| HS Code | 843776 |
| Polymer Type | PA12-I (impact-modified polyamide 12) |
| Density | 1.01 g/cm³ |
| Tensile Modulus | 1350 MPa |
| Tensile Yield Stress | 45 MPa |
| Elongation At Break | >200% |
| Charpy Notched Impact At 23 C | No break |
| Melting Temperature | 174 °C |
| Vicat Softening Temperature | 145 °C |
| Water Absorption At Saturation | 1.5% |
| Melt Volume Flow Rate | 10 cm³/10 min at 235°C/2.16 kg |
As an accredited Arkema Rilsamid AESN BLACK P302 TL PA12-I factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Arkema Rilsamid AESN BLACK P302 TL PA12-I is supplied in 25 kg bags as black polyamide 12 granules. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Arkema Rilsamid AESN BLACK P302 TL PA12-I: polyamide 12 granules packed in sealed bags on pallets, secured for transport. |
| Shipping | Arkema Rilsamid AESN BLACK P302 TL PA12-I is a polyamide 12 resin supplied as solid granules/pellets. It ships as non-hazardous cargo in sealed moisture-barrier bags, supersacks, or drums. Protect from moisture, high heat, and direct sunlight during transit. Standard dry container or covered truck transport is suitable. |
| Storage | Store Arkema Rilsamid AESN BLACK P302 TL PA12-I in its original, unopened packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, moisture, heat, and ignition sources. Keep away from incompatible materials. Avoid prolonged exposure to humidity to prevent moisture pickup. Follow standard resin storage practices and use within the manufacturer’s recommended shelf life. |
| Shelf Life | Shelf life is 2 years from manufacture date when stored unopened, cool, and dry. |
Arkema Rilsamid AESN BLACK P302 TL is an unfilled impact-modified PA12-I injection-moulding grade supplied with carbon black pigmentation and combined heat and UV stabilization. The material is processed at melt temperatures of 230 °C to 270 °C, with mould temperatures between 40 °C and 80 °C depending on dimensional tolerance and crystallinity targets. Moisture must be reduced below 0.1 % before melt processing using a desiccant dryer at 80 °C for 4 h to 6 h with a dew point of −40 °C or lower. As an unfilled PA12, equilibrium moisture uptake at 23 °C and 50 % RH is approximately 0.7 % to 1.0 %, and density is 1.01 g/cm³ to 1.03 g/cm³ per ISO 1183-1:2019. The following application zones are limited to verified downstream uses where PA12-I injection grades are already specified, avoiding speculative cross-industry placement.
Material selection for gasoline and diesel fuel quick connectors is conditioned by combined exposure to reference fuels, permeation limits, and thermal cycling under underhood conditions. Automotive fuel wetted components in this segment are typically validated to SAE J2044 for mechanical engagement geometry and pull-off force, while immersion resistance is assessed under ISO 175:2010 using ASTM Reference Fuel C and CE10 test fluids at 60 °C for 500 h. Additional permeation requirements for fuel system components are frequently referenced from SAE J2260, although the connector body itself is usually validated as part of a full system rather than as an isolated coupon. Flammability classification for the connector body is generally UL 94 HB at the supplied wall thickness, which is acceptable for most fuel-line connector locations where the part is not a primary load-bearing enclosure. The grade is normally processed at 100 wt% as supplied; no additional colorant is required because carbon black is already dispersed in the resin. Regrind use in fuel-wetted primary connector bodies is typically prohibited by OEM specifications because of the risk of microvoids increasing permeation and reducing burst-pressure consistency. Where regrind is permitted by an OEM for non-wetted retention brackets, clean single-source runner regrind is capped at 20 wt% and the blend must be re-qualified for notched impact under ISO 179-1/1eA. Downstream production uses injection moulding machines with screw L/D ratios of 20:1 to 22:1 and compression ratios of 2.5:1 to 3:1, with melt temperature held at 245 °C to 265 °C and mould temperature at 50 °C to 70 °C to stabilize sealing interface dimensions. Hold pressures of 60 MPa to 90 MPa and fast injection speeds of 150 mm/s to 250 mm/s are used to avoid premature freeze-off in wall thicknesses between 1.5 mm and 3.0 mm. Valve-gated hot runners with sequential opening are preferred to eliminate cold sprue vestige at sealing faces; residence time above 5 min at 270 °C must be avoided to prevent brown speck formation and molecular-weight loss in the hot runner. Finished product types include SAE J2044-style fuel line quick connectors, evaporative canister connectors, diesel return line couplers, fuel filter caps, and carbon canister fittings.
In compressed-air distribution systems, coupling bodies made from the grade are specified where moisture uptake must not shift thread pitch diameter or alter insertion force after repeated assembly. Pneumatic push-in fittings and threaded coupling bodies are tested to ISO 14743:2004 for push-in connector requirements and to ISO 228-1:2000 for non-pressure-tight thread geometry, while flexural modulus after moisture conditioning is evaluated under ISO 178:2019. Because the grade is supplied with internal lubrication, additional external lubricant masterbatch is generally unnecessary in the formulation; any secondary anti-friction additive above 1 wt% has been observed on production-scale tooling to increase mould deposit at vent edges and reduce weld-line strength. The material is therefore used at 100 wt% as the base resin, and any dilution with natural PA12 for color coding is not recommended because thread-bearing parts rely on the black grade's dimensional stability under 50 % RH conditioning. Downstream processing of internal threads requires unscrewing cores driven by hydraulic or servo motors, with core temperature held at 80 °C to prevent over-cooling of thread crests and reduce core pull-out scrap. Mould temperature is maintained at 60 °C to 80 °C to stabilize post-mould thread diameter within ±0.05 mm, which is critical for repeatable assembly torque in compressed-air manifolds. Published burst-pressure data for this specific unfilled grade in threaded coupling bodies above 15 bar continuous air pressure at 60 °C is limited, and the material should not be substituted into hydraulic applications where continuous pressure exceeds this threshold without supplementary validation. Terminal finished products include push-to-connect pneumatic fittings, threaded adaptors, compressed-air manifolds, quick-disconnect coupling bodies, and silencer housings.
Cable ties and harness clips based on the black PA12-I grade are selected for outdoor electrical routing where moisture absorption must not alter locking pawl flexural fatigue or cause dimensional growth after wet conditioning. After 1,000 h of xenon-arc exposure under ISO 4892-2:2013, the carbon black stabilization limits surface chalking and tensile elongation loss, although specific elongation-retention values for this grade should be verified on the lot-specific technical datasheet. Cable management components are tested to UL 62275 for cable tie mechanical performance and to IEC 60695-2-11 for glow-wire ignition at 650 °C; the unfilled material is classified UL 94 HB and is not intended for live-part enclosures requiring V-0 without separate flame-retardant addition. In formulation terms, regrind addition up to 30 wt% is acceptable for non-safety conduit clips if the mixture is homogenized in-line and Charpy impact after moulding is verified under ISO 180/A. For self-locking cable ties where pawl flexural fatigue dominates, regrind is limited to 15 wt% to preserve locking retention after repeated engagement. Downstream production uses multi-cavity moulds with 32 to 64 cavities and hot runner systems, with melt temperature held at 250 °C, mould temperature at 60 °C, and cycle times of 15 s to 25 s for wall thicknesses under 2.5 mm. Gate vestige height must be kept below 0.2 mm on the cable contact surface to prevent harness abrasion during vehicle body installation. Terminal finished product types include self-locking cable ties, corrugated conduit clips, harness guides, relay sockets, and battery cable clamps.
| Application domain | Primary standard or method | Property assessed | Typical boundary condition |
|---|---|---|---|
| Fuel quick connectors | SAE J2044, ISO 175:2010 | Pull-off force, Fuel C/CE10 resistance | 60 °C, 500 h immersion |
| Pneumatic couplings | ISO 14743:2004, ISO 228-1:2000 | Push-in retention, thread geometry | Thread diameter within ±0.05 mm |
| Cable ties and clips | UL 62275, ISO 4892-2:2013 | Locking strength, UV stability | 1,000 h xenon-arc |
| Outdoor sports components | ISO 179-1/1eA, ISO 5355:2019 | Low-temperature impact, release function | −40 °C Charpy |
| Cold-chain door hardware | ISO 179-1/1eA, ISO 178:2019 | Impact after cold exposure, flexural modulus | −35 °C operating floor |
| Thin-wall electronics housings | IEC 60664-1, UL 94 HB | Creepage distance, flammability | Wall 0.8 mm to 2.0 mm |
Low-temperature ductility is the governing failure mode when moulded ski touring bindings, snowboard binding ladders, and bicycle quick-release bodies are dropped onto packed snow or rock at −40 °C. The impact-modified PA12-I matrix is used as the base polymer at 100 wt% because the incorporated elastomer phase already provides the low-temperature notched impact response required under ISO 179-1/1eA at −40 °C. No additional elastomer addition is necessary for most snap-fit levers and housings; if higher stiffness is required for a specific lever geometry, blending with a glass-filled PA12 masterbatch at 10 wt% to 20 wt% raises flexural modulus but reduces notched impact and shifts failure from ductile hinge yielding to crack initiation at the gate. Published multi-axial impact data for this exact grade in ski binding geometries is limited, and validation on production-scale parts remains mandatory because the notch sensitivity observed in standardized Charpy coupons does not fully transfer to ribbed components with weld lines. Downstream production deliberately uses a lower mould temperature of 20 °C to 40 °C rather than the higher temperatures used for dimensional stiffness applications. The lower mould temperature suppresses spherulite growth and can shift the failure mode from brittle fracture to ductile deformation in snap-fit levers under dynamic loading, but it also increases cycle time and warp tendency in asymmetric parts. For ski touring components, post-mould conditioning at 23 °C and 50 % RH for 48 h is performed before release testing to stabilize the semi-crystalline morphology. Terminal product types include ski binding toe and heel housings, touring latch levers, snowboard binding ladders, and bicycle quick-release bodies.
For walk-in freezer door hinges exposed to repeated opening at chamber temperatures between −35 °C and −5 °C, the substitution of glass-filled PA66 with this PA12-I grade removes the moisture-induced dimensional swing that causes hinge pin binding after defrost cycles. The material is used at 100 wt% as the moulding compound; if color-coded latch caps are required, a pigment masterbatch at 1 wt% to 3 wt% may be added, but the addition must be checked for notched impact loss under ISO 179-1/1eA at −40 °C. Because the grade already contains carbon black for UV and heat stabilization, no additional black masterbatch is required. Structural load performance is evaluated under ISO 178:2019 for flexural modulus after cold soaking, with the test specimen conditioned at −35 °C for at least 4 h before testing. The production process uses thick-section injection moulding with wall thicknesses from 2 mm to 5 mm, melt temperature at 250 °C, and mould temperature at 60 °C to 80 °C to maximize dimensional stability of hinge pin bores. Condensation on cold tool surfaces must be managed through dry-cycle stabilization and mould temperature control, otherwise surface splay occurs in the first shots after production pauses. Food-contact suitability is not claimed for this grade, and the material is specified only for non-food-contact door hardware and structural brackets. Terminal product types include walk-in freezer door hinges, sliding door roller brackets, latch housings, and evaporator fan guard clips.
Thin-wall connector housings for industrial sensors and solenoid coils show non-linear mould filling behaviour at wall thicknesses below 1.0 mm, where the unfilled PA12-I grade requires fast injection speeds and elevated mould temperature to prevent flow hesitation at weld lines. Electrical clearance and creepage distances are evaluated under IEC 60664-1, and flammability is limited to UL 94 HB at the minimum supplied wall thickness; applications requiring V-0 are outside the operational boundary of this specific unfilled grade unless a separately validated flame-retardant system is used. In formulation terms, the resin is processed at 100 wt% without additional flame retardant or filler. If demoulding of long core pins becomes difficult, an external wax-based masterbatch at 1 wt% to 2 wt% may be introduced, but this can reduce laser marking contrast on black surfaces and is not recommended for parts requiring high-resolution traceability codes. Production-scale experience shows that injection speeds of 250 mm/s to 350 mm/s are required to fill thin-wall sections of 0.8 mm to 2.0 mm, with melt temperature set at 265 °C to 270 °C and mould temperature at 80 °C to reduce premature wall solidification. Weld lines in thin-wall connector bodies must be positioned away from snap-fit engagement edges; if weld-line placement cannot be moved, the moulding must be evaluated by tensile testing with weld line under ASTM D638-14, because published spiral flow data for this exact grade in sub-millimetre walls is limited and lot-to-lot viscosity variation is the dominant processing risk. Terminal product types include M12 connector bodies, industrial sensor housings, solenoid coil housings, and low-voltage busbar insulators.
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Arkema Rilsamid AESN BLACK P302 TL PA12-I is a black-pigmented, heat-stabilized, impact-modified polyamide 12 supplied as ready-to-process granules. The ISO 1043-1 designation PA12-I identifies an impact-modified polyamide 12, not an unmodified PA12 grade or a short-chain aliphatic polyamide. The material belongs to the Rilsamid polyamide 12 portfolio and is specified for extrusion and injection moulding where low-temperature ductility, low moisture uptake, and stability in hydrocarbon environments are required. The black colour is achieved with carbon black loading during compound manufacture; this removes in-line masterbatch addition and its associated shot-to-shot dispersion variability on production lines.
Representative physical data for the material indicate a density of 1.01–1.02 g/cm³ when tested under ISO 1183-1:2019 and a melting temperature of 172–175°C under ISO 11357-3:2018. The compound is softer and more ductile than unfilled unmodified PA12; published tensile modulus values for this class of impact-modified polyamide 12 typically fall within 350–600 MPa under ISO 527-2:2012, and elongation at break may exceed 200%. Exact lot-specific values should be taken from the certificate of analysis. Equilibrium moisture uptake at 23°C and 50% RH remains below 1.0%, consistent with the long-chain aliphatic PA12 backbone.
The principal difference from short-chain aliphatic polyamides is water absorption. Under ISO 62:2008 equilibrium at 23°C and 50% RH, PA66 typically absorbs 2.5–3.0% moisture, while PA12 and impact-modified PA12 remain near 0.7–0.9%. The lower moisture equilibrium reduces hydrolytic dimensional changes and limits stiffness loss in humid service. Density is also lower: PA12 is approximately 1.01–1.02 g/cm³, compared with 1.13–1.14 g/cm³ for PA66 and 1.04 g/cm³ for PA11. In weight-sensitive tubing or cable sheathing, that mass reduction can be obtained without moving to foamed or thin-wall structures that may compromise burst strength.
Compared with PA11, the PA12 base has a lower melting point: PA11 melts near 189°C, while this grade melts near 172–175°C. This reduces melt-processing temperature and energy input in extrusion and injection moulding. Both PA11 and PA12 outperform short-chain polyamides in moisture resistance, but PA12 is frequently specified for fuel-vapour and pneumatic tubing because of established approval histories and supply continuity. Compared with unmodified PA12, the PA12-I impact modification changes mechanical response from stiff and relatively brittle to semi-flexible and ductile. Tensile modulus is substantially reduced: unmodified PA12 commonly exhibits 1400–1800 MPa under ISO 527-2:2012, whereas this grade and equivalent impact-modified formulations fall to 350–600 MPa. Notched impact resistance at low temperature also improves.
| Property | Test standard | Rilsamid AESN BLACK P302 TL PA12-I | Unmodified PA12 | PA66 |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 1.01–1.02 g/cm³ | 1.01 g/cm³ | 1.13–1.14 g/cm³ |
| Melting temperature | ISO 11357-3:2018 | 172–175°C | 178°C | 260°C |
| Equilibrium moisture 23°C/50% RH | ISO 62:2008 | 0.7–0.9% | 0.7–0.8% | 2.5–3.0% |
| Tensile modulus | ISO 527-2:2012 | 350–600 MPa | 1400–1800 MPa | 2800–3200 MPa |
| Notched Charpy impact 23°C | ISO 179-1/1eA:2010 | No break or high ductility | 5–10 kJ/m² | 4–6 kJ/m² |
The pre-compounded black colour is another practical difference. Natural unmodified PA12 requires metering of carbon black masterbatch, which can produce shot-to-shot colour variation if hopper segregation or screw mixing is poor. The P302 TL black pigment is incorporated during compound manufacture, shifting colour dispersion responsibility to the supplier and removing one feed-stream variable from the processor. The impact-modifier phase also increases shear sensitivity compared with unmodified PA12, so screw speed changes produce a non-linear effect on die pressure and melt temperature.
Residual moisture in the granulate must be reduced below 0.10% by weight before melt processing. A dehumidifying dryer operated at 80°C for 4–6 h is sufficient for freshly opened packaging; material exposed to ambient air above 60% RH should be dried for 8 h or until the exit dew point indicates -30°C to -40°C. Airflow should be maintained at 1.0–1.5 m³/h per kg/h of granulate throughput. Moisture remaining at the die is not a cosmetic variable: hydrolysis in the melt shortens chain length, reduces elongation at break, and creates porosity in thin-walled tube extrusions.
For single-screw extrusion, barrel temperatures from 220°C to 250°C with die temperatures between 230°C and 250°C are typical. Melt temperature measured at the die exit should not exceed 260°C; residence time above 10 min can degrade the heat-stabilizer package and produce surface defects at the die lip. Screws with L/D ratios of 24:1 to 30:1 and compression ratios of 2.5:1 to 3.0:1 are common; grooved feed sections increase output but can raise melt temperature by 5–15°C, requiring lower barrel setpoints. If melt temperature is too low, high melt elasticity may generate sharkskin on the tube surface; raising only the die zone to 245°C often reduces this without increasing overall melt temperature.
Injection moulding of the grade is usually performed with a reverse barrel profile: nozzle temperature near 240°C, centre zone 230–240°C, and rear feed zone 210–220°C. Mould temperature should be controlled between 40°C and 80°C; higher mould temperatures improve crystallinity and dimensional stability but increase cycle time. Clamp force is determined by part mass and projected area, with production equipment in the 800–2500 kN range typically used for medium-sized fittings and housings. Parts should be conditioned at 23°C and 50% RH for 48 h before final dimensional inspection because post-mould moisture uptake shifts dimensions by a measurable amount.
When regrind is used, the proportion should not exceed 25–30% by weight unless extensive property testing is performed. Regrind must be dried to the same moisture specification and should not be blended with PA66 or PA6 regrind unless compatibility is verified, because phase separation and differential moisture uptake reduce notched impact strength and weld-line integrity. If custom masterbatch addition is required, co-rotating twin-screw extruders with L/D ratios of 32:1 to 44:1 and distributive mixing elements are preferred to avoid excessive shear heating.
In production-scale extrusion of black PA12-I tubing, process stability is sensitive to melt-temperature excursions. An increase of 5°C above the upper barrel setpoint can shift melt viscosity enough to alter wall thickness in free-form tube extrusion, while a decrease of 5°C can increase orientation stress and raise post-extrusion shrinkage. This narrow window is not unique to the P302 TL grade, but the impact-modifier phase increases shear sensitivity relative to unmodified PA12. Capillary rheometry under ISO 11443 shows pronounced shear thinning; therefore, screw speed changes have a non-linear effect on die pressure in production tools.
Failure modes observed on manufacturing lines include die-lip deposit when melt temperature exceeds 260°C for prolonged intervals, and surface splay when hopper loading introduces moisture from poorly sealed vacuum conveyors. The die-lip deposit is typically black, waxy, and caused by additive migration rather than gross polymer decomposition; it can be reduced by lowering die temperature to 245°C and ensuring that no stagnant melt pool exists behind the breaker plate. Surface splay in injection-moulded parts often traces to moisture above 0.15% and is corrected by increasing drying time rather than raising melt temperature, which does not reverse hydrolytic damage. For dimensional control in pipe and tube, haul-off speed and vacuum sizing calibration must match the crystallization rate of heat-stabilized PA12. The grade’s lower melting point allows fast sizing, but rapid quenching produces high amorphous content and later dimensional growth after fuel or humidity exposure. A two-stage water bath with first-stage water at 40–60°C and second-stage water at 20–25°C is often used to set surface quality and reduce post-extrusion shrinkage.
Black pigmentation in P302 TL supplies UV resistance by absorbing radiation at the surface, reducing photo-oxidation and crack initiation in outdoor cable sheathing and exposed tubing. The carbon black package does not by itself set the high-temperature limit; the heat-stabilizer package determines retention of elongation after thermal ageing. For continuous hot-air exposure above 90°C, oven-ageing trials under ISO 2578 or a customer-specific time-temperature protocol should be performed on finished parts or standard tensile bars. Published data for prolonged ageing of this exact black P302 TL formulation are limited outside Arkema’s internal studies and customer-specific validations. A UL Yellow Card may list a relative thermal index under UL 746B, but the specific rating should be obtained from the supplier because black heat-stabilized grades can differ from natural grades.
Fuel and oil contact must be validated with the actual fluid. Immersion testing under ISO 175:2010 or SAE J2260:2015 measures volume swell, mass change, and retained tensile properties. The PA12 backbone generally resists aliphatic hydrocarbons, diesel, and many automotive fluids, but aggressive sour fuel, biodiesel blends, and hot aqueous acids can extract low-molecular-weight stabilizer components or attack the polymer. The impact modifier and heat-stabilizer package may influence extraction levels; therefore, unmodified PA12 values cannot be applied directly to this grade.
Low-temperature impact resistance is a primary reason for selecting this material over unmodified PA12. Notched Charpy impact under ISO 179-1/1eA:2010 can be measured at -30°C to screen incoming lots, but component-level cold-impact testing at -40°C is required for fuel clips and pneumatic fittings because geometry and processing orientation control final ductility. When conditioned to 50% RH, PA12 absorbs less water than PA6 or PA66, but some plasticizing effect still occurs; this increases ductility slightly and reduces modulus. Dimensional stability under humidity cycling is therefore better than short-chain polyamides, but it is not zero.