| HS Code | 477004 |
| Color | Black |
| Material Family | Polyamide 11 (PA11) |
| Density | 1.04 g/cm³ |
| Melting Point | 186 °C |
| Vicat Softening Temperature | 170 °C |
| Glass Transition Temperature | 40 °C |
| Tensile Modulus | 1400 MPa |
| Tensile Strength At Yield | 55 MPa |
| Elongation At Break | 280 % |
| Flexural Modulus | 1200 MPa |
| Notched Izod Impact At 23 C | 70 J/m |
| Shore Hardness D | 78 |
| Water Absorption At Saturation | 1.1 % |
| Heat Deflection Temperature At 0 45 Mpa | 150 °C |
| Flammability Ul94 | HB |
As an accredited Arkema Rilsan BESN BLACK P210 TL PA11-I 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 BESN BLACK P210 TL PA11-I, a black polyamide 11 powder/resin for industrial applications. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Arkema Rilsan BESN BLACK P210 TL PA11-I polyamide resin, packed on pallets, secured for safe transport. |
| Shipping | Arkema Rilsan BESN BLACK P210 TL is a PA11 thermoplastic granulate. Ship in sealed moisture-proof packaging to prevent humidity absorption. Keep dry, cool, and away from intense heat or ignition sources. It is non-hazardous under normal transport, but avoid dust accumulation and handle with standard industrial care. |
| Storage | Store Rilsan BESN BLACK P210 TL PA11-I in its original, unopened packaging in a cool, dry, well-ventilated area. Keep away from direct sunlight, heat sources, moisture, and oxidizing agents. Maintain temperatures below 25°C to prevent moisture uptake or degradation. Use sealed containers after opening, and protect from mechanical damage and contamination. Follow standard safe handling and disposal practices. |
| Shelf Life | Shelf life is approximately 2 years when stored sealed, dry, and cool in original packaging. |
Truck and trailer pneumatic brake circuits operating at a nominal service pressure of 8.5 bar with transient reservoir overpressures of 14.5 bar are produced in monolayer from Arkema Rilsan BESN BLACK P210 TL PA11-I because the grade combines low plasticizer volatility with −40°C cold impact resistance. The material is specified at 100 parts by mass; up to 20 wt% clean internal regrind may be incorporated when validated against SAE J844 burst and cold impact requirements, while external plasticizer addition is excluded because it reduces dimensional stability after 100°C heat ageing. Pre-drying is mandatory above 60% relative humidity: 80°C to 90°C for 4–6 h in a desiccant dryer with a dew point at or below −30°C to achieve residual moisture ≤0.10% measured by ISO 15512 Karl Fischer titration. Downstream extrusion uses a single-screw extruder with 25:1 to 30:1 L/D, a 2.5:1 compression ratio, vacuum venting at the metering zone, and a breaker plate with 80/120/80 mesh screen pack; barrel profile is 210°C to 235°C increasing toward the die at 230°C to 240°C. Melt temperature uniformity of ±5°C across the die, verified by immersion thermocouples, remains the controlling variable because local shear above approximately 1000 s⁻¹ at the die land generates surface melt fracture that cannot be corrected by downstream sizing. Vacuum calibration at −0.6 bar to −0.8 bar with closed-loop water temperature of 15°C to 25°C sets final ovality and internal bore closure. Terminal products include 6.35 mm × 4.30 mm, 8.00 mm × 6.00 mm, 10.00 mm × 8.00 mm, and 12.00 mm × 9.00 mm air brake lines cut to length with swaged brass fittings; end-use conformity is assessed against SAE J844, DIN 73378-1, and ECE R13 brake system approval protocols.
In offshore pressure sheath and subsea flowline liner production, the limiting variable is not melt viscosity but residual moisture because hydrolysis at melt temperatures above 240°C reduces molecular weight and creates microvoids that degrade explosive decompression resistance in sour gas service. Arkema Rilsan BESN BLACK P210 TL PA11-I is processed at 100 parts by mass without filler or external lubricant; carbon black is already dispersed as the compound’s UV and thermal stabilizer system. If masterbatch is added for lot-specific pigmentation adjustment, the dosage is held at ≤2.0 wt% of a PA11-compatible carrier to prevent melt inhomogeneity in thick walls from 4.0 mm to 15.0 mm. Compliance frameworks include API 17J / ISO 13628-2 for unbonded flexible pipe, ISO 13628-5 for umbilical components, and NORSOK M-710 qualification requirements for non-metallic sheath and seal materials where applicable. Drying to ≤0.08% residual moisture, measured via ISO 15512:2019, is tighter than automotive tubing practice because the downstream extrusion path uses a 24:1 to 30:1 L/D single-screw barrier line with melt pressure 150 bar to 250 bar and output limited by multi-stage water cooling rather than plastication. Barrel temperatures from 220°C to 245°C are held to a ±5°C window; a soak at 245°C beyond 20 min promotes oxidative yellowing and a decline in elongation at break verified by ISO 527-2 Type 1A specimens. Terminal product forms are pressure sheaths, subsea jumper liners, hydraulic control line cores, and umbilical tubes with outside diameters from 6 mm to 50 mm and wall thicknesses dictated by collapse and burst calculations. Published qualification data for this exact black P210 TL grade under API 17J Annex B rapid gas decompression testing are limited, so OEM-specific testing is required before service above 100 bar partial pressure.
| Parameter | Test standard | Boundary condition |
|---|---|---|
| Residual moisture for pressure sheath extrusion | ISO 15512:2019 | ≤ 0.08% by mass |
| Melt volume-flow rate release window | ISO 1133-1:2022 | 235°C / 2.16 kg; supplier lot certificate range |
| Dry density | ISO 1183-1:2019 | 1.03–1.05 g/cm³ |
| Dry tensile elongation at break | ISO 527-2 Type 1A | > 200% |
| Notched Charpy impact at −40°C | ISO 179-1/1eA | Report value against OEM acceptance |
In pneumatic logic and compressed-air distribution circuits with outside diameters from 4.00 mm to 16.00 mm, PA11-I is specified as a direct replacement for PA12 where lower equilibrium moisture regain and pressure retention at −20°C are design requirements. The resin is extruded at 100 parts by mass; ≤10 wt% clean edge trim is re-fed only after granulation and re-drying to ≤0.10% moisture. Process settings are typically 235°C melt temperature, 24:1 L/D single-screw, 0.8–1.0 bar vacuum sizing, and tri-axis laser diameter gauging at haul-off speeds up to 80 m/min. Terminal products include FRL manifold jumpers, robot arm airlines, push-in fitting tube ends, and corrugated protective sleeves. Dimensional conformance is assessed under ISO 14743 for push-in connector tube ends and ISO 4414 for pneumatic system safety.
Multilayer fuel and vapour return lines built around PA11-I as the inner hydrocarbon contact layer address the permeation threshold of SAE J2260 for heavy-duty diesel applications, particularly where low-temperature impact after fuel saturation must remain above the OEM acceptance limit at −40°C. In a three-layer construction, the PA11-I inner layer is specified at 25–40 parts by mass of total wall thickness, typically 0.30 mm to 0.50 mm; the middle EVOH barrier is 10–15 parts, and the outer plasticized PA12 or polyether block amide jacket supplies clip retention and abrasion resistance at 45–60 parts. If a monolayer fuel vapour return tube is retained, the material is processed at 100 parts by mass with ≤15 wt% clean in-house regrind and no additional external plasticizer. Downstream coextrusion requires three extruders with melt streams at 220°C to 240°C, a spiral mandrel die with layer sequencing sensors, and post-die vacuum calibration; residence time in the die adapter must remain below 90 s to limit PA11-I thermal oxidation. Terminal products are diesel fuel vapour return hoses, evaporative emission connectors, fuel tank vent lines, and heavy-duty engine crankcase ventilation tubes. Compliance verification includes SAE J2260, ISO 13775-1, and CARB/EPA evaporative emission leak-down protocols where applicable.
For offshore control umbilical and dynamic cable outer jackets, PA11-I is pressure-extruded at 100 parts by mass over a cable core, with 2.0–3.0 wt% carbon black masterbatch added only when the base resin lot is below target carbon black dispersion for UV endurance. The processing line uses a pressure extrusion crosshead, 24:1 L/D single-screw, melt temperature 230°C to 245°C, and a water trough length that limits line speed to 10–30 m/min for jacket wall thicknesses 1.5 mm to 4.0 mm. Terminal products are subsea control umbilical jackets, ROV tether cables, and offshore power cable sheathing. Performance is assessed under IEC 60092-359 for shipboard and offshore electrical cable sheath compounds, ISO 13628-5 for umbilical components, and where dynamic flexural fatigue applies, fatigue test protocols derived from API 17E remain project-specific rather than generic material certifications.
Within chemical transfer hose liners and pump diaphragm stock, PA11-I remains restricted to aliphatic hydrocarbon, diesel, hydraulic oil, and mild water-glycol service; aromatic solvents above 10% by volume and strong mineral acids fall outside the permissible operating envelope because plasticization and permeation losses accelerate once the fluid temperature exceeds 50°C. The resin is compounded at 100 parts by mass with 5.0–10.0 wt% of PA11-compatible internal lubricant only in injection-grade modifications; for extrusion-grade stock, the addition is 0.5–1.5 wt% processing aid to counter melt fracture in thin liners. Downstream processes include monolayer hose extrusion with a 25:1 L/D barrier screw at 225°C to 245°C, as well as calendering into diaphragm stock with subsequent compression molding at 230°C and 40–60 bar. Terminal products are diesel transfer hose liners, hydraulic oil suction and discharge tubes, pump diaphragm interlayers, and water-glycol cooling circuit hoses. Compliance is anchored to ISO 23936-1 for thermoplastics in oil and gas fluid service, with chemical resistance data generated by ISO 1817 immersion testing and post-immersion tensile retention measured by ISO 527-2.
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Arkema markets Rilsan BESN BLACK P210 TL as an impact-modified polyamide 11 extrusion material. The grade carries the classification PA11-I under ISO 1874-1, with the C11 aliphatic repeat unit and impact-modifier package distinguishing it from PA6, PA66, and PA12. The product is a carbon-black-pigmented formulation carrying the P210 viscosity designation and the TL stabilizer/lubricator package. It is used in monolayer tube and hose extrusion where low moisture uptake, fatigue resistance under flexural cycling, and processability on single-screw extruders are evaluated together. The printed Arkema datasheet and certificate of analysis remain the controlling documents for batch-specific values; the following sections reproduce engineering data anchored to ISO, ASTM, and DIN methods.
The model designation decodes as follows: BESN identifies the Arkema polyamide 11 base series, BLACK identifies carbon-black pigmentation, P210 identifies the melt-viscosity band used by Arkema for extrusion-grade PA11, and TL identifies the stabilizer and lubricant package. The PA11-I designation indicates impact modification under the ISO 1874-1 nomenclature. Published data for the exact black TL variant is often combined with the natural BESN P210 TL series in technical documentation. Processors should not assume identical rheology between natural and black variants because carbon-black pigmentation can alter thermal conductivity, melt viscosity, and surface appearance. For this specific grade, published data on the magnitude of that rheological shift is limited.
Table 1 lists representative values published for the Arkema BESN P210 extrusion family. The black-pigmented TL variant is typically specified within these ranges, but each shipment should be verified against the supplier certificate of analysis.
| Property | Test method | Typical value or range |
|---|---|---|
| Density at 23°C | ISO 1183-1 | 1.04 g/cm³ |
| Melting temperature, DSC, 10 K/min | ISO 11357-3 | 186–190°C |
| Water absorption, 24 h immersion at 23°C | ISO 62 | 0.6% |
| Water absorption at saturation in water at 23°C | ISO 62 | 1.8–2.0% |
| Tensile modulus | ISO 527-2/1BA | 1,150 MPa |
| Tensile stress at yield | ISO 527-2/1BA | 45 MPa |
| Nominal strain at break | ISO 527-2/1BA | >200% |
| Charpy notched impact at 23°C | ISO 179-1/1eA | No break or >30 kJ/m² |
| Shore hardness D | ISO 7619-1 | 74–78 |
The combination of a tensile modulus near 1,150 MPa and nominal strain at break above 200% under ISO 527-2/1BA places the material in the semi-rigid extrusion class. This balance supports tube bending without kinking, but it does not by itself qualify the finished tube for a given service pressure. Pressure rating must be calculated from wall thickness, temperature, and service factor according to the applicable line standard, such as ISO 7628-1 for air brake tubing or the end-user specification for hydraulic tube jackets.
Because the PA11 backbone contains fewer amide groups per unit mass than PA6 or PA66, equilibrium water absorption under ISO 62 is lower. That difference stabilizes tensile modulus across humidity changes and reduces the dimensional growth observed in PA6. However, the material is not hydrolytically inert. Pre-drying in a desiccant dryer at 80°C for 4–8 hours to a residual moisture content below 0.1% is recommended before melt processing. Moisture above 0.15% at melt temperatures above 230°C can produce hydrolysis-driven molecular weight loss, visible as surface roughness, melt-pressure drift, and a reduction in final tube burst strength.
Compared with PA6 extrusion grades, the C11 repeating unit in PA11-I reduces the amide-group density. Under ISO 62, PA6 reaches saturation water absorption near 9–10% by mass, whereas PA11 typically saturates at 1.8–2.0%. This difference produces different dimensional and dielectric stability in humid service. A PA6 tube can exhibit measurable diameter and length change after long-term water exposure, while a PA11 tube is expected to remain closer to its as-extruded dimensions. The exact linear growth for this specific black TL grade should be measured according to ISO 62 conditioning protocols because published data for the finished tube geometry is often project-specific.
Compared with PA12, PA11 has a higher melting point. The PA11 thermal range in Table 1 is 186–190°C under ISO 11357-3, while typical plasticized PA12 extrusion grades melt near 172–178°C. This higher thermal onset can be relevant for under-hood air tubing and fluid-transfer lines exposed to intermittent peak temperatures. The PA11-I impact-modifier package also shifts low-temperature fracture behavior relative to unmodified PA12 extrusion grades. Any direct substitution should compare notched Charpy data under ISO 179-1/1eA at the intended minimum service temperature, because impact-modifier efficiency is temperature-dependent and cannot be inferred from room-temperature data alone.
The black carbon-black pigmentation provides ultraviolet stabilization and long-term weathering resistance when evaluated under ISO 4892-2 or equivalent outdoor exposure standards. Natural PA12 or PA11 grades without a carbon-black package may require separate UV stabilization to meet the same surface-retention targets. This grade is not marketed as an electrically conductive compound; the carbon-black loading is formulated for pigmentation and UV protection rather than antistatic surface resistivity. Applications requiring conductive tubing should use a dedicated conductive PA11 grade and verify surface resistivity under IEC 60093.
For fuel or hydrocarbon service, PA11 is often evaluated because it can be qualified under ISO 23936-1 for oil and gas non-metallic materials. Published data for this specific BESN BLACK P210 TL configuration in aggressive sour hydrocarbon immersion is limited, so end users should require test reports generated under ISO 23936-1 or the applicable project specification. The grade is not a drop-in replacement for PA12 in every fuel-line system; permeation testing under SAE J2260 or ISO 13775-1 is required before substitution.
On a 45 mm single-screw extruder with L/D 30:1 and a compression ratio of 3:1 to 3.5:1, the feed throat is typically kept below 60°C to prevent pellet agglomeration. Barrel temperatures for PA11 extrusion usually start at 220°C in the rear zone and increase to 245°C at the die. A melt thermocouple reading above 270°C should be treated as a process deviation. At that point, oxidative degradation can generate black specks, gels, and drift in die pressure. The black pigment and impact modifier may make degradation products less visually obvious at first, so melt-pressure stability and final tube ovality are more reliable process indicators than color alone.
If the granulate is not pre-dried below 0.1% residual moisture, hydrolytic chain scission can reduce molecular weight during extrusion. The typical failure signature is a steady decrease in die pressure at constant screw speed, accompanied by an increase in die swell or a loss of dimension control. Batch-to-batch moisture content in freshly opened packaging is a more significant variable than usually assumed. Airtight packaging should not be interpreted as dry packaging, especially when storage has occurred below dew point or in unheated warehouses.
Regrind use requires conservative validation. Because the material contains an impact modifier and carbon black, repeated heat histories can shift melt viscosity and reduce low-temperature impact. A terminal regrind fraction above 20% should be supported by internal melt-flow and notched Charpy data under the same standards used for virgin material. Published data for this exact black TL grade under multiple regrind cycles is limited; processors should conduct a three-pass retention study before setting a production regrind limit.
Where hydrocarbon contact or sour service is required, PA11 grades are selected because they can be evaluated under ISO 23936-1 and API 17J for suitability in oil and gas equipment. For food-contact extrusion, the resin family may be referenced under FDA 21 CFR 177.1500 and EU Regulation No 10/2011, but the finished tube must satisfy the applicable overall and specific migration limits. Regulatory compliance under REACH and RoHS 2011/65/EU is product-grade and batch dependent. Table 2 summarizes the common compliance headings relevant to this material.
| Regulation or standard | Scope | Application boundary |
|---|---|---|
| FDA 21 CFR 177.1500 | Nylon resins for repeated food contact | Finished article migration testing required |
| EU Regulation No 10/2011 | Plastic materials and articles intended for food contact | Overall migration limit 10 mg/dm²; specific migration limits apply |
| REACH Regulation (EC) No 1907/2006 | Registration, evaluation, authorization, and restriction of chemicals | Supplier SDS controls SVHC disclosure and safe use |
| RoHS Directive 2011/65/EU | Restriction of lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE | Supplier declaration required per lot or grade |
| ISO 23936-1:2009 | Oil and gas non-metallic materials in sour service | End-user qualification and test report required |