| HS Code | 269212 |
| Density | 1.01 g/cm³ |
| Water Absorption 24h 23 C | 0.2 % |
| Melting Temperature | 178 °C |
| Tensile Modulus | 1100 MPa |
| Tensile Stress At Yield | 33 MPa |
| Tensile Strain At Break | >50 % |
| Flexural Modulus | 950 MPa |
| Charpy Notched Impact Strength 23 C | 70 kJ/m² |
| Charpy Notched Impact Strength 40 C | 25 kJ/m² |
| Shore D Hardness | 58 |
| Vicat Softening Temperature | 120 °C |
| Heat Deflection Temperature 1 8 Mpa | 50 °C |
As an accredited Evonik VESTAMID® LX9042 NC Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Evonik VESTAMID® LX9042 NC Nylon 12 is supplied in a 20 kg moisture-protective sealed container, ensuring safe handling and stable powder quality. |
| Container Loading (20′ FCL) | 20′ FCL: VESTAMID LX9042 NC packed in 25kg bags on pallets, shrink-wrapped, and container-loaded with proper securing. |
| Shipping | Evonik VESTAMID® LX9042 NC Nylon 12 ships as a non-hazardous thermoplastic granulate in sealed moisture-proof bags, typically on pallets. Protect from humidity, direct sunlight, and excessive heat during transport. Keep packaging intact to prevent contamination. Standard dry freight is suitable; avoid condensation and store in a cool, dry area before processing. |
| Storage | Store Evonik VESTAMID® LX9042 NC Nylon 12 in its original, unopened packaging in a cool, dry, well-ventilated area. Keep away from heat, sparks, open flames, and direct sunlight. Maintain temperature below 50°C and ensure low humidity to prevent moisture absorption. Reseal containers tightly after use. Avoid prolonged storage under adverse conditions. |
| Shelf Life | Shelf life is typically 2 years when stored dry, cool, and in original unopened packaging. |
Automotive evaporative emission architectures operating from -40°C cold-soak to 125°C under-bonnet peaks use plasticizer-free PA12 as the fuel-contact layer and outer protective layer in multi-layer vapour return tubing. The selection of VESTAMID LX9042 NC is driven by low moisture uptake, resistance to zinc chloride road-salt attack, and retention of impact strength after fuel conditioning; these properties are not evaluated in isolation but on complete tube assemblies according to SAE J2260 and SAE J1737. For a nominal wall thickness of 1.5 mm, the co-extruded wall distribution is commonly inner PA12 35–45%, maleic anhydride grafted polyolefin tie 5–10%, ethylene vinyl alcohol barrier 5–8%, and outer PA12 plus residual tie 40–50%. The inner layer is run virgin-only because solvent extractables tested under ISO 6427 must remain inside line-specific limits; outer-layer regrind is capped at 20 wt%. Pre-drying is performed in a desiccant dryer at 80°C for 4–6 h to achieve a pellet moisture content below 0.08% by ISO 15512. The extruder is a single-screw machine with L/D 30:1 and compression ratio 2.5:1 to 3.0:1; barrel temperatures from feed to die are set at 180–200°C, 210–230°C, 230–245°C, and 225–240°C, with melt temperature at the die entry held below 250°C to suppress gel formation. Vacuum calibration is operated at -0.6 to -0.8 bar and water temperature 20–40°C; the cooled tube is cut, coil-set, and leak-tested. Published burst-pressure data for this exact four-layer configuration are limited, so qualification is performed on complete tube assemblies rather than on extrudate plaques. The terminal products are gasoline and diesel evaporative vapour-return lines, canister purge lines, and quick-connector stub tubing for light-duty vehicles.
| Layer sequence | Nominal wall fraction | Function | Control method |
|---|---|---|---|
| Inner PA12 | 35–45% | Fuel contact, chloride resistance | Extractables by ISO 6427 |
| Tie layer | 5–10% | Adhesion to EVOH | Peel test per coextrusion line specification |
| EVOH barrier | 5–8% | Permeation reduction | Total hydrocarbon permeation by SAE J1737 |
| Outer PA12 plus tie | 40–50% | Mechanical protection, regrind carrier | Burst test per SAE J2260 |
The burst pressure requirement for truck air brake tubing under SAE J844 is evaluated after heat ageing because PA12 post-crystallization and antioxidant depletion shift the ductile-brittle transition. The processing limit that controls final burst retention is residual axial orientation from drawdown. In monolayer tube extrusion of VESTAMID LX9042 NC, the drawdown ratio between die gap and final tube wall is kept below 1.1:1; values above this threshold create longitudinal craze lines at cold impact -40°C measured under SAE J844. The line configuration uses a single-screw extruder with L/D 30:1, a barrier screw with metering section 8–10 D, and a vacuum sizing tank at -0.5 bar; sizing water is maintained at 20°C. Cylinder temperature profile is 190–240°C, die temperature 225–235°C, and melt temperature measured at the die entry is limited to 250°C. Regrind content is held at or below 15 wt% for wall thicknesses above 1.5 mm; for thin-wall 1.0 mm tube, regrind is excluded to reduce gel-related burst scatter. Pellet moisture is dried to 0.1% at 80°C for 4–6 h; higher moisture produces internal voids that localize burst failure at 100°C. The finished tube is stabilized with an antioxidant package compatible with continuous air exposure; published data for long-term burst pressure of this specific grade are limited, so production qualification relies on batch heat-age testing at 100°C and cold impact testing at -40°C. Terminal products include 8 mm and 12 mm OD air brake lines for heavy-duty trucks, trailers, and bus pneumatic circuits.
| Verification point | Standard / method | Condition | Monitored failure mode |
|---|---|---|---|
| Pellet moisture | ISO 15512 | 80°C, 4–6 h drying | Internal voids, burst scatter |
| Cold impact | SAE J844 | -40°C, 5 h soak | Longitudinal splits, ring cracking |
| Heat-age burst | SAE J844 | 100°C dry air | Blistering, burst below drawing limit |
| Dimensional stability | Laser micrometer, three-axis | In-line at 20°C | Ovality above drawing tolerance |
Subsea production control systems specified under ISO 13628-5 and API 17E use seamless PA12 sheathing over individual steel tubes in hydraulic and methanol injection umbilical bundles. The sheath is extruded in a crosshead die with preheated tube of 80–120°C and a melt temperature of 230–245°C. Jacket thickness is in the range 1.0–2.5 mm for tube outside diameters from 6.35 mm to 25.4 mm. The drawdown ratio is limited to 1.15:1 and the cooling water is staged at 60–80°C to reduce locked-in hoop stress; subsequent cold water quenching is avoided because it promotes stress corrosion in 3.5% NaCl environment under ISO 9227. Pellet moisture is reduced to 0.06% at 80°C for 6 h before extrusion; higher moisture causes steam-induced weld lines at the crosshead die that are exposed as blisters after 1000 h of salt spray at 35°C. Adhesion to the steel surface is validated by pull-off testing under ISO 4624; the required value is project-specific and must be verified on the production line because published data for this exact steel surface and primer combination are limited. The outer layer contains a UV package if the umbilical is stored above water in tropical yards; otherwise the NC grade is processed without carbon black. The PA12 sheath is optional when a central stainless steel tube is armoured; however, in exposed jumpers and pull-in heads, the sheath prevents corrosion under insulation and gives mechanical abrasion resistance. Terminal products are hydraulic control, chemical injection, electrical flying leads, and fibre optic umbilical jackets for subsea trees and manifolds.
In hot-dip galvanizing floors, flux fume containing zinc chloride and ammonium chloride raises the conductivity of surface moisture and produces ammonium chloride stress-corrosion failure in PA6 and PA66 pneumatic control lines. Plasticizer-free PA12 replaces these materials because the lower amide group concentration reduces equilibrium moisture uptake and slows chloride-induced crack propagation. For control air at 0.6–0.8 MPa, the tubing is extruded as monolayer with outside diameter 10 mm and wall thickness 1.0 mm. The grade is dried to 0.1% moisture at 80°C for 4 h; barrel zones are 200–240°C, die 225–235°C, and melt temperature below 250°C. A grooved feed extruder with L/D 25:1 and a barrier screw provides stable volume delivery; the cooling tank is maintained at 20–30°C and vacuum at -0.4 to -0.6 bar. If the tube is exposed to direct sunlight in open-top plants, 2.0–2.5 wt% carbon black masterbatch or an equivalent UV-stabilized PA12 compound is used; natural NC grade alone is not UV-stable. For poorly bonded joints to push-in fittings, insertion depth is checked against the fitting manufacturer’s tolerance; no solvent cement is used because nylon 12 does not accept solvent welding under production conditions. Hydrostatic burst validation is performed under ISO 1402 at 23°C and 60°C. Terminal products are pneumatic control tubes, valve actuator feeds, and sensor cable protective jackets in galvanizing plants, waste incineration air systems, and fertilizer bagging lines.
Natural PA12 granulate conveying pipes of VESTAMID LX9042 NC exhibit surface resistivity above 10^12 Ω when measured under IEC 62631-3-2; this value places the material outside the dissipative classification accepted by IEC 60079-0 for non-conductive surfaces in potentially explosive dust atmospheres. In dilute-phase pneumatic conveying of plastic granules, the pipe is therefore fitted with an external copper grounding conductor and the conveying gas velocity is restricted according to VDI 2263; the natural NC grade is not acceptable as the sole antistatic element. Where the process requires a dissipative inner surface, a co-extruded carbon-black-loaded PA12 layer at 15–20 wt% conductive carbon black and 10–15% of total wall thickness is applied; the conductive layer is a separate compound and alters the natural colour of the bore. For granulate transfer lines from 50 mm to 110 mm OD with wall thickness 3–5 mm, the extruder uses a grooved feed section and L/D 30:1; cylinder temperatures are set at 200–240°C with a die temperature of 220–230°C. The resin is pre-dried at 80°C for 5 h to a moisture level below 0.08%; the pipe is cooled in a water bath at 20–40°C. During installation, bending radius is held above 10 times OD at ambient temperatures above 0°C; below 0°C, bending radius is increased to 15 times OD to prevent whitening at tensile yield. Terminal products are pneumatic transfer pipes for polyethylene and polypropylene granulate, dedusting lines, and docking spouts on railcar loading stations.
Rail vehicle jumper cables routed in roof cavities are specified under EN 45545-2 for smoke density, oxygen index, and toxic gas emission; thin-wall PA12 sheathing of 0.3–0.7 mm over insulated copper conductors is used because it reduces harness mass compared with cross-linked polyethylene while retaining low-temperature flex at -40°C. The sheathing is applied in a pressure crosshead extruder with melt temperature 220–240°C and drawdown ratio below 1.2:1; pre-drying is set at 80°C for 4–6 h to 0.1% moisture by ISO 15512. The NC grade is not inherently flame retardant; the final cable construction passes the required hazard level only when combined with flame-retardant bedding and insulation layers. Terminal products are halogen-free jumper cables for rail carriages, traction converters, and trackside signalling jumpers.
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Evonik VESTAMID® LX9042 NC Nylon 12 is a natural-color, unfilled polyamide 12 powder developed for powder bed fusion processes, principally selective laser sintering. The grade designation LX9042 identifies a controlled particle-size distribution and melt viscosity profile intended for laser-based additive manufacturing, while the NC suffix indicates natural color and absence of pigment loading. In comparison with pigment-compounded grades, the unpigmented formulation reduces melt-viscosity variation and infrared absorption scatter, which can otherwise shift the effective melting window during scanning. The powder is supplied as a free-flowing bulk solid with an apparent density of 0.44 g/cm³ to 0.50 g/cm³ measured under ISO 60, and a median particle diameter typically between 50 µm and 60 µm by laser diffraction. Typical uses include functional prototypes, fluid-handling manifolds, surgical guides, snap-fit enclosures, and automotive brackets requiring dimensional accuracy and resistance to aliphatic hydrocarbons. In powder form, the material is processed in laser-based powder bed fusion machines with preheated build chambers; the powder is not designed for injection molding or extrusion, because the particle size and stabilizer package are tailored to powder spreading and layer-wise melting.
Maximum particle size controls the thinnest reliable powder layer. When the upper particle diameter exceeds 80 µm, recoater blades cannot spread uniform layers below 100 µm without dragging, streaking, or leaving particle-free channels. The controlled upper cut of this powder supports 100 µm layer thickness on production SLS platforms, while finer sieving below 45 µm is applied when vertical resolution below 0.25 mm is required. Laser diffraction data for this class generally show a span of 1.1 to 1.4, defined as (D90−D10)/D50; a narrower span reduces segregation during recoating and stabilizes bed density. On a machine equipped with a 22 W CO₂ laser and 0.15 mm scan spacing, edge curl is observed when the powder bed temperature falls below the recrystallization onset of polyamide 12 or when fine particles are depleted from the surface layer. This failure mode is recognized by a visible upward bow at part edges during the recoater return stroke.
In practice, a 0.15 mm scan spacing and 0.10 mm slice thickness produce a calculated energy density that must be tuned to the melt pool temperature. The effective melt pool temperature should exceed 180 °C but remain below 200 °C to avoid bubble nucleation from residual moisture or degradation products. Delamination at the mid-plane is frequently traced to a thermal offset between upper and lower layer boundaries; reducing the wait time between recoater passes from 4 s to 2 s or raising the chamber heater duty cycle can correct the defect. Published data for this specific configuration is limited.
Bulk powder flow is equally constrained by interparticle friction and ambient humidity. The Hausner ratio, calculated from tapped and apparent density, typically remains between 1.20 and 1.30 for dry powder; values above 1.40 after exposure to humid air indicate cohesive flow and require drying or sieving. Powder containing 0.2 wt% moisture exhibits a measurable increase in avalanche angle and can produce non-uniform layer thickness across the build platform. Before use, powder should be passed through a 150 µm screen to remove fused agglomerates generated in previous builds and to restore the particle population lost through selective consumption of fines.
Sintered tensile specimens produced at an energy density of 0.10 J/mm² to 0.12 J/mm² typically exhibit an ultimate tensile strength between 45 MPa and 52 MPa when tested dry-as-printed according to ISO 527-2. Tensile modulus is commonly reported near 1500 MPa; elongation at break ranges from 15% to 25% depending on build orientation, powder refresh rate, and chamber temperature uniformity. Flexural modulus under ISO 178 is generally near 1400 MPa, and notched impact strength measured by ISO 180/1A falls in the 4 kJ/m² to 5 kJ/m² interval for fully dense parts. Conditioning of printed specimens at 23 °C and 50% relative humidity for 48 h reduces strength and modulus slightly while increasing impact resistance due to moisture plasticization; dry-as-printed values therefore represent the upper end of stiffness and the lower end of ductility. In repeated production runs on a 30 W laser system, flat plaque warpage was observed when the cooling bed temperature deviated by more than ±2 °C from the setpoint; unsupported spans above 120 mm showed concave deformation toward the upper surface. The anisotropic shrinkage behavior is consistent with the semicrystalline nature of polyamide 12.
| Property | Method | Reported range / typical value |
|---|---|---|
| Bulk density | ISO 60 | 0.44–0.50 g/cm³ |
| Median particle diameter (D50) | Laser diffraction | 50–60 µm |
| Upper particle diameter (D90) | Laser diffraction | ≤80 µm |
| Melting peak | ISO 11357-3 | 176 °C |
| Tensile modulus | ISO 527-2 | 1500 MPa |
| Tensile strength | ISO 527-2 | 45–52 MPa |
| Elongation at break | ISO 527-2 | 15–25 % |
| Flexural modulus | ISO 178 | 1400 MPa |
| Notched impact strength | ISO 180/1A | 4–5 kJ/m² |
| Water absorption (23 °C, saturation) | ISO 62 | 0.8 % |
In SLS builds exceeding 36 h, the powder bed is held at 170 °C to 174 °C. Polyamide 12 undergoes thermo-oxidative chain scission in heated air; the degradation rate accelerates with moisture and oxygen partial pressure. Accelerated aging of molded PA12 at 140 °C in forced-air ovens shows time-to-embrittlement typically in the range of 500 h to 1000 h, depending on stabilizer content and sample thickness. SLS powder repeatedly exposed to chamber temperatures may consume phenolic antioxidants; this can be monitored by carbonyl index via FTIR but is not routine on production lines. Nitrogen inerting with an oxygen sensor alarm set above 1.5 vol% O₂ reduces carbonyl formation and yellowing; for builds longer than 24 h, an oxygen level below 1.0 vol% is preferred.
Material handling on the manufacturing floor must prevent fines generation and prolonged hold times. Vacuum conveying should avoid high-speed rotary valves that fracture particles and alter the particle-size distribution. Hopper residence time should be limited to 8 h when ambient relative humidity exceeds 60% unless dry-air purging is active. The powder should not be blended with amine-containing additives or acid-functionalized polymers because premature chain extension or hydrolysis can shift the melting and crystallization curve outside the SLS processing window.
Chemical resistance of sintered polyamide 12 follows its aliphatic hydrocarbon backbone. The material resists greases, fuels, aliphatic solvents, and neutral salt solutions at ambient temperature; continuous exposure to strong mineral acids, phenols, or concentrated formic acid is not recommended. For fluid-handling parts intended for food contact, compliance may be assessed under FDA 21 CFR 177.1500 for nylon resins, but the final printed part geometry, surface porosity, and post-processing history must be verified for extractive limits. Under REACH and RoHS the unfilled natural grade contains no intentionally added heavy-metal stabilizers or halogenated flame retardants; downstream dyeing, coating, or bonding operations can alter the final regulatory classification.
Blending virgin and reclaimed powder is standard practice, but the recycled fraction changes particle statistics and laser absorption. Sieve analysis after high-temperature exposure shows an upward shift in D10 and a reduction in fines because small particles are preferentially consumed or fused into the part cake. Bulk density may increase by 0.02 g/cm³ to 0.04 g/cm³ after repeated cycles, while flow time measured through a 25 mm orifice under ASTM D1895 can lengthen if moisture uptake exceeds 0.2 wt%. When the reclaimed fraction exceeds 40 wt%, aged particles develop surface oxidation and altered crystalline morphology that scatter the laser beam; operators often increase energy density by 0.01 J/mm² to 0.02 J/mm² for blends above 50 wt% reclaim to restore interlayer fusion. Powder that agglomerates or shows electrostatic adhesion to the recoater should be sieved and dried before returning to the feed hopper; if flow time exceeds 40 s through the orifice, the powder should be evaluated for moisture and fines content. The upper practical boundary is generally 60 wt% reclaim for mechanically demanding parts, though published data for this specific formulation is limited.
Unopened packaging should be stored at 20 °C to 30 °C and below 50% relative humidity. If opened powder is exposed to ambient humidity above 60%, drying in a vacuum oven or desiccant dryer at 80 °C for 4 h to 6 h is required to reduce residual moisture below 0.1 wt% before transfer to the build chamber. The grade is not intended for use in extrusion or injection molding; its particle size and stabilizer package are optimized for powder bed fusion, and reprocessing through melt-intensive routes may shift molecular weight and color. The absence of pigments in the NC grade permits consistent infrared absorption, but carbon black or graphite contamination from shared equipment can increase localized absorption and cause overheating. Dedicated powder handling lines and hoppers are therefore recommended.
Compared with general-purpose polyamide 12 laser-sintering powders, LX9042 NC is differentiated by a narrower particle-size window and lower pigment-related process variability. Against glass-filled or mineral-filled VESTAMID® grades, this unfilled system offers lower stiffness but higher elongation, easier post-build machining, and reduced recoater wear. Against polyamide 6 or 66 powders, it exhibits lower water absorption and a lower melting point, which reduces chamber temperature demand and improves dimensional stability in humid service. The lower melting point relative to polyamide 6 also permits use of lower preheat temperatures, reducing the thermal load on machine seals and limiting polymer degradation. When an application requires higher heat deflection temperature or lower thermal expansion, glass-filled PA12 or carbon-fiber-filled polyamide grades are often substituted, but those materials require abrasive-resistant recoater blades and more frequent maintenance of the recoater and powder-handling surfaces.
| Attribute | Unfilled PA12 (LX9042 NC) | Glass-filled PA12 analogs | Polyamide 6 powder |
|---|---|---|---|
| Melting peak | 176 °C | similar | 220 °C |
| Tensile modulus | 1500 MPa | 2500–3500 MPa | 2500 MPa |
| Water absorption | 0.8 % | lower | 2.5–3.0 % |
| Laser processing window | broad | narrower due to filler thermal conductivity | narrow; high chamber temperature required |
| Abrasion on recoater | low | high | moderate |