| HS Code | 100817 |
| Density | 1.06 g/cm³ |
| Melting Point | 186 °C |
| Tensile Strength | 44 MPa |
| Elongation At Break | 300% |
| Flexural Modulus | 900 MPa |
| Notched Izod Impact At 23 C | No Break |
| Notched Izod Impact At 40 C | 10 kJ/m² |
| Shore D Hardness | 66 |
| Water Absorption 24h | 1.2% |
| Water Absorption Saturation | 3.0% |
| Vicat Softening Point | 95 °C |
| Glass Transition Temperature | -20 °C |
As an accredited Arkema Rilsan BESNO P40 TLO PA11 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 25 kg bag of Arkema Rilsan BESNO P40 TLO PA11, a fine polyamide 11 powder used for durable industrial coating applications. |
| Container Loading (20′ FCL) | 20′ FCL loaded with palletized Arkema Rilsan BESNO P40 TLO PA11 bags, securely stowed, protected from moisture and heat during transit. |
| Shipping | Arkema Rilsan BESNO P40 TLO PA11 is a fine, bio-based polyamide powder for coating applications. Ship in sealed, moisture-proof packaging in dry, ventilated conditions. Avoid ignition sources and dust accumulation. Not typically classified as hazardous, but protect from humidity and extreme heat during transit. |
| Storage | Store Rilsan BESNO P40 TLO PA11 in its original, tightly sealed container in a cool, dry, and well-ventilated area. Protect from direct sunlight, excessive heat, and open flames. Keep away from moisture sources to prevent powder degradation. Maintain ambient temperature and moderate humidity for optimal shelf life. |
| Shelf Life | Shelf life is typically 2 years when stored unopened in original packaging, in a cool, dry place. |
During extrusion of thick-wall flexible riser pressure sheaths, Arkema Rilsan BESNO P40 TLO is processed on single-screw extruders equipped with grooved feed sections and barrier screws of L/D 30 or higher. Barrel set points from 220 °C to 250 °C are held to maintain melt homogeneity, while the adapter and die are limited to 240 °C maximum because the plasticized matrix develops visible yellowing and skin roughness above that threshold. The melt is fed to a spiral mandrel die and vacuum-calibrated to maintain wall-thickness deviation below ±0.1 mm on sheath diameters of 75 mm to 150 mm. In unbonded flexible pipe constructions governed by API Spec 17J, the PA11 layer functions as a fluid-retaining pressure sheath over the interlocked carcass; the plasticized grade lowers flexural stiffness during reeling, but its tensile modulus is below that of unplasticized PA11, so hoop stress at the design temperature must be recalculated using tensile data generated to ISO 527-2. Material screening for oilfield service is performed under ISO 23936-1, with aging commonly conducted in simulated produced water at 90 °C for 1,000 h; published data for this specific plasticized compound under wet sour gas is limited, and the annulus fluid composition must govern property-retention verification. Residual moisture in pellets must be reduced below 0.08 wt% by desiccant drying at 80 °C for 4–8 h before extrusion, because water carry-over creates microvoids that act as initiation points for blistering during depressurization. Plasticizer extraction becomes an operational boundary at sustained surface temperatures above 70 °C in contact with wet hydrocarbon fractions; the resulting loss of flexibility is monitored by hardness change measured to ISO 868 and by low-temperature impact testing to ISO 179-1/1eA at -40 °C.
In truck and trailer air brake lines, the dominant process failure is not melt fracture but moisture-induced microvoiding that reduces burst-pressure retention after temperature cycling. Pellets of BESNO P40 TLO are dried to a moisture content below 0.08 wt% and conveyed with a desiccant-dry air supply to the feed throat. On a 45 mm single-screw extruder with L/D 30 and a 3:1 compression ratio, barrel temperatures rise from 210 °C at the feed zone to 245 °C at the metering zone; melt temperature is held at 235 °C to 245 °C because lower temperatures produce inner-wall shark-skin and higher temperatures accelerate plasticizer volatilization. The tube is pulled through a vacuum sizing tank at -0.2 bar to -0.6 bar, and the die gap is set at 1.4 × nominal wall thickness to compensate for drawdown. A drawdown ratio between 1.1:1 and 1.5:1 is maintained to prevent excessive axial orientation, which reduces circumferential burst strength. Dimensional windows follow DIN 73378 for 6 mm, 8 mm, 10 mm, and 12 mm outside diameters; wall-thickness variation is controlled by closed-loop ultrasonic measurement to ±0.05 mm. Qualification is carried out against SAE J844 for nonmetallic air brake tubing, with cold impact at -40 °C and hot burst at 100 °C forming the critical test pair. Elongation at break measured to ISO 527-2 after aging to ISO 188 at 100 °C for 72 h typically retains more than 50 % of the original value, though the binding requirement is set by the SAE class and wall-thickness segment.
On jacketing lines for offshore control cables, BESNO P40 TLO is applied over spiral-wrapped screened cores with a pressure extruder fitted with a barrier screw and a 20/40/60 mesh screen pack to trap unmelted resin and increase back pressure. The melt enters the crosshead at 235 °C and the die at 240 °C; screw speed is constrained by shear heating, and the plasticizer begins to plate out on calibrator surfaces when local melt temperature exceeds 250 °C. The compound develops jacket tensile elongation above 150 % when tested to IEC 60811-501, which provides sufficient flexibility for dynamic riser bend zones without cracking. Water absorption at saturation is approximately 1.8 wt% by ISO 62, so moisture ingress must be considered in submersible cable designs because the plasticized matrix becomes slightly less resistive in prolonged wet service. In applications governed by IEC 60794-1-21, the jacket is subjected to repeated bending and tensile loading while maintaining optical attenuation within specified limits; the PA11 sheath reduces microbending losses at low temperatures compared with rigid polyamide grades. The compound does not inherently meet UL 94 V-0; if flame-retardant jacketing is required for cable trays in enclosed compartments, a flame-retardant grade or a different polymer must be specified. For cold installation, the cable jacket is conditioned at -20 °C for 4 h and then bent around a mandrel of 6 × cable diameter; failure is recorded when surface cracks exceed 0.1 mm in depth.
Core-tube extrusion for hydraulic return lines with BESNO P40 TLO uses a crosshead die with a preheated mandrel at 80 °C and a melt temperature of 235 °C. The plasticized PA11 exhibits lower melt viscosity than comparable PA12 grades, so screw speed on a 38 mm extruder is limited to 20–40 min⁻¹ to avoid shear overheating and localized temperatures above 250 °C. The extruded liner is cooled in a water trough at 20–40 °C, then coiled to an inner diameter of at least 20 × tube outside diameter to prevent kink stress whitening. Oil resistance is measured to ISO 1817 after immersion in IRM 903 at 100 °C for 72 h; tensile strength retention above 80 % and elongation retention above 70 % are typical for unplasticized PA11, whereas the plasticized compound may show slightly lower retention due to plasticizer extraction, and published data for this specific formulation is limited. Hose validation is performed under SAE J517 or ISO 3949, depending on the assembled hose type. In service, plasticizer migration in hot, high-detergent hydraulic fluids becomes a boundary at liner surface temperatures above 70 °C; hardness measured to ISO 868 gradually increases as the plasticizer fraction decreases. This progressive stiffening must be accounted for in minimum bend radius calculations after extended thermal exposure.
| Application segment | Reference standard | Critical measured property | Test method |
|---|---|---|---|
| Flexible riser pressure sheath | API Spec 17J, ISO 23936-1 | Tensile property retention after produced-water aging | ISO 527-2 |
| Air brake tubing | SAE J844, DIN 73378 | Cold impact and hot burst stability | ISO 179-1/1eA |
| Offshore cable jacket | IEC 60794-1-21, IEC 60811-501 | Elongation and cold-bend crack resistance | IEC 60811-501 |
| Hydraulic return-line liner | SAE J517, ISO 3949 | Aged tensile retention in IRM 903 | ISO 1817 |
| Fuel quick connector | SAE J2044 | Conditioned notched impact at -40 °C | ISO 179-1/1eA |
Fuel-line quick connectors moulded from BESNO P40 TLO are gated at the collar to move weld lines away from the sealing lip. Processing on a 100 t injection press uses barrel set points of 220 °C to 260 °C, back pressure of 0.5–1.0 MPa, injection speed of 50–100 mm/s, and holding pressure of 60–80 MPa. Mold temperature is maintained between 40 °C and 70 °C; below 40 °C the plasticized melt can freeze prematurely around the gate, producing surface delamination and dimensional instability. Drying is performed at 80 °C to 0.08 wt% moisture or below, because residual moisture causes splay on the sealing surfaces and lowers weld-line strength. After ejection, connectors are conditioned at 23 °C and 50 % RH for 48 h, raising the moisture content to approximately 1.5 wt%; this conditioning step is necessary for low-temperature assembly impact resistance at -40 °C. Notched Charpy impact strength to ISO 179-1/1eA moves from a brittle failure mode in dry-as-moulded specimens to a ductile yield mode after moisture conditioning. For fuel-contact applications, compliance with SAE J2044 covers dimensional and performance requirements for quick connectors; material validation includes resistance to fuel crazing using a soak-to-dry cycling procedure and final leak testing at 0.5 MPa air pressure.
Spiral-reinforced pneumatic tubing for automated production cells is extruded as a monolayer tube from BESNO P40 TLO before being reheated and spiral-wrapped with glass fibre or polyester reinforcement under tension. The core tube is produced with a 40 mm extruder at 230 °C melt temperature and sized to a wall thickness of 1.0–1.5 mm; because the plasticized grade has low melt strength, line speed is kept below 30 m/min to avoid sag in the vacuum calibration trough. After wrapping, a transparent polyurethane or co-polyamide cover may be applied; the PA11 substrate provides the working pressure barrier and the cover supplies cut and ultraviolet protection. Long-term pressure retention at 0.8 MPa air pressure is tested to ISO 1402, with elongation of the assembly measured under 10 % axial strain. The operational limit in dry compressed-air service is governed by oxidative embrittlement of the plasticized layer; heat aging to ISO 188 at 120 °C for 168 h is therefore used to screen batches for signs of surface cracking before release. Published data for this specific hose configuration is limited, so burst-pressure values after long-term hot air exposure must be generated on the final assembled hose rather than inferred from pellet properties.
Competitive Arkema Rilsan BESNO P40 TLO PA11 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 Rilsan BESNO P40 TLO is a plasticised polyamide 11 (PA11) grade supplied as natural granules for melt processing. The polymer backbone is synthesised from 11-aminoundecanoic acid derived from castor oil, giving a renewable carbon fraction typically reported at 98% by ASTM D6866-24. The designation BESNO identifies the base PA11 chemistry, P40 denotes the plasticiser package, and TLO indicates a natural, light-stabilised formulation. The grade is intended for monolayer and multi-layer flexible tubing, hose liners, cable sheathing, and technical films. Compared with unplasticised BESNO TL, BESNO P40 TLO exhibits lower flexural modulus, higher elongation at break, and improved impact at sub-zero temperatures, while retaining the long-chain aliphatic polyamide resistance to hydrocarbon stress cracking, zinc chloride solutions, and aliphatic solvents.
In automotive air brake tubing, the grade is evaluated against SAE J844 and ISO 7628; in hydraulic and pneumatic control lines it is specified where dimensional stability, low extractables, and stress-crack resistance are required. The material can be run at similar melt temperatures to other PA11 grades, but the plasticiser reduces melt viscosity relative to BESNO TL and requires adjustment of barrel profiles, die land lengths, and melt pump settings to avoid surging.
The repeating unit contains ten methylene groups between amide linkages. This lower amide density relative to PA6 and PA66 is the main source of reduced moisture uptake. Saturation water uptake for BESNO P40 TLO is reported in the range 1.6–2.0% under ISO 62:2008, whereas PA6 and PA66 typically absorb 8–10% and 7–8% at saturation. The monomer is not obtained from C6 caprolactam or hexamethylene diamine; it is produced from castor oil via transesterification and cracking to 11-aminoundecanoic acid. Bio-based carbon content is therefore measured on the whole polymer by ASTM D6866-24. The P40 plasticiser may include petroleum-derived co-components, so the bio-based carbon content of the formulated product can be lower than that of the base PA11 resin.
Substitution of BESNO P40 TLO into an existing BESNO TL tube specification illustrates the design trade-offs. At 23°C and 50% RH, the tensile modulus is typically 20–30% lower than unplasticised PA11, which permits a tighter minimum bend radius in pneumatic control lines. At the same time, the plasticiser lowers the temperature at which permanent deformation under constant load becomes significant. Continuous service above 90°C should be validated by heat ageing according to ISO 188 and tensile retention measurements, because plasticiser migration can increase surface tack and reduce notched impact.
Production-scale conversion of this grade into fluid transport tubing frequently reveals three processing failure modes: die-face moisture marks from incomplete drying, diameter oscillation from screw surging when the plasticiser is not fully homogenised, and black specks from degraded material accumulating in the crosshead. These are controlled by a balanced barrel profile, a gear pump at the die, and purging with a low-viscosity PA11 or polyolefin purge at shutdown.
The values in Table 1 summarise typical ranges from the supplier technical datasheet and third-party certification summaries. They are not guaranteed minimums; mechanical values are generated under ISO 291 or as-dry conditions and vary with water content, thermal history, and specimen geometry.
| Property | Test method | Typical value or range |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.03–1.05 g/cm³ |
| Melting temperature | ISO 11357-3:2018 | 188–190°C |
| Tensile modulus | ISO 527-2:2012 | 1000–1200 MPa |
| Tensile strength at yield | ISO 527-2:2012 | 38–45 MPa |
| Nominal elongation at break | ISO 527-2:2012 | >250% |
| Charpy notched impact at 23°C | ISO 179-1/1eA | 6–9 kJ/m² |
| Vicat softening temperature | ISO 306:2022 | 150–165°C |
| Water absorption at saturation | ISO 62:2008 | 1.6–2.0% |
| Melt volume-flow rate | ISO 1133-1:2022, 235°C/2.16 kg | 1.0–2.5 cm³/10 min |
The property set places the grade closer to flexible PA12 in modulus while retaining the PA11 melting point near 189°C. Unplasticised BESNO TL is generally reported near 1400 MPa tensile modulus under ISO 527-2. The modulus reduction in BESNO P40 TLO is therefore approximately 20–30%. The plasticiser also increases elongation at break; however, it can increase the permeation rate of low molecular weight hydrocarbons. Emission-sensitive fuel lines should be qualification-tested under SAE J2260 or SAE J1737 on finished tube, because extrusion draw ratio, wall thickness, and plasticiser distribution affect permeation.
Differences from PA12 are measurable in thermal and environmental terms. PA12 melts near 178°C and has density near 1.01 g/cm³; PA11 melts near 189°C and provides a higher temperature margin in underhood air brake and fuel line routing. The renewable carbon content of PA12 is typically lower unless bio-based feedstocks are specifically used. Differences from PA6 and PA66 are dominated by moisture absorption: PA66 can absorb 7–8% at saturation compared with 1.6–2.0% for this grade, leading to greater dimensional change and modulus drift in humid service.
Residual moisture control remains mandatory. The supplier processing guide specifies drying at 80°C in a desiccant dryer with a dew point of −40°C or lower for 4–6 h, targeting residual moisture below 0.08%. On a 25 mm co-rotating twin-screw extruder with L/D 30:1, undried material at ambient relative humidity above 60% generates splay and melt-pressure drift because steam hydrolyses amide linkages at melt temperatures above 240°C. A typical barrel profile runs from 220°C in the feed zone to 250°C in the metering zone; the measured melt temperature should not exceed 260°C for residence times beyond 6 min. At 290°C, chain scission and plasticiser volatilisation are rapid and produce yellowing, lower melt viscosity, and acidic degradation products.
Single-screw extruders below L/D 24:1 may not provide sufficient mixing when regrind exceeds 20 wt%. Any such blend should be validated by ISO 1133-1:2022 MVR and ISO 179-1 impact data before production. Open containers stored at 50% RH for more than 8 h should be re-dried. The equilibrium moisture content of PA11 at 50% RH is approximately 1.1%, but melt processing requires only 0.08%, so even visually dry granules can carry enough water to cause hydrolysis.
For injection moulding, melt temperatures of 230–260°C and mould temperatures from 30°C to 60°C are typical. Clamp force is calculated from the projected area using a peak cavity pressure of 400–600 bar; no grade-specific derating factor is published. The semi-crystalline solidification rate of PA11 is lower than that of PA66, so packing pressure should be maintained until gate freeze and hot-runner channels should avoid stagnant zones that extend residence time.
Long-chain PA11 is resistant to aliphatic and aromatic hydrocarbons, hot oils, ester-based hydraulic fluids, and many chloride salt solutions. The grade can be considered for hydraulic hose inner liners and diesel fuel lines where fluid contact is continuous but not strongly aqueous acidic. Immersion testing according to ISO 175:2020 should be performed on finished parts rather than granules, because orientation and crystallinity generated during extrusion change sorption kinetics. The grade is not recommended for continuous contact with concentrated mineral acids, formic acid, phenols, and strong oxidising agents. PA11 is soluble in phenol and strong acids; aqueous acidic conditions above 40°C accelerate hydrolysis. Alcohol-blended gasoline above E10 can plasticise the amorphous phase and increase permeation. Published data for this specific P40 configuration in methanol-containing fuels beyond E10 is limited; qualification on the final tube or hose is required.
Long-term heat ageing of P40-modified PA11 should be conducted at candidate service temperatures because the plasticiser can migrate toward the surface over time. A typical accelerated test is 1000 h at 100°C in an air-circulating oven according to ISO 188 followed by tensile retention and visual assessment. Retention of at least 70% tensile strength is a common internal acceptance criterion, but OEM specifications vary. In thin-wall tube, surface plasticiser loss may reduce notched impact before bulk tensile properties decline.
Regulatory statements are lot-level. The natural PA11 base resin is generally supported under chemical inventories, but the P40 package includes additives that may require substance-of-concern screening under REACH and 2011/65/EU Annex II. Food-contact status for a plasticised grade cannot be assumed from the base polymer; migration testing under EU Regulation 10/2011 or 21 CFR 177.1500 must cover the full formulation. The grade should not be combined with phenolic additives, strong acid catalysts, or oxidising agents in masterbatch or regrind streams.