| HS Code | 488500 |
| Material | Polyram PlusTek RD302G6 Nylon 12, 30% Glass Fiber |
| Glass Fiber Content | 30% |
| Density | 1.23 g/cm³ |
| Tensile Strength | 150 MPa |
| Tensile Modulus | 11000 MPa |
| Elongation At Break | 3.5% |
| Flexural Strength | 200 MPa |
| Flexural Modulus | 10000 MPa |
| Izod Impact Notched | 11 kJ/m² |
| Heat Deflection Temperature 1 8 Mpa | 165 °C |
| Melting Point | 178 °C |
| Water Absorption 24h | 0.7% |
| Mold Shrinkage | 0.3% |
As an accredited Polyram PlusTek RD302G6 Nylon 12, 30% Glass Fiber factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg moisture-resistant polyethylene-lined bags, sealed to protect Polyram PlusTek RD302G6 Nylon 12, 30% Glass Fiber from contamination. |
| Container Loading (20′ FCL) | 20′ FCL loaded with Polyram PlusTek RD302G6 Nylon 12 (30% glass fiber) in sealed bags on pallets, securely stowed and ventilated. |
| Shipping | Ship as non-hazardous plastic granules in sealed, moisture-proof bags or drums. Keep dry, avoid direct sunlight and excessive heat. Use covered transport to prevent contamination. No special dangerous-goods classification required. Label as “Nylon 12, 30% Glass Fiber” with lot number and handling instructions. |
| Storage | Store in a cool, dry area away from direct sunlight and heat sources. Keep the original sealed container to prevent moisture absorption, as nylon 12 is hygroscopic. Ideal temperature: below 30°C (86°F). Use desiccants if necessary. Ensure good ventilation and protect from physical damage. Follow manufacturer guidelines for shelf life and handling. |
| Shelf Life | Shelf life is typically 2 years from manufacturing date when stored in original, unopened packaging under dry, cool conditions. |
Before any downstream application, Polyram PlusTek RD302G6 Nylon 12, 30% Glass Fiber is dried to a residual moisture content below 0.10 wt% in a desiccant dryer with a dew point not higher than -30°C for 4 h at 80°C. Moisture above 0.15 wt% at melt temperature causes hydrolysis at the polyamide 12 amide linkage, visible as silver streaks on moulded surfaces and a drop in melt viscosity of 15–25% when checked against dried baseline under 2.16 kg load per ISO 1133-1:2022. A general-purpose three-zone screw with L/D 20:1–24:1 and compression ratio 2.0:1–2.5:1 is specified on production injection machines, with back pressure held at 0.5–1.5 MPa to limit glass-fibre attrition. Barrel set points from feed to nozzle are 230–260°C, the nozzle is kept below 265°C to suppress surface oxidation, and mould temperature is maintained between 60°C and 100°C; for parts with knit lines, the lower end of this range is avoided because reduced interflow-layer entanglement lowers weld-line strength. These handling boundaries govern every downstream conversion operation described in the application scenarios that follow.
Fuel-line quick connectors for gasoline and diesel passenger cars are moulded from RD302G6 in profiles corresponding to SAE J2044, with nominal flow diameters of 8 mm, 10 mm, and 12 mm. The 30 wt% glass-fibre loading is selected because the polyamide 12 matrix maintains low equilibrium water absorption of 0.7–1.0 wt% after immersion per ISO 62:2008, limiting dimensional movement in humid under-hood environments, while the reinforcement raises dry-as-moulded tensile modulus into the range of 6,500–8,500 MPa measured under ISO 527-2:2012 on type 1A specimens at 23°C. On a 1,200 kN hydraulic injection moulding cell with a 40 mm screw, an eight-cavity quick-connector tool is run at melt temperature 250–260°C, mould temperature 80–90°C, and holding pressure 60–80 MPa. The dominant process conflict is weld-line placement behind the locking tabs: a single side gate forces a knit line at the retaining lip with tensile strength of only 55–65 MPa, while two valve gates relocated to opposing body extremities move the knit line into a non-load-bearing wall section and raise weld-line tensile strength to 70–85 MPa, equivalent to 70–80% of the non-weld tensile value. Mould temperature below 80°C further reduces interflow-layer entanglement and produces a 10–15% loss in burst pressure after 1,000 h at 125°C thermal aging assessed under ISO 16750-4. Continuous exposure to sour gasoline at 60°C for 500 h produces mass change below 2.5% when tested per ISO 175:2010, but published data for RD302G6 in methanol-containing fuel blends above 20 vol% are limited; methanol at high concentration can plasticize the PA12 matrix and reduce tensile modulus by 15–25%, so such blends require part-specific extraction and dimension checks before homologation.
| Condition | Tensile strength at break | Tensile modulus | Elongation at break | Test method |
|---|---|---|---|---|
| Dry-as-moulded, 23°C | 120–140 MPa | 7,000–8,500 MPa | 3.0–4.5% | ISO 527-2:2012 |
| Conditioned, 50% RH, 23°C | 85–105 MPa | 4,800–6,200 MPa | 5.0–7.0% | ISO 1110:2019 |
The values above are representative class data for a 30 wt% glass-fibre-reinforced PA12 compound; published grade-specific data for RD302G6 are limited, and lot-specific certificate-of-analysis values take precedence. Terminal quick-connector parts are checked for dimensional stability after conditioning, with shrinkage measured per ISO 294-4:2018; typical flow-direction shrinkage is 0.25–0.55% and cross-flow shrinkage is 0.55–0.85%. Amine-based processing aids are avoided in this application because residual amines can accelerate post-crystallisation and raise shrinkage variance during fuel exposure.
Pneumatic fitting bodies for compressed-air brake systems are injection moulded with threaded ports from M5 to G1/2 and qualified as push-in connectors under ISO 14743:2020. In a production-scale trial using a 900 kN all-electric moulding cell and a 30 mm screw at 240–255°C, the limiting failure mode after 1,000 h at 125°C was not tensile rupture of the body but microcrack initiation at the root of the first load-bearing thread, where local hoop stress under 1.6 MPa cyclic pressure exceeds 45 MPa. The 30 wt% glass-fibre reinforcement reduces linear thermal expansion to 3.0–5.0×10⁻⁵ K⁻¹ in flow direction and 5.0–7.0×10⁻⁵ K⁻¹ cross-flow, but the anisotropy produces thread ovality of 0.03–0.08 mm on moulded threads unless a 0.2 mm collapse allowance is designed into the core pin. Mould temperature is held at 90°C to promote post-fill crystallinity near the thread surface; reducing it to 70°C increases thread shrinkage variation by 0.10–0.20% and lowers burst pressure from 5.0 MPa to 4.2 MPa after 1,000 h at 125°C. Pressure cycling at 0–1.6 MPa and 2 Hz for 10⁶ cycles creates fatigue cracks at knit lines when the gate is placed at thread runout; moving the gate to the central hex face increases minimum burst pressure after cycling by 12%. The compound is not specified with zinc chloride-containing thread sealants because zinc chloride at residual levels can depolymerise PA12 above 120°C. Terminal parts for truck air brake systems are additionally checked against ISO 7628-1:2010 for tubing compatibility, not as tubing itself.
Cooling-line unions in battery electric vehicles are moulded from RD302G6 where glycol-water coolant at 50:50 ratio and 90°C is sealed by radial O-rings on quick-connect spigots. The part is exposed to 1.5 bar system pressure with cold-start excursions to -40°C, and thermal cycling is performed under ISO 16750-4 from -40°C to 105°C for 1,000 cycles. In this environment the polyamide 12 matrix absorbs 0.3–0.5 wt% coolant at equilibrium, lower than PA66, giving a dimensional change of 0.10–0.25% across the sealing diameter. The glass-fibre content prevents creep collapse of the spigot under constant O-ring compression of 15–25%; however, a gate placed at the spigot end produces longitudinal fibre alignment and reduces hoop strength at the O-ring groove by 10–15%, so tool trials use a diaphragm gate at the flange centre to orient fibres circularly around the groove. Mould temperature of 85–95°C is required to achieve skin crystallinity of 25–35% by differential scanning calorimetry; lower mould temperatures leave an amorphous skin that post-crystallises during coolant aging and opens the groove diameter by 0.05–0.12 mm. The union body is not post-annealed above 120°C because oven ageing can oxidise the glass-fibre sizing and reduce weld strength at the spigot-to-flange transition.
Subsea umbilical clamp bodies and hydraulic coupling supports are injection moulded from the same 30 wt% glass-fibre PA12 grade, then qualified as non-metallic load-bearing components under NORSOK M-710:2014 for rapid gas decompression and ISO 23936-2:2011 for sour-fluid aging. In a decompression sequence from 15 MPa methane/carbon dioxide at 100°C to atmospheric pressure in 1 min, the acceptance criterion is no internal cracking deeper than 0.5 mm after 10 cycles. The controlling processing variable is final through-thickness crystallinity: parts moulded at 80°C with 30 s holding time show crystallinity of 30–35% and pass the RGD sequence, while parts cooled rapidly to 50°C show core crystallinity below 20% and develop microvoids at the fibre-matrix interface under explosive decompression. Because glass fibres create wicking paths, the gate and weld line are located away from sealing faces; a tab gate at the body centre with a 0.8–1.0 mm radius transition is used to avoid notch stress at the gate scar. The material is not specified for continuous exposure to more than 5 vol% hydrogen sulfide at temperatures above 100°C without crack-growth validation, because acid hydrolysis can attack the glass-fibre interface. A 50 mm screw with accumulator is used on a production machine; filling time below 0.8 s is avoided because shear heating at glass-fibre tips raises local melt temperature above 280°C, causing matrix discoloration and a 10% loss in notched Charpy impact strength measured per ISO 179-1:2020.
| Requirement | Document/standard | Verification condition |
|---|---|---|
| Rapid gas decompression | NORSOK M-710:2014 | 15 MPa, 100°C, 10 cycles |
| Sour fluid aging | ISO 23936-2:2011 | 100°C, 5 vol% H₂S, 168 h |
| Tensile strength retention | ISO 527-2:2012 | ≥ 80% retention after aging |
Hydrogen peroxide sterilisation of reusable medical equipment housings introduces a separate compliance boundary for RD302G6: moulded parts with skin-contact surfaces are validated under ISO 10993-5:2009 for cytotoxicity and ISO 10993-10:2021 for skin sensitisation. Low-temperature hydrogen peroxide plasma sterilisation is performed at 45–55°C and 0.5–2.0 mbar for 28–55 min; after 200 cycles the compound shows no visible surface crazing when the housing is produced with a fully vented cold-runner system and without stearate-based mould release agents. The 30 wt% glass-fibre content reduces sink marks on structural ribs, but it also creates microchannels at the fibre-matrix interface that can retain condensate; patient-contact zones are therefore limited to a surface roughness of Ra 0.8–1.6 µm and must be dried at 60°C for 2 h after each sterilisation cycle before packaging. Mould temperature is set at 80°C and melt residence time is limited to 6 min at 255°C to prevent oxidative species that could later leach into aqueous extract and raise the in vitro cytotoxicity score. The grade is not used for implants or long-term mucosal contact, because the glass-fibre reinforcement is not permitted in such categories under FDA 21 CFR 177.1500 interpretations for polyamide 12 and because fibre release at wear surfaces is a validation risk.
Electrical connector housings for industrial automation are specified under IEC 60664-1:2020 up to overvoltage category III, pollution degree 2, when the comparative tracking index of the compound is at least 600 V. The injection-moulded 30 wt% glass-fibre formulation gives volume resistivity in the range of 10¹³–10¹⁵ Ω·cm after 48 h at 23°C and 50% RH; values below 10¹³ Ω·cm indicate moisture uptake above 0.2 wt% or charred material from thermal degradation. The terminal product is a two-piece connector shell with snap arms; gate location is set at the thickest section near the cable entry to avoid a knit line across the snap arm, because glass-fibre orientation at the arm hinge reduces flexural fatigue life by 30–40% compared with a non-weld region. Mould temperature of 90–100°C is used for these parts, but the grade is not appropriate for connectors with living hinges because the required flexural strain exceeds the dry-as-moulded elongation at break of 3.0–4.5%. In outdoor installations, an additional 2–3 wt% carbon black masterbatch is blended for ultraviolet stability, and parts are marked per ISO 11469:2016.
For industrial cable ties used in outdoor photovoltaic installations, RD302G6 is moulded with 2–3 wt% carbon black masterbatch and marked per ISO 11469:2016 as >PA12-GF30<; the key acceptance test is notched Charpy impact at -30°C of at least 15 kJ/m² per ISO 179-1:2020, because glass-fibre orientation at the tie wedge cannot be corrected by gate relocation.
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Polyram PlusTek RD302G6 is a 30% by weight glass-fiber reinforced polyamide 12 injection-molding grade supplied as cylindrical pellets. The product belongs to the PA12-GF30 category and is specified by loss-on-ignition under ISO 3451-1 for filler content. Selection of PA12 as the matrix differentiates the compound from PA6-GF30 and PA66-GF30 grades in three measurable respects: lower equilibrium moisture uptake, lower density, and improved retention of low-temperature ductility. The compound is typically processed on conventional reciprocating-screw injection molding machines with a desiccant drying system and is used where hydrocarbon exposure, condensation cycling, and tight dimensional tolerances after moisture conditioning are design constraints. Because the glass reinforcement is discontinuous and flow-oriented, mechanical properties are anisotropic; weld lines, gate locations, and fiber-length retention in the plastication zone determine final part performance.
At 30% glass loading, the deformation mechanism in RD302G6 shifts from yielding of the polyamide 12 matrix to fiber-dominated load transfer. Unfilled PA12 commonly exhibits tensile modulus values between 1,400 MPa and 1,700 MPa; the reinforced compound reaches approximately 6,500–7,000 MPa under ISO 527-2. The tensile stress at break is approximately 115 MPa, while flexural strength reaches 165 MPa under ISO 178. Elongation at break falls to 3–5%, which is characteristic of a rigid short-fiber composite and removes the large plastic deformation reserve of unfilled PA12. Snap-fit designs with high assembly strain should therefore be re-evaluated using the reinforced compound’s lower strain-to-failure.
Thermal performance under short-term load is reported as 172°C at 1.80 MPa per ISO 75-2/A. Because this value is close to the melting point of the PA12 matrix, the material can briefly tolerate paint-bake or under-hood peaks, but continuous-use temperature must be validated by heat-aging and creep data. The coefficient of linear thermal expansion is anisotropic: 25 × 10⁻⁶ K⁻¹ in the flow direction and 45 × 10⁻⁶ K⁻¹ transverse to flow. This anisotropy is lower than unfilled PA12 and lower than many semi-crystalline polyamides, but it remains sufficient to produce warpage if gate placement produces asymmetric orientation in flat housings.
At 23°C and 50% relative humidity, the equilibrium moisture absorption for a 30% glass-filled PA12 is approximately 0.5–0.6% under ISO 62. This is roughly one-third to one-fourth of the moisture uptake reported for PA6-GF30 and PA66-GF30 under the same conditions. The practical consequence is reduced hygroscopic expansion and better retention of modulus and strength in humid engine-compartment service. Nevertheless, the material is not hydrophobic; long-term water immersion increases uptake, and mechanical properties should be verified after conditioning to the relevant service atmosphere.
| Property | Value | Test method |
|---|---|---|
| Glass fiber content | 30% | ISO 3451-1 |
| Density | 1.24 g/cm³ | ISO 1183-1 |
| Tensile stress at break | 115 MPa | ISO 527-2 |
| Tensile modulus | 6,800 MPa | ISO 527-2 |
| Flexural modulus | 6,200 MPa | ISO 178 |
| Flexural strength | 165 MPa | ISO 178 |
| Charpy notched impact at 23°C | 12 kJ/m² | ISO 179-1/1eA |
| Charpy notched impact at -40°C | 8 kJ/m² | ISO 179-1/1eA |
| Heat deflection temperature at 1.80 MPa | 172°C | ISO 75-2/A |
| Moisture absorption at 23°C/50% RH | 0.55% | ISO 62 |
| Molding shrinkage, flow direction | 0.2% | ISO 294-4 |
| Molding shrinkage, transverse direction | 0.4% | ISO 294-4 |
| CLTE, flow direction | 25 × 10⁻⁶ K⁻¹ | ISO 11359-2 |
| CLTE, transverse direction | 45 × 10⁻⁶ K⁻¹ | ISO 11359-2 |
Values in the table are representative for a 30% glass-fiber reinforced PA12; lot-specific certificates from the manufacturer supersede these figures. Impact values are sensitive to fiber length distribution, moisture content, and gate-induced orientation; incoming inspection on a standard multipurpose specimen alone does not predict weld-line impact in a complex cavity.
The limiting processing factor for RD302G6 is residual moisture rather than drying temperature alone. Although PA12 absorbs less atmospheric moisture than PA6 or PA66, melt hydrolysis can occur when moisture exceeds 0.10%. Closed-loop desiccant drying at 80°C for 4–6 h is recommended; material left in open hoppers or exposed to high relative humidity should be dried for 8 h. Dew point at the dryer inlet should remain below -30°C. Residual moisture can be verified by Karl Fischer titration according to ISO 15512.
Melt temperature measured at the nozzle should remain in the 250–270°C band. A three-zone barrel profile from rear to nozzle of 230°C, 240°C, 250°C, and 255°C is a common starting point on a 25:1 L/D screw. The compression ratio should be 2.0:1–2.5:1; high-shear mixing elements are not required and may promote glass fracture. A reverse-taper shut-off nozzle prevents drool when the barrel remains at temperature during semi-cyclic operation. Back pressure should be maintained at 0.5–1.5 MPa, and screw speed should be held between 100 rpm and 200 rpm. At the upper end of the screw-speed range, viscous heating can raise melt temperature above 275°C and initiate polymer degradation; residence time at melt temperature should not exceed 10 min. Mold temperature should be set at 60–80°C. The upper portion of the range improves surface replication and fusion at weld lines; the lower portion may reduce cycle time but can increase residual stress in thick sections.
Injection fill time for thin-wall parts should be 0.5–1.5 s. High injection speed increases shear heating at the gate and can reduce fiber length, but low speed may produce hesitation lines and poor glass distribution. Hot runner systems should be heated to 240–260°C, not to the upper melt-temperature limit, because hot-runner residence time adds to the barrel residence history. Manifold channels should be sized to avoid dead zones; full-round cross-sections are preferred.
Production-scale records for similar PA12 GF30 compounds indicate that fiber-length attrition in the plastication zone is a primary source of batch-to-batch impact variation. Lowering screw speed from 200 rpm to 120 rpm can preserve a larger fraction of long fibers; however, the associated increase in melt viscosity may require higher injection pressure to fill thin sections. The use of regrind should be limited to 20% by weight unless process capability studies show stable tensile and impact properties.
| Parameter | Recommended window | Equipment note |
|---|---|---|
| Pre-drying temperature | 80°C | Closed-loop desiccant dryer, dew point ≤ -30°C |
| Pre-drying time | 4–6 h | 8 h after exposure to uncontrolled atmosphere |
| Maximum residual moisture | 0.10% | ISO 15512 Karl Fischer |
| Melt temperature | 250–270°C | Measured at nozzle; shot-to-shot variation ≤ ±5°C |
| Barrel profile, rear/center/front/nozzle | 230/240/250/255°C | Three-zone 25:1 L/D screw |
| Mold temperature | 60–80°C | Upper range for tight-tolerance parts |
| Injection pressure | 60–120 MPa | Hydraulic machine with non-return valve |
| Hold pressure | 40–70 MPa | Gate-freeze verification required |
| Back pressure | 0.5–1.5 MPa | Low-to-moderate to limit glass fracture |
| Screw speed | 100–200 rpm | For 25:1 L/D; lower range for more fiber-length retention |
| Injection speed | Medium-to-high | Fill time 0.5–1.5 s for thin-wall sections |
| Nozzle type | Reverse-taper shut-off | Prevents drool at high glass content |
Set-points in the table are starting conditions; part geometry, hot-runner balance, and clamp force dictate final values. For molds with sequential valve gating, gate timing should be established with short-shot progression to move weld lines into low-stress regions.
Substitution is not a direct tensile-strength equivalence. RD302G6 tensile stress at break of approximately 115 MPa is lower than the 170 MPa commonly reported for PA6-GF30 and the 185 MPa reported for PA66-GF30. At equal wall thickness, this difference reduces the safety factor in pressure-loaded connectors and in bolted joints requiring clamp-load retention. The stiffness gap is narrower: RD302G6 tensile modulus of 6,800 MPa is within the lower end of the 7,000–8,000 MPa range for many PA6-GF30 and PA66-GF30 grades. The offsetting advantages are density, moisture uptake, and low-temperature impact retention. RD302G6 density of 1.24 g/cm³ is approximately 9–10% lower than PA6-GF30 and PA66-GF30, and equilibrium moisture at 23°C/50% RH is 0.5–0.6% versus 1.5–2.0% for typical PA6/PA66-GF30 materials.
These differences directly affect component design. A fuel-line quick-connector body molded in PA12-GF30 may retain its press-fit interference after exposure to condensation because the radial growth from moisture uptake is smaller than with PA6-GF30. Conversely, a thin structural bracket originally designed for PA66-GF30 may require an increase in wall thickness or rib height to compensate for the lower tensile strength of PA12-GF30. Comparative tabulation is not a substitute for CAE prediction with moisture-dependent stress-strain data.
Relative to an impact-modified unreinforced PA12, RD302G6 provides higher tensile modulus and lower elongation; it is not an impact-modified grade and should not be used as a direct replacement in snap-fit designs requiring large assembly deflections. The product’s 30% glass fiber filler differentiates it from glass-bead-filled PA12. Glass fiber gives higher anisotropic stiffness and strength in the flow direction but larger shrinkage anisotropy; glass bead gives more isotropic shrinkage and lower surface roughness but less tensile reinforcement.
Primary application areas for RD302G6 include fuel-system quick connectors, brake hose clips, pneumatic line clamps, sensor brackets, and other transportation components in which PA12’s resistance to aliphatic hydrocarbons and zinc chloride under stress is required. In humid-to-dry cycling, the compound’s lower equilibrium moisture uptake supports dimensional stability compared with PA6-GF30; however, published field data for this specific formulation are limited. Component validation should include thermal cycling with the actual mating hardware, pressure cycling for fluid connectors, and tensile testing of weld lines after assembly. Under dry conditions, glass-reinforced PA12 typically has volume resistivity above 10¹³ Ω·cm per IEC 62631-3-1. The material is not an electrical conductor; if static dissipation is required, a conductive PA12 variant is necessary.
The compound exhibits the chemical resistance of PA12 in fuels, oils, greases, and many aliphatic hydrocarbons. Direct contact with concentrated mineral acids, formic acid, phenols, strong oxidizing agents, or methanol-containing fuel blends above 15% should be avoided or validated under ISO 175. Natural or light-colored grades are not UV-stabilized; outdoor exposure can cause surface chalking and reduction in tensile properties. Black grades containing carbon black provide improved UV retention.
Operational boundaries for RD302G6 include the avoidance of prolonged melt residence above 270°C, the use of moisture management, and restriction of regrind to processes with documented mechanical property stability. The compound should not be exposed to concentrated sulfuric acid, formic acid, or phenols; stress-cracking resistance in methanol-containing fuels must be tested under ISO 175 at representative temperature and strain. Welded joints will generally fail at 30–50% of the parent tensile strength because the glass fibers do not flow across the weld interface; weld-line placement and joint design are therefore critical. Compliance documentation for REACH, RoHS Directive 2011/65/EU, and automotive IMDS entries should be obtained from the manufacturer for the exact production lot; the compound is not intended for food-contact applications unless a specific food-contact approval is provided.