| HS Code | 964961 |
| Density | 1.01 g/cm³ |
| Melt Flow Rate 230 C 2 16 Kg | 4.0 g/10 min |
| Tensile Strength At Break | 50 MPa |
| Elongation At Break | 250 % |
| Flexural Modulus | 1300 MPa |
| Izod Impact Strength Notched 23 C | 110 J/m |
| Heat Deflection Temperature 1 80 Mpa | 45 °C |
| Melting Point | 178 °C |
| Water Absorption 24h | 0.25 % |
| Mold Shrinkage | 0.8 % |
| Rockwell Hardness | R107 |
| Recommended Drying Temperature | 80 °C |
As an accredited Polyram PlusTek RD101 Nylon 12, Injection Molding factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg sealed multiwall paper bags with PE liner, palletized and shrink-wrapped for safe handling and injection molding use. |
| Container Loading (20′ FCL) | One 20-foot FCL loaded with Polyram PlusTek RD101 Nylon 12 injection-molding resin, securely packed in bags and containerized for transport. |
| Shipping | Polyram PlusTek RD101 Nylon 12 is shipped as moisture-sensitive injection-molding pellets in sealed, desiccant-lined bags or drums. Keep containers closed and dry, avoiding direct sunlight, high humidity, and temperatures above 30°C. Standard dry cargo transport is suitable; protect from physical damage and forklift punctures during handling. |
| Storage | Store in a dry, cool, well-ventilated area, away from direct sunlight, heat sources, and oxidizers. Keep the original container tightly sealed to prevent moisture absorption, which can degrade the nylon. Avoid exposure to excessive humidity. Use within recommended shelf life; preferably process material from freshly opened packaging. |
| Shelf Life | Store unopened in cool, dry conditions away from moisture. Typical shelf life is two years from manufacture date. |
| Application geometry | Wall thickness range (mm) | Melt temperature (°C) | Mold temperature (°C) | Residual moisture target (wt%) | Regrind limit (wt%) |
|---|---|---|---|---|---|
| Fuel vapor quick connectors | 1.2–2.5 | 250 ± 5 | 60 ± 5 | ≤0.10 | 10 |
| Air brake valve bodies | 3.0–6.0 | 250–265 | 70–80 | ≤0.08 | 0–10 |
| Cable tie straps | 0.8–1.2 | 270 | 40–50 | ≤0.10 | 15 |
| Thin-wall connector housings | 0.5–1.0 | 265–280 | 80–90 | ≤0.08 | 10 |
| Application | Primary test standard | Conditioning anchor | Acceptance criterion |
|---|---|---|---|
| Fuel vapor quick connectors | SAE J2044-2019 | 23 °C / 50% RH, 24 h | Pressure decay and extraction resistance |
| Air brake valve bodies | ASTM D638-14 | −40 °C after thermal cycling | Tensile pull-out of inserts |
| Cable ties and harness clips | ISO 179-1 | 23 °C, 50% RH | Notched Charpy impact retention |
| Sealed enclosures | IEC 60529 | 85 °C / 85% RH, 1,000 h | IP67 pressure decay |
| Fluid-handling components | ISO 175:2010 | 60 °C, 7 d immersion | Mass and swell change |
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Polyram PlusTek RD101 is a pelletized polyamide 12 (PA12) injection molding grade supplied for thin-wall industrial components, snap-fit clips, pneumatic fittings, cable-management hardware, and housings in which lower moisture uptake than PA6 or PA66 is required. Under ISO 1043-1, the base resin is designated PA12; its aliphatic segment between amide groups is longer than that of shorter-chain polyamides, which reduces amide-group concentration and governs the compound’s response to humid environments, chlorides, dimensional change, and melt processing. The material is intended specifically for injection molding rather than extrusion-grade or powder-bed fusion operations. Product-specific rheological and mechanical data are controlled by the manufacturer’s technical data sheet and certificate of analysis, and test specimens should be prepared according to ISO 294-1 and ISO 294-3 using the gating and plaque geometry stated in the product data block. Generic laboratory compression molding should not be substituted for injection-molded specimen preparation when qualifying lot consistency.
Pre-drying of PA12 feedstock is a threshold control because moisture above the recommended limit can reduce molecular weight through hydrolytic degradation in the barrel. For PA12 injection molding compounds of this class, desiccant-dryer settings commonly include a hopper temperature of 80 °C to 90 °C, a dew point below -30 °C, and residence times of 4 h to 6 h when starting from ambient storage. The target residual moisture is generally below 0.10 %; at relative humidity above 60 % RH, prolonged hopper residence or a nitrogen blanket should be used to prevent re-adsorption. Actual residual moisture should be confirmed by coulometric Karl Fischer titration according to ISO 15512, not inferred from drying time alone.
The barrel temperature profile for PA12 requires a narrower range than PA66 because the melting peak is lower and prolonged exposure to elevated temperatures accelerates thermo-oxidative degradation. Class-typical profiles for 20 mm to 40 mm general-purpose injection screws include a rear zone at 190 °C to 210 °C, a middle zone at 210 °C to 230 °C, a front zone at 230 °C to 250 °C, and a nozzle set at 230 °C to 250 °C. Melt temperature measured with a needle pyrometer should remain below 270 °C and be minimized if hot-runner manifold volume is large. Reverse-taper nozzles and hot-runner valve gates require separate verification because extended residence time in the manifold can generate oxidized fractions that affect cavity filling and surface appearance.
Mold temperature exerts direct control over crystallinity, shrinkage, and low-temperature ductility. A mold temperature of 40 °C to 60 °C is commonly selected for dimensional stability; lower mold temperatures reduce cycle time but can freeze surface layers prematurely and increase post-molding dimensional shift. For thin walls below 1.5 mm, actual cavity pressures at the melt front may exceed 60 MPa, so orifice dimensions and clamp-force calculations must be based on measured viscosity under shear rates in the 102 s−1 to 104 s−1 range, not on low-shear capillary data alone. Screws with an L/D of 18:1 to 22:1 and compression ratios from 2.0:1 to 2.5:1 may be used; a high-shear barrier screw is not required, but check-ring travel should be verified to avoid short-shot drift during screw recovery.
In comparison with PA6 and PA66, the defining property of PA12 is lower equilibrium water absorption under ISO 62 immersion conditions. Class-typical saturation in water at 23 °C is approximately 1.4 % to 1.6 % for PA12, compared with roughly 9.5 % for PA6 and 8.5 % for PA66. Because water uptake influences dimensional change as well as tensile modulus, the selection of PlusTek RD101 over a shorter-chain polyamide is often driven by service environments with high relative humidity or intermittent contact with aqueous coolants. The density of PA12 at 1.01 g/cm³ to 1.02 g/cm³ is also lower than that of PA66 at 1.13 g/cm³ to 1.14 g/cm³; this difference can reduce part mass without altering wall thickness. The melting point of PA12 lies near 175 °C to 180 °C, which reduces energy input during processing but also reduces the continuous service temperature relative to PA66. The material should therefore not be selected solely on chemical resistance if sustained load exposure above 100 °C is required.
Snap-fit and thin-wall designs in outdoor equipment or under-hood service require validation of low-temperature impact and insert retention. For PA12 injection molding compounds, low-temperature behavior is commonly assessed using ISO 179-1/1eA notched Charpy at -40 °C, with specimens cut from plaques prepared under controlled mold-temperature conditions. Because PA12 has a lower continuous use temperature than PA66, load-bearing parts in continuous thermal environments above 100 °C should be evaluated for creep and oxidative aging. The longer aliphatic sequence in PA12 reduces water uptake, but it also limits stiffness and hardness relative to glass-fiber-reinforced PA66 or PBT. The choice of PlusTek RD101 over a reinforced short-chain polyamide is therefore typically governed by the combination of moisture exposure, chloride stress, and low-temperature ductility rather than by tensile strength alone.
Product-specific values for the RD101 formulation are stated in the manufacturer’s technical data sheet and should be used for tooling calculations. The matrix below lists standard methods commonly applied to PA12 injection molding compounds of this class. The absence of a published value in this document is not a product deficiency; it reflects the requirement to work from the batch-specific certificate of analysis.
| Property/Characteristic | Standard designation | Test condition or specimen type |
|---|---|---|
| Density | ISO 1183-1 | Immersion in water at 23 °C after conditioning |
| Melt volume-flow rate | ISO 1133-1 | Condition stated on manufacturer’s data sheet; class-typical PA12 melt tests use 190 °C to 250 °C |
| Tensile modulus, yield stress, elongation | ISO 527-2 | Type 1A injection-molded specimen, 4 mm thickness |
| Flexural modulus and strength | ISO 178 | 80 mm × 10 mm × 4 mm specimen, 2 mm/min test speed |
| Charpy notched impact | ISO 179-1/1eA | Type 1eA notched specimen, edgewise impact |
| Heat deflection temperature | ISO 75-2 | Method A at 1.8 MPa or Method B at 0.45 MPa, flatwise |
| Vicat softening temperature | ISO 306 | Method B50; 50 N loading, 50 °C/h heating rate |
| Water absorption | ISO 62 | Immersion to saturation at 23 °C |
| Mold shrinkage | ISO 294-4 | 60 mm × 60 mm × 2 mm plaque, parallel and normal flow |
| Flammability | UL 94 | Thickness specified on product data sheet |
Published data for this specific RD101 configuration is limited outside the manufacturer’s controlled documentation; design calculations should therefore be updated with the latest batch certificate before mold steel is ordered. The listed test methods establish a common basis for incoming inspection and production validation, but they do not replace application-specific testing under actual service temperatures, chemical contact, and molded-in strain.
In automotive and industrial fluid-handling components, exposure to zinc chloride, calcium chloride, and road-salt brines can induce environmental stress cracking in PA6 and PA66. The higher amide-group concentration in short-chain polyamides increases sensitivity to polar chloride solutions under molded-in stress. PA12 has a lower amide-group density and is selected for clips, connectors, cable ducts, and housings in wheel arches, engine bay channels, and de-icing service areas. Immersion screening is commonly conducted according to ASTM D543 or ISO 22088-3 for environmental stress cracking resistance, with testing performed on injection-molded plaques rather than machined coupons. Published data for the RD101 formulation under all chloride brine concentrations is limited; component validation should therefore include exposure to the actual service concentration at the upper operating temperature and at the expected molded-in strain level.
Tooling for PlusTek RD101 should account for the relatively low melt peak and potential for nozzle freeze-off when cold sprue bushings are used. A heated nozzle tip with a land length of 0.5 mm to 1.0 mm can prevent solidification during mold-open pauses. Gate design must avoid excessive shear heating; small pin gates below 0.8 mm may generate localized melt temperatures above the degradation threshold in fast-fill cycles. Post-molding performance of PA12 depends on moisture conditioning. For ISO 1110 accelerated conditioning or storage at 23 °C and 50 % RH, dimensions and tensile properties migrate until equilibrium uptake is reached. Close-tolerance parts should therefore be dimensionally checked after conditioning rather than immediately after ejection. The compound should not be purged with halogenated flame-retardant grades or with acetal in the same barrel without thorough cleaning, because incompatible residues can produce acidic byproducts at processing temperatures. If the granulate has been exposed to relative humidity above 60 % RH for more than 8 h, drying should be repeated before processing. Processors observing silver streaking, black specks, or viscosity shifts should verify barrel residence time, nozzle thermocouple accuracy, and hopper dew point before altering mold geometry. Melt cushion position should also be recorded continuously; a stroke variation of more than 1.0 mm may indicate check-ring wear or inconsistent plastication rather than a formulation defect.