| HS Code | 692109 |
| Density | 1.03 g/cm³ |
| Glass Fiber Content | 4% |
| Water Absorption 24h 23 C | 0.2% |
| Tensile Modulus | 1100 MPa |
| Tensile Stress At Yield | 38 MPa |
| Tensile Strain At Yield | 5% |
| Charpy Notched Impact Strength 23 C | 5 kJ/m² |
| Shore D Hardness | 72 |
| Melting Point | 178 °C |
| Vicat Softening Temperature | 170 °C |
| Heat Deflection Temperature 0 45 Mpa | 95 °C |
| Heat Deflection Temperature 1 8 Mpa | 55 °C |
| Volume Resistivity | 1.0e13 Ω·cm |
| Dielectric Strength | 30 kV/mm |
As an accredited Evonik VESTAMID® LXM4 Nylon 12, 4% Glass Fiber Reinforced factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg net sealed multi-ply paper bags with polyethylene liner, palletized and shrink-wrapped for safe transport. |
| Container Loading (20′ FCL) | 20′ FCL container loading of Evonik VESTAMID LXM4 Nylon 12, 4% glass fiber reinforced, securely packed and stowed for safe transport. |
| Shipping | Evonik VESTAMID® LXM4 Nylon 12 with 4% glass fiber ships as dry, sealed pellets in moisture-barrier bags or drums. Avoid exposure to humidity, as the resin is hygroscopic. Keep containers closed, store in a cool, dry area, and protect from physical damage during transit. |
| Storage | Store VESTAMID® LXM4 in its original, unopened packaging in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Keep containers tightly sealed to prevent humidity absorption, which can degrade the nylon. Avoid exposure to UV radiation and contamination. Under proper conditions, shelf life is typically indefinite. |
| Shelf Life | Evonik VESTAMID LXM4 has a shelf life of at least two years when stored dry, sealed, and unopened. |
The substitution of unreinforced PA11 or PA12 grades in heavy-duty air brake circuits is qualified through burst-pressure stability of coiled tubing after the conditioning sequence of SAE J844 and ISO 7628-1:2015. Evonik VESTAMID® LXM4 Nylon 12 is pre-dried in a closed-loop desiccant dryer to a residual moisture of ≤ 0.05 wt% at 80 °C for 4 h to 6 h; converter batches with residual moisture above 0.08 wt% produce splay at the vacuum-calibration die and lower secondary burst-pressure retention. The extrusion stock is charged at 100 wt% virgin material or with closed-loop in-house regrind capped at 20 wt%. Regrind fractions above 20 wt% reduce short-glass fiber aspect ratio and generate a measurable shift in melt-flow index when tested according to ISO 1133-1:2022, requiring die-pressure compensation on the line. Color concentrate in a PA12 carrier is permitted at 1 wt% to 3 wt%; secondary glass-fiber addition is not made on the shop floor. Tubing is extruded on a single-screw extruder with 30:1 to 36:1 L/D, a grooved feed section, and barrier mixing flights. Melt temperature is maintained between 230 °C and 250 °C; excursions above 260 °C initiate oxidative yellowing and film accumulation at the die exit. Downstream vacuum calibration and closed-loop ultrasonic diameter gauging constrain ovality to ≤ 0.15 mm over outside-diameter ranges of 6.0 mm to 16.0 mm. Terminal products include Type A and Type B coiled air brake lines with push-to-connect fittings for commercial vehicle trailers and straight truck chassis.
Multiple 4 mm to 8 mm outside-diameter pneumatic control lines bundled in cable carriers require dimensional repeatability at the push-in connector interface and consistent pull-out resistance after cyclic bending. VESTAMID® LXM4 is extruded at 100 wt% resin for this application; an antistatic carbon black masterbatch in PA12 carrier is added at 3 wt% to 5 wt% only where equipotential bonding or ATEX equipment-level requirements are specified in the circuit design. Additional glass fiber is not blended at the converting step because the as-supplied 4 wt% short-glass reinforcement already increases connector pull-out retention when finished tube is tested against ISO 14743:2004. The downstream process employs a single-screw extruder with 24:1 to 28:1 L/D, a pressure-type die, and a two-stage cooling trough with water temperatures stepped from 45 °C to 20 °C. Melt temperature is held between 220 °C and 240 °C, with the lower limit constrained by melt fracture and the upper limit by surface gloss instability. The governing system-level standard is ISO 4414:2010, and burst/collapse margins are verified on finished tube according to pressure-test references in ISO 7628-1:2015. Terminal outputs are color-coded pneumatic control line sets for automated packaging, assembly, and machine-tool actuation.
In AC and DC charging cable constructions, the outer sheath must maintain flexibility at -40 °C while resisting curb abrasion and connector strain-relief tearing. VESTAMID® LXM4 is extruded as a jacketing layer over the assembled power and pilot cores via pressure tooling on a 25:1 to 30:1 L/D single-screw jacketing line. Melt temperature is controlled between 225 °C and 245 °C; post-extrusion cooling is staged from 60 °C to 20 °C to minimize crystallinity gradients across the sheath wall. Formulation limits are 95 wt% to 100 wt% VESTAMID® LXM4, with UV stabilizer masterbatch at 2 wt% to 4 wt%; no secondary glass-fiber concentrate is added because the as-supplied 4 wt% reinforcement already reduces sheath elongation at break when tested under IEC 60811-501. Cold impact and low-temperature flexing are governed by IEC 60811-504 and ISO 6722-1:2021 where automotive-compliant charging harnesses are supplied. Converter molding trials must verify that the reduced elongation of the glass-filled sheath is compatible with the specific charging connector strain-relief socket geometry. Terminal products include flexible EV charging cables for residential AC and public fast-charge stations, with outer sheath wall thicknesses typically between 0.8 mm and 1.5 mm depending on cable outside diameter.
Five-layer co-extruded fuel vapor return lines replace formed steel tubes when evaporative emission limits require a low-permeation thermoplastic architecture with conductive inner-surface dissipation. In this structure, the outer jacket layer is charged at 100 wt% VESTAMID® LXM4; an inner conductive PA12 layer contains 8 wt% to 12 wt% conductive carbon black additive; and the regrind-bearing core layer is limited to 40 wt% to 50 wt% in-house process scrap from the same line. The downstream operation is a five-extruder co-extrusion cell feeding a spiral mandrel die, with individual melt temperatures of 215 °C to 240 °C and an ultrasonic wall-thickness gauge scanning at 100 Hz to maintain layer-to-layer concentricity. Vacuum calibration follows the die; after calibration, the tube passes through an internal ID/OD laser inspection stage before cutting. Leak-tightness and permeation performance are validated under SAE J2260 low-permeation fuel system requirements. Terminal products include fuel vapor return lines routed from the carbon canister to the fuel tank and fill-neck vapor recovery lines in light-duty vehicle platforms.
For outdoor fiber optic drop cables routed through duct banks with documented rodent attack, the outer buffer must resist localized compressive loads without transferring micro-bend to the optical fiber. VESTAMID® LXM4 is compounded directly into the loose tube buffer at 100 wt% resin, with a carbon black masterbatch at 2 wt% to 3 wt% for weathering resistance. The material enters a high-speed single-screw extrusion line with 30:1 to 34:1 L/D and a precision gear pump, with melt temperature maintained between 225 °C and 245 °C. Tube diameters from 1.5 mm to 3.0 mm outside diameter are held to a wall-thickness tolerance of ± 0.05 mm by laser telemetry; line speeds are intentionally reduced relative to unreinforced PA12 to avoid melt fracture at the die entry. Compliance is anchored to mechanical crush, impact, and tensile test methods of IEC 60794-1-21, with material-level oxidative induction time measured under ISO 11357-6. Published third-party data for this exact 4 wt% glass-filled grade in loose-tube buffers is limited; qualification programs therefore rely on converter-specific validation against field samples. Terminal products include loose tube buffers and outer stem sheaths for rodent-protected outdoor optical fiber cables.
| Application scenario | Primary standard | Formulation boundary | Process equipment |
|---|---|---|---|
| Air brake tubing | SAE J844, ISO 7628-1:2015 | ≤ 20 wt% regrind; ≤ 0.05 wt% residual moisture | Single-screw extruder, 30:1–36:1 L/D |
| Pneumatic control lines | ISO 4414:2010, ISO 14743:2004 | 100 wt% LXM4; 3 wt%–5 wt% antistatic masterbatch | Single-screw extruder, 24:1–28:1 L/D |
| EV charging cable sheath | IEC 62893-1, IEC 60811-504 | 95 wt%–100 wt% LXM4; 2 wt%–4 wt% UV masterbatch | Pressure tooling, 25:1–30:1 L/D jacketing line |
| Fuel vapor return lines | SAE J2260 | Outer jacket 100 wt%; core regrind 40 wt%–50 wt% | Five-extruder spiral mandrel co-extrusion |
| Optical loose tube buffer | IEC 60794-1-21, ISO 11357-6 | 100 wt% LXM4; 2 wt%–3 wt% carbon black | High-speed extruder, 30:1–34:1 L/D with gear pump |
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Evonik VESTAMID® LXM4 Nylon 12, 4% glass fiber reinforced, is a compound in the VESTAMID L polyamide 12 family. The polymer matrix is synthesised by hydrolytic polycondensation of laurolactam. The grade-specific modification is a nominal short glass fiber addition of 4% by mass, which is low enough to preserve the chemical resistance and low moisture uptake of PA12 while raising tensile modulus, creep resistance, and dimensional repeatability relative to an unfilled PA12 base. In supplier documentation the customary test designations include ISO 1183-1 for density, ISO 527-1/-2 for tensile properties, ISO 179-1/1eA for Charpy impact, ISO 1133-1 for melt volume-flow rate, ISO 11357-3 for melting temperature, ISO 75-1/-2 for heat deflection temperature, and ISO 294-4 for mould shrinkage. Published data for this exact configuration is limited; tooling and process capability studies should be validated against the current Evonik datasheet rather than against generic PA12 literature.
The 4% fiber fraction is below the concentration at which short glass fibers dominate the in-plane shrinkage field. In injection moulded plaques, the large flow-direction and cross-flow shrinkage divergence observed in 30% glass fiber PA12 grades is muted. Unfilled PA12 commonly exhibits mould shrinkage between 0.9% and 1.4% under ISO 294-4, while PA12-GF30 can fall below 0.4% in the flow direction. The low-glass compound occupies an intermediate band, with the practical consequence that flat covers and clamping rails are less prone to out-of-plane warpage than equivalent parts moulded from neat PA12. The low fiber loading also reduces the degree of anisotropic post-shrinkage after exposure to elevated temperature. Weld-line strength is a separate constraint. When two melt fronts meet in a double-gated tensile specimen, fiber orientation at the weld plane is predominantly parallel to the front, leaving little fiber bridging across the interface. The result is a weld-line tensile strength below the bulk value. For wall sections below 2 mm, production tooling should include overflow wells, sequential valve gating, or gate positions placed away from the principal stress vector. Mould-filling analysis should be used to identify the meeting angle of the flow fronts because low meeting angles below 45° produce a longer weld plane and a higher probability of low-temperature crack initiation.
Melt processing of this product is governed by moisture control and tool temperature. The material is less hygroscopic than PA6 or PA66, but absorbed moisture above 0.1% by ISO 15512 Karl Fischer titration is capable of hydrolytic chain scission and surface splay. Sealed bags are usually supplied dry. Once opened, exposure to relative humidity above 60% for more than 8 h justifies re-drying. Desiccant drying at 80 °C to 90 °C for 4 h to 6 h with a supply-air dew point below -30 °C is adequate for most injection moulding operations. The compound is processed on a single-screw injection moulding machine equipped with a general-purpose polyamide screw of L/D ≥ 20 and a shut-off nozzle. Barrel profiles between 220 °C and 250 °C are typical, with a tool temperature of 40 °C to 60 °C. Tool temperature below 30 °C is not recommended for thin sections because the quenched skin layer can delaminate under ejection stress when the low fiber content does not provide sufficient melt stiffness. In capillary rheometry per ISO 11443, the low fiber volume fraction has limited effect on shear viscosity at shear rates above 1,000 s⁻¹, but at shear rates below 10 s⁻¹ the dispersed fiber network can raise viscosity and reduce die swell. This means that thick-walled parts with long flow lengths may require slightly higher pack pressures than unfilled PA12 to compensate for low-shear melt stiffness.
The product sits between unfilled PA12 and PA12-GF30 in stiffness, density, and ductility. Generic unfilled PA12 grades report tensile elongation at break above 200% by ISO 527-1/-2, whereas PA12-GF30 grades often fall below 5%. The 4% glass fiber loading reduces elongation relative to neat PA12 but leaves enough permanent deformation capacity for snap-fit and press-fit assemblies that would be marginal in a high-glass compound. Tensile modulus of unfilled PA12 is commonly near 1,500 MPa; a low-glass formulation can be expected to add a few hundred MPa, while PA12-GF30 is typically reported between 6,500 MPa and 8,000 MPa depending on fiber length distribution and orientation. Density follows the same hierarchy. Unfilled PA12 is near 1.01 g/cm³, PA12-GF30 is commonly near 1.23 g/cm³, and the low-glass grade remains marginally above the unfilled density. Heat deflection temperature under 1.8 MPa per ISO 75-1/-2 is expected to fall between the unfilled PA12 value, often below 60 °C, and the PA12-GF30 value, often above 90 °C. The low fiber content therefore does not constitute a structural upgrade in the same sense as 30% glass fiber reinforcement; it is a controlled stiffness modification.
Component classes suited to this material include electrical connector backshells, cable glands, pneumatic clips, automotive interior brackets, and fluid-line retention clips. In fluid-contact service, PA12 is established for aliphatic hydrocarbons, mineral oils, greases, and automotive fuels. The 4% glass fiber fraction introduces no significant barrier enhancement over neat PA12 and does not create the permeability advantage of high-fiber compounds. Published data for this specific configuration is limited; converters designing fuel-contact components should perform OEM-level fuel exposure rather than relying solely on coupon immersion. For dry electrical applications, the material is typically evaluated for comparative tracking index and glow-wire performance according to IEC 60112 and IEC 60695-2 where a fire rating is required for the assembled part. Electrical grade performance depends on pigments, regrind level, and conditioning; it should be re-tested on production-coloured resin.
PA12 has a lower amide-group density than PA6 or PA66, which limits moisture absorption and the associated dimensional change. Saturation water uptake for neat PA12 is commonly near 1.4% by ISO 62, while PA6 can exceed 9%. The 4% glass fiber fraction lowers the absolute dimension change per unit moisture uptake without changing the fundamental absorption kinetics. The material is therefore suitable for humid interior environments and outdoor enclosures where PA6 would accumulate excessive moisture. Limitations include concentrated mineral acids, phenols, benzyl alcohol, and saturated steam above 140 °C. Stress cracking should be validated with production lubricants and cleaning agents because low-fiber PA12 can show environmental stress cracking under aggressive surfactants at elevated temperature. The compliance matrix below summarises the standard designations and regulatory boundaries commonly associated with a VESTAMID PA12 compound.
| Parameter or obligation | Reference method or regulation | Condition relevant to VESTAMID LXM4 |
|---|---|---|
| Density | ISO 1183-1 | PA12 baseline near 1.01 g/cm³; glass-containing grade slightly higher |
| Tensile properties | ISO 527-1/-2 | Test temperature 23 °C; specimens conditioned per ISO 1110 |
| Charpy impact, notched | ISO 179-1/1eA | Type 1 specimen; notch radius 0.25 mm |
| Melting temperature | ISO 11357-3 | DSC second heating scan; PA12 melting range usually 175 °C to 180 °C |
| Moisture threshold | ISO 15512 | Maximum 0.1% before melt processing |
| Mould shrinkage | ISO 294-4 | Dependent on flow direction, wall thickness, gate geometry |
| RoHS | 2011/65/EU and (EU) 2015/863 | Supplier declaration required for final article |
| REACH SVHC | Regulation (EC) 1907/2006, Article 33 | Concentration below 0.1% w/w per article or declaration |
| Food contact | 21 CFR 177.1500 and 21 CFR 174.5 | Final article migration testing required; end-use conditions apply |
At 23 °C and 50% relative humidity, conditioned PA12 absorbs roughly 0.7% water. In constrained assemblies this moisture-driven expansion can exceed thermal expansion effects. The 4% glass fiber fraction reduces the effective linear coefficient of expansion in the flow direction but leaves the cross-flow coefficient closer to neat PA12. Designers should not assume isotropic expansion in thin ribs, bosses, or weld regions. Conditioned specimens used for mechanical testing should be equilibrated per ISO 1110; dry-as-moulded data overstate modulus and understate toughness. This is a common source of discrepancy when lot-to-lot process capability studies are compared across different plants.
For extrusion of tubing and small profiles, the low glass fiber loading reduces melt strength relative to PA12-GF30. The air gap between die and calibration sleeve should be minimised, and vacuum calibration tanks should be operated at water temperatures between 20 °C and 40 °C. Melt temperatures in the 240 °C to 260 °C range improve surface uniformity, but screw-speed variations above ±5% can produce wall-thickness instability in annular dies because the low fiber content provides less structural retention in the melt. Screens finer than 60 mesh are generally avoided upstream of thin-wall profile dies because the pressure increase can exceed the barrel pressure limit of small single-screw extruders with L/D 25 to 30.
Regrind use is limited to 20% by mass in non-appearance parts where glass fiber length distribution remains within the supplier's accepted range. Multiple re-melting cycles reduce fiber length and lower notched impact; when regrind content exceeds this threshold, shot-to-shot variability increases because the mixture contains a bimodal distribution of glass fiber lengths. For appearance parts with exposed surfaces, the low fiber fraction is less abrasive than PA12-GF30 but can still produce surface roughness after prolonged runs exceeding 20,000 shots if hot-runner tips are not maintained.