| HS Code | 159763 |
| Density | 1.02 g/cm³ |
| Moisture Absorption At 50 Rh | 0.30% |
| Tensile Modulus | 900 MPa |
| Tensile Yield Stress | 40 MPa |
| Tensile Strain At Yield | 5% |
| Tensile Strain At Break | 300% |
| Flexural Modulus | 950 MPa |
| Charpy Notched Impact Strength | 10 kJ/m² |
| Melting Point | 178 °C |
| Vicat Softening Temperature | 145 °C |
As an accredited Evonik VESTAMID® LX9039 NC Nylon 12, Conditioned factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied in 25 kg sealed polyethylene bags: Evonik VESTAMID® LX9039 NC Nylon 12 conditioned pellets, palletized and labeled for transport. |
| Container Loading (20′ FCL) | 20′ FCL: load palletized, conditioned VESTAMID LX9039 NC Nylon 12 securely, protect from moisture, and distribute weight evenly. |
| Shipping | This conditioned nylon 12 ships as pellets in sealed, moisture-barrier bags on pallets. Protect from moisture, heat, and direct sunlight during transit. Use dry, covered transport, and avoid rough handling to preserve product quality. Not classified as hazardous under standard shipping conditions. |
| Storage | Store VESTAMID® LX9039 in its original, unopened packaging in a cool, dry area away from direct sunlight and heat sources. Keep containers tightly sealed to prevent moisture absorption, as nylon 12 is hygroscopic. Avoid temperature extremes and condensation; ideal storage is 20–25°C with low humidity. Properly stored, material maintains specified properties for at least two years. |
| Shelf Life | Shelf life: 2 years from manufacture date if stored unopened, in original packaging, in a cool, dry place. |
In plant-wide compressed air networks operating at 0.4–1.0 MPa, push-fit polyamide tubing converted from VESTAMID LX9039 NC Conditioned is specified where vibration from reciprocating compressors transmits through copper or stainless steel lines and initiates fatigue cracking at thread roots. The conditioned state supplies pellet moisture within a processing window that prevents hydrolysis-induced bubble formation during tube extrusion; open-bag storage at 60% RH or higher for more than 4 h requires re-drying with a -40°C dew point dryer at 80°C until moisture content measured by ISO 15512:2019 Method B falls below 0.10 wt%. ISO 14743:2020 governs dimensional compatibility and leak-tightness of push-fit connectors with thermoplastic tubing; flow-rate characteristics of the converted line are evaluated by ISO 6358-1:2013. Compliance under REACH Regulation (EC) 1907/2006 Annex XVII applies to industrial installations in the EU, and RoHS Directive 2011/65/EU restricts hazardous substances in associated control cabinet wiring. Formulation addition ratio: 100 phr VESTAMID LX9039 NC Conditioned is dry-blended with 0.5–2.0 phr PA12-compatible colour masterbatch; clean post-industrial regrind from the same tubing line may replace up to 20 phr of virgin resin only after melt filtration through a 50 µm screen. Blending with PA6 or PA66 is not recommended because differences in melt crystallization rate and moisture uptake create interfacial stress discontinuities that reduce burst pressure at 60°C. Downstream production process: a single-screw extruder with L/D 28:1–30:1 and a barrier-style three-zone screw runs at 30–60 rpm with barrel temperatures from 210°C in the feed section to 235°C at the die, yielding melt temperatures between 220°C and 240°C. The tube is calibrated under -0.02 to -0.05 bar vacuum in a water tank held at 15–25°C; draw ratio is limited to 1.05:1–1.15:1 to avoid excessive molecular orientation that raises split resistance but lowers radial impact strength. A post-extrusion conditioned cycle of 48–72 h at 23°C/50% RH stabilizes dimensions before printing or coiling. On production lines with screw wear above 0.15 mm flight clearance, melt temperature fluctuation above 245°C causes plasticizer migration to the tube surface, producing tackiness and an outside-diameter tolerance worse than ±0.05 mm. Terminal finished product types include: push-fit pneumatic tubing from 4 mm to 16 mm outside diameter, coiled airline assemblies with re-coil memory, robotic end-effector air supply lines, and vacuum sensing tubes where low water absorption maintains sensor response time after repeated washdown.
Because air brake circuits on heavy commercial vehicles remain charged at 0.85 MPa and are exposed to salt spray, ethanol, and low-temperature flexing, PA12 tubing based on VESTAMID LX9039 NC Conditioned is used where a brake line must satisfy both burst pressure and cold impact requirements after 100,000 km of service. SAE J844:2019 Type A covers thermoplastic tubing for compressed air brake systems, while DIN 73378:2007 establishes material-specific requirements for polyamide air brake tubing in vehicle installations. Burst pressure is measured at 20°C and 100°C according to ISO 1402:2021; tensile yield and elongation are determined by ASTM D638-14, and cold impact by ISO 179-1:2010 Charpy notched specimens at -40°C. Formulation addition ratio: 100 wt% VESTAMID LX9039 NC Conditioned; 0.1–0.3 phr hindered phenolic antioxidant masterbatch is added when in-house regrind rate exceeds 10 wt%. For underbody-exposed tubes, 0.5–1.5 wt% UV-stabilized carbon black masterbatch is used. Regrind from edge trim or failed startup runs is restricted to 15 wt% and only after drying to <0.12 wt% moisture, because lower molecular weight fractions generated by multiple heat histories reduce sustained pressure resistance at 80°C by up to 12% across a production batch. Downstream production process: a grooved-feed single-screw extruder with L/D 30:1 is fitted with a melt pump downstream of a 40–60 µm screen pack; melt pump pressure fluctuation is held below ±0.05 MPa to prevent wall-thickness variation that creates burst-pressure weak spots. The barrel profile is set from 210°C to 240°C, die temperature at 235°C, and die land length between 10:1 and 15:1 relative to the annular gap to generate circumferential molecular orientation. After vacuum sizing, the tube passes through an 80°C annealing water bath to reduce frozen-in stress, then through a laser micrometer with closed-loop speed control holding outside diameter to ±0.03 mm. Post-extrusion conditioning at 23°C/50% RH for 72 h brings the tube to approximately 0.6–0.8 wt% moisture; over-conditioning to saturated moisture reduces burst pressure by 8–12% and should be avoided for assembled brake lines. Terminal finished product types include: 6–16 mm OD air brake tubes for tractor-trailer brake circuits, clutch servo lines, air suspension height-control tubing, and coiled trailer-to-tractor gladhand air lines.
Robot dress-pack cable sheathing made from VESTAMID LX9039 NC Conditioned addresses the failure pattern observed in 5-axis welding cells where PA6 jackets absorb moisture from ambient air and lose tensile modulus, causing the cable bundle to sag into the robot arc envelope. This application demands a jacket compound that retains dimensional stability and flexural fatigue life after 3 million cycles on a bending radius of 10× the cable outside diameter. IEC 60332-1-2:2015 vertical flame propagation, IEC 60754-1:2011 halogen acid gas evolution, and UL 1581:2001 VW-1 flame test serve as the acceptance test set for machine cable jackets; RoHS Directive 2011/65/EU Annex II applies to all jacket compounds sold into EU automation equipment. Formulation addition ratio: 100 phr VESTAMID LX9039 NC Conditioned is compounded with 2.0–4.0 wt% PA12-carrier colour masterbatch or 0.5 wt% carbon black for UV resistance, and 0.2–0.6 phr PTFE micropowder to lower die-lip build-up during pressure extrusion. Silicone-based process aids above 1.0 wt% are excluded because they migrate to the jacket surface and reduce print adhesion and connector gland friction. Clean regrind may be used up to 20 wt% if the fracture strain after reprocessing remains above 200% per ASTM D638-14. Downstream production process: the jacket is pressure-extruded onto laid-up cable cores through a crosshead die at melt temperature 235–250°C; draw ratio is held at 1.02:1–1.05:1 to avoid introducing longitudinal stress that concentrates at the fixed-end clamp of a cable carrier. Screw geometry is a 24:1 L/D low-compression design with a water-cooled feed throat. Pre-drying at 80°C for 4–6 h to <0.08 wt% moisture is mandatory if the original foil bag has been open at RH > 60% for more than 1 h. Inline spark testing at 6 kV and a laser diameter gauge at ±0.05 mm tolerance are standard. Jacketed cables are post-cured at 23°C/50% RH for 24–48 h before flex testing. Terminal finished product types include: energy-chain cables for bottling lines, robot dress-pack cables for arc welding, servo and encoder cable jackets for CNC machine tools, and halogen-free control cable jackets for automated warehouse shuttles.
Diesel tank vent lines extruded from VESTAMID LX9039 NC Conditioned replace PA6 vent tubes that embrittle in cold-weather condensing service and crack when hydrocarbon vapor interacts with urea-derived ammonia in selective catalytic reduction systems. SAE J1737:2007 is used as the permeation benchmark for fuel system hose sections, while evaporative emission limits for nonroad mobile machinery are assessed under EPA 40 CFR Part 1060 and CARB EVAP test protocols where applicable. UV resistance for underbody mounting is evaluated by ISO 4892-2:2013 cycle 1 with 1,000 h exposure; cold flexibility after heat ageing is tested per ISO 4672:2015 or equivalent OEM specification. Formulation addition ratio: 100 phr VESTAMID LX9039 NC Conditioned; 0.5–1.5 wt% carbon black masterbatch is added for UV stability; no external plasticizer is required because the grade is pre-plasticized during polymerization. In-house regrind from inline cutting and corrugating scrap can be added up to 15 wt% after drying to <0.10 wt% moisture. Copper halide heat stabilizer is incorporated in the base resin, and additional copper-based masterbatch should not be added because it can accelerate surface oxidation at weld zones during corrugation. Downstream production process: small-diameter tube extrusion runs a 30:1 L/D single-screw extruder at 220–245°C melt temperature, with a vacuum calibration tank at 10–20°C and haul-off speed controlled to give ±0.05 mm outside-diameter tolerance. For corrugated vent lines, the tube enters a blow-mould corrugator with forming die temperature 140–160°C; the corrugation step reduces bend radius by 35% while maintaining a minimum wall thickness of 0.8 mm at the corrugation root. Post-extrusion dimensional annealing is performed at 120°C for 20 min in a hot-air tunnel to reduce spring-back and ensure consistent fitting retention. Field failures have been traced to extrusion screw speeds above 80 min⁻¹, where frictional heating creates local melt temperatures above 255°C and initiates oxidative gel formation; gel content is controlled to <5 particles per 10 kg by inline screen pack filtration. Terminal finished product types include: diesel tank vent lines from 8 mm to 12 mm OD, fuel filler neck drain tubes, onboard refueling vapor recovery tubes, and corrugated fuel-system protection conduits.
Across forming fabric and spiral dryer belt production lines, 0.6–0.8 mm PA12 monofilament exhibits less edge curling after wet/dry cycling than PA6 monofilament because saturated water absorption of PA12 is approximately 1.3 wt% versus 9.5 wt% for PA6. VESTAMID LX9039 NC Conditioned is drawn into monofilament with retained elongation high enough to withstand fabric weaving tension without filament breakage. Mechanical property acceptance uses ISO 527-1:2019 for tensile modulus and break strength, ISO 2062:2009 for package yarn break force, and ISO 62:2008 for water absorption verification. Food-contact suitability, where required, is limited to compliance verification of the final filament under FDA 21 CFR 177.1500 and EU Regulation (EU) 10/2011; this grade-specific additive package must be confirmed before use in direct food-contact mesh. Formulation addition ratio: 100 phr VESTAMID LX9039 NC Conditioned; 0.05–0.15 phr talc nucleating agent is used to refine spherulite size and stabilize monofilament diameter during the quench; 0.2–0.5 phr phosphite-based processing stabilizer is added if the line operates above 250°C melt temperature. Clean post-industrial PA12 scrap may be introduced up to 20 wt% after melt filtration through a 50 µm screen and after tensile testing of the reprocessed filament confirms break elongation above 30%. Downstream production process: a 25:1 L/D single-screw extruder feeds a gear pump into a multi-hole spinneret at 230–245°C. The extruded filament is quenched in water at 40–60°C, then drawn in two stages. First-stage drawing at 80–100°C applies a draw ratio of 3.2:1; second-stage drawing at 150°C increases total draw ratio to 4.0:1–5.0:1. A relaxation stage of 8–12% at 120°C removes frozen-in elongation and stabilizes loop diameter on the winder. Winding tension is limited to 0.1–0.3 cN/dtex to prevent package collapse. Batch-to-batch variation in conditioned pellet moisture above 0.15 wt% produces surface roughness and filament breakage at the draw pin; pellet hopper residence time should not exceed 30 min without dry-air purge. Terminal finished product types include: screen printing mesh, paper machine forming fabrics, spiral mesh belts for infrared or convection dryers, and filter cloth for mineral slurry dewatering.
When rail vehicle underframe space reduces the permissible bend radius of pneumatic multi-tube bundles to 25 mm for a 6 mm tube, the bundle must maintain low-temperature impact strength and fire-performance compliance without excessive wall thickness. VESTAMID LX9039 NC Conditioned is extruded into individual tubes, then grouped and over-jacketed with a PA12-based compound. Fire safety is assessed by EN 45545-2:2013 requirements R22/R23 at hazard level HL3; smoke density is tested by ISO 5659-2:2017, and tensile properties are verified after 3,000 h of thermal ageing at 100°C according to ISO 527-2:2012. Published data for this specific multi-tube bundle configuration is limited; burst and impulse test results should be generated on the finished assembly. Formulation addition ratio: inner tubes are 100 phr VESTAMID LX9039 NC Conditioned; the outer over-jacket uses 100 phr of the same base resin compounded with 2.0 wt% UV-stabilized carbon black and, where fire class demands, a proprietary halogen-free flame-retardant masterbatch at 25–35 wt% loading. The flame-retardant masterbatch must be PA12-carrier based to maintain interlayer adhesion; PA6-carrier FR masterbatch causes jacket-to-tube delamination after thermal cycling between -40°C and 100°C. Downstream production process: individual tubes are extruded under the same barrel conditions as pneumatic control tubing, then cut into bundle lengths. The bundle is fed through an over-jacket crosshead at melt temperature 225–240°C, with draw ratio 1.03:1 and pressure tooling to force the molten jacket between individual tubes. A vacuum calibrator or pressure-sizing die holds the outer diameter to ±0.10 mm; cooling is staged at 25°C water, then 60°C warm water to minimize differential shrinkage between tube and jacket. In rail shops, cold bending below 0°C without pre-heating can crack the outer jacket; pre-heating the bundle to 40°C for 10 min before installation is specified. Terminal finished product types include: multi-tube pneumatic bundles for door actuators, brake control bundles for light rail vehicles, trackside sanding system air supply bundles, and roof-mounted pantograph air feed lines.
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Evonik VESTAMID® LX9039 NC Nylon 12, Conditioned is a semi-crystalline polyamide 12 extrusion grade supplied in natural colour. The term “Conditioned” in this designation refers to a pre-testing moisture state, typically established at 23 °C and 50 % relative humidity until mass equilibrium in accordance with ISO 291:2008, and is not a polymer-modifier description. The grade is based on polyamide 12, which contains repeating amide linkages separated by relatively long aliphatic segments between functional polar groups. Published data for this specific conditioned grade is limited in public literature; lot-specific values should be obtained from Evonik technical information. Engineering screening may use class-wide nylon 12 data only where the test method and conditioning protocol are explicitly stated.
Conditioning introduces water molecules preferentially into the amorphous regions of the polyamide 12 matrix, where they interrupt hydrogen bonding between carbonyl and amide groups. The result is a plasticized amorphous phase with reduced glass transition temperature and lower short-term creep resistance relative to dry-as-moulded coupons. Tensile modulus values for nylon 12 tested under ISO 527-2:2012 are commonly reported to be 10–25 % lower after conditioning at 23 °C and 50 % RH than in the dry-as-moulded state, while elongation at break typically increases. These shifts must be separated from molecular-weight or additive effects specific to VESTAMID® LX9039 NC.
Dimensional excursions during conditioning are small compared with PA6 and PA66. Class-wide water absorption at saturation in 23 °C water measured by ISO 62:2008 is approximately 1.5 % for polyamide 12, whereas PA6 and PA66 are commonly reported near 9.5 % and 8.5 %, respectively. At 50 % RH, the equilibrium moisture content of nylon 12 is typically below 1.0 %. This lower moisture uptake is the principal reason why dimensional change in humid service is less severe for PA12 than for short-chain polyamides.
For processors conditioning mouldings or extrudates before quality-laboratory testing, the conditioning atmosphere must be controlled not only for temperature but also for air velocity and tray spacing. A forced-air chamber with dew-point control and a ventilated stainless-steel rack is preferred. Coupons stacked without clearance can develop moisture gradients and non-representative tensile yield stress data. Where conditioning time is compressed, vacuum-assisted water exposure is not a substitute for equilibrium moisture conditioning because diffusion kinetics through the semi-crystalline phase differ substantially.
In monofilament and small-diameter tube extrusion, a quench bath maintained below 40 °C can generate a fine spherulitic skin on VESTAMID® LX9039 NC Nylon 12, Conditioned. The higher undercooling suppresses the growth of large spherulites and can improve surface gloss and short-term stiffness. However, the same thermal history may increase residual hoop stress in tubing, and subsequent moisture conditioning can relax these stresses unevenly, producing ovality. A two-stage water bath is therefore used on some production lines: the first stage at 35–45 °C controls skin formation, and the second stage at 60–80 °C permits slower secondary crystallization without excessive thermal shock.
Mechanical testing of such extrudate should follow ASTM D638-14 or ISO 527-2:2012 as specified by the end-user drawing. For tubing, burst pressure is measured on conditioned lengths rather than standardized tensile bars because molecular orientation and weld-line effects in the annular cross-section are not captured by moulded coupon geometries. Published data for this specific configuration is limited; burst testing should be carried out at 23 °C and 80 °C to bracket service exposure.
Polyamide 12 is widely used in contact with aliphatic hydrocarbons, diesel, mineral oils, and grease. Its resistance derives from the low amide density along the polymer backbone and the semi-crystalline morphology that limits solvent penetration. Chemical resistance testing for extruded tubes should be conducted under ISO 1817:2022 with tensile property retention measured before and after immersion. In fuel-contact applications, PA12 tubes can show sufficient resistance to sour gasoline and diesel, but evaporative emissions control often requires a fluoropolymer barrier layer or an exterior polyamide/EVOH composite structure.
Zinc chloride stress cracking is a known failure mode for polyamides. Class-wide experience indicates that PA12 is less susceptible than PA6 or PA66 because of its lower equilibrium water affinity and higher chain mobility, but it is not immune. Any specification for VESTAMID® LX9039 NC in automotive underhood applications should include a controlled stress-cracking test at 50 °C with 50 % ZnCl₂ solution on conditioned specimens, using a defined strain jig. Results without immersion time and strain level are not technically sufficient for release.
Injection moulders running hot-runner manifolds with VESTAMID® LX9039 NC Nylon 12, Conditioned should maintain uniform manifold temperatures and avoid dead spots where resin can stagnate and degrade. The screw check ring and non-return valve must be free of sharp corners and undercuts because nylon 12 has a relatively low melt viscosity and is sensitive to long residence time at elevated temperature. Mould temperatures between 40 °C and 80 °C are commonly used for PA12, and injection pressures should be set to produce a short cushion and consistent switchover. Conditioning after demoulding remains necessary before tensile tests if the drawing requires conditioned properties.
The following class-level comparison is provided for engineering screening. It does not replace the current Evonik product data sheet for VESTAMID® LX9039 NC, because additive package, molecular weight, and processing history alter the measured values.
| Comparative factor | PA12 class | PA11 class | PA6 class | PA66 class | Test basis |
|---|---|---|---|---|---|
| Density at 23 °C | 1.01–1.02 g/cm³ | 1.03–1.04 g/cm³ | 1.13–1.14 g/cm³ | 1.13–1.15 g/cm³ | ISO 1183-1:2019 |
| Water saturation at 23 °C in water | ≈1.5 % | ≈1.9 % | ≈9.5 % | ≈8.5 % | ISO 62:2008 |
| Moisture-induced modulus shift at 50 % RH | moderate | moderate | severe | severe | ISO 527-2:2012 |
| Low-temperature impact retention | high relative to PA6/66 | high | lower | lower | ISO 179-1:2010 |
| Hydrocarbon resistance | high | high | moderate | moderate | ISO 1817:2022 |
Compared with a lower-viscosity natural PA12 moulding grade such as VESTAMID® L1600, the LX9039 melt is intended for high melt-strength tube and profile extrusion. Direct comparison of tensile stress-strain curves should be made on identically conditioned specimens, because conditioning closes some of the dry-state difference between PA12 and PA11. The principal differentiator is not short-term modulus but long-term hydrolytic and dimensional stability in humid service.
Where regulatory documentation is required, VESTAMID® LX9039 NC Nylon 12, Conditioned may be evaluated under FDA 21 CFR 177.1500 for nylon resins intended for repeated food-contact use, subject to end-use limitations on food type and temperature. European food-contact compliance is assessed under Regulation (EU) No 10/2011, with migration testing performed on the finished article rather than on unfabricated resin. Potable-water components require separate verification under NSF/ANSI/CAN 61 or equivalent national standards. Electrical and electronic applications may need RoHS conformity under Directive 2011/65/EU, and REACH registration under Regulation (EC) No 1907/2006 is maintained through Evonik. Current certificates of compliance should be requested for each production lot.