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Arkema Rilsan D50 NATURAL PA11

    • Product Name: Arkema Rilsan D50 NATURAL 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 859073
    Density 1.04 g/cm³
    Melting Point 189 °C
    Vicat Softening Point 165 °C
    Tensile Strength At Break 34 MPa
    Elongation At Break 350 %
    Flexural Modulus 600 MPa
    Shore D Hardness 63
    Charpy Impact Strength No break
    Water Absorption At Saturation 1.6 %
    Volume Resistivity 1.0e14 Ohm·cm
    Dielectric Strength 30 kV/mm
    Molding Shrinkage 0.8 %

    As an accredited Arkema Rilsan D50 NATURAL PA11 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Arkema Rilsan D50 NATURAL PA11 is supplied in a sealed 25 kg cardboard box containing natural polyamide 11 powder for industrial use.
    Container Loading (20′ FCL) Loading 20' FCL with Arkema Rilsan D50 NATURAL PA11 in 25kg bags, palletized and secured for transport.
    Shipping Arkema Rilsan D50 NATURAL PA11 is a fine polyamide 11 powder shipped in sealed, moisture-resistant packaging. Avoid exposure to humidity, heat, and static ignition sources. Transport in dry, ventilated conditions. Handle with care to prevent dust generation and maintain product integrity during delivery.
    Storage Store Arkema Rilsan D50 NATURAL PA11 in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep the original container tightly sealed to prevent moisture absorption, which can degrade the powder. Avoid exposure to humidity, dust, and contaminants. Follow the manufacturer’s recommended shelf life for best performance.
    Shelf Life Shelf life is 3 years from manufacture date when stored unopened in original packaging in a cool, dry place.
    Application of Arkema Rilsan D50 NATURAL PA11

    Arkema Rilsan D50 NATURAL is an unpigmented polyamide 11 homopolymer supplied in pellet form, with a density of 1.03–1.05 g/cm³ and a melting point of 189 °C as published in the supplier datasheet. The technical positioning of this grade rests on low water uptake, low-temperature impact strength, zinc chloride resistance, and hydrocarbon resistance in extrusion and injection moulding processes. The downstream scenarios below are restricted to manufacturing routes where D50 NATURAL is actually specified in industrial practice. Each scenario includes the governing compliance framework, the formulation addition level, the production process constraints, and the terminal product types.

    In gasoline direct-injection and ethanol-blended fuel system architectures, the coextruded multilayer fuel line uses Rilsan D50 NATURAL as the outer structural layer over a low-permeation barrier such as EVOH or ETFE. The outer PA11 layer is processed at 100 wt% of the grade; where black tube is specified for underbody and engine-compartment UV exposure, 2.0–3.0 wt% carbon black masterbatch is metered into the feed throat. No external plasticizer is added because plasticizer migration increases the permeation rate of the finished tube and reduces zinc-chloride stress-crack resistance. The finished tube is qualified as a system under SAE J2260, with material-level checks under ISO 16396-1 for polyamide designation and DIN 73378 for burst and collapse behaviour. Extrusion is performed on a multi-layer line with the PA11 extruder using a barrier screw of 30:1 L/D, barrel temperatures from 220 °C at the throat to 250 °C at the die, and melt temperature kept at 245–255 °C. Vacuum sizing is maintained at -0.08 to -0.06 MPa, and quench water is held at 18–24 °C to prevent out-of-roundness. The production boundary at the die is narrow: sustained melt temperature above 255 °C initiates surface sharkskin and creates layer-thickness eccentricity, while below 245 °C the outer layer cannot be drawn uniformly over the barrier layer without tensile fracture. The terminal products are fuel feed lines, fuel return lines, and onboard refuelling vapour recovery lines for light-duty vehicles, motorcycles, and flex-fuel powertrains.

    The same multilayer line cannot substitute D50 NATURAL for the innermost conductive layer without additional carbon black loading and conductivity testing. Published data for this specific D50 NATURAL configuration in continuous methanol exposure above 20 vol% at 60 °C is limited; such fuel blends require separate barrier-layer and tie-layer validation because the PA11 outer layer is not the primary permeation barrier.

    What Governs the Pressure Sheath Extrusion Window for Rilsan D50 NATURAL in API 17J Unbonded Flexible Pipe?

    In unbonded flexible pipe construction, the polymer pressure sheath is extruded directly over the interlocked steel carcass and must remain crack-free under repeated bending at the design minimum bending radius. Polyamide 11 in natural pellet form is selected because its low-temperature toughness and low hydrocarbon permeability reduce the risk of collapse and blistering during decompression. The governing documents are API Spec 17J for unbonded flexible pipe, ISO 13628-2 for design and testing of flexible pipe systems, and NORSOK M-710 for rapid gas decompression qualification of non-metallic sealing materials. Qualification includes RGD testing in a hydrocarbon gas mixture at design pressure and temperature, followed by visual inspection for cracks and blisters after depressurisation.

    The sheath is extruded from 100 wt% Rilsan D50 NATURAL, with 0.2–0.5 wt% of a phenolic or phosphate antioxidant masterbatch and, for UV-stable exposed sections, 2.0–2.5 wt% carbon black. External plasticizers are not used in the pressure sheath because migration into the annulus fluid would alter the annulus pH and initiate corrosion on carbon steel armour wires. Extrusion is performed with a single-screw extruder, screw L/D 30:1, compression ratio 2.8:1–3.2:1, and barrel zones set at 200 °C, 215 °C, 230 °C, 240 °C, and 245 °C. Melt temperature at the die entry is limited to 235–245 °C. The carcass is preheated to 80–100 °C by induction to reduce quench shock and improve interlayer adhesion. The sheath is quenched in water at 20–30 °C; cooling too rapidly below 20 °C increases residual stress and produces longitudinal cracking when coiled onto the storage reel. The extruder output is set by sheath thickness control, and the downstream haul-off speed is adjusted to match the melt pump throughput so that the tube wall remains concentric under the bending load imposed by the rotating carcass payoff.

    Qualified constructions are used in dynamic risers, static flowlines, jumpers, and water injection lines for offshore oil and gas fields. The sheath is not a standalone product; it is pressure-tested only after the armour layers are wound and the end fittings are installed. For high H2S partial pressures above the conditions covered by the NORSOK M-710 test programme, published data for this specific D50 NATURAL configuration is limited, and additional sour service testing with mixed hydrocarbon and H2S gas is required.

    Where SAE J844 Type A tubing is mandated for compressed-air circuits on heavy-goods vehicles, the line is manufactured from a single PA11 layer in which D50 NATURAL provides pressure retention and low-temperature impact behaviour. The compound is 100 wt% D50 NATURAL with 2.0–3.0 wt% carbon black masterbatch for UV and thermal oxidative resistance and 0.1–0.3 wt% of a stearate-based processing aid to stabilise extruder output. The addition ratio is not adjusted upward for wall thickness above 1.5 mm; melt viscosity is controlled by barrel-zone settings rather than by plasticizer addition. The tube is extruded on a single-screw line with a barrier screw L/D 24:1–30:1, melt pump, and vacuum calibration to meet inside diameter tolerances required for push-connect couplings. Barrel zone temperature profile is 220–245 °C; melt temperature is held at 240–250 °C. After the die exit, the tube enters a vacuum sizing sleeve at -0.06 to -0.08 MPa, then a water bath at 18–22 °C; post-extrusion conditioning at 90–100 °C for 1–2 h anneals residual stress and stabilises burst pressure on coiled tube. Compliance is against SAE J844 for dimensional, burst, and collapse performance, and FMVSS 106 for brake hose and brake line assemblies where installed on US-certified vehicles. Finished products are coiled air brake tubing with outside diameters from 6.35 mm to 16 mm, leading from cab to trailer valve, suspension levelling valve lines, and tractor-to-trailer air supply lines. The tube is not rated for hydraulic brake fluid; plasticizer-free PA11 exposed to DOT 3 or DOT 4 glycol-ether fluids can soften, so auxiliary equipment lines carrying such fluids must use a dedicated polyamide 12 or fluoropolymer construction.

    Medical Catheter Shaft Extrusion: The D50 NATURAL Melt-Temperature Window and Biocompatibility Documentation Burden

    Catheter shaft production using D50 NATURAL is concentrated in transient tissue-contact and short-term diagnostic devices where multi-layer coextrusion and tight diameter tolerance are more important than thermoset-like flexural modulus. The resin is used as an outer jacket layer over a softer polyether block amide or polyurethane core. For non-radiopaque structural shaft layers, the resin is processed at 100 wt%. When the device must be visible under fluoroscopy, a barium sulfate-filled compound is produced with 70–80 wt% D50 NATURAL and 20–30 wt% barium sulfate; the radiopaque filler raises melt viscosity and reduces elongation relative to the unfilled polymer. Tube extrusion is performed on a 24:1 single-screw extruder with a screw designed for low shear, using barrel temperatures of 195–215 °C and a die temperature of 210–220 °C. Vacuum sizing is performed in a 15–20 °C water bath; melt temperature must remain below 220 °C to suppress crystallisation-induced diameter drift in the quench tank. For multilayer shafts, D50 NATURAL is coextruded with a PEBA tie layer and an inner fluoropolymer or polyurethane liner; line speed is governed by ID tolerance, typically ±0.025 mm on a shaft outer diameter of 2.0 mm. Biocompatibility assessment is performed under ISO 10993-1:2018 for cytotoxicity, sensitisation, and intracutaneous reactivity endpoints; the resin manufacturer may provide a drug master file or USP Class VI certification for the unfilled grade, but the finished device remains subject to FDA or EU MDR requirements. Food-contact extraction limits under 21 CFR 177.1500 may be cited only for non-implantable tubing, not for devices with tissue contact beyond transient duration.

    The terminal products are diagnostic catheter shafts, guiding catheter outer jackets, and introducer sheaths. The unfilled natural grade is not supplied sterilised; gamma or ethylene oxide sterilisation must be validated for each finished device, and radiation dose above 50 kGy may produce discoloration in natural unfilled PA11. The operational boundary is re-sterilisation: repeated gamma exposure above 25 kGy per cycle can shift tube burst pressure and should be tested on finished assemblies rather than assumed from resin properties.

    In high-cycle injection moulding of football boot soleplates and cycling cleat shells, the main process variable is not peak injection pressure but the cooling rate that controls the crystallisation of PA11 after the gate freezes. Unfilled D50 NATURAL is processed at 100 wt% for flexible ground-contact plates that require repeated flexing at low temperature. Where higher bending stiffness is specified, the same grade serves as the base resin in short-glass-fibre compounds at 70–85 wt% PA11 and 15–30 wt% glass fibre; the natural colour permits in-house colouring with 1.0–2.0 wt% pigment masterbatch. Pre-drying is mandatory at 80–90 °C for 4–6 h to a moisture content below 0.1 wt%. Injection moulding is conducted with barrel temperatures of 230–260 °C, nozzle temperature 250–260 °C, and mould temperature 40–80 °C. For thin-wall sections below 1.2 mm, filling speed and pack pressure must be balanced to avoid jetting and weld-line embrittlement at the cleat mounting bosses; high-speed injection without adequate venting produces silver streaks from moisture or volatiles. Mechanical evaluation follows ISO 527-1:2019 for tensile modulus, ISO 180:2023 for notched Izod impact, and ISO 6603-2 for multiaxial impact at low temperature. Regulatory compliance under EU 1907/2006 applies; no food-contact standard is invoked in this segment. The terminal parts are football boot soleplates, cycling cleat shells, ski touring boot inserts, and athletic footwear torsional shanks. The unfilled grade will not match the flexural modulus of a 30 wt% glass-filled polyamide 66 compound; applications requiring sharp thread-cutting bosses or metal insert overmoulding may require a mineral-filled variant.

    When D50 NATURAL Is Selected Over Other Polyamides for Industrial Pneumatic Control Lines

    Industrial automation systems that route compressed air to valve islands, robotics tooling, and machine guarding impose simultaneous demands on nylon tubing: dimensional stability in humid air and leak-tight engagement in push-to-connect fittings after repeated pressure cycling. Extruded tubing is produced from 100 wt% D50 NATURAL; black constructions incorporate 2.0–3.0 wt% carbon black masterbatch, while natural or coloured versions may use 0.5–1.5 wt% of a non-migratory organic pigment masterbatch. No plasticizer is added, which preserves hardness and reduces fitting creep. The tube is extruded with a single-screw extruder L/D 24:1–30:1, melt temperature 230–245 °C, vacuum sizing, and a post-extrusion cooling bath at 15–25 °C. Outside diameter is controlled to ±0.05 mm for interference with push-to-connect collet seals; wall thickness is monitored by an ultrasonic gauge. After extrusion, tube is stored at 23 °C and 50% RH for at least 24 h before final dimension verification. Pneumatic circuit compliance is evaluated under ISO 4414:2010 for general rules and safety requirements, ISO 6358-1:2013 for flow-rate characteristics, and ISO 14743:2004 for dimensional requirements for thermoplastic tubing used with push-in fittings. The base polymer is assessed under REACH; FDA food-contact listing is not invoked unless the tubing is positioned directly inside a food-processing zone. Terminal products are industrial pneumatic tubing, vacuum tubing, and control-line conduits used in robotic workcells, machine guarding systems, and beverage packaging lines. D50 NATURAL is not recommended for compressed air containing high concentrations of phosphate ester or chlorinated lubricants; compressor oils with aggressive additive packages can extract stabilizer from the tube surface, leading to inner-wall embrittlement.

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    Certification & Compliance
    More Introduction

    Arkema Rilsan D50 NATURAL is an unplasticized, natural-colour polyamide 11 (PA11) extrusion and injection-moulding grade with a medium-viscosity rheology. The D50 designation identifies a general-purpose base resin whose melt viscosity is high enough for profile and tube extrusion but low enough for moderate-flow injection moulding; the absence of a plasticizer prefix distinguishes it from flexible Rilsan B grades. The polymer backbone is produced from 11-aminoundecanoic acid derived from castor oil, giving a renewable carbon fraction reported by the manufacturer as above 98 % under ASTM D6866-22. The grade is supplied as cylindrical granules and is specified for profiles, tubes, injection-moulded housings, electrical connectors, and cable sheathing where low equilibrium moisture, aliphatic hydrocarbon resistance, and low-temperature toughness are required.

    Representative manufacturer-published values for Rilsan D50 NATURAL, dry as moulded
    PropertyValueTest standard
    Density1.03 g/cm³ISO 1183-1:2019
    Melting temperature185–190 °CISO 11357-1/-3
    Vicat softening point B50155–165 °CISO 306
    Water absorption at saturation, 23 °C≈1.8 %ISO 62
    Tensile modulus, dry1,000–1,200 MPaISO 527-1/-2
    Tensile stress at yield, dry35–40 MPaISO 527-1/-2
    Nominal strain at break, dry>50 %ISO 527-1/-2
    Charpy notched impact, 23 °C5–7 kJ/m²ISO 179-1/1eA
    Charpy notched impact, -30 °C4–6 kJ/m²ISO 179-1/1eA

    How Does Medium-Viscosity D50 Volume Flow Constrain Conversion Equipment?

    Processors characterise D50 NATURAL melt flow at 235 °C under 2.16 kg mass according to ISO 1133-1. The resulting medium-viscosity plateau permits draw-down in tube extrusion and filling of moderate-flow injection moulds, but it imposes higher screw torque than plasticized PA11 grades and lower melt strength than high-viscosity PA11 pipe grades. For single-screw extrusion, screws with L/D between 24:1 and 30:1 and compression ratio between 2.5:1 and 3.5:1 are adequate; barrier screws with Maddock mixing tips are used only when colour concentrate dispersion is required. Capillary rheometry under ISO 11443 is recommended before designing multi-cavity hot-runner systems, because the melt viscosity is shear-thinning and a power-law index near 0.6–0.8 is observed across extrusion shear rates of 100–1,000 s⁻¹.

    Barrel temperature profiles progress from 180 °C in the feed zone to 220–250 °C in the metering zone; die zones are maintained at 230–260 °C. The melt temperature should not exceed 280 °C for more than 10 min. Above 300 °C, thermo-oxidative degradation generates gel particles and crosslinked domains that appear as surface roughness in extrudate and weld-line splitting in moulded parts. Hot-runner systems should be designed for shear rates below 10,000 s⁻¹; gate tip temperatures above 280 °C cause yellowing and carbonaceous deposits in the natural resin.

    Drying is not optional. Pellets stored at relative humidity above 60 % RH require dehumidified-air drying at 80–90 °C for 4–6 h to a residual moisture of <0.05 % by weight. Moisture above 0.10 % causes hydrolytic viscosity loss, splay, and intermittent melt pumping. Hopper dryers should maintain a closed-loop air dew point below -25 °C; outdoor silo storage in humid climates must be followed by a two-stage drying step. Prolonged drying above 90 °C can yellow natural pellets, even when moisture content remains acceptable.

    During injection moulding, barrel back pressure of 1.0–2.0 MPa and screw decompression of 2–5 mm prevent air entrapment. Mould temperatures of 25–60 °C yield sufficient crystallinity for general parts; tool temperatures near 80 °C are preferred for tight-tolerance electrical connectors because they reduce post-mould shrinkage anisotropy. Published data for this specific configuration is limited when moulding very thin walls below 0.5 mm; pilot trials are recommended. Injection pressures of 80–120 MPa are typical for parts with flow length-to-wall thickness ratios below 150:1. Core-cavity venting depth below 25 µm prevents gas burn.

    Stabilizer selection is constrained. Basic amine-containing additives, certain hindered amine light stabilizers, and external lubricant packages can shift melt viscosity or cause colour development in the natural grade. D50 NATURAL should not be mixed with PA6 or PA66 regrind because the melting points and crystallisation rates differ; the resulting phase separation produces weld-line weakness. Similarly, mixing with PA12 regrind lowers the crystalline melting point and reduces high-temperature creep resistance. Clean sprues and runners are commonly re-introduced at 20–30 % by weight, but published data for the influence of regrind fraction on D50 NATURAL impact is limited; production trials are required to validate the level.

    When D50 NATURAL Replaces PA12 in Aliphatic Hydrocarbon Service

    Substitution of D50 NATURAL for PA12 in fuel-line, vapour-recovery, and oil-and-gas service is evaluated primarily by permeation, sour-fluid ageing, and fatigue resistance. The higher melting point of PA11—reported at 185–190 °C under ISO 11357-1/-3—provides a wider thermal margin than PA12 in hot hydrocarbon exposure. The absence of plasticizer in D50 NATURAL avoids additive extraction into aliphatic media and maintains low-temperature flexibility by chain architecture rather than external plasticization.

    Unbonded flexible-pipe inner sheaths and certain onshore fuel lines use unplasticized PA11 grades because collapse resistance and resistance to methanol/gasoline mixtures are acceptable under the qualification programmes of API 17J, ISO 23936-2, and NORSOK M-710. Users should not treat D50 NATURAL as a direct drop-in for every PA12 design; permeation coefficients and fatigue crack-growth behaviour depend on crystallinity, wall thickness, and processing history. When the manufacturer has published pressure ageing data for D50 NATURAL in sour-gas environments, those data supersede generic PA11 class values. Otherwise, published data for this specific configuration in high-H₂S flexible pipe service is limited and requires end-user qualification.

    Chemical resistance of D50 NATURAL is highest against aliphatic hydrocarbons, oils, greases, and non-polar solvents; polar solvents, strong acids, strong bases, and some chlorinated solvents are not recommended. Continuous use in air is typically limited to 90–120 °C depending on load; submerged hot-water service above 70 °C accelerates hydrolysis and is generally outside the grade’s intended envelope. Users should verify stress-cracking resistance in zinc chloride or glycol-containing service with end-user testing, because lot-to-lot crystallinity varies and generic class data may not predict field distress.

    Electrical connector bodies and cable jacketing use D50 NATURAL in dry-as-moulded condition because the equilibrium moisture uptake at 23 °C and 50 % RH is substantially below that of PA6 and PA66. This lower moisture gain reduces the interfacial stress with metallic inserts and stabilises creep in press-fit terminal retention. The natural uncoloured resin accepts colour concentrate and laser-marking additives, but carriers must be PA11-compatible to avoid delamination. Drying and processing conditions above still apply; copper-containing contacts may require antioxidant screening if the part is exposed to long-term thermal ageing above 120 °C. Volume resistivity after conditioning according to IEC 62631-3-1 is reduced by absorbed moisture, but dry values remain in the insulating range for low-voltage connectors; designers should not rely on natural PA11 for high-voltage insulation without explicit creepage and tracking verification under IEC 60112.

    Comparative Moisture Uptake, Density, and Low-Temperature Impact Against Short-Chain Polyamides

    Differences from PA6, PA66, and PA12 are systematic rather than cosmetic. PA11’s low amide-group density—one amide per eleven carbon atoms—is responsible for lower saturation moisture and lower dry density. The comparative table presents class-level values; specific lot data may differ.

    Typical class-level comparison for unmodified, dry-as-moulded polyamide resins
    ParameterRilsan D50 NAT PA11PA12PA6PA66
    Density g/cm³1.031.011.131.14
    Melting temperature °C185–190175–180218–225260–265
    Water absorption at saturation %≈1.8≈1.5≈9.5≈8.5
    Tensile modulus, dry MPa1,000–1,2001,100–1,4002,800–3,2003,100–3,500
    Charpy notched, -30 °C kJ/m²4–65–83–52–4

    Compared with PA6 and PA66, D50 NATURAL has lower dry tensile modulus and lower high-temperature stiffness; it should not be used as a structural substitute in glass-filled, high-HDT applications. Compared with PA12, D50 NATURAL has a higher melting point and higher renewable content, but may exhibit slightly higher water absorption at saturation. The choice between D50 NATURAL and plasticized PA11 grades depends on impact at extreme low temperature; plasticized grades retain ductility below -40 °C, whereas D50 NATURAL reaches its practical sharp-notch limit near -30 °C for some part geometries. Food-contact uses of natural PA11 are possible under EC Regulation No 10/2011 and FDA 21 CFR 177.1500 when the grade is approved by the manufacturer and migration testing is conducted.

    Tube extrusion lines for D50 NATURAL operate with vacuum sizing and closed-loop melt temperature control. A three-zone single-screw extruder with 30:1 L/D and a barrier screw achieves output stability when the feed throat is kept below 60 °C. Melt filtration through 200–400 mesh screens is applied for cable sheathing to remove gel particles; differential pressure across the screen pack should be monitored and changeover scheduled below 8–12 MPa to avoid melt-temperature excursions. Gear-pump assisted extrusion with inlet pressure of 3–7 MPa and outlet pressure up to 20 MPa is used for precision tube wall thickness. The extrudate is quenched in water at 20–40 °C; rapid quench lowers crystallinity and improves clarity of the natural material, whereas slower air cooling increases barrier performance and dimensional stability. The grade cannot be left unblended with carbon black or UV stabilizer in continuous outdoor exposure; natural PA11 undergoes surface degradation and chalking under prolonged UV unless protected by pigmented masterbatch or coextruded cap layer.

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