| HS Code | 988716 |
| Density | 1.03 g/cm³ |
| Water Absorption 24 Hr | 0.3 % |
| Tensile Strength At Yield | 50 MPa |
| Elongation At Break | 45 % |
| Flexural Modulus | 1.4 GPa |
| Impact Strength Izod Notched | 40 J/m |
| Melting Point | 201 °C |
| Glass Transition Temperature | 45 °C |
| Thermal Conductivity | 0.3 W/(m·K) |
| Volume Resistivity | 1e14 ohm·cm |
| Dielectric Strength | 30 kV/mm |
| Hardness Shore D | 72 |
As an accredited Overview of materials for Nylon 11, Powder factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Nylon 11 powder is supplied in sealed 25 kg bags with moisture-proof liners, ensuring safe transport and storage. |
| Container Loading (20′ FCL) | 20′ FCL containing Nylon 11 powder in sealed bags/pails, palletized, secured, and containerized for safe, efficient transport. |
| Shipping | Ship nylon 11 powder in sealed, moisture-resistant containers to prevent contamination and clumping. Avoid exposure to excessive heat, ignition sources, and static buildup. Ensure proper labeling and documentation for safe transport. Store in a cool, dry area during shipping to maintain product integrity and material performance. |
| Storage | Store Nylon 11 powder in a cool, dry, well-ventilated area away from heat, open flames, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid generating dust; use proper grounding and static-control measures. Protect from direct sunlight and incompatible materials until ready for use. |
| Shelf Life | Typically 2–3 years when stored in a sealed, dry, cool container away from sunlight and moisture. |
During selective laser sintering of Nylon 11 powder on production-scale systems with 30 W or 60 W CO₂ lasers operating at 10.6 µm, the powder bed is maintained at 175–180 °C under nitrogen with residual oxygen held at or below 1.0 vol%. Layer thicknesses of 100–120 µm are standard for a powder with D50 of 45–55 µm because the recoater must form a dense, defect-free layer without dragging pre-sintered surfaces. The formulation for the powder feedstock is not always 100% virgin Nylon 11; machine operators commonly blend 30–50 wt% fresh powder with 50–70 wt% recycled unconsumed powder. The recycled fraction normally contains 0.1–0.5 wt% hindered phenolic heat stabilizer and 0.1–0.3 wt% fumed silica flow agent that were present in the original powder formulation. Industry compliance for mechanical certification of fused powder parts includes ISO 178:2019 for flexural properties, ISO 1133-1:2022 for melt mass-flow rate of the powder, ASTM D638-14 for tensile properties of printed coupons, ASTM D3418-21 for melting and crystallization inflection, and ISO 13320-1:2020 for laser diffraction particle size distribution. On a 50:50 recycled-to-virgin blend, the melt mass-flow rate shifts by roughly 20–40% relative to virgin feedstock, and elongation at break measured by ASTM D638-14 can fall from 30–40% on virgin builds to 10–20% on builds with high recycled content because polyamide chain scission reduces molecular weight. This process conflict is most visible at the powder bed temperature setpoint: a bed temperature above 180 °C accelerates oxidative yellowing and increases the risk of part curl, while a setpoint below 172 °C reduces interlayer adhesion and creates delamination along the Z-axis. The equipment configuration varies, but laser power of 30–60 W and scan speeds adjusted to deliver energy density values in the range of 0.06–0.12 J/mm² are used to maintain a stable melt pool. After the build, parts are cooled slowly in the cake to minimize warpage, then bead blasted with glass media to remove residual surface powder. Terminal finished product categories include air intake duct brackets, fuel system connector housings, custom orthotic insoles, cable clips, and low-volume functional test components where chemical resistance and low water absorption relative to Nylon 12 are required.
| Feedstock state | Melt mass-flow rate by ISO 1133-1:2022 | Tensile yield stress by ASTM D638-14 | Elongation at break by ASTM D638-14 | DSC recrystallisation peak by ASTM D3418-21 |
|---|---|---|---|---|
| 100% virgin | 2–6 g/10 min | 45–50 MPa | 30–40 % | 152–158 °C |
| 30% recycled / 70% virgin | 4–8 g/10 min | 42–46 MPa | 20–30 % | 148–154 °C |
| 50% recycled / 50% virgin | 5–12 g/10 min | 38–43 MPa | 10–20 % | 145–151 °C |
Preheated steel sheet components coated with Nylon 11 powder by electrostatic spray deposition operate in a different process window than fluidised bed dipping. The substrate is first grit blasted to Sa 2.5 under ISO 8501-1:2007 and cleaned with a degreasing bath, then heated to 230–260 °C before the powder is applied. The powder formulation is a dry blend consisting of 95–97 wt% Nylon 11 base powder, 3–5 wt% semi-crystalline pigment masterbatch, and 0.2–0.5 wt% flow additive; no solvent or liquid carrier is present. Electrostatic guns charged at 60–90 kV deliver the powder through 1.5–2.5 bar atomising air, and the part is then post-cured at 190–210 °C for 10–15 min to allow levelling and coalescence. The target film thickness is normally 250–400 µm when measured according to ISO 2360:2017. Compliance for coated metal hardware is verified by ISO 9227:2022 neutral salt spray testing for corrosion resistance, ASTM D4060-19 Taber abrasion with CS-17 wheels for wear resistance, ISO 4624:2016 pull-off adhesion, and ASTM D3363-21 pencil hardness. The operational boundary is narrow: preheat below 210 °C results in high melt viscosity and pinhole defects, while preheat above 285 °C causes oxidative yellowing and sagging on vertical faces. Cross-contamination with epoxy or polyester powder in the same spray booth produces cratering and should be avoided. Downstream terminal products include dishwasher rack hooks, hospital furniture frame brackets, outdoor handrail fittings, automotive seat belt latch covers, and valve body exteriors where impact toughness and corrosion resistance under repeated cleaning cycles are specified.
Fluidised bed dip coating of Nylon 11 powder requires a preheat temperature that is intentionally higher than electrostatic spray because the heat stored in the metal part drives the initial melt and film build. For small- to medium-mass components, preheat is commonly set at 290–340 °C. At 320–340 °C, the first defects are edge drips and bubble inclusions, followed by oxidative discoloration if the immersion time exceeds 5 s. The powder bath is composed of 100% Nylon 11 powder with a particle size range of 80–250 µm and a moisture content below 0.15 wt%; some operations add 0.5–2.0 wt% metallic pigment or 0.1–0.3 wt% fumed silica to adjust fluidisation and colour. The process involves fluidising the powder with dry compressed air at a dew point below -20 °C, dipping the heated part for 2–8 s, allowing the powder to coalesce, and then post-fusing at 195–210 °C for 10–15 min in a forced-air oven. Coating thickness is normally controlled between 300 and 600 µm depending on part heat capacity. Required compliance standards include ISO 2177:2009 for coating thickness by anodic dissolution or microscopic methods, ISO 9227:2022 for salt spray exposure, ISO 2812-1:2017 for chemical resistance in immersion, and ASTM D3363-21 for pencil hardness. The process is commonly used for wire goods, tubular frames, transformer brackets, exterior railings, pump impellers, and conveyor rollers. Operational limitations include the need to isolate the fluidised bed from relative humidity above 50% RH; powder exposed to moisture must be dried at 80–90 °C for 4–6 h before reintroduction, as wet powder collapses the fluidised bed and produces pinholing.
Because biaxial rotational moulding operates outside the particle size window used for laser sintering, the powder specification for Nylon 11 rotomoulding is sieved to 200–500 µm and dried to below 0.10 wt% moisture before being charged into the mould cavity. The formulation may be 100% Nylon 11 powder with 0.1–0.4 wt% antioxidant and 0.2–0.5 wt% carbon black or pigment masterbatch added by dry blending. The mould is rotated biaxially at 4–8 rpm on the major axis and 10–20 rpm on the minor axis while heated in an oven at 280–300 °C for 20–30 min, depending on wall thickness. After the powder has fully coalesced on the mould surface, forced-air and water mist cooling is used to bring the part below the crystallization range of 150–158 °C before demoulding. Industry compliance for finished parts includes ASTM D638-14 for tensile properties, ISO 180:2019 for Izod impact, ISO 75-2:2013 for heat deflection temperature, and FDA 21 CFR 177.1500 or EU Regulation 10/2011 where the part contacts food or potable water. The terminal products include small fuel tanks, chemical storage liners, pump housings, water reservoir liners, and corrosion-resistant covers for valves. A practical limitation is that wall thickness uniformity depends on maintaining a maximum powder bed temperature swing below 5 °C during the heating phase; uneven oven airflow causes thin spots at mould corners and must be corrected by tooling adjustments or extended heating.
Threaded stainless steel fasteners coated with Nylon 11 powder solve galling and corrosion problems in aggressive environments. The coating is deposited either electrostatically or by fluidised bed on fasteners that have been degreased and preheated to 250–280 °C. The powder formulation is typically 100% Nylon 11 with 0.1–0.3 wt% internal lubricant such as polytetrafluoroethylene micro-powder to reduce thread friction; the addition ratio is tightly controlled because PTFE above 0.5 wt% reduces film strength. In downstream production, the fasteners are heated on a mesh belt oven at 260 °C for 15–20 min, coated, and then cured at 195–205 °C for 5–10 min. Torque-tension behaviour is usually validated by ISO 16047:2015, and corrosion resistance by ISO 9227:2022; dimensional fit is checked with ISO 965-1:2013. Terminal products include marine rail bolts, chemical plant flange bolts, bicycle frame fasteners, and food machinery adjustment screws. A known operational boundary is that the coating must not exceed 25–40 µm on thread flanks; thicker films alter pitch diameter and prevent nut assembly.
In colour cosmetics, Nylon 11 powder functions as a spherical texturising filler, anti-caking agent, and soft-focus opacifier. Cosmetic powders use a D50 range of 5–15 µm; the narrow distribution is necessary to avoid gritty skin feel and to maintain uniform dispersion in pressed powder formulations. The addition ratio varies from 1–10 wt% in anhydrous foundations and blushes to 10–20 wt% in pressed powders and 0.5–3 wt% in oil-in-water emulsions. Manufacturing uses high-shear dispersion equipment such as vacuum homogenizers or ribbon blenders; the powder is added after pigments and before wax binders in pressed powder processing to prevent agglomeration. Compliance is assessed under EU Regulation EC 1223/2009 for cosmetic product safety, with residual heavy metals monitored according to national pharmacopoeia methods; where sustainability reporting is required, ISO 16128-1:2016 and ISO 16128-2:2017 provide bio-based carbon content calculations for Nylon 11 derived from castor oil. Terminal finished product types include loose powders, pressed foundations, anhydrous blushes, tinted lip balms, and deodorant sticks. Nylon 11 powder should not be blended with cationic actives at high concentration in low-pH formulations because surface adsorption can reduce preservative availability; formulators also pre-dry the powder at 60–70 °C for 4 h when ambient storage humidity exceeds 70% RH.
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Overview of materials for Nylon 11, Powder is a material-category entry that aggregates natural unfilled polyamide 11 powder grades used in powder coating, fluidized-bed coating, and polymer laser sintering. It is not a single commercial model; the overview consolidates publicly reported property ranges for multiple PA11 powder designations, including fine coating powders and narrow-distribution additive manufacturing grades. Polyamide 11 is a semi-crystalline aliphatic polyamide prepared by polycondensation of 11-aminoundecanoic acid. In the commercial castor-oil route, this monomer is obtained from methyl undecylenate, giving PA11 a partially renewable carbon backbone that can be characterized by ASTM D6866 when bio-based carbon content is relevant. The repeat unit contains eleven methylene groups between amide groups, which produces lower moisture affinity than PA6 or PA66 and a higher melting point than PA12. Unless otherwise specified, the numerical envelope given here applies only to natural unfilled PA11 powder and fused forms; it does not describe glass-fiber-reinforced, impact-modified, plasticized, or flame-retarded PA11 compounds.
Both PA11 and PA12 are selected where dimensional stability under humidity is critical, but the amide-group density and chain architecture produce measurable differences. In the unfilled state, PA11 typically exhibits saturated water absorption at 23 °C of 1.6–2.0% per ISO 62, while PA12 is often reported at 1.3–1.7%. This difference is narrow compared with the gap to PA6 and PA66, which absorb roughly 8–10% at saturation. The processing implications of moisture uptake depend on equilibrium moisture content and conditioning time. PA11 powder pre-dried below 0.1% water can be held in dry-air hoppers or desiccant enclosures for limited periods; prolonged exposure to relative humidity above 60% can reintroduce enough water to create pinholing in coatings or porosity in sintered parts. The eleven-carbon chain also raises the peak melting point relative to PA12: PA11 peak melting is commonly 183–190 °C by ISO 11357-3, whereas PA12 peak melting is typically 175–180 °C. This higher thermal budget permits PA11 powder to serve in hot-fluid and underhood applications where PA12 may approach its continuous-use ceiling. However, the elevated melt point also narrows the laser-sintering build window, because the powder bed must remain close to the crystallization temperature without prematurely fusing the surrounding powder.
| Property | PA11 powder | PA12 powder | PA6 general-purpose | PA66 general-purpose |
|---|---|---|---|---|
| Density | 1.03–1.05 g/cm³ (ISO 1183-1) | 1.01–1.03 g/cm³ (ISO 1183-1) | 1.13–1.15 g/cm³ (ISO 1183-1) | 1.13–1.15 g/cm³ (ISO 1183-1) |
| Melting peak | 183–190 °C (ISO 11357-3) | 175–180 °C (ISO 11357-3) | 220–223 °C (ISO 11357-3) | 255–265 °C (ISO 11357-3) |
| Tensile yield, dry as molded | 32–48 MPa (ISO 527-2) | 35–48 MPa (ISO 527-2) | 75–85 MPa (ISO 527-2) | 80–90 MPa (ISO 527-2) |
| Flexural modulus, dry as molded | 900–1250 MPa (ISO 178) | 1000–1400 MPa (ISO 178) | 2600–3000 MPa (ISO 178) | 2700–3300 MPa (ISO 178) |
| Water saturation at 23 °C | 1.6–2.0% (ISO 62) | 1.3–1.7% (ISO 62) | 9–10% (ISO 62) | 8–9% (ISO 62) |
For melt processing and powder coalescence, the principal parameters are peak melting temperature, crystallization temperature, viscosity number, particle morphology, and residual moisture. Unfilled PA11 powder commonly crystallizes from the melt at 150–160 °C when cooled at 10 °C/min under ISO 11357-3; the exact onset depends on molecular weight and nucleating additives. The viscosity number measured in m-cresol per ISO 307 is more informative for powder grades than melt flow rate because PA11 is sensitive to moisture-induced hydrolysis during melt testing. Commercial coating and laser-sintering PA11 powders commonly fall in a viscosity number range of 120–180 cm³/g, while extrusion grades can exceed 200 cm³/g. Lower viscosity number generally improves coalescence and leveling in powder coatings but can reduce ductility and impact resistance of fused or molded parts. Melt volume-flow rate values, when reported under ISO 1133-1, are often specified at 235 °C with 2.16 kg load for PA11; the test requires dried polymer at <0.1% moisture to avoid hydrolytic degradation. Pre-drying of PA11 powder is typically conducted at 80–90 °C for 4–6 h in a desiccant or vacuum dryer with an air dew point of -30 °C or lower. Drying above 90 °C is not recommended because fine particles may sinter or oxidize. The powder should not be stored in open containers under high-humidity conditions; even a few hours at 60–80% relative humidity can measurably increase moisture content and alter electrostatic transfer behavior.
| Characteristic | Typical test method | Purpose in powder qualification |
|---|---|---|
| Particle-size distribution | ISO 13320-1 | Classification of coating grades and SLS layerability |
| Apparent bulk density | ASTM D1895 | Hopper fill, powder-bed homogeneity |
| Melting and crystallization | ISO 11357-3 | Substrate preheat and build-chamber setpoint |
| Viscosity number | ISO 307 | Melt-coalescence and molecular-weight proxy |
| Water content | ISO 15512 or Karl Fischer | Drying verification before melt operations |
| Tensile properties of fused specimens | ISO 527-2 | Laser-sintered part qualification |
Fluidized-bed coating lines and electrostatic spray systems use PA11 powder as a dry solid, so flow behavior is governed by particle-size distribution, shape, and bulk density rather than by pellet viscosity alone. Fine coating grades are often supplied with top sizes below 100 µm, while laser-sintering grades generally require a narrower distribution centered near 40–60 µm. Apparent bulk density typically falls in the range 0.40–0.50 g/cm³ when measured by ASTM D1895 method A, below the solid density of 1.03–1.05 g/cm³ because of interstitial air. Production-scale fluidized-bed coating lines use electrostatic guns with nozzle voltages commonly between 40–100 kV; substrate preheat is matched to the powder melting peak so that particles adhere, melt, and level into a continuous film. Coating thickness is controlled by part heat capacity, immersion time, and powder particle size, not solely by applied voltage. PA11 powder is used for corrosion-protective and low-friction coatings on automotive clips, springs, dishwasher baskets, cable trays, and handles. In laser sintering, PA11 is spread in layers of 100–120 µm under a heated build chamber and selectively melted. The resulting parts are ductile enough for functional hinges and snap-fit prototypes, but build orientation creates measurable anisotropy. Tensile elongation in the z-direction is commonly lower than in the x-y plane; reductions of 20–40% in elongation have been reported across supplier process trials. Published data for this specific configuration is limited, so orientation-specific mechanical response should be qualified on each machine.
Compliance status for PA11 powder is grade-specific and application-specific, not intrinsic to the polymer. Unmodified PA11 grades may meet the compositional requirements of FDA 21 CFR 177.1500 for nylon articles intended for food contact, provided the pigment, antioxidant, and processing-aid package is cleared for the intended food type and use temperature. For European food-contact applications, the finished article must be evaluated under EU Regulation 10/2011, including specific migration testing for 11-aminoundecanoic acid and any added substances. Some PA11 powder formulations have been tested for potable-water contact to NSF/ANSI 61 for pipes, fittings, and protective coatings, but certification is product-specific and does not automatically extend across all powder grades. Under REACH, PA11 as a polymer is generally exempt from registration, but the monomer and any intentionally released additives remain subject to registration, evaluation, and restriction obligations. Unfilled PA11 powder can be formulated to meet the restricted heavy-metal thresholds of RoHS Directive 2011/65/EU, including cadmium at 100 ppm and lead, mercury, and hexavalent chromium at 1000 ppm, but compliance requires batch-specific testing and controlled raw-material sourcing.
In polymer laser sintering, PA11 powder is held in a heated build chamber near its crystallization temperature to minimize the thermal gradient between fused and unfused regions. If the build temperature is too low, the rastered melt solidifies rapidly and produces planar curl; if it is too high, the surrounding powder agglomerates and loses flowability. Build temperatures for PA11 are generally maintained in the range 165–180 °C, depending on molecular weight and powder coalescence behavior. On commercial polymer laser-sintering machines, PA11 is typically processed with a 10.6 µm CO₂ laser, and machine suppliers adjust energy density by controlling laser power, scan speed, and beam spacing to fuse a 100–120 µm layer without excessive fume generation. Recovered powder is sieved through 125–150 µm mesh to remove fused agglomerates and blended with virgin material. Prolonged near-melt exposure increases carbonyl formation and can shift the viscosity number upward in some grades, while other grades may exhibit chain scission; the direction and magnitude depend on the antioxidant package and thermal history. Machine suppliers may recommend a virgin-powder refresh rate of 30–50% for demanding applications, but published data for this specific configuration is limited. Process qualification across the full reclaim ratio is required to establish elongation and notched impact retention. PA11 powder should not be processed in a wet powder bed; residual moisture above 0.1% produces steam, increases surface porosity, and degrades mechanical strength. Chemical incompatibilities include concentrated mineral acids, formic acid, cresol, and phenol, which can dissolve or strongly swell the resin. For outdoor service, unstabilized PA11 requires UV protection, typically carbon black or a hindered amine light stabilizer package, to limit surface embrittlement.