| HS Code | 407881 |
| Material | Polyram PlusTek RD120 Nylon 12 |
| Processing Method | Injection Molding |
| Density | 1.01 g/cm³ |
| Tensile Strength | 45 MPa |
| Elongation At Break | 200% |
| Flexural Modulus | 1200 MPa |
| Flexural Strength | 55 MPa |
| Izod Impact Notched | 40 kJ/m² |
| Heat Deflection Temperature At 1 8 Mpa | 50 °C |
| Melting Temperature | 178 °C |
| Water Absorption 24h | 0.25% |
| Mold Shrinkage | 1.2% |
| Melt Volume Flow Rate | 15 cm³/10 min |
As an accredited Polyram PlusTek RD120 Nylon 12, Injection Molding factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polyram PlusTek RD120 Nylon 12 injection molding grade, supplied in 25 kg moisture-resistant bags, ready for processing. |
| Container Loading (20′ FCL) | 20′ FCL loading of Polyram PlusTek RD120 Nylon 12 in sealed, palletized bags, safely secured for injection molding transport. |
| Shipping | Polyram PlusTek RD120 Nylon 12 is an injection-molding thermoplastic resin supplied as dry pellets. Ship in sealed moisture-barrier bags or drums to prevent water absorption. Not regulated as hazardous material; store away from extreme heat, humidity, and direct sunlight to maintain processing quality. |
| Storage | Store Polyram PlusTek RD120 Nylon 12 in its original, sealed packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, heat sources, and moisture to prevent degradation and water absorption. Keep away from ignition sources and oxidizers. Avoid dust accumulation; use proper grounding. Maintain moderate temperatures and follow FIFO rotation to preserve material properties. |
| Shelf Life | Shelf life is typically 2 years if stored dry, cool, and in original sealed packaging. Protect from moisture. |
Automotive fuel quick connectors molded from Polyram PlusTek RD120 Nylon 12 injection-molding grade are processed under desiccant drying at 80°C for 4 h to a residual moisture level below 0.10 wt%, verified by ISO 15512 Method A before the first shot of each production shift. The screw barrel temperature profile is staged from 220°C in the feed throat to 250°C in the metering zone, with a melt temperature measured by an immersion pyrometer at 245°C to 255°C and mold circuits held at 50°C to 60°C through turbulent water flow. Neat resin or a 40:1 let-down of carbon black masterbatch at 2.5 wt% is used; the addition of external impact modifiers is omitted unless sub-ambient impact at −40°C is specified by SAE J2044 quick-connector validation. Connector bodies molded in 8-cavity cold-runner tooling with 0.8 mm pin gates require transfer from velocity to holding pressure at 92–95% of the screw stroke because gate freeze for this geometry at a 50°C mold is observed in the 0.6–1.0 s range; holding pressure is maintained at 60 MPa to 80 MPa for 2.0–3.0 s to compensate PA12 crystallinity-driven volumetric shrinkage. Automotive qualification includes ISO 527-1/-2 tensile testing with a yield stress above 40 MPa and elongation at break beyond 200% after ISO 1110 conditioning at 23°C and 50% RH, ISO 180/A notched Izod impact above 5 kJ/m² at 23°C, ISO 868 Shore D hardness near 72, and ISO 1183 density in the range of 1.01–1.03 g/cm³. The terminal components are SAE J2044-compliant fuel quick connectors and evaporative emission line retainers; long-term fuel exposure is screened by ISO 1817 immersion, with dimensional change monitored on bosses and sealing ribs because PA12 low water and fuel absorption minimizes seal-bore distortion.
Lot-to-lot melt viscosity variation, measured by ISO 1133-1 at 235°C and 2.16 kg, generally falls within 8–14 cm³/10 min for this PA12 grade; on a 4-cavity quick-connector tool, that range corresponds to a fill-time variation of 0.12–0.18 s at fixed injection speed. Production lines therefore set the transfer position by integration of screw stroke and cavity pressure, not by timer, to maintain gate seal at 95–100%. Clamp force for a projected area of 1,200 mm² per part at 60 MPa melt pressure is calculated at 288 kN plus 20% margin, placing the tool in a 400–500 kN hydraulic or servo-electric press. After molding, a 24 h conditioning step at 23°C and 50% RH is applied before mating with nylon 12 tubing to stabilize seal-ring snap-fit interference and confirm dimensional reproducibility across batch changes.
Thin-wall cable tie and harness-management clip production is driven by the low melt viscosity of RD120 PA12 and its retention of elongation after moisture conditioning. The material is dried in hopper dryers with a supply air dew point no higher than −30°C to maintain residual moisture below 0.08 wt% because hydrolysis at 260°C reduces molecular weight and notched impact strength faster than in an unhydrated melt. Let-down of black or pigmented masterbatch is set at 2.0–3.0 wt% in a 25:1 to 33:1 ratio, and regrind from sprue and runner systems is capped at 15 wt% to avoid molecular weight distribution broadening. Barrel profile from feed to nozzle is 230°C to 250°C, and actual melt temperature at the nozzle is held at 245°C to 255°C; mold temperature is staged from 60°C to 80°C to stabilize tie strap hinge zones and avoid brittle fracture at the pawl root. Injection speed is set to fill 0.8–1.2 mm wall sections in 0.20–0.35 s, with velocity-controlled filling followed by holding pressure of 70–90 MPa for 0.5–1.5 s; screw recovery is delayed until the final pack stage to avoid gate drool in hot-tip systems. Compliance for finished cable ties follows UL 62275, UL 94 HB at 1.6 mm for the natural grade, with UL 94 V-2 at 0.8 mm attained only when a flame-retardant masterbatch is added, ISO 527-1/-2 tensile strength above 35 MPa, and ISO 180/A notched Izod above 7 kJ/m². Terminal products are cable ties in 100 mm to 300 mm lengths, push-mount harness clips, and convoluted-tube retainers used in engine-compartment and climate-control harness routing.
In compressed-air distribution systems, push-to-fit fittings injection molded from RD120 are dimensionally constrained by thread engagement standards ISO 228-1 and ISO 14743:2004, because thermoplastic pitch diameters shift when the part is conditioned at 23°C and 50% RH. The material is processed from a dry-pellet state at 0.06–0.10 wt% residual moisture; a reverse-barrier screw with an L/D of 20:1 and compression ratio of 2.0:1 is used at a rotation speed of 80–120 rpm to avoid frictional heat peaks above 260°C. A 3.0 wt% color masterbatch with a PA12 carrier is added for grey or blue body identification, while mineral-filled variants are not used because soft-seal retention demands a Shore D hardness of 70–74 per ISO 868. Tooling includes 1.0–1.5 mm wall cores for push-ring retention ledges; filling is performed at reduced screw speed and injection speed to limit jetting at the retention groove, with holding pressure of 50–70 MPa and a cooling time of 6–10 s at mold temperatures of 40°C to 50°C. Finished fittings are tested for insertion and retraction force under ISO 14743 after ISO 1110 equilibration; the low water uptake of PA12 under ISO 62 24 h immersion—reported below 0.3% versus over 1.3% for PA66—keeps male thread pitch diameter change within tolerance bands at relative humidity from 20% to 80%. Terminal components include BSPP and metric push-to-fit connectors for 4 mm, 6 mm, 8 mm, and 10 mm polyurethane tubing, used in factory automation and packaging machinery.
Hot-runner valve-gate systems with internally heated tips of 0.8 mm bore are preferred over cold sprue bushings because the PA12 freeze-off in the runner shuts after 1.0–1.5 s at 50°C, causing pressure loss if runner diameter is below 4.0 mm. In production, the screw buffer is maintained at 3.0–5.0 mm and decompression after recovery is set at 1.0–2.0 mm to prevent nozzle drool; cavity pressure sensors reading 40–55 MPa at the post gate confirm consistent packing of the retention ledge. Dimensional audits after ISO 291 conditioning show that pitch diameter drift on G 1/8 and G 1/4 threads remains below 0.05 mm when ambient relative humidity cycles between 20% and 80%, a range that would produce substantially greater drift in PA66 fittings.
Cold-temperature toughness and stress-crack resistance are the controlling property set when RD120 is selected for ski touring components such as toe-piece levers, heel release cams, and adjustment knobs. The molding composition is natural PA12 or a 2.0 wt% UV-stabilized carbon black masterbatch at a 50:1 let-down; glass fiber reinforcement is excluded from these components because transverse elongation at −30°C is more important than modulus. Pre-drying at 75°C for 5 h to below 0.10 wt% moisture is maintained, then the melt is processed at 240°C to 250°C, with mold temperature set to 60°C to 80°C to produce larger spherulites and lower internal stress in thick bosses. Holding pressure is set at 60–80 MPa and reduced in steps over 8–12 s to avoid sink marks at the barrel pivot; cycle time is less critical because flow length in a 2.0–4.0 mm wall is reached with moderate injection speed. Components are qualified by ISO 180/A notched Izod at −30°C above 4 kJ/m², ISO 527-2 tensile elongation at yield above 10%, and ISO 4892-2 xenon-arc weathering with no visible surface cracking. Terminal products are ski touring toe and heel levers, boot-locking adjustment knobs, and post-mold-tapped camera mount rails; the tapped holes are cut post-molding rather than molded because tapped threads in PA12 at low temperature show ductile stripping rather than brittle fracture.
Polyram PlusTek RD120 Nylon 12 is converted into dry-powder inhaler chassis and dose-counter housings only when the resin and colorant package have been reviewed under ISO 10993-5 cytotoxicity and ISO 10993-10 sensitization; the base polymer is also expected to satisfy FDA 21 CFR 177.1500 for nylon resins used in repeat-contact food and drug applications, though the specific compounded lot must be subjected to USP <661.1> plastic material testing. Virgin resin and regrind are blended at a maximum 20 wt% regrind level from a closed cleanroom moulding line with an ISO 14644-1 Class 7 environment, and no external mold release is applied to cavity surfaces. Drying is performed at 70°C for 5 h to keep residual moisture below 0.07 wt% because low-molecular-weight volatile residues are a rejection criterion for inhaler components. Barrel temperatures are lowered to 230°C to 245°C and mold temperature is set to 35°C to 45°C to minimize spherulite-induced surface roughness and sink on datum faces; injection velocity is profiled with a short 0.2 s boost followed by slow packing at 50 MPa to avoid silver streaks from gas entrapment in thin clip features. Terminal components include inhaler chassis bodies, dose-indicator housing halves, and cartridge retainers; post-mold annealing is not applied because the as-molded crystallinity in a 40°C tool already provides adequate dimensional stability under ISO 291 atmosphere. Published data for the exact Polyram RD120 lot in prolonged metered-dose inhaler chemical exposure is limited; qualification therefore uses a project-specific contaminant leachables protocol based on ISO 10993-18 analytical evaluation.
Industrial cable glands and strain-relief parts made from RD120 are dimensionally specified against IEC 62444 for metric and PG threads, and environmental sealing is verified by IEC 60529 after installation on polyurethane or rubber-sheathed cable. The production composition uses a 3.0 wt% black masterbatch with carbon black at 25% in a PA12 carrier, giving a finished carbon black content near 0.75 wt%; UV stabilizer is also added at 0.2 wt% where outdoor use is specified. Drying before processing is 4 h at 80°C to below 0.10 wt% residual moisture, with batch verification by a halogen moisture analyzer calibrated to ISO 15512. Barrel temperatures are set from 225°C at the feed to 245°C at the nozzle, mold temperature at 50°C to 60°C, and screw back pressure at 3–5 MPa to homogenize the additive package without generating high shear heating. Gland bodies are molded with 0.8 mm thread profile details; holding pressure is 70–85 MPa, and core pins are temperature-controlled separately at 60°C to prevent crab-claw cracking at the cable entry. Finished parts are subjected to dimensional audit under ISO 291 with thread go/no-go gauges per ISO 965-1, torque testing per IEC 62444, and conditioning for IP68 tests under IEC 60529. Terminal products include nylon cable glands for 5 mm to 20 mm cable diameters, locknuts, thread adapters, and multi-cable flat-gland plates.
Competitive Polyram PlusTek RD120 Nylon 12, Injection Molding prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Polyram PlusTek RD120 is an unfilled polyamide 12 injection-molding compound supplied as pellets for parts that require low equilibrium moisture uptake, stable dielectric properties after conditioning, and retained impact resistance below 0 °C. Under ISO 1043, the base polymer is designated PA12; under ISO 16396-1, the grade-specific designation appears with the viscosity and impact-modification codes that identify the RD120 formulation on the certificate of analysis. The product is aimed at thin-wall, high-flow tool layouts; typical unfilled PA12 grades in this class exhibit a density of 1.01–1.04 g/cm³ when tested to ISO 1183-1 and a melting temperature of 175–180 °C by ISO 11357-3. The low moisture absorption of PA12—commonly 0.7–0.9 % at 23 °C and 50 % RH by ISO 62—means that mechanical performance shifts less between dry-as-molded and service-conditioned states than with PA6 or PA66.
Unlike extrusion-oriented PA12 grades, RD120 is compounded for injection molding rheology: higher melt-flow consistency and release behavior suited to cold-runner or hot-runner tools. The grade is not recommended for blow molding or profile extrusion unless validated under separate process conditions. Material substitution decisions for RD120 should compare supplier datasheet values against the class-level ranges presented here, because nucleating agents, lubricant systems, or molecular-weight modifiers can shift specific values away from the unfilled-PA12 class average.
The practical difference between RD120 and shorter-chain polyamide grades is most visible in humid environments and in parts with tight post-molding tolerances. PA12 has a lower amide-group concentration per unit chain length than PA6 or PA66, which reduces hydrogen-bonding sites for water absorption. When specimens are conditioned to equilibrium at 23 °C and 50 % RH according to ISO 62, the absorbed moisture for PA12-class materials typically remains below 1.0 %, whereas PA6 reaches 2.5–3.0 % and PA66 reaches 2.0–2.5 %. This moisture differential translates into lower dimensional change in service: an unfilled PA12 part may show a coefficient of linear expansion of 1.0–1.2 × 10⁻⁴ K⁻¹ in the flow direction by ISO 11359-2, while the property remains sensitive to orientation and mold constraint. The lower density of PA12 reduces part mass relative to PA6 or PA66 at equal wall thickness.
| Property | Test method | PA12 class | PA6 | PA66 |
|---|---|---|---|---|
| Density | ISO 1183-1 | 1.01–1.04 g/cm³ | 1.13–1.15 g/cm³ | 1.13–1.15 g/cm³ |
| Water absorption, 23 °C/50 % RH | ISO 62 | 0.7–0.9 % | 2.5–3.0 % | 2.0–2.5 % |
| Melting temperature | ISO 11357-3 | 175–180 °C | 220–225 °C | 255–265 °C |
| Tensile yield stress, dry | ISO 527-2 | 40–50 MPa | 75–85 MPa | 80–90 MPa |
| Notched Izod impact, 23 °C | ISO 180/A | 6–10 kJ/m² or partial break | 5–7 kJ/m² | 5–7 kJ/m² |
| Heat deflection temperature, 1.8 MPa | ISO 75-2 | 50–55 °C | 65–75 °C | 70–80 °C |
Compared with the same supplier’s extrusion-oriented PA12 grades, RD120 is adjusted to a narrower molecular weight distribution and may contain a lubricant package to reduce ejection force. Published data for this exact configuration is limited; the supplier’s certificate of analysis should be consulted before substitution. Component designers should not assume that the higher toughness of PA12 compensates for a lower tensile yield stress in load-bearing sections.
RD120 is processed on reciprocating-screw injection molding machines with a general-purpose or low-compression screw. On machines with screw diameters of 25–40 mm and L/D ratios of 18:1–22:1, screw recovery should be set so that melt cushion remains between 2–5 mm and decompression distance does not exceed 2–3 mm to avoid nozzle drool. Pre-drying is required when residual moisture is above 0.10 %; a desiccant dryer with dew point ≤ −30 °C at 80 °C for 4–6 h is sufficient for sealed pellets. Melt temperature measured by pyrometer is normally maintained in the 230–260 °C range; barrel zones may be set from 210 °C at the rear to 250 °C at the nozzle, while the mold temperature is controlled between 40 °C and 80 °C. Total residence time at melt temperature should remain below 8–10 min; longer holdup can shift melt viscosity and generate surface splay from volatile degradation products.
Low-compression screws with a compression ratio of 2.0:1–2.5:1 and a check ring with a sliding clearance of 0.03–0.06 mm are used to avoid excessive shear heating. Injection speed is set at 100–250 mm/s for wall sections of 1.0–2.5 mm, with holding pressure of 60–100 % of injection pressure and holding time of 0.5–1.5 s/mm of wall thickness. The required clamp force is typically 3–5 kN/cm² of projected part area for thin-wall parts, but this depends on melt temperature, mold temperature, and gate geometry.
During hot-runner molding of high-cavitation tools, manifold temperature uniformity is more critical for RD120 than for PA66 because the solidification range is narrower. A manifold set-point difference of more than 8–10 °C across nozzles can produce non-uniform filling, gate freeze-off variation, and inconsistent part mass. Straight-bore hot-runner nozzles with thermal profiles measured by surface thermocouples are recommended; externally heated nozzles should be calibrated to the manufacturer’s tolerance of ±2 °C.
In automotive fluid-contact parts, RD120 is used for quick connectors, fuel-vapor line fittings, and cable clips that require zinc-chloride road-salt resistance and retained toughness after fuel exposure. Qualification programs commonly include tensile strength retention after immersion in ASTM Reference Fuel C at 60 °C for 500 h and stress-cracking evaluation in 50 % zinc chloride solution at 23 °C. On multicavity production tools, parts below 15 g are often molded with clamp forces of 600–1000 kN, with gate dimensions of 0.8–1.5 mm chosen to delay freeze-off and maintain packing. Molded parts should be ejected with draft angles of at least 1° on textured surfaces; ejection plates are preferred over pin-only ejection for thin-wall designs because PA12 exhibits a lower room-temperature modulus after moisture conditioning.
PA12 injection-molding grades are frequently selected for snap-fit closures and cable-management parts in which assembly hinges require high elongation and low friction. For RD120, the relevant mechanical comparisons are tensile elongation at break and notched impact, but mold design determines whether the material property is actually used. Rib-to-wall ratios should be kept below 0.6:1 to limit sink marks, and corner radii should be at least 0.5 mm to reduce notch stress. Snap-fit retention is influenced by the flexural modulus after conditioning; unfilled PA12 of this class typically shows a flexural modulus of 1.2–1.6 GPa at 23 °C by ISO 178, decreasing after moisture uptake. Where ejection temperatures exceed 80 °C, the part may deform under ejection forces because the heat deflection temperature of PA12 under 1.8 MPa is lower than that of PA6 or PA66.
Tool shrinkage for unfilled PA12 is generally 0.8–1.5 %, with anisotropy between flow and transverse directions of 0.1–0.3 % depending on gate location. Prototype tooling should be measured after 24 h at 23 °C and 50 % RH before final cavity scaling. Insufficient holding pressure or excessively short gate dimensions in snap-fit areas can produce frozen-in stress that manifests as delayed crack formation after propellant or fuel vapor exposure.
| Standard or directive | Designation / clause | Relevance to RD120 part certification |
|---|---|---|
| ISO 1043 | PA12 designation | Material identification on drawings |
| ISO 1133-1:2022 | Melt mass-flow rate | Batch-to-batch rheology |
| ISO 527-2 | Type 1A specimen | Tensile specification |
| ISO 178 | Three-point flexure | Snap-fit design data |
| ISO 180/A | Notched Izod | Impact verification |
| ISO 1183-1 | Immersion density | Material density control |
| ISO 62 | Water absorption, 23 °C/50 % RH | Conditioning effects |
| RoHS Directive 2011/65/EU | Annex II restricted substances | Electronics housings and clips |
| REACH Regulation (EC) 1907/2006 | SVHC declaration | Article supply obligations |
Published data for the specific RD120 formulation under combined fuel immersion and thermal cycling is limited; component qualification should include prototype testing to the relevant OEM standard. Because PA12 has a lower heat deflection temperature and lower tensile modulus than PA6 or PA66, structural parts designed for continuous loads above 60 °C may require finite-element validation of creep and stress relaxation. Substitution of RD120 into parts originally tooled for POM or PA66 should include a dimensional audit after conditioning at 23 °C and 50 % RH, because the lower moisture uptake of PA12 does not eliminate mold-shrinkage differences caused by crystallization rate and cavity pressure history.