| HS Code | 349829 |
| Density | 1.01 g/cm³ |
| Melting Point | 168 °C |
| Vicat Softening Temperature | 130 °C |
| Hdt 1 8 Mpa | 55 °C |
| Tensile Strength At Break | 38 MPa |
| Elongation At Break | 300 % |
| Tensile Modulus | 600 MPa |
| Flexural Modulus | 500 MPa |
| Charpy Impact Strength 23 C | No break |
| Shore Hardness D | 62 |
| Water Absorption 24 H Immersion | 1.0 % |
| Melt Volume Flow Rate 235 C 2 16 Kg | 30 cm³/10 min |
As an accredited Arkema Rilsamid AESNO TL PA12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Arkema Rilsamid AESNO TL PA12 polyamide is supplied in 25 kg sealed, moisture-proof bags for safe transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL: 20 metric tons of Rilsamid AESNO TL PA12 in 25kg moisture-proof bags, palletized, secured for safe transit. |
| Shipping | Rilsamid AESNO TL PA12 is supplied as solid granules in sealed multi-layer bags, typically on pallets. It is classified as non-hazardous for transport, but should be kept dry and protected from moisture during shipment. Avoid extreme heat or prolonged UV exposure to maintain product quality. |
| Storage | Store Rilsamid AESNO TL PA12 in its original, unopened container in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and ignition risks. Keep tightly sealed to prevent moisture absorption, which can affect performance. Avoid contact with strong oxidizers. Maintain moderate temperatures and protect from physical damage. Use first-in, first-out rotation. |
| Shelf Life | Shelf life is typically 2 years when stored in original, unopened packaging in a cool, dry place. |
In evaporative emission control systems for spark-ignition and full-hybrid passenger vehicles, Arkema Rilsamid AESNO TL PA12 is specified as the outer cover layer in coextruded multilayer vapour return and filler-neck vent tubing. The resin is not selected as the primary hydrocarbon barrier; its function is to provide low-temperature impact resistance, abrasion resistance against underbody clips and stone impingement, and controlled surface friction for installation. In representative coextrusion constructions, an inner barrier layer of PVDF or EVOH is supported by a polyamide tie material and an outer AESNO TL layer. Published layer-thickness distributions vary by fuel tank architecture, but an 8 mm outside diameter vapour return line commonly places the AESNO TL cover between 0.25 mm and 0.45 mm. Extrusion on a single-screw machine with an L/D of 30:1 and a barrier screw with Maddock shear mixing is recommended; the melt temperature window is held between 230 °C and 245 °C. The melt viscosity of the plasticized PA12 permits stable parison formation at line speeds of 20 m/min to 60 m/min when vacuum calibration is employed. The finished assembly is not considered compliant on the basis of resin selection alone; evaporative emission certification requires vehicle-level or system-level testing under 40 CFR 86.1818-18 and CARB LEV III protocols, because permeation is geometry-dependent and layer-thickness-dependent. Terminal parts include tank vent-to-canister lines, canister-to-purge valve lines, and filler-neck recirculation tubes. The upper continuous service limit in fuel vapour environments should be qualified against the plasticizer content and the specific aromatic hydrocarbon profile of the fuel; strong phenolic vapour exposure is outside the recommended operating envelope.
Truck and trailer air brake coil lines manufactured from AESNO TL are qualified predominantly under SAE J844 and ISO 7628:2010. The grade is used for Type A and Type B single-wall thermoplastic tubing in outside diameters of 6.4 mm, 9.5 mm, and 12.7 mm. For a 9.5 mm outside diameter line, a wall thickness between 1.25 mm and 1.50 mm is common when the working pressure is 0.86 MPa; the burst pressure margin is verified on finished coils after thermal conditioning rather than on unfilled resin plaques. Cold impact retention at -40 °C is critical because coiled trailer lines are exposed to wind chill during winter operation. Pre-drying is mandatory when the resin has been stored in humid conditions: desiccant drying at 80 °C for 4 h to 6 h to a dew point of -30 °C lowers head-space moisture below 0.08 %. Extrusion uses a single-screw extruder with a grooved feed zone and an L/D of 30:1; the barrel reaches a steep compression ratio in the feed section to compact the pellets before plastication. Vacuum tank calibration controls the outside diameter to ±0.05 mm when the line is fitted with laser diameter feedback. A black concentrate is added at 2.0 wt% to 3.0 wt% for UV resistance in chassis-exposed installations; natural unpigmented tube should not be stored outdoors for extended periods. The terminal product is cut to specified coil lengths, marked at intervals, and fitted with push-to-connect brass or composite fittings. The principal processing boundary is excessive residence time above 255 °C, which accelerates plasticizer volatilisation and produces visible gel bodies in the tube wall.
| Application segment | Governing standard or regulation | Test or design parameter |
|---|---|---|
| Multilayer fuel vapour return tube | 40 CFR 86.1818-18 / CARB LEV III | System evaporative emission, geometry-dependent permeation |
| Heavy-duty air brake coil | SAE J844 / ISO 7628:2010 | Cold impact, burst pressure, wall thickness |
| Rail and machine cable conduit | EN 45545-2 / IEC 60811-404 | Finished assembly flame behaviour, oil ageing, low-temperature impact |
| Pneumatic control tubing | ISO 14743 / ISO 8573-1 | Pressure range, dimensional tolerance, air quality class |
| Hydraulic return hose cover | SAE J517 / ISO 3949 | Cover adhesion, impulse, oil resistance |
| Protective spiral wrap | ISO 4892-2 / UL 94 | UV ageing, flammability rating |
Because the plasticized PA12 grade contains no halogenated flame-retardant chemistry, extruded cable jackets and split conduits are evaluated on the finished assembly rather than on the pellet alone when flame propagation limits apply. In rail vehicle interior applications, the completed cable or conduit must demonstrate the required hazard level under EN 45545-2; AESNO TL may be a candidate jacket material but does not by itself confer HL2 or HL3 classification because jacket thickness, conductor insulation, and bundling dominate fire load. For industrial machine sensor cables, oil resistance is typically assessed under IEC 60811-404 immersion conditions, while low-temperature bending is checked at -40 °C using a mandrel diameter appropriate to the cable outside diameter. Extrusion through a pressure crosshead onto a cable core is carried out at a melt temperature of 235 °C to 250 °C; the die land length is selected to avoid excessive die swell and to maintain jacket thickness uniformity of ±0.05 mm. The drawing line is operated between 20 m/min and 80 m/min depending on core diameter and cooling bath length. Jacket thickness for 5-core control cables typically falls between 0.5 mm and 1.5 mm. Carbon black masterbatch at 2.0 wt% to 3.0 wt% is required for outdoor durability; the unpigmented natural variant of AESNO TL is intended for indoor or protected routing. The grade is not suitable as primary insulation where continuous conductor temperatures exceed 105 °C in dry service; the combined thermoplastic insulation system must be thermally coordinated with the short-circuit rating of the cable.
For factory automation circuits operating between 0.6 MPa and 1.0 MPa, AESNO TL is extruded as unreinforced single-layer pneumatic tubing in outside diameters from 4 mm to 16 mm. These tubes are dimensionally assessed to ISO 14743, which governs thermoplastic tubing for pneumatic fluid power use. The wall thickness range is typically 1.0 mm to 2.5 mm, with the larger values used for 14 mm and 16 mm tube where vacuum service or long unsupported routing is specified. The extrusion process uses a fixed-centre annular die and a vacuum sizer; a melt temperature of 225 °C to 240 °C keeps the plasticizer uniformly dispersed while avoiding surface tack. In-line laser diameter heads provide correction every 0.2 m of line length; the tube is cut into coils or straight lengths after cooling to below 45 °C. The finished tube is compatible with compressed air that meets ISO 8573-1 class 2:2:2 for particle size, pressure dew point, and oil content; the presence of compressor oil mist does not cause immediate softening because the PA12 backbone resists mineral oil uptake. The push-in fitting interface relies on dimensional stability, and insertion force increases noticeably below 0 °C but remains practical down to -40 °C. Avoid routing the tubing in continuous contact with concentrated phosphoric acid or hot ethylene glycol above 80 °C, because these fluids attack or plasticize the amide phase. Terminal products include machine-to-valve control lines, vacuum sensing lines, and mobile pneumatic suspension circuits.
Substitution of a plasticized PA12 cover onto a polyester or aramid braided hose is performed on a crosshead extrusion line, not on a conventional straight die. The cover compound is melted at 230 °C to 245 °C and applied at a thickness of 0.8 mm to 1.5 mm; thicker constructions are unusual because the plasticizer-containing cover lowers the hose bending radius but adds mass without improving impulse life. The inner tube is typically nitrile-based for mineral oil resistance, and an adhesive tie layer is required between the braid and the PA12 cover. Braid movement during the crosshead pass is controlled by balanced braid tension and a restricted die land length. Finished low-pressure hydraulic return hoses are commonly qualified to SAE J517 with an operating pressure not exceeding 1.0 MPa in the return circuit; the cover is not intended to substitute for an inner barrier or to withstand high-pressure impulse above the hose specification. Oil resistance is checked by immersion in IRM 903 reference oil at 100 °C for 70 h; the PA12 cover exhibits lower volume swell than many PA6 jacketing compounds, but the exact value must be measured on the full hose assembly because the tie layer and plasticizer migration affect the result. The extrusion boundary condition is melt temperature: excursions above 250 °C produce pinholing at the braid interface, while temperatures below 225 °C create poor braid penetration and cover-core adhesion failure in burst testing. The terminal product is a jacketed return hose for off-road hydraulic steering and implement circuits where chafing and cold flexure are the primary failure modes.
High-cycle flexural fatigue data for spiral-wrap profiles made from AESNO TL are limited in published literature; however, the grade is used in interlocking protective conduit with inside diameters from 10 mm to 50 mm. Injection moulding and profile extrusion convert the pellet into slit or interlocking spiral wrap that bundles hydraulic hoses and electrical cables in offshore and machine tool installations. Moulding uses a reciprocating-screw machine with a three-zone cylinder profile of 230 °C to 250 °C and a mould coolant inlet temperature of 10 °C to 20 °C; ejection is assisted by a release coating formulated for polyamide, because the flexible grade exhibits higher surface tack than unplasticized PA12. For outdoor hydraulic bundle protection, the finished conduit is tested to ISO 4892-2 method A for UV exposure; unpigmented natural AESNO TL develops surface chalking unless a black or UV-stabilized masterbatch is used. The flammability rating in thin section is typically UL 94 HB; no claim of V-2 or V-0 performance should be made without a specific FR-modification study, because halogen-free FR loadings alter the impact properties that justify the selection of this grade. The lower service boundary is set by impact strength retention; at -40 °C the grade remains ductile in low-temperature impact testing performed on finished single-layer tube geometry, but thick-section moulded parts can develop notch sensitivity if sharp corners are injection-moulded. Terminal products are slit conduit, harness sheathing, and sectional wear sleeves.
Competitive Arkema Rilsamid AESNO TL PA12 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!
Arkema Rilsamid AESNO TL is a polyamide 12 extrusion grade based on laurolactam and 12-aminododecanoic acid chemistry. The material is classified as a natural, unfilled, heat-stabilized PA12 grade designed for tube, hose, and profile extrusion where low moisture uptake, chemical resistance, and low-temperature flexibility are specified. In comparison with PA6 and PA66, the lower amide-group density of PA12 restricts equilibrium water absorption under ISO 62 to approximately 1.5–2.0 % at 23 °C in water, whereas PA6 grades commonly absorb above 9 % under the same exposure. That difference reduces the dimensional movement and glass-transition suppression caused by humidity cycling in service. The supplier's grade nomenclature identifies the AESNO base as a natural polyamide 12; the TL suffix is associated with tube-oriented stabilization and processing characteristics, but the complete additive package is defined only in the manufacturer technical datasheet and safety datasheet. Lot-specific values for density, melt viscosity, tensile modulus, and impact strength are controlled by the current Arkema technical datasheet rather than by generic PA12 ranges.
Melt temperature control begins with residual moisture removal. The polymer is a hygroscopic semicrystalline thermoplastic and must be pre-dried in dehumidified air at 80 °C for 4–6 h to a residual moisture level below 0.10 wt%. Industrial tube lines using single-screw extruders with an L/D ratio of 24:1 to 30:1 and a compression ratio of 2.5:1 to 3.0:1 typically distribute barrel set points from 220 °C in the feed zone to 250 °C at the metering section and die. If melt moisture exceeds 0.15 wt%, hydrolytic chain scission occurs at processing temperature and produces a measurable loss in relative viscosity under ISO 307. The direct processing consequence is reduced melt strength at the die, unstable draw-down, and wall-thickness variation in thin sections.
The upper melt temperature should be held below 280 °C for prolonged operation. Above that threshold, thermal-oxidative degradation accelerates and can generate yellowing, gel specks, and a drop in extrudate surface quality. Published data for the oxidation induction time of this specific grade is limited; processors therefore verify the upper temperature limit with on-line melt pressure transducers and capillary rheometry rather than relying on a single manufacturer number. On production-scale equipment, melt temperature measured at the die adapter should be recorded alongside barrel set points because the difference between the two can exceed 5 °C when screw speed exceeds 80 rpm on a 45 mm single-screw extruder.
In start-up and calibration, an internally lubricated tube grade such as AESNO TL can produce lower die pressure than an unlubricated PA12 grade of identical viscosity number. Operators should not translate screw speed directly between grades. The gear pump inlet pressure and die pressure must be recalibrated against melt volume-flow rate measured under ISO 1133-1:2022. A practical control method is to record the melt volume-flow rate at 235 °C with a 2.16 kg load before drying and after drying to detect lot-to-lot variation. Without this calibration, the dimensional tolerance of tubing with wall thickness below 1.0 mm can drift outside the limits required by downstream pneumatic assembly.
At a melt temperature of 250 °C, PA12 has a finite residence-time window before measurable discoloration and viscosity shift occur. Extrusion lines are typically tooled to keep the average residence time below 10 min. In barrier screws with a grooved feed section, stagnant regions at the screw root and in the crosshead distribution channel can increase local residence time beyond the bulk average. The use of polished, chrome-plated screw surfaces and streamlined die geometries reduces the risk of gel accumulation. When gel specks appear, the first diagnostic step is to reduce the barrel temperature in the compression zone by 5 °C and increase screw speed moderately to shorten residence time.
The finished-tube quality after thermal processing is evaluated through oxidative and hydrolytic degradation indicators. Changes in relative viscosity determined by ISO 307 should be below the interlaboratory repeatability limit of the method; larger shifts indicate either insufficient drying or excessive melt temperature. For pneumatic brake tubing, the relevant long-term performance test is ISO 9080 hydrostatic strength testing at 80 °C, which detects not only immediate processing damage but also the slower effects of stabilizer depletion. Published data for the specific effect of accumulated regrind on AESNO TL hydrostatic strength is limited; processors commonly generate internal control curves by testing virgin, 20 % regrind, and 50 % regrind mixtures under ISO 9080 before qualifying any closed-loop regrind ratio.
Pneumatic brake tubing produced from PA12 is specified where sustained pressure at elevated temperature, cold impact resistance, and chemical resistance to road salt solutions are required. Acceptance testing under ISO 7628 and SAE J844 includes burst pressure at 20 °C and 80 °C, dimensional stability after heat aging, and low-temperature impact. The low moisture absorption of PA12 preserves tube length and outside diameter after wet conditioning, which is decisive in multi-line bundles where parallel tubes must remain clamped. For fuel-vapour lines, permeation resistance and resistance to aggressive oxygenated fuel fractions are evaluated according to the vehicle manufacturer specification; however, published data for this specific grade under all oxygenated fuel formulations is limited, and the final application must be validated on the production tube.
Polyamide 11 and polyamide 12 are often compared for flexible tube applications because both offer lower moisture uptake than short-chain polyamides. Unplasticized PA11 grades typically exhibit a melting endotherm near 185–190 °C by ISO 11357-3, whereas PA12 generally melts near 176–180 °C. The lower melting point of PA12 can permit lower barrel set points and can reduce residual thermal stress in thick-walled tube, but it also narrows the upper service temperature margin. At -40 °C, both polymers can retain ductile behaviour if the extrusion process avoids excessive melt temperature and if the part is properly conditioned; comparative selection should use notched impact data from ISO 179-1:2023 on dry-as-moulded and moisture-conditioned specimens.
From a dimensional and chemical standpoint, PA11 and PA12 are closer to each other than either is to PA6 or PA66. Equilibrium water absorption for both is in the 1.5–2.0 % range under ISO 62, and both have lower density than PA6. The choice between PA11 and PA12 therefore often depends on regional availability, renewable-carbon content targets, and grade-specific stabilizer approvals rather than on a large difference in base polymer properties. Within the Rilsamid PA12 range, a tube grade such as AESNO TL is specified when the application requires a consistent tube-oriented processing package, while other PA12 grades may be selected for injection moulding or thick-wall profile extrusion. The exact difference in melt viscosity, lubricant level, and stabilizer loading is disclosed in the manufacturer datasheet and should not be inferred from the grade suffix alone.
The table identifies the test framework used to verify a PA12 tube grade rather than reproducing lot-specific values that belong in the current Arkema technical datasheet. Final compliance is always established on the finished tube because processing history changes crystallinity, orientation, residual stress, and long-term hydrostatic strength.
| Test category | Standard | Condition or specimen | Data source for release |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 23 °C, immersion method | Arkema technical datasheet |
| Melt volume-flow rate | ISO 1133-1:2022 | 235 °C, 2.16 kg | Arkema technical datasheet |
| Melting temperature | ISO 11357-3 | 10 °C/min, nitrogen | Arkema technical datasheet |
| Tensile modulus and yield stress | ISO 527-1/2 | 23 °C, conditioned specimen | Arkema technical datasheet |
| Charpy notched impact strength | ISO 179-1:2023 | 23 °C and -40 °C | Arkema technical datasheet |
| Water absorption | ISO 62 | 23 °C, saturation in water | Arkema technical datasheet |
| Long-term hydrostatic strength | ISO 9080 | 80 °C, water | Finished tube qualification |
Regulatory use of PA12 in food-contact, automotive, or medical applications requires a supplier letter of compliance. Polyamide 12 base resin may be evaluated under FDA 21 CFR 177.1500 for nylon resins and under EU Regulation (EU) No 10/2011 for plastic food-contact materials, but the presence of stabilizers or processing aids in the grade must be confirmed in the supplier declaration. Electrical and electronic applications are not generally constrained by RoHS heavy-metal limits for the base polymer; however, colorants or flame-retardant masterbatches added downstream can alter the regulatory position. The processor is responsible for verifying the final part against REACH Article 33 communication duties and any automotive OEM restricted-substance list.