| HS Code | 776490 |
| Density | 1.01 g/cm³ (ISO 1183) |
| Melt Volume Rate | 8 cm³/10 min at 240 °C, 5 kg (ISO 1133) |
| Tensile Modulus | 1700 MPa at 1 mm/min (ISO 527-2) |
| Yield Stress | 48 MPa at 50 mm/min (ISO 527-2) |
| Yield Strain | 4.5 % (ISO 527-2) |
| Nominal Strain At Break | >50 % (ISO 527-2) |
| Charpy Impact Strength Unnotched 23 C | No break (ISO 179/1eU) |
| Charpy Impact Strength Notched 23 C | 18 kJ/m² (ISO 179/1eA) |
| Melting Temperature | 178 °C (DSC, ISO 11357-3) |
| Heat Deflection Temperature 0 45 Mpa | 140 °C (ISO 75-2) |
| Vicat Softening Temperature | 160 °C (ISO 306, method B50) |
As an accredited Evonik VESTAMID® LX9041 black 9.7504 | PA12 Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Evonik VESTAMID LX9041 black 9.7504 PA12 Nylon 12 is supplied as 25 kg sealed bags of black granules, moisture-protected. |
| Container Loading (20′ FCL) | 20′ FCL of VESTAMID® LX9041 black PA12 pellets, packed in moisture-protective bags, loaded and secured for safe transport. |
| Shipping | VESTAMID® LX9041 black 9.7504 is a PA12 nylon granulate supplied in sealed moisture-proof bags. Ship as non-hazardous material in standard dry freight containers. Protect from moisture, direct sunlight, and high heat during transit. Keep bags upright, avoid puncturing, and store in a cool, dry area. |
| Storage | Store Evonik VESTAMID® LX9041 black 9.7504 in its original, unopened packaging in a cool, dry, well-ventilated area. Keep away from direct sunlight, moisture, and heat sources. To prevent moisture absorption, reseal partially used containers tightly. Under these conditions, shelf life is typically two years from production. |
| Shelf Life | Evonik VESTAMID LX9041 black PA12 has a shelf life of at least two years when stored sealed, dry, and away from direct sunlight. |
In automotive diesel fuel vapour return and evaporative emission circuit applications, VESTAMID® LX9041 black 9.7504 is processed as a monolayer flexible conduit or as a convoluted outer jacket over a multi-layer barrier pipe. The black compound is supplied with carbon black already dispersed in the melt, which removes on-line masterbatch addition and the screw slip variability associated with dry colour feeding. The base resin is a PA12 backbone internally modified for low modulus without the use of a migratory monomeric plasticizer; this compositional choice eliminates exudation that can otherwise change fitting retention torque after prolonged diesel vapour exposure. Drying is performed in a desiccant-bed hopper dryer at 80°C for 4 h to 6 h until residual moisture falls below 0.10 wt%. When granulate has been stored at relative humidity above 60%, the 4 h cycle is insufficient and the die exit develops longitudinal silver streaks; in these conditions the residence time is increased to 8 h at the same temperature, provided the dryer air dew point remains at −40°C or lower. A single-screw extruder with L/D 24:1 to 30:1, a three-zone barrier screw, and a compression ratio of 2.3:1 to 2.8:1 is used. The barrel profile is set from 210°C at the feed throat to 230°C in the metering zone, with adapter and die temperatures capped at 245°C; the melt temperature measured by an immersion probe should remain between 225°C and 240°C. Above 260°C the material exhibits progressive chain scission and black speck deposition in the head. A melt pump and a 60/80/60 breaker plate protect downstream calibrators. Vacuum sizing at 0.6 bar to 0.8 bar vacuum and a water bath temperature of 35°C to 45°C stabilise wall thickness. Terminal products include diesel fuel return lines, carbon canister purge lines, and convoluted sleeving over rigid underbody fuel rails. Dimensional acceptance is checked against the quick-connect profiles referenced in SAE J2044, while the finished line’s resistance to zinc chloride road-salt exposure is evaluated because PA12 withstands chloride-induced stress cracking that may fracture PA6 or PA66 clips and retainers in the same bundle.
The failure mechanism controlling pressure ratings in industrial push-to-connect pneumatic tubing made from VESTAMID® LX9041 black 9.7504 is not short-term burst but time-dependent creep rupture at elevated compressed-air temperature. In a 6.0 mm outside diameter 4.0 mm inside diameter tube, short-term burst values at 23°C may fall in a multiple-of-working-pressure range, but at 80°C the working pressure is derated to 4 bar to 5 bar depending on fitting type and safety factor. Ovality remains the dominant dimensional defect because push-in fittings seal on the tube outer surface through an internal O-ring and gripping collet; a two-axis laser gauge is set with a maximum ovality of 0.05 mm, and production is rejected at 0.08 mm. The extrusion line uses a vacuum calibration sleeve with an initial bore 3% to 5% larger than the final outside diameter to compensate for radial shrinkage after cooling. Melt temperature is held at 230°C to 240°C, and the cooling water is maintained at 40°C to minimise frozen-in stress while retaining the dimensional calibration window. No external silicone or migratory lubricant is applied to the tube surface because lubricant transfer into the fitting can reduce collet grip and delay response in pneumatic valves. For panel assembly, the tube is cut with rotary blade cutters and inserted into push-to-connect connectors without heating; the material is specified to resist cyclic bending around robots and to maintain pressure under a safety factor derived from ISO 4414. Terminal products include 4 mm and 6 mm control signal lines used in high-speed packaging machines, semiconductor cleanroom pneumatic circuits, and end-of-arm robotic tooling. If the tube is intended for washdown chemical exposure, chemical compatibility with hydrogen peroxide and quaternary ammonium sanitisers is verified by immersion test according to ISO 175 rather than inferred from polyamide generic behaviour.
Where heavy-truck air brake tube coextrusion must retain impact properties below −40°C, VESTAMID® LX9041 black 9.7504 is run as the outer flexible layer without external plasticizer, avoiding plasticizer phase separation and low-temperature embrittlement observed in monomeric plasticized PA12 formulations after long-term gravel-road vibration. The application requires a smooth black outer surface for clip retention and abrasion resistance against adjacent axle wiring. Grade-specific drying follows the 80°C desiccant cycle to 0.10 wt% moisture, and the line is extruded at a melt temperature of 230°C to 245°C with an L/D 30:1 barrier screw. If gauge repeatability across the tube circumference drifts above 0.03 mm, the calibration tank vacuum is adjusted in increments of 0.05 bar before changing die temperature, because die temperature changes introduce residual axial orientation that later manifests as shrinkage during hot cargo hold exposure. Finished tube is subjected to heat ageing at 100°C for 72 h and cold impact testing under ISO 7628; the line’s burst strength is derived from measured hoop stress rather than raw tensile strength because the service load is biaxial. Terminal products include trailer air brake and air suspension tubes, hose bundling conduits, and cab tilt cylinder control lines. The material is chosen over low-density polyethylene in cold-weather fleets because the polyamide hardness retains fitting insertion force stability and clip cut-through resistance after prolonged exposure to triethylene glycol de-icing spray. If a fully homologated set of burst values is needed for a specific wall thickness, published data for the exact grade and colour should be requested from the supplier because line-specific safety factors depend on fitting geometry and vehicle OEM derating curves.
Hydraulic hose inner-core extrusion based on VESTAMID® LX9041 black 9.7504 begins with melt filter selection, because particulate defects in the core become adhesion delamination sites when a polyester or polyurethane cover is bonded under crosshead die pressure. A 25 µm screen pack is recommended before the gear pump, and the pressure differential is monitored with a clogging limit of 80 bar; when the pressure drop exceeds 80 bar, the breaker plate is changed to avoid melt stagnation and black speck formation. The core is extruded at a melt temperature of 235°C to 245°C with a ratio of core outside diameter to die land length of 10:1 to 15:1 to eliminate melt fracture at draw speeds above 30 m/min. The external surface of the cooled core is then activation-treated by corona discharge until the surface energy exceeds 40 mN/m, verified by test inks according to ISO 8296; this step is required because non-polar PA12 surfaces otherwise produce low peel strength with solvent-based polyurethane adhesives. Regrind addition is limited to 15 wt% to preserve impulse fatigue performance. Terminal products include thermoplastic hydraulic hoses for construction equipment, aerial work platforms, and agricultural implements, with covers typically composed of polyurethane or polyester elastomer. Assembly-level testing follows ISO 18752 or SAE J517 depending on the OEM specification, with impulse cycling at 100°C and dynamic bend radius conditions prescribed by the hose manufacturer rather than by the core material alone. The black 9.7504 colour is advantageous in hydraulic lines where ultraviolet exposure occurs on exterior covers, because the core does not generate visible yellowing that could be mistaken for oxidative degradation during fleet inspection.
When charging harness sheathing is designed for cyclic track flexing at −35°C, VESTAMID® LX9041 black 9.7504 is selected over cross-linked polyethylene where the outer jacket must resist puncture and cut-through from metal chain links. The compound is dried to 0.10 wt% moisture and extruded in a pressure-tooling configuration at 225°C to 235°C, with the screw cooled in the feed zone to prevent premature melting and irregular feed in the high-carbon black compound. Wall thickness is controlled to 0.8 mm to 1.2 mm depending on cable outside diameter, and the quench trough is split into three zones with first zone water temperature at 40°C, second zone at 25°C, and final chill at 10°C to control eccentricity while avoiding internal voids. In cable bending tests, failure initiated at sheath surface scratches from sharp steel edges; the jacket must be spark-tested at 4 kV to 6 kV continuous AC after coiling. Terminal products include electric vehicle charging cable outer jackets, drag-chain power conductors for automated warehouses, and robotic dress-pack sensor cables. Electrical system compliance is assessed under ISO 6722-1 or the vehicle OEM’s LV 112 requirement; flammability class is product-dependent and must be confirmed from the supplier, because published data for this exact black 9.7504 colour may not be directly transferable from natural PA12 grades. The base PA12 chemistry is halogen-free, and REACH and RoHS 2011/65/EU declarations are obtained through the supplier’s technical documentation.
Routing spiral wrap produced from VESTAMID® LX9041 black 9.7504 is evaluated under moving reciprocating harness contact because the wrap protects hydraulic and pneumatic tubes against cut-through from sheet metal edges. The process allows up to 20 wt% clean post-industrial regrind from the same grade, provided the regrind moisture is measured separately; no more than 2 wt% of incidental dust should be added, because dust causes local viscosity differences that show as surface rough patches on the spiral’s outer radius. The extruder uses a 1.2 mm profile slit die and a water quench at 45°C to build a radial modulus gradient that keeps the spiral wrap self-closing after installation. Drawing is limited to 3.5:1 to avoid excessive axial orientation, which increases splitting tendency when the wrap is cut. The qualification test uses a reciprocating abrasion fixture with a 500 g loaded steel edge and a stroke of 50 mm at 1 Hz; the acceptance criterion is no cut-through to underlying tubing after 10,000 cycles when the bundle is retained at 60°C. Terminal products include spiral wrap for agricultural hydraulic bundling, off-road equipment harness protection, and aftermarket cable management in engine compartments. The grade is tested for dimensional recovery after thermal ageing at 125°C for 168 h; if recovery exceeds 5%, the spiral wrap is rejected because reduced grip on the bundled components occurs. This application relies on the full black compound because post-coloration of natural PA12 would reduce regrind consistency and require separate feeder calibration.
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At article level, Evonik VESTAMID® LX9041 black 9.7504 is a black-pigmented polyamide 12 (PA12) granulate supplied within the VESTAMID® L extrusion family. The colour suffix 9.7504 designates the carbon-black-containing formulation rather than a natural or custom-colour grade. Because the base resin is a long-chain aliphatic polyamide, equilibrium moisture uptake at standard room humidity is lower than that of PA6 or PA66. The principal technical distinction of this grade is therefore not a change in polymer class, but a shift toward higher elongation, low-temperature toughness, reduced water-induced dimensional movement, and retention of PA12 processability. The material is intended for melt-extruded tubular articles and injection-moulded connectors where dry-as-moulded dimensional stability and low-temperature impact are specified.
Melting stock should be dried before processing. PA12 granulate equilibrates to approximately 0.7 wt% moisture at 23 °C and 50% RH; this level can generate surface splay, internal voids, and viscosity loss during high-temperature extrusion. In a dehumidifying dryer, the recommended drying condition is 80 °C for 4–8 h to a residual moisture target below 0.10 wt%. Batches exposed to ambient air for more than 30 min after drying may require sealed hopper loading or dry-air conveying. Lot-to-lot variation in carbon black dispersion can influence melt filtration and thin-gauge wall-thickness control; screw speed, melt pressure, and take-off speed should therefore be recorded against incoming lot number to detect batch-to-batch shifts. Residual moisture is verifiable by Karl Fischer titration or hot-laboratory weight loss using ISO 15512. Melt volume-flow rate is measured at 235 °C under 5 kg piston load according to ISO 1133-1; a deviation of more than ±10% from the supplier’s typical value may indicate moisture uptake, thermal history, or cross-contamination with another polyamide.
Carbon black in the 9.7504 formulation functions as a UV-absorbing pigment and may act as a nucleating agent. The black pigmentation increases opacity and raises surface-heat absorption during radiant preheating, but this effect is secondary in conventional screw plastication. Because carbon black can raise melt viscosity slightly relative to unpigmented PA12 of similar molecular weight, melt pressure at a given screw speed may be higher by 5–15%; this should not be interpreted as evidence of degradation. The grade is not designed as an electrostatically dissipative compound; volume resistivity remains in the insulating range, while surface resistivity can be lower than that of natural PA12. If insulation resistance is controlled, end-use testing should be performed on the finished article according to IEC 62631-3-2 rather than on granulate. For outdoor exposure, the carbon black provides UV shielding within the surface layer; weathering performance is evaluated by ISO 4892-2 rather than inferred from colour alone. Black colour does not confer flame retardancy, and no halogen-free flame-retardant classification should be assumed without end-use testing.
Under production-floor conditions, VESTAMID® LX9041 black 9.7504 is processed on single-screw extruders with 24:1 to 30:1 L/D and a three-zone barrier screw; grooved feed sections are used where higher output per rpm is required. The barrel profile is typically set from 200 °C at the feed throat to 220–240 °C in the metering section, with the die head maintained at 230–245 °C. Melt temperature measured at the adapter should not exceed 250 °C for continuous runs; excursions above 280 °C initiate thermo-oxidative chain scission and can generate black specks or gel particles. Use of screen packs from 40/60 mesh to 80/120 mesh is standard for tubing; a sharp increase in screen pressure indicates carbon black agglomerates or degraded gel from a previous run. After a shutdown, purging with a low-melt-viscosity PA12 or purge compound is preferred before restarting to avoid cross-contamination with PA6 or PA66 residues, which are melt-incompatible and can form lamellar delamination in the extrudate.
Downstream, water quenching is used for flexible tube; rapid cooling reduces spherulitic crystallinity and retains ductility. A water bath at 15–30 °C and a vacuum tank with closed-loop diameter control are typical. Because PA12 crystallizes slowly relative to PA6, the tube may exhibit post-extrusion shrinkage; dimensional checks should be performed after 24 h conditioning at 23 °C and 50% RH. For injection moulding, barrel settings between 220 °C and 250 °C and mould temperatures between 40 °C and 80 °C are common. Because the grade is flexible, ejection can be more difficult than rigid PA12 if deep undercuts are present; use of 0.5°–1° draft and ejector sleeves is recommended. Hold pressure should be minimized in thin-wall connectors to reduce post-moulding stress cracking.
The following representative values are cited from PA12 product literature and may be used for material pre-selection. They are not to be used as guaranteed design values; lot-specific certificates from Evonik remain the controlling data. Published data for the black 9.7504 colour can differ slightly from natural-grade data.
| Parameter | Test Method | Typical Value |
|---|---|---|
| Density at 23 °C | ISO 1183-1 | 1.04 g/cm³ |
| Melt volume-flow rate at 235 °C/5 kg | ISO 1133-1 | 8 cm³/10 min |
| Tensile modulus, 1 mm/min | ISO 527-1/-2 | 430 MPa |
| Tensile stress at break, 50 mm/min | ISO 527-1/-2 | 45 MPa |
| Nominal strain at break | ISO 527-1/-2 | >200% |
| Charpy notched impact strength at 23 °C | ISO 179-1/1eA | no break |
| Charpy notched impact strength at -30 °C | ISO 179-1/1eA | 7 kJ/m² |
| Vicat softening temperature, B50 | ISO 306 | 145 °C |
| Melting point, DSC | ISO 3146 | 173 °C |
| Water absorption at saturation, 23 °C | ISO 62 | 1.5 wt% |
| Shore hardness D, 15 s | ISO 868 | 58 |
The selection of VESTAMID® LX9041 black 9.7504 over shorter-chain polyamides is driven primarily by water interaction and low-temperature impact. PA12 absorbs less water at saturation than PA6 or PA66, which produces smaller changes in tensile modulus and dimensions when components are exposed to humid cabin or underhood air. Compared with an unmodified PA12 extrusion grade, LX9041 shifts the stiffness-to-flexibility balance: tensile modulus is lower, elongation at break is higher, and notched Charpy impact is generally higher, especially at sub-zero temperatures. The black colour code adds UV opacity but does not improve chemical resistance beyond the PA12 base; resistance to aliphatic hydrocarbons, greases, and dilute salt solutions is retained, while strong mineral acids, phenols, and concentrated zinc chloride solutions are aggressive. Continuous service above 100 °C in air is not recommended without heat-ageing data because oxidative embrittlement can occur over time.
| Attribute | VESTAMID® LX9041 black 9.7504 | Unmodified PA12 extrusion grade | PA6 | PA66 |
|---|---|---|---|---|
| Density at 23 °C | 1.04 g/cm³ | 1.01–1.02 g/cm³ | 1.13 g/cm³ | 1.14 g/cm³ |
| Water absorption at saturation | 1.5 wt% | 1.5 wt% | 9.5 wt% | 8.5 wt% |
| Melting point | 173 °C | 176–180 °C | 220 °C | 260 °C |
| Tensile modulus | 430 MPa | 1400–1800 MPa | 2800–3200 MPa | 2900–3300 MPa |
| Notched Charpy at -30 °C | 7 kJ/m² | 4–6 kJ/m² | 5 kJ/m² | 5 kJ/m² |
Air-brake and pneumatic tubing produced from VESTAMID® LX9041 black 9.7504 is typically tested to SAE J844 and DIN 73378 for dimensional stability, burst pressure, and cold impact. In such applications, the grade is processed with vacuum sizing so that outer diameter and wall thickness are controlled to ±0.05 mm on high-speed lines. Because PA12 has a lower amide-group density than PA6 or PA66, fuel and aqueous media cause less plasticization and less dimensional growth; this supports use in diesel fuel-vapour lines, clutch tubing, pneumatic lines, and cable jacketing. The black pigmentation is used where UV opacity and visual coverage are required, but the product is not a substitute for electrostatically dissipative compounds. In applications requiring flame-retardant performance, the standard grade is not classified as halogen-free flame-retardant; end-use testing to IEC 60695-11-10 or the applicable automotive horizontal burn standard is required.