| HS Code | 520139 |
| Melting Point | 185 °C |
| Crystallization Temperature | 139 °C |
| Glass Transition Temperature | 50 °C |
| Density | 1.01 g/cm³ |
| Bulk Density | 0.45 g/cm³ |
| Particle Size D50 | 50 µm |
| Tensile Modulus | 1700 MPa |
| Tensile Strength | 50 MPa |
| Elongation At Break | 18 % |
| Charpy Impact Strength Notched | 4.5 kJ/m² |
| Shore D Hardness | 75 |
| Water Absorption | 1.5 % |
As an accredited Evonik VESTAMID® LX9012 PA 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 20 kg sealed bags to protect VESTAMID LX9012 PA12 powder from moisture and contamination for safe transport. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Pack Evonik VESTAMID® LX9012 PA12 palletized, dry, and secured in a clean, ventilated 20-foot container. |
| Shipping | VESTAMID® LX9012 is a PA 12 grade supplied as dry pellets. It is non-hazardous for transport. Ship in sealed original packaging to prevent moisture absorption. Avoid excessive heat and humidity; keep containers upright. Standard ground and air freight are suitable with proper labeling. |
| Storage | Store Evonik VESTAMID® LX9012 PA 12 in its original, unopened packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, heat, and moisture, as the material absorbs humidity. Keep away from strong oxidizers and food products. Under proper conditions, shelf life is approximately two years from delivery. |
| Shelf Life | Stored sealed, dry, and cool, VESTAMID® LX9012 retains specified properties for up to two years from delivery. |
Evonik VESTAMID® LX9012 PA 12 is a plasticized polyamide 12 compound whose melt viscosity range is formulated for extrusion of small-diameter flexible tubing, multi-layer barrier structures, and cable protection profiles. The granulate is predried in a desiccant dryer at 80°C for 4–6 h to a moisture content below 0.10%; the drying air dew point is held below -20°C, and residence time is extended to 8 h when ambient relative humidity exceeds 60%. Residual moisture above 0.10% hydrolyzes the amide groups during melt processing and produces surface sharkskin, wall-thickness oscillation, and a measurable intrinsic viscosity drop. The downstream applications described below are separated by governing compliance specification, layer architecture or additive package, extrusion hardware configuration, and final dimensional audit method.
In truck and trailer air brake systems, the finished tube is validated against SAE J844 and ISO 7628-1 for wall thickness, outside diameter, burst pressure, cold impact, and fitting retention after thermal aging. Standard production dimensions are 8 mm × 1 mm and 12 mm × 1.5 mm. The extruder is a single-screw machine with L/D 30:1, a grooved feed section, and a barrier screw; the barrel profile is set from 200°C at the feed throat to 225°C at the metering zone, and the die head is controlled at 225 ± 5°C. A gear melt pump between the screw and die stabilizes pressure and suppresses throughput pulsation that would otherwise show as outside diameter variation in the vacuum calibrator. A screen pack of 60/80/60 mesh is placed ahead of the breaker plate to build filtration pressure and trap agglomerated pigment or carbon black. Black tube is produced with 2.0–2.5 wt% carbon black masterbatch; natural or colored tube uses 1.0–2.0 wt% color concentrate, with no additional plasticizer because the grade is already plasticized. The melt enters a closed vacuum calibration tank where water temperature is held at 18–22°C and vacuum is set at -0.3 bar relative to atmosphere; a laser gauge controls haul-off speed and holds outside diameter within ±0.05 mm. Melt temperature above 240°C for more than 15 min generates oxidative gel particles that originate at the screw root and migrate to the inner wall, where they act as burst-initiation points in the SAE J844 test. Melt temperature below 215°C results in poor layer consolidation and axial die lines that the calibration sleeve cannot remove. The terminal article is coiled truck air brake tubing conditioned at 23°C and 50% RH according to ISO 291 before final dimensional and burst lot release.
Low-permeation evaporative fuel vapor return lines are produced by five-layer coextrusion in which VESTAMID® LX9012 occupies the outer polyamide layer over an ethylene vinyl alcohol copolymer barrier, with maleated polyolefin tie layers on both sides of the barrier. The outer PA12 layer is specified at 0.40–0.50 mm, the barrier at 0.10–0.15 mm, and each tie layer at 0.05–0.10 mm; the inner layer is either VESTAMID® LX9012 or a carbon-loaded PA12 compound at 0.25–0.35 mm. The coextrusion line uses a 25 mm single-screw extruder for the outer PA12 layer, a 20 mm extruder for the barrier polymer, and a 30 mm extruder for the inner layer, all feeding a spiral mandrel die. The outer PA12 melt temperature is constrained to 210–230°C; the feedblock and die are held at 225 ± 5°C. Temperatures above 230°C degrade the EVOH layer at the tie interface and produce delamination, while temperatures below 210°C reduce amide adhesion at the polyolefin tie layer. The finished line is quenched in a water trough at 16–20°C, laser-measured for ovality below 0.10 mm, and cut for fuel tank vapor return applications. Evaporative emissions compliance is evaluated under SAE J2260 and the applicable CARB or EPA evaporative emission protocol; the barrier layer governs permeation, while the outer LX9012 layer contributes burst resistance and fitting retention. The terminal article is a multi-layer fuel vapor line combining the barrier layer’s permeation resistance with the dimensional stability of the PA12 outer layer.
| Layer position | Material function | Typical thickness |
|---|---|---|
| Outer | VESTAMID® LX9012 PA 12 | 0.40–0.50 mm |
| Tie | Maleated polyolefin | 0.05–0.10 mm |
| Barrier | Ethylene vinyl alcohol copolymer | 0.10–0.15 mm |
| Tie | Maleated polyolefin | 0.05–0.10 mm |
| Inner | Carbon-loaded PA12 or VESTAMID® LX9012 | 0.25–0.35 mm |
For push-in fittings used in robotics and automated assembly lines, the sealing performance is governed by ISO 14743, and the tube outside diameter must remain within ±0.05 mm on a 6 mm OD line. VESTAMID® LX9012 is processed on a single-screw extruder with L/D 24:1 and a pin-and-sleeve die; the die melt temperature is set at 220–230°C. The calibration sleeve bore is 6.05–6.10 mm for a 6 mm × 1 mm tube, and the vacuum-pressure calibration circuit with thermal control of ±1°C maintains ovality below 0.06 mm. For colored pneumatic tube, 1.0–2.0 wt% masterbatch is added; natural tube runs without additive. The haul-off speed is set to a draw ratio of 0.95–1.05 between melt velocity and haul-off speed, because excessive draw-down raises axial orientation and increases post-connection dimensional recovery. After extrusion, the tube is conditioned for 24 h at 23°C and 50% RH according to ISO 291 before final diameter audit. An in-line ultrasonic wall-thickness scanner rejects sections with wall variation greater than 0.08 mm. The terminal article is cut into lengths for pneumatic manifolds, where push-in retention is checked at a working pressure of 1.0 MPa on the assembly cell and the axial movement of the tube in the fitting is recorded during the pressure hold.
Rail rolling-stock cable harness protection uses corrugated slit-conduit extruded from VESTAMID® LX9012 with nominal outside diameters from 16 mm to 50 mm, wall thickness 0.6–1.2 mm, and corrugation pitch 10–12 mm; the profile is formed in a vacuum corrugator at a die temperature of 225–235°C, and the compound is used either unmodified within installations outside the fire load boundary or with 20–30 wt% halogen-free flame-retardant masterbatch when EN 45545-2 fire performance is required for the finished cable conduit.
On construction machinery and agricultural equipment, spiral-cut PA12 hose wrap is produced by profile extrusion of VESTAMID® LX9012 into a flat ribbon with width 8–12 mm and thickness 0.8–1.2 mm, followed by heat-forming into a helix over the hydraulic hose. The abrasion resistance is evaluated under ISO 4649; published data for this specific configuration is limited, so the mass loss value must be verified on the actual hose assembly because the result depends on the rubber outer cover compound, surface roughness, and helix pitch. Processing uses a single-screw extruder with a flat slit die and a polished three-roll stack; roll temperatures are maintained at 60–80°C to control orientation relaxation. A laser width gauge monitors ribbon width before the three-roll stack. The compound is predried to moisture below 0.10% and the melt temperature is held at 225–235°C. A UV-stabilized carbon black masterbatch is added at 2.0–2.5 wt% for outdoor service; this addition reduces surface gloss variability but does not replace the need for the hose base cover to resist oil. The operational incompatibility is with hydraulic mineral oil containing aromatic extracts: prolonged contact causes PA12 swelling, tensile-strength loss, and premature helix distortion. The terminal article is an external spiral sheath for hydraulic hose protection in construction and agricultural machinery, where abrasion and impact resistance govern service life.
Competitive Evonik VESTAMID® LX9012 PA 12 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8615365186327 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8615365186327
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
VESTAMID® LX9012 PA 12 is a semi-crystalline polyamide 12 extrusion compound supplied by Evonik Industries. The grade is positioned for applications in which unmodified PA 12 is too stiff and a thermoplastic elastomer is chemically or economically unnecessary. Supplier datasheet values place density at 1.01 g/cm³ (ISO 1183-1) and tensile modulus below 500 MPa (ISO 527-1/-2), with Shore D hardness typically below 65 (ISO 868). The crystalline melting peak is reported near 176 °C (ISO 11357-3). The material is supplied as unfilled natural or black pellets and is processed on conventional single-screw extruders with general-purpose polyamide screw geometry.
The molecular structure is based on laurolactam, giving a longer hydrocarbon sequence between amide groups than PA 6 or PA 66. This structure reduces equilibrium moisture uptake. Published saturation values for PA 12 are typically 1.3–1.7% by weight (ISO 62), compared with 9.0–10.0% for unfilled PA 6. The lower uptake reduces dimensional change and tensile-property drift when extruded tube or cable jacketing moves from dry-as-molded conditions to humid service. In processing terms, the grade is not drying-optional: residual moisture above 0.10% (ISO 15512) can produce surface roughness, melt-pressure fluctuation, and pitting in thin-wall profiles below 1.0 mm wall thickness.
Low-temperature ductility separates the material from rigid polyamide alternatives. Unmodified PA 12 grades such as VESTAMID L1600/L1700 typically exhibit notched Charpy impact energies between 5 kJ/m² and 8 kJ/m² at −30 °C (ISO 179/1eA). Unfilled PA 6 in the dry condition is commonly below 5 kJ/m² under the same test. Impact-modified PA 12 grades of the LX class are reported with notched Charpy values above 10 kJ/m² at −30 °C, with failure in many extruded parts being ductile yielding rather than brittle cracking. This distinction matters for pneumatic brake tubing and hydraulic hose jackets that are assembled outdoors and then pressurized at temperatures below −20 °C.
Water absorption also changes material selection. At saturation (ISO 62), unfilled PA 6 absorbs approximately 9–10% water by weight and loses a substantial fraction of its dry-state tensile modulus. PA 12 variants stabilize at roughly 1.3–1.7%. For extruded monolayer air-brake or fuel-vapor tubing, this keeps ovality and longitudinal expansion more predictable after exposure to humid air or drained condensate. The lower density of PA 12 at 1.01 g/cm³ (ISO 1183-1) also reduces coil weight per running meter compared with PA 6 at 1.14 g/cm³ for the same wall section.
Chemical resistance differences follow from amide group concentration. PA 12 contains a longer hydrocarbon sequence than PA 6 or PA 66, so the swelling and stress-cracking response in calcium chloride, zinc chloride, and diesel fuel is generally less aggressive. Compatibility is not unlimited. Fluid-contact performance should be validated against the actual formulation, including organic acids and oxidizing media, using immersion testing under ISO 175 rather than generic PA 12 resistance tables.
The most frequent production failure on single-screw lines is not a melting problem but a moisture-induced melt-viscosity change. Equipment behavior observed on polyamide extrusion lines with screw diameters of 30–60 mm and L/D ratios of 28:1–30:1 shows that resin with surface moisture above 0.10% produces pulsating melt pressure at the breaker plate, irregular parison size, and pitting on the inner surface of vacuum-calibrated tube. Pre-drying in a desiccant dryer at 80 °C for 4–8 h to a dew point of −30 °C or lower is therefore mandatory for opened bags processed in ambient relative humidity above 60%. Hopper loaders should be blanketed with dried air because regrind can reach 0.25% moisture within a single shift under humid conditions.
Barrel profiles used for the grade lie in the 210–240 °C range, with the die head held at 220–230 °C. Melt temperature measured by an immersion probe should remain below 250 °C for continuous operation. Excursions above 260 °C accelerate chain scission and produce gels in the extrudate after 15–20 min of residence time. A three-zone screw with a compression ratio of 2.5:1–3.0:1 and a fitted breaker plate with 80/120 mesh screens is adequate for unfilled material. For wall thicknesses below 0.5 mm, a gear pump between the extruder and die is used to suppress pressure variation below ±2% of setpoint.
Downstream calibration is performed with a vacuum sizer at −0.2 to −0.6 bar and cooling water at 20–40 °C. The air gap between die exit and calibrator entry is set between 5 mm and 25 mm for tubing diameters from 4 mm to 16 mm; larger diameters may require a supporting pressure die. At wall thickness below 0.75 mm, the lower melt stiffness of the impact-modified matrix increases eccentricity if vacuum draw is too high. Published data for this specific configuration is limited, and line trials should map haul-off ratio against die swell for each die set.
The table summarizes representative dry-as-molded property ranges for the impact-modified PA 12 class containing VESTAMID LX9012, compared with unmodified PA 12 and unfilled PA 6. Ranges are compiled from supplier datasheets and are provided for selection screening only; lot-specific values should be verified against certification data.
| Property | Test method | VESTAMID LX9012 PA 12 | Unmodified PA 12 | Unfilled PA 6 dry |
|---|---|---|---|---|
| Density | ISO 1183-1 | 1.01 g/cm³ | 1.01 g/cm³ | 1.14 g/cm³ |
| Tensile modulus | ISO 527-1/-2 | 250–500 MPa | 1400–1800 MPa | 2600–3200 MPa |
| Shore D hardness | ISO 868 | 55–65 | 75–78 | 80–83 |
| Notched Charpy at −30 °C | ISO 179/1eA | 10–20 kJ/m² | 5–8 kJ/m² | 3–5 kJ/m² |
| Water absorption at saturation | ISO 62 | 1.3–1.7% | 1.3–1.7% | 9.0–10.0% |
| Melting peak | ISO 11357-3 | 176–180 °C | 176–180 °C | 220–225 °C |
For pneumatic brake lines, coiled tubing, and hydraulic hose jackets, VESTAMID LX9012 PA 12 is processed into monolayer or coextruded structures where low-temperature impact retention is specified. The grade itself is unfilled and does not provide electrical conductivity; antistatic variants require a separate carbon-black-filled compound or coextruded stripe. Dimensional inspection after extrusion normally follows supplier drawing tolerances rather than a single ISO plastic-part standard. First-article inspections should therefore include ovality, wall-thickness variation, and burst strength measured according to the specific hose or tubing specification, such as SAE J844 for nonmetallic air brake tubing or ISO 7628 for road-vehicle air brake tubing.
In cable sheathing and industrial hose jackets, the material is selected for resistance to hydrolysis and for retention of flexibility after outdoor aging. PA 12 has lower equilibrium moisture uptake than PA 6, which reduces the shift in electrical properties after humid aging. Electrical property statements should be verified by the relevant cable specification rather than by generic resin values; published data for this specific configuration is limited. When abrasion resistance is critical, formulations with additional high-density polyethylene or crosslinked outer layers are used because unfilled impact-modified PA 12 does not match the abrasion benchmarks of crosslinked polyethylene or polyurethane.
When post-extrusion forming or welding is required, the material can be joined by hot-plate, laser, or ultrasonic welding under conditions suitable for semi-crystalline PA 12. The heat-affected zone is more susceptible to stress relaxation than higher-modulus PA 12 because of the lower stiffness and crystalline orientation after drawing. No joining performance claim is made without joint-specific validation under ISO 13954 or a customer-equivalent peel-tensile procedure.