| HS Code | 535668 |
| Material | Arkema Rilsan BMNO P20 TLD PA11 (Polyamide 11) |
| Density | 1.02 g/cm³ |
| Melting Point | 186 °C |
| Glass Transition Temperature | 45 °C |
| Tensile Strength | 48 MPa |
| Tensile Modulus | 1450 MPa |
| Elongation At Break | 50% |
| Flexural Modulus | 1200 MPa |
| Charpy Impact Strength Notched | 10 kJ/m² |
| Shore Hardness | 70 Shore D |
| Water Absorption Saturation | 1.8% |
As an accredited Arkema Rilsan BMNO P20 TLD PA11 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied as 20 kg net in a sealed, moisture-protective cardboard box with a polyethylene liner for safe storage. |
| Container Loading (20′ FCL) | 20′ FCL loading of Arkema Rilsan BMNO P20 TLD PA11: palletized, securely braced, sealed container for safe transport. |
| Shipping | Arkema Rilsan BMNO P20 TLD PA11 is a polyamide powder shipped as non-hazardous material. It should be transported in sealed, moisture-proof packaging to prevent clumping. Keep dry, away from heat and ignition sources. Standard freight is acceptable, with no special transport classification required. |
| Storage | Store Arkema Rilsan BMNO P20 TLD PA11 powder in its original sealed container, in a cool, dry, well-ventilated area away from heat, open flames, and direct sunlight. Keep tightly closed to prevent moisture absorption, since PA11 is hygroscopic; use desiccant if necessary. Ideal storage temperature is 15–25°C. Avoid exposure to humidity to maintain powder flow and print quality. |
| Shelf Life | Shelf life is typically two years when stored unopened in original packaging in a cool, dry place. |
In mono-layer and coextruded automotive fuel system tubing, Arkema Rilsan® BMNO P20 TLD PA11 is processed as the hydrocarbon-contact layer in fuel feed, return, vapor purge, and filler-neck vent lines. The pre-extrusion drying step uses a desiccant dryer at 80 °C to 90 °C for 4 h to 6 h, with a supply air dew point of -30 °C or lower; residual moisture above 0.08 wt% produces surface splay and a measurable drop in melt viscosity during the run. Single-screw extrusion on a barrier screw with a 30:1 L/D ratio and a vacuum vent at -0.08 MPa gauge permits processing between 230 °C and 250 °C, while die head temperature is held 10 °C to 15 °C below the final barrel zone to suppress melt fracture. In coextruded constructions, the BMNO P20 TLD layer is paired with an EVOH barrier core and tie layers; the outer layer is selected for abrasion and clip retention. Tube validation follows SAE J2260 for low-permeation nonmetallic fuel system tubing, with additional chemical resistance screening in Fuel C, CE10 and CM15 according to ISO 175 at 60 °C for 168 h. Low-temperature impact fixtures are conditioned at -40 °C for 4 h before burst and drop-weight testing. The terminal parts are formed by hot-knife cutting, cold sawing, and heated-collar barbing; the plasticized PA11 retains enough ductility for barbed quick-connect assembly without stress whitening at the undercut radius.
Coiled air brake tubing made from BMNO P20 TLD PA11 is extruded at a slightly lower melt-temperature band of 220 °C to 240 °C because the downstream coil former imposes a fixed-strain geometry at the mandrel contact points. The critical failure mode at fleet level is not initial burst but gradual outer-wall cracking at the coil apex after accumulated ozone and thermal cycling. Tubing is sized in a vacuum calibration sleeve at -0.02 MPa to -0.04 MPa gauge, quenched in water at 15 °C to 25 °C, and coiled onto a rotating mandrel maintained at 80 °C to 100 °C to reduce frozen-in stress. Validation follows SAE J844 for air brake tubing, including burst-pressure retention at -40 °C and 100 °C, plus boiling-water and compressed-air aging cycles. Impact after conditioning is measured on the finished coil assembly rather than straight tube specimens because the mandrel-set curvature changes wall eccentricity by 0.02 mm to 0.05 mm depending on extrusion rate. Gear-pump suction pressure is maintained between 3 MPa and 5 MPa to stabilize the melt stream into the die; a residence time in the barrel beyond 12 min accelerates yellowing and reduces burst retention after 1,000 h of heat aging at 100 °C. The finished assemblies are fitted with push-in couplings and support-coil lugs, and the terminal application is a tractor-trailer service brake or emergency brake line bundle.
Extrusion of liner stock for unbonded flexible risers shifts the process bottleneck from dimensional speed to melt-sag resistance across a thick annular cross-section. BMNO P20 TLD PA11 is processed through a large-diameter annular die with a wall thickness range of 5 mm to 15 mm; the die gap is set 1.5 mm to 2.5 mm below the target final wall to compensate for die swell and calibration shrinkage. Melt temperatures are held at 235 °C to 250 °C, but the outer die lip temperature is reduced by 5 °C to 10 °C relative to the inner body to build a surface skin that resists gravitational sag before the first cooling bath. Cooling water enters at 10 °C to 20 °C and is applied progressively, because quenching too rapidly freezes in low crystallinity and reduces barrier performance, while slow cooling increases crystallinity but can lock in internal voids in thick walls. The liner is the pressure-retaining barrier in flexible risers and flowlines designed under API 17J and ISO 13628-2. Sour-service and methanol exposure are project-specific; publicly available qualification data for this specific plasticized PA11 formulation in high-sour gas riser liner service is limited, and compatibility is evaluated on a case-by-case basis. The terminal product is the inner pressure sheath inside an unbonded flexible pipe, over which steel armour layers are subsequently wound. Residual plasticizer migration into the contact surfaces of carcass tooling is controlled by wiping the liner external surface with stearate-free process aids only after full solidification.
| Conversion line | Pre-drying | Melt temperature | Tooling or bath temperature | Primary control limit |
|---|---|---|---|---|
| Automotive fuel tube extrusion | 80 °C to 90 °C, 4 h to 6 h | 230 °C to 250 °C | Die 215 °C to 235 °C | Residual moisture ≤0.08 wt% |
| Truck air brake helix coil | 80 °C, 4 h | 220 °C to 240 °C | Mandrel 80 °C to 100 °C | Barrel residence ≤12 min |
| Flexible riser inner liner | 90 °C, 6 h | 235 °C to 250 °C | Cooling water 10 °C to 20 °C | Wall sag ≤0.5 mm per linear metre |
| Industrial cable jacket | 80 °C, 4 h | 220 °C to 240 °C | Core preheat 60 °C to 80 °C | Draw-down ratio ≤1.5:1 |
| Hydraulic or pneumatic tube | 80 °C, 4 h | 230 °C to 245 °C | First bath 30 °C to 40 °C | Annealing 120 °C, 2 h to 4 h |
| Injection-moulded coupling body | 80 °C, 4 h to 6 h | 240 °C to 260 °C | Mould 30 °C to 60 °C | Regrind ≤20 wt% |
Jacketing of signal, control, and fibre-optic cables for rail rolling stock and offshore platforms uses the same BMNO P20 TLD PA11 in pressure-extrusion tooling to fill interstices and exclude air from the cable core. The conductor bundle is preheated to 60 °C to 80 °C immediately before the crosshead, preventing a cold core from quenching the inner jacket surface and creating shrink-back during thermal cycling. Melt temperature is kept between 220 °C and 240 °C; draw-down ratio is set below 1.5:1 to retain impact strength in thin walls. For outdoor installations, a carbon black masterbatch is metered at 2 wt% to 3 wt% final concentration; the masterbatch carrier must be PA11-compatible to avoid hard-spot formation at the die. Compliance for mechanical properties is assessed under IEC 60811-501 for tensile and elongation of sheathing compounds, and flame classification is documented as UL 94 HB where the application requires a general-purpose horizontal burn rating. The terminal parts are continuous cable jackets over twisted pairs, triads, or optical fibres, often printed with ink-jet markers after a corona surface treatment of 40 mN/m to 48 mN/m. The processing window is comparatively wide compared with fuel tubing because the residual moisture specification and melt-temperature limits are the only hard constraints; the jacket wall is normally 0.3 mm to 1.2 mm, and the line speed is adjusted to maintain a constant outer diameter within 0.1 mm.
If the terminal operation bends hydraulic and pneumatic tube at ambient temperatures below -10 °C, the cooling rate during sizing becomes the primary variable governing stress-crack resistance. Tube made from BMNO P20 TLD PA11 is extruded at 230 °C to 245 °C, then passed through a two-stage water bath where the first stage is held at 30 °C to 40 °C and the second stage at 15 °C to 20 °C. This staged quench raises crystallinity at the outer skin while preserving a ductile core, reducing the tendency for outer-surface whitening at the bend extrados. Post-extrusion conditioning in a forced-air oven at 120 °C for 2 h to 4 h stabilizes the crystalline phase, but treatment beyond 4 h increases stiffness to a level that may exceed the allowable insertion force for push-in fittings. Burst testing follows ISO 7628 for thermoplastic tubing in air brake systems and is supplemented by fatigue cycling under hydraulic pressure between 0.5 MPa and 12 MPa at 60 °C when the tube is used in mobile hydraulic return lines. Compatibility with phosphate ester and glycol-based fluids is screened by immersion at 80 °C for 168 h using ISO 175; weight change, elongation retention, and surface tack are recorded. The terminal parts are pre-bent hydraulic return tubes, pneumatic control lines, and lubrication lines on construction and agricultural equipment. This is one of the deeper processing windows because the barrier properties of PA11 become increasingly sensitive to crystallinity when wall thickness drops below 1.0 mm, and the plasticizer in BMNO P20 TLD can migrate to the surface if the tube is annealed while contaminated with cutting-fluid residues.
Injection moulding of fuel vapour couplings, cable ties, and pneumatic connector bodies from BMNO P20 TLD PA11 requires a melt-residence-time control that tubular extrusion does not impose. The dried pellets are processed at melt temperatures of 240 °C to 260 °C, with the lower half of the range preferred for thin-wall connectors to avoid flash and the upper half used only when moulding long glass-free flow paths above 60 mm. Mould temperature is maintained between 30 °C and 60 °C; tools with hot-runner tips above 80 °C can accelerate surface discolouration if the shot-to-shot pause exceeds 30 s. Screw recovery is set to 0.2 m/s to 0.4 m/s peripheral speed, and back pressure is held at 0.5 MPa to 1.0 MPa to homogenize the melt without excessive shear heating. Regrind use is limited to 20 wt% maximum, and the regrind fraction must be re-dried to the same 0.08 wt% residual moisture threshold as virgin material; exceeding 20 wt% can shift the melt flow index measured under ISO 1133-1:2022 beyond the supplier-controlled lot band. Tensile strength and elongation of moulded specimens are checked against ASTM D638, and low-temperature impact of the finished coupling is assessed at -40 °C using a notched specimen geometry agreed with the tier-one buyer. The terminal parts are assembled into quick-connect fuel fittings, wire harness retention clips, and push-button connectors. Silicone-based mould release agents are avoided because they reduce the weld-line strength of barbed bosses and interfere with later ultrasonic welding. The primary processing risk is gas entrapment in thick bosses, controlled by a shot-size cushion of 2 mm to 4 mm and a holding profile that decays from 60 MPa to 25 MPa over 3 s to 5 s.
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Arkema Rilsan BMNO P20 TLD is a polyamide 11 (PA11) powder coating grade derived from 11-aminoundecanoic acid obtained from castor oil. The product is supplied as a fine powder for electrostatic spray and fluidized-bed application to metal substrates, where it forms a semi-crystalline thermoplastic coating after fusion and cooling. The grade designation identifies a controlled particle size distribution and surface treatment intended for application uniformity in electrostatic coating lines. As a PA11 material, it combines a relatively low density of 1.03–1.05 g/cm³ per ISO 1183-1, a melting peak of 183–187 °C per ISO 11357-3, and a measurable renewable carbon content above 98% when assessed by ASTM D6866. These characteristics position BMNO P20 TLD in corrosion-resistant coating applications for metal parts, including dishwasher baskets, automotive fluid-handling components, and industrial pipe fittings.
Powder particle size distribution controls transfer efficiency, edge coverage, and film smoothness in electrostatic spray operations. The P20 designation corresponds to a fine particle size cut with a typical median particle size near 20 µm when measured by laser diffraction per ISO 13320, although lot-to-lot variation should be confirmed against the manufacturer’s certificate of analysis. Fine powders with a d50 near 20 µm improve film leveling under low film thickness conditions but can be sensitive to humidity-induced agglomeration. In corona-charging systems operating at 70–100 kV, particles below 10 µm tend to produce overspray and reduced first-pass transfer efficiency, while particles above 80 µm may deposit with excessive surface roughness. Reclaim systems using cyclonic recovery and sieving at 125 µm are generally specified to remove agglomerates and coarse contamination without excessively stripping the fines fraction needed for good edge coverage. Production-scale electrostatic lines report that transfer efficiency drift can occur when the d50 shifts by more than ±5 µm across batches because charging and aerodynamic behavior are both particle-size-dependent. The resulting film thickness is typically controlled in the 80–300 µm range for corrosion service, with higher builds reserved for impact- or erosion-prone areas.
Melting behavior of this semi-crystalline polyamide is characterized by differential scanning calorimetry according to ISO 11357-3, with the principal endotherm appearing between 183 °C and 187 °C. Crystallization exotherm temperature and enthalpy should be monitored because rapid cooling from melt can suppress crystallinity and alter barrier properties. Density values for PA11 are lower than those of PA6 and PA66, which reduces mass per coated part at equivalent film thickness. Water absorption of PA11 under immersion at 23 °C for 24 h is approximately 0.3% by ISO 62, with saturation values commonly cited in the 1.7–1.9% range at 50% RH and 23 °C. These moisture uptake levels are significantly below those of PA6 and PA66 and support dimensional stability in humid service environments, although they still require pre-drying of the powder before electrostatic application when the material has been stored at relative humidity above 60%.
In fluidized-bed dipping operations, the metal component is preheated to a surface temperature above the PA11 melting point, commonly in the 300–350 °C range depending on section thickness and heat capacity. Immersion time is typically 2–10 s, after which the component is removed and allowed to complete fusion and leveling in a post-heat oven. If the preheat temperature is too low, the powder sinters without fully coalescing, producing a porous coating with poor adhesion. If the temperature exceeds 380 °C, visible discoloration and oxidation of the PA11 can occur before the film has stabilized. For electrostatic spray coating, the substrate is usually preheated to 200–230 °C and coated in multiple passes to build film thickness without excessive melt flow. Cure schedules of 190–210 °C for 5–10 min are representative for PA11 powder coatings, but thermal mass, line speed, and substrate geometry require validation by differential scanning calorimetry or solvent resistance testing. Substrate preparation is critical: grit-blasting to Sa 2.5 per ISO 8501-1 with an angular profile of 50–100 µm is typically specified for carbon steel, followed by degreasing and optional zinc phosphate or iron phosphate pretreatment. Inadequately profiled surfaces produce adhesion failures detectable by ISO 2409 cross-cut testing.
Published mechanical data for unreinforced PA11 indicate a tensile stress at break of approximately 50–55 MPa per ISO 527-2, elongation at break exceeding 200%, and flexural modulus in the 1000–1200 MPa range per ISO 178. The coating form of BMNO P20 TLD cannot be directly equated to bulk tensile specimens, but these polymer values provide an upper-bound reference for cohesive strength. Impact resistance of PA11 coatings at low temperature is generally superior to that of PA66 coatings, with notched Charpy testing of PA11 often reported in the range of 4–6 kJ/m² at -40 °C by ISO 179-1. Abrasion resistance is evaluated on coated panels by ASTM D4060 using CS-17 wheels, although published data for this specific configuration is limited and must be generated on the actual substrate and film thickness. Chemical resistance is broad against aliphatic hydrocarbons, oils, and salt solutions, but strong mineral acids, phenol, and concentrated formic acid attack PA11. The coating should not be specified for continuous immersion in aggressive solvents without immersion testing per ISO 2812-1.
| Property | Test method | Typical PA11 value |
|---|---|---|
| Melting temperature | ISO 11357-3 | 183–187 °C |
| Density | ISO 1183-1 | 1.03–1.05 g/cm³ |
| Tensile stress at break | ISO 527-2 | 50–55 MPa |
| Elongation at break | ISO 527-2 | >200% |
| Flexural modulus | ISO 178 | 1000–1200 MPa |
| Water absorption, 24 h immersion | ISO 62 | 0.3% |
| Water absorption, saturation at 50% RH | ISO 62 | 1.7–1.9% |
The selection of PA11 over PA12, PA6, or PA66 for a coating resolves to four measurable differences: melting point, moisture uptake, low-temperature impact behavior, and renewable carbon content. PA12 has a lower melting point near 176–180 °C and slightly lower density, but PA11 provides a somewhat higher thermal resistance and a comparable chemical resistance profile. PA11 also exhibits a higher bio-based carbon content than PA12, which is produced from petroleum-derived laurolactam unless otherwise specified. PA6 and PA66 provide higher strength and stiffness, but their equilibrium moisture absorption of 8–10% by ISO 62 can cause dimensional instability in humid service. PA11 retains superior elongation and lower density, which reduces embrittlement risk in thin-film coatings subjected to thermal cycling. The table below summarizes typical published ranges for unreinforced grades; these values are not direct coating specifications but illustrate the polymer-level differences that influence coating performance.
| Property | PA11 | PA12 | PA6 | PA66 |
|---|---|---|---|---|
| Melting temperature, ISO 11357-3 | 183–187 °C | 176–180 °C | 220–225 °C | 255–265 °C |
| Density, ISO 1183-1 | 1.03–1.05 g/cm³ | 1.01–1.03 g/cm³ | 1.12–1.14 g/cm³ | 1.13–1.15 g/cm³ |
| Water absorption at saturation | 1.7–1.9% | 1.5–1.7% | 9–10% | 8–9% |
| Flexural modulus, dry | 1000–1200 MPa | 900–1100 MPa | 2300–2800 MPa | 2700–3000 MPa |
| Elongation at break, dry | >200% | >200% | 50–100% | 20–40% |
Neutral salt spray performance of PA11 powder coatings is highly dependent on film thickness, substrate preparation, and cure completeness. Typical industrial specifications for PA11-coated steel in atmospheric corrosion service require a minimum dry film thickness of 250 µm and evaluate performance by ISO 9227 neutral salt spray for 1000 h or longer. Published data for BMNO P20 TLD in this specific configuration is limited, so qualification testing on the production substrate is required. Adhesion after exposure is assessed by ISO 2409 cross-cut and pull-off testing per ISO 4624, with acceptable systems typically retaining substrate adhesion without blistering or under-film corrosion. The coating also provides electrical insulation, with surface resistivity often exceeding 1012 Ω, although anti-static modifications may be required where electrostatic discharge is a concern. Edge coverage is a known limitation for powder coatings; sharp edges can exhibit reduced film thickness and should be radiused or coated with a reinforced tie layer to avoid premature corrosion.
Moisture absorption influences not only dimensional stability but also electrostatic behavior and powder flow. BMNO P20 TLD should be stored in sealed containers at temperatures below 30 °C and relative humidity below 60%. If the powder is exposed to ambient humidity above 60% RH for more than 24 h, pre-drying in a dry-air oven at 80 °C for 4–6 h is commonly recommended to restore free-flowing behavior. Overdrying above 90 °C can cause partial sintering of fine particles and should be avoided. The powder is thermoplastic and does not undergo chemical crosslinking, so it should not be blended with amine-based thermoset curing agents, epoxy resins, or reactive accelerators used in epoxy or polyester powder systems. Contamination with even 1–2 wt% of other powder chemistries can cause cratering, delamination, or loss of PA11 crystallinity. Reclaim systems must be dedicated or thoroughly cleaned because inter-polymer contamination cannot be corrected by adjusting cure conditions. The material is also incompatible with strong oxidizing environments and certain phenolic compounds, which can cause chain scission and embrittlement at elevated service temperatures above 120 °C.
For regulatory documentation, Arkema Rilsan PA11 powder grades are generally accompanied by declarations covering EU Directive 2011/65/EU (RoHS Recast) and REACH Regulation (EC) No 1907/2006. Users must verify application-specific compliance, including food-contact status under 21 CFR 175.300 for resinous and polymeric coatings, because the formulated final system—not the raw powder alone—determines suitability. Halogen-free construction and absence of intentionally added per- and polyfluoroalkyl substances are frequently cited for PA11 coatings, but each batch-specific certificate of analysis should be checked before use. Material safety data sheets specify the respirable dust exposure limits for powder handling; production lines should use local exhaust ventilation and Class II dust collection equipment to keep airborne dust below 10 mg/m³ total particulate. The powder is not biodegradable under ambient conditions, but the PA11 base resin has a renewable carbon content above 98% by ASTM D6866, which is a documented difference from petroleum-derived PA6, PA66, and standard PA12.
Dishwasher basket coating lines provide a representative production-scale example of PA11 powder application. Steel wire baskets are degreased, grit-blasted, preheated in a gas-fired convection oven to 320–340 °C, and dipped into a fluidized bed of Rilsan BMNO P20 TLD. The hot metal fuses the fine powder into a continuous film, and auxiliary heating at 190–210 °C completes leveling. Film thickness is commonly specified at 250–400 µm to withstand detergent exposure and mechanical loading. In this application, the key processing limits are preheat uniformity across the wire basket and avoidance of powder contamination from lint or phosphate residues. Batch-to-batch particle size variation above ±5 µm in d50 can alter fluidization density and film build, making laser diffraction analysis per ISO 13320 a routine incoming-material check. When line speed is increased, insufficient post-heat residence time produces under-cured films that fail ISO 2409 adhesion testing after exposure to hot alkaline detergents. These production constraints define the practical operating window for the grade more narrowly than the polymer’s intrinsic thermal stability would suggest.