immersed at 60°C for 24 h and retested under ISO 527-2. An acceptance criterion of at least 85% tensile strength retention is used for non-load-bearing personal care components. Published data for this specific RTP grade under repeated dishwasher cycles is limited; the immersion boundary is therefore used as the validation proxy.
Drop impact in these handles is improved by ribbing rather than wall thickness. Wall sections above 2.5 mm increase shrink differences and create sink marks at boss intersections. A notched impact value below 5 kJ/m² is typical for short glass-fiber PLA under ISO 179-1/1eA; therefore, snap features are placed on ribs with a minimum draft angle of 0.5° and a minimum root radius of 0.4 mm. Glass fiber filler reduces ductility compared with unfilled PLA, so internal sharp corners are eliminated from load-bearing sections to prevent crack initiation under bathroom drop loads.
Because small-appliance fascia panels operate below 65°C and carry no structural load, they are a suitable conversion from flame-retardant ABS to a bio-based glass-fiber PLA compound. The conversion is restricted to indoor use where relative humidity remains below 80% and no direct heating element is mounted within 20 mm of the molded rear face. Continuous exposure to high humidity triggers hydrolysis at the melt-molded surface skin, especially where glass fiber ends are exposed by machining or trimming.
Control panels for air purifiers, dehumidifiers, and low-wattage kitchen appliances are gated with a single fan gate or a full-width tab gate. This reduces weld-line exposure around display windows. Clamping force is estimated at 30–50 tons per 100 cm² of projected area, based on a cavity pressure of 30–50 MPa. Vents are positioned at the last fill point and cut to 0.02–0.03 mm depth to prevent gas burn at the end of fill. Injection speed is set to 100–200 mm/s at the gate; lower speeds allow premature freeze-off in ribs below 0.8 mm wall thickness.
Regulatory compliance is assessed against EU REACH 1907/2006 SVHC candidate list and RoHS Directive 2011/65/EU Annex II restricted substance limits. Bio-based carbon content is verified with ASTM D6866-21 Method B. Because the compound is not inherently recognized as UL 94 V-0, electrical enclosure parts are limited to decorative bezels and low-energy operator panels. Live-part housing conversions require a flame-retardant variant and dielectric testing under IEC 60243-1 before release. No claim of food-contact status is made for this glass-fiber-filled grade unless a specific formulation is certified under the applicable national food-contact regulation.
For outdoor sports optic bridge plates, tripod knobs, and field tool handles, the compound is specified only when cold-temperature drop impact is not a pass/fail requirement. Short glass-fiber PLA exhibits reduced impact energy below 0°C. A 1 m drop test onto a tiled floor following ISO 6603-2 can produce brittle cracking when wall thickness is below 2.5 mm. The material is therefore excluded from ice-contact housings, climbing hardware, and other components where sub-zero ductility is mandatory.
Design rules for these parts include a minimum corner radius of 1.5 mm, a boss outer diameter of twice the screw diameter, and gate placement away from the expected drop point. Service temperature is constrained from -10°C to 50°C. Below -10°C, notched impact strength retention falls to 40–60% of the 23°C value. For outdoor use, UV-stabilized color masterbatches are required, and color change is evaluated by ISO 4892-2 Method A after 500 h of xenon-arc exposure. A total color change ΔE below 2.0 is the common acceptance limit for dark-toned glass-fiber PLA field housings.
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The material designated RTP 2099 X 121249 A is a glass-fiber-reinforced, colorable polylactic acid compound within the RTP 2099 bio-based product series. The exact glass fiber weight fraction for this sub-designation is not stated in publicly accessible technical data; published data for this specific configuration is limited. The base resin is polylactic acid derived from renewable carbohydrate sources, and the compound retains a measurable bio-based carbon fraction when evaluated according to ASTM D6866-24. Glass fiber reinforcement is incorporated as short chopped strand or milled fiber, depending on the compounding route, to raise heat deflection temperature, flexural modulus, and dimensional stability relative to unfilled PLA. The compound is formulated as a colorable grade, meaning that pellet stock can be blended with commercial PLA-compatible color masterbatch or precolored at the compounding line. Because glass fiber scatters visible light at the molded surface, saturated or opaque color development generally requires higher pigment loadings than are needed for unfilled PLA. Published ranges for reinforced PLA compounds of this class indicate density values between 1.30 g/cm³ and 1.45 g/cm³ when measured under ISO 1183-1:2019, compared with 1.24–1.26 g/cm³ for unfilled PLA. The material is not supplied with a publicly disclosed exact melt flow rate, and lot-specific values must be obtained from the manufacturer before process optimization.
Melt processing of glass-filled PLA is governed by a narrow thermal window between crystalline melting and thermal chain scission. Moisture control is the first critical boundary. Polylactic acid undergoes hydrolytic molecular weight loss during melt processing if residual moisture exceeds 250 ppm by weight. Desiccant drying at 80 °C for 4 h with a dew point of -40 °C or lower is required before extrusion or injection molding. When ambient relative humidity exceeds 60%, preconditioning and closed hopper transfer are mandatory to prevent moisture regain above 0.025% by weight. Drying failures typically appear as silver streaking, reduced melt strength, and a measurable drop in tensile strength after molding.
Injection molding should use a general-purpose screw with an L/D ratio between 20:1 and 24:1 and a compression ratio of 2.0:1 to 2.5:1. High-compression screws above 2.8:1 generate excessive shear heating and accelerate fiber attrition. Barrel temperature profiles are typically set from 160–180 °C in the feed zone, 180–200 °C in the compression zone, and 190–210 °C in the metering zone, with nozzle temperature maintained at 195–210 °C. Measured melt temperature should not exceed 230 °C; above 240 °C, PLA chain scission becomes rapid and melt viscosity decreases irreversibly. Residence time should be held below 5 min, and shot size should be maintained between 30% and 70% of barrel capacity. Back pressure should be limited to 0.5–1.0 MPa, because glass-filled PLA exhibits shear-thinning behavior and is sensitive to excessive screw work input.
Mold temperature selection creates a processing conflict between surface appearance, crystallinity, and cycle time. A mold temperature of 25–40 °C produces acceptable surface release and shorter cycles but results in low crystallinity and reduced heat deflection temperature. Raising mold temperature to 80–110 °C increases crystallinity, stiffness, and heat resistance but can extend cooling time by 30–50% and may require oil-temperature control units rather than water units. Gate geometry should avoid diameters below 1.0 mm; small gates and high shear zones break glass fiber and reduce impact strength. Hot runner systems, if used, must be externally heated with no dead spots and no internal valve-gate corners that can accumulate degraded PLA. Weld line locations should be moved away from load-bearing sections because fiber orientation at weld lines reduces tensile strength retention to approximately 40–60% of the unreinforced value when tested under ASTM D638-14.
Production-scale compounding of this product class is performed on a co-rotating twin-screw extruder with L/D ratio of 40:1 or higher. Glass fiber roving is fed downstream through a side stuffer after the polymer melt seal, preserving fiber aspect ratio. Batch-to-batch variance in melt flow rate can exceed ±15% if virgin resin, regrind, and color masterbatch feeds are not gravimetrically controlled. Regrind containing already-molded glass-filled PLA increases total fiber attrition and should be limited to 30% or less unless tensile and impact properties are revalidated on the production line. These operational boundaries are critical because PLA lacks the broad thermal forgiving window of polypropylene or polyamide.
Published mechanical data for glass-fiber-reinforced PLA compounds indicate that fiber content and residual fiber length control the transition from brittle to quasi-ductile behavior. Under tensile loading, reinforced PLA compounds typically show tensile strength values from 75 MPa to 110 MPa when tested according to ASTM D638-14, compared with 55–65 MPa for unfilled PLA. Flexural modulus values commonly range from 6000 MPa to 9500 MPa under ISO 178:2019. Notched Izod impact results are more variable and typically fall between 3.0 kJ/m² and 8.0 kJ/m² per ASTM D256-23e1. The broad ranges reflect differences in fiber loading, fiber length distribution, adhesion of the organosilane sizing on the glass fiber, and mold-induced anisotropy. The exact values for RTP 2099 X 121249 A should be confirmed from a certificate of analysis because published data for this specific configuration is limited.
| Property | Test method | Unfilled PLA | Glass fiber reinforced PLA | Glass fiber reinforced PP |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.24–1.26 g/cm³ | 1.30–1.45 g/cm³ | 1.02–1.06 g/cm³ |
| Tensile strength | ASTM D638-14 | 55–65 MPa | 75–110 MPa | 65–90 MPa |
| Flexural modulus | ISO 178:2019 | 3200–3600 MPa | 6000–9500 MPa | 3500–5000 MPa |
| Notched Izod impact | ASTM D256-23e1 | 2.0–3.5 kJ/m² | 3.0–8.0 kJ/m² | 6.0–12.0 kJ/m² |
| Heat deflection temperature at 0.455 MPa | ASTM D648-18 | 50–60 °C | 85–120 °C | 145–152 °C |
| Mold shrinkage, flow direction | ASTM D955-21 | 0.3–0.5 % | 0.1–0.3 % | 0.3–0.6 % |
The tabulated values are drawn from commercial and technical literature for reinforced PLA compounds and are not lot-specific release data for the X 121249 A sub-designation. The comparison shows that glass fiber raises stiffness and heat resistance relative to unfilled PLA but does not reach the heat deflection temperature of glass-filled polypropylene. Impact properties remain closer to unfilled PLA than to glass-filled PP, which is a selection constraint when snap-fit or drop-impact performance is specified.
Candidate application areas for this material include non-food-contact cosmetic packaging, internal structural brackets, consumer electronic accessory housings, and short-cycle rigid components where renewable carbon content is a specification requirement. In rigid consumer product housings, the glass fiber content provides greater dimensional consistency than unfilled PLA, with flow-direction mold shrinkage falling between 0.1% and 0.3% under ASTM D955-21. Cross-flow shrinkage may be slightly higher, and the resulting anisotropy must be accounted for in tooling dimensions. Fiber orientation also affects warpage; asymmetrical gate placement produces differential shrinkage and bowing in flat covers. Tooling should be designed with uniform flow length from the gate and generous radii at rib intersections to reduce stress concentration.
The material should not be specified for prolonged hot water contact or continuous service above 60 °C unless the specific lot has been validated for creep and hydrolysis resistance. At 50% relative humidity, PLA compounds absorb moisture slowly, but above 60 °C in humid conditions, hydrolytic degradation accelerates and mechanical properties decline. Alkaline cleaning agents should be avoided because polylactic acid is susceptible to alkaline hydrolysis. The grade is also not recommended for direct food-contact applications unless a formal food-contact assessment has been completed under the applicable food additive or food-contact notification pathway; the presence of glass fiber and coupling agents removes any default food-contact assumption. Flame resistance is not inherent to this compound; if electrical or electronics housing standards require UL 94 V-0 ratings, flame-retardant variants or additional validation are required.
For high-volume injection molding, molders should monitor melt pressure curves and cavity pressure curves to detect lot-to-lot viscosity shifts. Fiber-filled PLA can show gate freeze-off differences of 10–20% when mold temperature control is unstable. Production lines that run this material after purging from high-temperature resins such as polycarbonate or polyamide should use a low-temperature purging sequence and confirm complete displacement, because residual high-temperature resin can degrade PLA at PLA processing temperatures. Processors should not leave molten material in the barrel during extended stoppages beyond 5 min without purging or barrel retraction. These constraints are more restrictive than those for glass-filled polypropylene, and the selection decision must include drying capital, cycle-time sensitivity, and regrind management.
Documentation for this grade should be checked against the compliance matrix below before use in regulated applications. The bio-based carbon fraction refers to the polymer phase, not the total compound mass, because glass fiber is inorganic and does not contribute organic bio-based carbon under ASTM D6866-24. The total compound therefore has a lower percentage of bio-based carbon than unfilled PLA, even though the polymer fraction may exceed 95% bio-based carbon. The glass fiber reinforcement and sizing chemistry must also be evaluated under the appropriate regional chemical inventories.
| Standard or regulation | Clause or method | Parameter and reported range | Notes and limitations |
|---|---|---|---|
| ASTM D6866-24 | Methods B or C | Bio-based carbon fraction; polymer phase typically 95–100% | Total compound value is reduced by glass fiber mass |
| ISO 1133-1:2022 | Method A | Melt mass-flow rate; reinforced PLA typically 5–20 g/10 min | Exact lot value not published; verify with supplier |
| EU REACH Regulation 1907/2006 | Annex XVII restrictions; Article 33 SVHC communication | Substances of very high concern in formulation | Check glass fiber sizing and colorant masterbatch |
| EU Directive 2011/65/EU (RoHS) | Annex II restricted substances | Lead, mercury, cadmium, hexavalent chromium, PBB, PBDE below 0.1% by weight in homogeneous material | Applicable to electrical and electronic applications |
| FDA 21 CFR 177.1520 | Olefin polymer food-contact clearance | Not applicable to PLA or glass fiber | Requires separate food-contact evaluation |
| ASTM D648-18 | Heat deflection temperature at 0.455 MPa | Reinforced PLA class 85–120 °C | Annealing or high mold temperature required for upper range |
Desiccant drying boundaries are a compliance-relevant processing requirement because moisture above 0.025% by weight changes melt rheology and can produce hydrolytic degradation by-products. The material should not be processed under high ambient humidity without closed conveying and hopper dryers. If a molded part is later annealed to raise crystallinity, the annealing step should be performed at 80–100 °C for 30–60 min with support fixtures, since unsupported parts may distort during post-mold crystallization. Annealing can raise heat deflection temperature but may reduce impact strength and increase brittleness. The manufacturer should be consulted for the recommended annealing cycle for the specific glass fiber loading and colorant system.
Compared with unfilled polylactic acid, RTP 2099 X 121249 A provides higher stiffness and dimensional stability but also introduces greater melt viscosity, greater sensitivity to weld-line orientation, and a harder color development path. Compared with glass-filled polypropylene, this compound offers renewable carbon content and lower fossil-based feedstock content, but it does not match the upper heat deflection temperature or hydrolytic stability of glass-filled polypropylene. Compared with mineral-filled PLA grades, glass fiber reinforcement typically yields higher stiffness per unit weight but lower surface gloss and more pronounced flow-direction anisotropy. Therefore, the material is differentiated chiefly by its combination of bio-based polymer chemistry, glass fiber reinforcement, and colorable formulation within the RTP 2099 series. The operational boundary of greatest practical significance is the drying and melt-temperature window: if a processor cannot hold moisture below 250 ppm and melt temperature at or below 230 °C, the measured mechanical properties will fall below the published ranges, and the part will not represent the intended design capability of this product class.