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Arkema Rilsan BESNO P40 TLX NL PA11

    • Product Name: Arkema Rilsan BESNO P40 TLX NL PA11
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 137588
    Density 23 C 1.04 g/cm³
    Melting Point Dsc 186 °C
    Glass Transition Temperature -20 °C
    Tensile Modulus 700 MPa
    Tensile Stress At Yield 32 MPa
    Elongation At Break >300 %
    Flexural Modulus 700 MPa
    Charpy Impact Strength 23 C No break
    Shore D Hardness 55
    Vicat Softening Temperature 100 °C
    Water Absorption Saturation 2.5 %
    Volume Resistivity 1×10¹¹ Ω·cm

    As an accredited Arkema Rilsan BESNO P40 TLX NL PA11 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in a 20 kg sealed, moisture-protected polyethylene-lined cardboard drum: Arkema Rilsan BESNO P40 TLX NL PA11 powder.
    Container Loading (20′ FCL) 20′ FCL: palletized bags of Arkema Rilsan P40 TLX NL PA11, stowed dry, secured, protected from moisture and damage.
    Shipping Arkema Rilsan BESNO P40 TLX NL PA11 is a bio-based polyamide 11 resin supplied as granules. Ship in sealed, moisture-proof bags or drums, away from heat and direct sunlight. No special hazard classification; standard dry cargo transport is suitable. Keep dry and store below 50°C to prevent clumping.
    Storage Store Arkema Rilsan BESNO P40 TLX NL PA11 in a cool, dry, well-ventilated area, away from direct sunlight and heat sources. Keep the original container tightly sealed to prevent moisture absorption, which can affect powder flow and performance. Avoid humidity, static sparks, and incompatible materials. Use within shelf life per SDS.
    Shelf Life Shelf life is typically two years from shipment when stored sealed, cool, and dry in original packaging.
    Application of Arkema Rilsan BESNO P40 TLX NL PA11

    Why Fuel Vapor Line Extruders Replace High-Density Polyethylene with Plasticized PA11?

    Low-permeation fuel system tubing manufactured from BESNO P40 TLX NL is governed principally by SAE J2260 and, where European quick-connectors are specified, by DIN 73379-2; the resin is processed after dehumidifying-hopper drying at 80–90 °C for 4–6 h to a moisture content below 0.08% by weight. The formulation at the feed throat is typically 100 parts by weight of BESNO P40 TLX NL, with 0.5–1.5 phr of a processing-stabilizer masterbatch and 0–2 phr of carbon-black concentrate for UV resistance; if in-line regrind is introduced, the maximum recommended addition is 20 wt% because higher recycle fractions reduce low-temperature notched impact in finished tube. Extrusion is performed on a single-screw extruder with 30:1 L/D ratio and a barrier screw, with barrel temperatures profiled from 200 °C at the feed throat to 240 °C at the metering zone; melt temperature measured downstream of the breaker plate is maintained between 215 °C and 245 °C, while die-head pressure typically falls between 8 MPa and 14 MPa at line speeds above 20 m/min. Vent-port vacuum is kept below −0.08 MPa to strip residual moisture and low-molecular-weight volatiles, and melt residence time should not exceed 10 min to avoid thermo-oxidative degradation. Vacuum sizing in a closed-loop water tank at 15–25 °C sets outer diameter and wall thickness, and online laser gauges control tolerance to ±0.05 mm. Terminal components include gasoline feed lines, fuel-vapor return hoses, evaporative emission connectors, and quick-connect fuel-leak protection assemblies; continuous service is limited to temperatures below 90 °C in dry hydrocarbon environments because plasticizer migration accelerates above that boundary.

    In air-brake tube production, the melt is held between 225 °C and 240 °C on a single-screw line of 24:1–30:1 L/D with a low-shear metering screw and a gear pump to suppress pulsation. The relevant compliance specification is SAE J844, with cold-impact checks performed at −40 °C after conditioning; where truck air lines enter North American service, FMVSS 571.106 also applies. The extrusion blend is 100 wt% BESNO P40 TLX NL and 1.0–2.5 wt% blue PA-compatible color masterbatch; no external plasticizer is added because it can reduce burst strength and increase dimensional drift during hot parking. Pre-drying requires a desiccant dryer with dew point ≤ −40 °C to reach moisture below 0.08%, and residence time is not to exceed 4 h at 80 °C to avoid yellowing; storage in ambient relative humidity above 60% makes the pre-drying step mandatory. The downstream process uses vacuum calibration sleeves to hold outside diameter within ±0.05 mm, followed by a spray-cooling trough and a haul-off that maintains constant tension; melt-pressure variation at the gear-pump inlet should be held within ±0.5 MPa to prevent wall-thickness variation in long coils. Each coil is pressure-tested at 1.0 MPa and 1.5× working pressure before release. Terminal parts are heavy-duty truck air-brake tubing, trailer air lines, and coiled push-to-connect assemblies for pneumatic braking systems.

    When Cable Jacketing Requires Halogen-Free Char Formation at <1.6 mm Wall Thickness

    Jacketing lines configured with pressure tooling and double-flighted barrier screws are used to extrude BESNO P40 TLX NL over copper or optical-fiber cores at melt temperatures of 230–250 °C. The halogen-free character of PA11 permits compliance with IEC 60754-1 for acid-gas generation, IEC 61034-2 for smoke density, and IEC 60332-1-2 for vertical flame propagation on a single cable; railway specifications often require additional NF C32-070 C2 or equivalent flame-spread classification. The compound at the hopper contains 82–88 wt% BESNO P40 TLX NL, 10–15 wt% UV-stabilized PA11 masterbatch, and 2–5 wt% flame-retardant masterbatch; additions above 5 wt% of the flame-retardant masterbatch are not recommended because tensile elongation measured by ISO 527-2 can fall below 200%, threatening cold-bend flexibility. The polymer must be dried to below 0.06% moisture, normally for 4–6 h at 80–85 °C, before entering the extruder; melt filtration through a 60/80/60 mesh screen pack removes char and gel particles. A draw-down ratio between 1.4 and 2.2 is maintained through the crosshead, and cooling is staged from 60 °C to 20 °C to prevent vacuum voids. Terminal products include submersible pump cable jackets, robotic dress-pack cable sheaths, railway rolling-stock wire sheathing, and signal-cable jackets in tunnel installations.

    Subsea umbilical continuous-length extrusion campaigns using BESNO P40 TLX NL require moisture content below 0.06% before the melt reaches the metering zone, because dissolved water in PA11 generates bubbles and surface pitting at melt temperatures above 210 °C. The governing documents are API 17E or ISO 13628-5 for umbilical design and, where gas diffusion is critical, API 17TR8 guidance on permeation in thermoplastic sheaths. The feed composition is 100 phr BESNO P40 TLX NL, with 0.3–0.6 phr high-temperature antioxidant masterbatch and 0–0.4 phr external processing lubricant; regrind is not permitted in pressure sheath or hydraulic tube layers. Extrusion is performed on a 30:1 L/D single-screw line with melt pump, melt temperature held between 210 °C and 230 °C, and a multi-zone vacuum calibration unit controlling outer diameter to ±0.08 mm. The tube is cooled slowly from 40 °C to 15 °C to limit residual stress, then spooled under controlled tension below 1.0% strain. Terminal product types are subsea hydraulic control tubes, methanol injection lines, chemical dosing tubes, and fiber-optic cable sheaths in steel-tube umbilicals. Continuous wet service above 70 °C represents an operational boundary for plasticized PA11 unless hydrocarbon resistance is revalidated for the specific fluid.

    Pneumatic Control Line Burst Retention After Plasticizer Migration

    A reduction in burst pressure after 1,000 h at 80 °C is the primary failure threshold for PA11 pneumatic control lines, and testing is conducted at 1.5× working pressure in accordance with ISO 14743; tubing also is validated for compressed-air quality classes under ISO 8573-1. The dry-blend formulation for this application is 95–100 wt% BESNO P40 TLX NL, 0–5 wt% color masterbatch, and 0.2–0.6 phr anti-blocking additive to prevent coil blocking; no plasticizer is added externally because the grade is already plasticized. Extrusion occurs on a 20:1–24:1 L/D single-screw line with a three-zone vacuum tank and a laser gauge in closed-loop control; melt temperature is held between 220 °C and 240 °C, and the die gap is set to maintain a draw-down ratio below 1.8 to minimize frozen-in orientation. The pre-drying step uses a dew point ≤ −40 °C air stream for 3–5 h at 80 °C, reducing moisture to below 0.08%. Finished pipe is cut into coils or straight lengths and fitted with push-in connectors; terminal product types are factory compressed-air distribution lines, robotic air-feed tubes, lubrication tube assemblies, and pneumatic control line bundles.

    A 6-Layer Die Head Is Not Required for Non-Implantable Medical Tubing

    For non-implantable medical tubing, single-layer extrusion of BESNO P40 TLX NL is run in an ISO 14644-1 Class 8 cleanroom using polished stainless tooling, melt temperature between 210 °C and 225 °C, and HEPA-filtered air cooling instead of water contact to avoid surface contamination. Biocompatibility evaluation follows ISO 10993-1, and where the final device requires USP plastic-class designation, tests are run under USP <88> Class VI protocols; manufacturing quality systems fall under ISO 13485. The formulation uses 100 wt% BESNO P40 TLX NL, with optional barium sulfate radiopaque filler at 10–20 wt% when x-ray visibility is required; no external slip agent or mold-release additive is used because surface lubricants may interfere with solvent bonding or biocompatibility test results. The resin is dried to below 0.05% moisture at 75–85 °C for 4–6 h before extrusion, and the melt is filtered through a 40/60/40 mesh pack to remove agglomerates. Produced tube outer diameters range from 2 mm to 6 mm, and wall thickness is controlled to ±0.04 mm by laser gauge. Terminal products are fluid drainage tubes, respiratory pressure monitoring lines, non-implantable surgical device pneumatic tubing, and laboratory instrument tubing. Published comparative data on plasticizer migration in this specific non-implantable PA11 configuration is limited, so end-use validation under ISO 10993-1 is required before clinical placement.

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    Certification & Compliance
    More Introduction

    Arkema Rilsan BESNO P40 TLX NL PA11 is supplied as a natural-colour, plasticised polyamide 11 extrusion grade based on 11-aminoundecanoic acid chemistry. The polymer backbone carries a longer aliphatic chain than PA6 or PA66, which reduces amide-group density and limits equilibrium moisture uptake. Within Arkema nomenclature, the suffix P40 identifies the plasticised formulation, TLX identifies the thermal and extrusion stabilisation package, and NL denotes natural, uncoloured pellets. Incoming inspection for this product commonly records melt volume-flow rate under ISO 1133-1:2022 at 235 °C with a 2.16 kg load, density under ISO 1183-1, and moisture content by ISO 15512. The grade is specified primarily for continuous tube, hose, and profile extrusion, not for thin-wall high-flow injection moulding. Bio-based carbon content can be determined by ASTM D6866; published data for this specific plasticised formulation should be requested from the manufacturer.

    Property Standard Typical range or value
    Density ISO 1183-1 1.03–1.05 g/cm³
    Melt volume-flow rate ISO 1133-1:2022 10–20 cm³/10 min at 235 °C/2.16 kg
    Melting temperature ISO 11357-3 186–190 °C
    Tensile modulus ISO 527-2 600–750 MPa
    Yield stress ISO 527-2 24–28 MPa
    Nominal strain at break ISO 527-2 >50 %
    Charpy notched impact at 23 °C ISO 179/1eA >60 kJ/m²
    Shore D hardness ISO 868 62–68
    Vicat softening temperature, 10 N ISO 306/A50 130–150 °C
    Water absorption at saturation ISO 62 1.6–2.0 %

    The plasticised system reduces room-temperature tensile modulus relative to unplasticised PA11 from roughly 1200–1400 MPa to 600–750 MPa under ISO 527-2, while nominal strain at break remains above 50 %. Charpy notched impact at 23 °C according to ISO 179/1eA exceeds 60 kJ/m²; at −30 °C the material retains sufficient ductility for air-brake line impact tests, though grade-specific low-temperature data should be confirmed with the manufacturer.

    What Process Boundaries Govern Safe Melt Processing?

    Desiccant drying to ≤0.08 wt% moisture is mandatory before extrusion. Moisture above this threshold shifts the hydrolysis equilibrium during melt residence and produces surface splay, viscosity loss, and reduced burst strength in thin-wall tube. At 80 °C, drying time is typically 4–6 h in a desiccant dryer with a dew point below −30 °C; at 90 °C, time may be shortened to 3–4 h, but temperatures above 100 °C can tack pellets and bridge the hopper. In a 30:1 L/D single-screw extruder fitted with a 3:1 compression barrier screw, the barrel profile runs from 210 °C at the feed throat to 240 °C at the die, with melt temperature at the die adapter not exceeding 250 °C. Vacuum venting at −0.08 MPa removes residual water and volatile plasticiser fractions; an open vent without vacuum is insufficient when ambient humidity exceeds 60 % RH.

    Lot-to-lot variation in plasticiser dispersion has been observed on production tube lines as a die-pressure shift of approximately 5–10 % at constant screw speed. Melt pressure upstream of the screen pack should therefore be recorded against the initial qualifying lot. A 600 µm screen pack upstream of a gear pump is common for thin-wall tube applications to remove carbonised fines and stabilise output. Extended holdup at melt temperatures above 250 °C accelerates thermo-oxidative chain scission and increases carbonyl index measured by infrared spectroscopy. On thin-wall tube lines, the practical melt-temperature window is approximately ±5 °C around 240 °C because lower temperatures produce melt fracture and higher temperatures generate die deposit.

    In automotive air-brake tubing, the product is selected because it combines low-temperature impact with resistance to zinc chloride road de-icing salts. Qualification work typically follows SAE J844 and Federal Motor Vehicle Safety Standard No. 106; the material is evaluated under the burst, collapse, and zinc chloride resistance clauses of those standards. For fuel-line systems, the grade is used as a flexible monolayer or as the outer jacket in multi-layer constructions. In monolayer form, hydrocarbon permeation is governed by wall thickness and test temperature under SAE J1737; where evaporative emission limits of the applicable regional regulation are more stringent, coextrusion with a polyolefin tie layer and an EVOH or fluoropolymer barrier is used. Flexible riser and offshore umbilical liners based on PA11 are qualified under API 17J and ISO 13628-2; published qualification data for this exact plasticised grade in sweet and sour hydrocarbon service are more limited than for unplasticised PA11 liner grades. For continuous immersion in produced water at 60 °C or higher, long-term hydrolysis resistance data should be requested.

    When PA12 or Unplasticised PA11 Is Evaluated as a Replacement

    Material Density (ISO 1183-1) g/cm³ Tensile modulus (ISO 527-2) MPa Melting temperature (ISO 11357-3) °C Water absorption at saturation (ISO 62) %
    Rilsan BESNO P40 TLX NL 1.03–1.05 600–750 186–190 1.6–2.0
    Unplasticised PA11 extrusion grade 1.04 1200–1400 188–190 1.7–1.9
    Plasticised PA12 extrusion grade 1.01–1.02 450–650 175–178 0.7–0.8

    Substitution is not a drop-in operation. Compared with unplasticised PA11, BESNO P40 TLX NL reduces room-temperature modulus by approximately 50 % and improves cold impact, but the plasticiser package lowers the upper service temperature and can increase time-dependent deformation under compressive load when tested according to ISO 815. Compared with plasticised PA12, the PA11 grade has a higher melting temperature and a renewable-carbon advantage; PA12 retains lower water absorption and lower density but crystallises at a different rate and requires downstream tooling adjustments. Published data for direct substitution in bonded fuel-line assemblies using polyolefin tie layers is limited.

    Compliance Standards and Material Handling Boundaries

    Material certification for food-contact, drinking-water, or medical use is not inferred from the NL suffix. When required, supplier confirmation should reference Regulation (EU) No 10/2011 Annex I and FDA 21 CFR §177.1500 for nylon resins; the plasticiser package may alter extractables and must be tested under the intended end-use condition. REACH registration is maintained under Regulation (EC) No 1907/2006; RoHS Directive 2011/65/EU Annex II restrictions apply to electrical and electronic equipment. The natural-colour grade does not contain intentionally added restricted phthalates, but a supplier statement should be obtained for each production site. For potable-water installations, confirm the specific formulation against NSF/ANSI 61 or equivalent because plasticiser migration may be the governing limit.

    Storage of unopened bags should be below 30 °C and below 60 % RH. Opened bags must be re-sealed with desiccant or consumed within four hours when ambient humidity exceeds 60 % RH. The grade is not UV-stabilised in natural colour; long-term outdoor exposure requires carbon-black masterbatch or a coextruded UV barrier. Contact with strong mineral acids, hot concentrated polar solvents, or phenols at elevated temperature attacks the polyamide backbone. Compatibility with methanol, ethanol, and glycol-based fluids should be verified under ISO 1817 or ASTM D543 because plasticiser extraction can change wall dimensions and low-temperature flexibility.

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