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Evonik VESTAMID® LXM8 Nylon 12, 8% Glass Fiber Reinforced

    • Product Name: Evonik VESTAMID® LXM8 Nylon 12, 8% Glass Fiber Reinforced
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 619320
    Density Iso 1183 1.06 g/cm³
    Tensile Modulus Iso 527 3400 MPa
    Tensile Stress At Break Iso 527 85 MPa
    Elongation At Break Iso 527 8 %
    Flexural Modulus Iso 178 3200 MPa
    Flexural Strength Iso 178 100 MPa
    Charpy Notched Impact Strength At 23 C Iso 179 1ea 4 kJ/m²
    Melting Temperature Dsc Iso 11357 178 °C
    Heat Deflection Temperature At 1 80 Mpa Iso 75 85 °C
    Water Absorption At Saturation In Air 23 C Iso 62 1.3 %
    Glass Fiber Content 8 %

    As an accredited Evonik VESTAMID® LXM8 Nylon 12, 8% Glass Fiber Reinforced factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Evonik VESTAMID® LXM8 Nylon 12, 8% glass fiber reinforced, supplied in 25 kg polyethylene bags.
    Container Loading (20′ FCL) Container Loading (20′ FCL): VESTAMID LXM8 Nylon 12, 8% glass fiber reinforced, shipped in sealed bags on pallets, securely loaded full container.
    Shipping VESTAMID® LXM8 ships as solid pellets in sealed, moisture-proof bags or drums to prevent moisture uptake. Store in a cool, dry area, away from incompatible materials. Handle with standard industrial precautions; avoid dust inhalation and contact with eyes or skin. No special transport classification required under normal conditions.
    Storage Store VESTAMID® LXM8 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 water absorption, which can degrade processing and mechanical properties. Under recommended conditions, shelf life is typically two years from manufacture.
    Shelf Life Shelf life is typically 2 years from date of manufacture when stored in original, unopened packaging under dry conditions.
    Application of Evonik VESTAMID® LXM8 Nylon 12, 8% Glass Fiber Reinforced
    Diesel fuel vapor return line stock produced from 8% glass fiber reinforced nylon 12 is routinely subjected to permeation testing under SAE J2260 or SAE J2043 protocols at 60°C with CE10 reference fuel. The 8% glass fiber loading alters wall-section crystallinity gradients relative to unfilled PA12, which in turn modifies both steady-state hydrocarbon permeation flux and the transient breakthrough window after initial fuel contact. Tube extrusion for this application typically runs melt temperatures between 225°C and 245°C, with downstream vacuum calibration holding outer diameter tolerance within ±0.05 mm on nominal diameters of 8 mm to 10 mm. Moisture control prior to extrusion is non-negotiable: resin moisture above 0.10% by weight promotes hydrolysis-induced molecular weight reduction during the melt residence window, and pre-drying at 80°C for 4 h to 8 h in a desiccant dryer with a dew point of −40°C or lower is the standard safeguard. Draw-down ratios in the sizing tank are held between 1.05:1 and 1.15:1 to preserve hoop tensile orientation without inducing unacceptable longitudinal shrinkage during post-extrusion annealing. Finished tube assemblies are connector-tested for pull-off retention after thermal cycling from −40°C to 90°C, because the glass fiber reinforcement raises tube stiffness and reduces radial compliance at barbed fitting interfaces. Terminal components in this segment include diesel fuel return lines, vapor recovery lines, and evaporative emission transfer tubing for heavy-duty diesel powertrains. Published data for this specific grade under long-term ethanol-blended fuel exposure remains limited, and accelerated soak testing in E10 and E25 media at 60°C is recommended before platform qualification.

    What Burst Pressure Window Governs SAE J844 Air Brake Tube Extrusions?

    Truck and trailer air brake tubing fabricated from PA12-GF8 must demonstrate burst pressure capacity well above the operating envelope defined in SAE J844 and ISO 7628. The 8% glass fiber reinforcement raises the hoop stress at break relative to unfilled PA12, but it simultaneously narrows the strain-to-failure margin, and processing must be tuned to preserve a consistent fiber orientation distribution through the tube wall. Cold impact resistance at −40°C is a qualifying pass/fail criterion under SAE J844, and the low glass fiber loading is selected specifically to retain low-temperature ductility while providing enough modulus to resist kinking at minimum bend radii. Extrusion equipment for this application typically employs a single-screw extruder with an L/D ratio between 24:1 and 30:1, a compression ratio of 2.5:1 to 3.0:1, and a barrier screw design to minimize shear heating. Melt temperatures are maintained at 230°C to 250°C, measured at the adapter, and melt pressure is held below 20 MPa to avoid excessive fiber attrition at the breaker plate. Failure modes observed on production lines include internal melt fracture at the die land when head pressure exceeds 18 MPa, and surface shark-skin defects when draw-down exceeds 1.20:1. The terminal product is coiled air brake tube in standard sizes with outside diameters of 6.35 mm, 9.53 mm, 12.7 mm, and 15.88 mm, color-coded per SAE J844 requirements. Burst testing is conducted at 23°C and at 80°C, with typical acceptance thresholds requiring a minimum burst-to-working-pressure ratio of 4:1 at ambient temperature and 3:1 at elevated temperature.Permeation resistance in PA12 fuel-contact layers is not solely a function of crystallinity. The glass fiber interface region creates microvoids during thermal cycling that can act as diffusion shortcuts under repeated exposure to aromatic fuel fractions. Consequently, processing parameters that minimize interfacial void formation—low melt residence time, controlled moisture, and sufficient packing pressure during calibration—are as critical as base resin selection. Wall thickness is typically specified at 0.8 mm to 1.5 mm for vapor lines and 1.5 mm to 2.0 mm for return lines, with the thicker sections favored when connector insertion retention forces exceed 200 N. Sourcing inspection includes a mandrel bend test at −40°C without fracture and a tensile elongation-at-break check under ISO 527-2 that typically must remain above 30% at 23°C to ensure sufficient assembly flexibility. The dispersion quality of the glass fiber is assessed metallographically on cryo-fractured cross-sections, where agglomerates larger than 50 µm are grounds for lot rejection.

    Hydraulic Hose Jacket Compounds for API 17K Service

    Glass fiber reinforced PA12 jacket stock for subsea hydraulic hoses is specified primarily for abrasion resistance and dimensional stability under hydrostatic loading. The material is extruded as a tight jacket over reinforced thermoplastic hose bodies, and the 8% fiber content provides modulus retention during spooling and deployment operations. No further elaboration is warranted for this established practice.

    Push-In Fitting Retention Forces and Fiber Orientation Effects

    Injection-molded pneumatic push-in fittings produced from PA12-GF8 require careful gate placement because glass fiber orientation follows flow direction and directly governs radial hoop strength at collet retention zones. A melt temperature of 240°C to 260°C and a mold temperature of 60°C to 80°C are typical for this geometry class, and holding pressure must be maintained between 50 MPa and 80 MPa to compensate for the higher melt viscosity introduced by fiber loading. Shrinkage is anisotropic: values range from 0.4% to 0.6% in the flow direction and 0.7% to 1.0% transverse to flow, which complicates thread form tolerances on NPT and BSPP port threads. Thread engagement torque testing follows ISO 6150 connection requirements for pneumatic quick couplings, and retention force testing at −20°C and 60°C is conducted to bracket field operating conditions. Terminal products include push-in fittings for compressed air distribution networks in factory automation and commercial vehicle pneumatic systems.Offshore dynamic cable sheathing is engineered for long-term flexural fatigue in wave-loaded environments. The PA12-GF8 sheath compound is extruded over power and control cable cores, and qualification testing includes the cyclic bending regime specified in IEC 60840 or project-specific dynamic cable test programs aligned with DNVGL-RP-0360. The glass fiber content is deliberately limited to 8% because higher loadings can initiate surface micro-cracks during high-cycle flexing at minimum bend radii, which propagates dielectric degradation in the underlying insulation. Processing temperature windows are held between 220°C and 240°C at the extruder die, with slow post-extrusion cooling in air to reduce frozen-in stress at the sheath-core interface. Terminal products include dynamic power cables used for floating offshore wind turbines and subsea control umbilical sheaths. Long-term seawater aging data for glass-filled PA12 outer sheaths remains limited for service life estimates beyond 25 years, and qualification programs should include accelerated aging in synthetic seawater at 45°C with weekly tensile property monitoring per ISO 527-2.

    When Coolant Contact Demands Low Extractable Profiles in PA12 Formulations

    Automotive coolant transfer lines made from PA12-GF8 must demonstrate hydrolytic stability in extended contact with organic acid technology coolants at service temperatures approaching 130°C. The glass fiber content creates additional polymer-fiber interfaces where coolant additive adsorption can occur, and extractable testing is performed per gravimetric methods aligned with ISO 6427 using a 1 M monoethylene glycol / water mixture. Tensile strength retention after 1,000 h exposure at 125°C is typically specified at not less than 70% of the unaged value when tested under ISO 527-2. Extrusion for this application follows the same moisture control and melt temperature practices described for fuel lines, but the terminal product demands are different: the finished tube is formed into convoluted sections by hot-air bending or corrugation, and the glass fiber reduces sag during post-extrusion thermoforming operations. Terminal products include turbocharger coolant feed tubes, battery thermal management circuit lines, and EGR cooler transfer hoses.Industrial compressed air distribution tubing manufactured from PA12-GF8 is pressure-rated for continuous service at 10 bar to 16 bar, depending on wall thickness and operating temperature class. The 8% glass fiber loading provides improved stiffness for suspended spans between support brackets, reducing sag deformation in plant installations compared to unfilled PA12 tube. Pressure cycling per ISO 19859 or manufacturer-specific fatigue protocols is used to qualify the material for applications involving frequent compressor start-stop sequences. Condensate compatibility is a practical concern: PA12 demonstrates resistance to synthetic compressor oil residues at temperatures up to 70°C, and the glass fiber content does not measurably alter this resistance profile. Terminal products include main distribution headers, drop legs, and machine-level air supply lines in automotive assembly plants, food packaging operations, and electronics manufacturing clean rooms.
    Application SegmentPrimary Compliance StandardReference TemperatureQualification Parameter
    Diesel fuel vapor return lineSAE J2260, SAE J204360°CCE10 permeation flux
    Truck air brake tubeSAE J844, ISO 7628−40°C to 80°CBurst ratio, cold impact
    Subsea hydraulic hose jacketAPI 17K4°C seawaterAbrasion, hydrostatic integrity
    Pneumatic push-in fittingISO 6150−20°C to 60°CRetention force, thread torque
    Offshore dynamic cable sheathIEC 60840, DNVGL-RP-0360−20°C to 45°CCyclic bending fatigue
    Automotive coolant transfer lineISO 6427, ISO 527-2125°CHydrolytic tensile retention
    Industrial compressed air lineISO 1985923°C to 70°CPressure cycling integrity
    Processing ParameterTube Extrusion (Fuel/Air)Injection Molding (Fittings)Sheath Extrusion (Cable Jacket)
    Melt temperature range225°C250°C240°C260°C220°C240°C
    Pre-drying condition80°C, 4–8 h, dew point −40°C80°C, 4–6 h, dew point −40°C80°C, 4–8 h, dew point −40°C
    Tooling / mold temperatureSizing sleeve 20°C40°CMold 60°C80°CDie head 210°C230°C
    Critical control limitMelt pressure < 20 MPaHolding pressure 50–80 MPaLine speed matched to < 50 m/min
    Process-specific defectInternal melt fractureFiber agglomeration at knit linesSurface micro-cracking at shear lips
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    Certification & Compliance
    More Introduction

    Evonik VESTAMID® LXM8 is a semicrystalline polyamide 12 compound carrying 8% by weight glass fibre, designated PA12 GF8 under ISO 1043-1. The base polymer is produced by polycondensation of laurolactam, and the glass phase is introduced in a compounding step that preserves discrete fibre rather than producing a chemically coupled matrix. Published physical data for natural injection-moulding grade list density of 1.05 g/cm³ when measured to ISO 1183, which is approximately 0.04 g/cm³ above unfilled PA12. The filler is not a mineral filler; the glass fibre raises short-term stiffness and reduces mould shrinkage but does not shift the melting point of the PA12 matrix, which remains at 176 °C per ISO 11357-1/-3. At 1.6 mm, the natural grade is classified HB under UL 94.

    Dry-as-moulded mechanical values at 23 °C include tensile modulus of 1,900 MPa, yield stress of 45 MPa, and nominal strain at break of 15% under ISO 527-1/-2. Notched Charpy impact strength is approximately 7 kJ/m² at 23 °C and 5 kJ/m² at -30 °C according to ISO 179/1eA. The Vicat softening point B50 is approximately 155 °C by ISO 306, and heat deflection temperature under 1.8 MPa is approximately 65 °C by ISO 75-1/-2. These values are published typical values for dry-as-moulded specimens; they are not lot-specific specification limits and must not be used for final part qualification without certificate data.

    How Does an 8% Glass Fibre Loading Alter Shrinkage, Impact, and Anisotropy?

    The low glass content positions the material between unfilled PA12 and 30% glass fibre PA12 in both stiffness and shrinkage. Moulding shrinkage measured by ISO 294-4 is approximately 0.8% in the flow direction and 1.0% transverse to flow. The 0.2 percentage point difference is small enough to permit cylindrical or box-like parts to be dimensioned with a single nominal shrinkage allowance, whereas higher glass loadings may require separate longitudinal and transverse allowances exceeding 0.4 percentage points. The anisotropic tensile response is similarly moderate; the elastic modulus increase from approximately 1,400 MPa for unfilled PA12 to 1,900 MPa is accompanied by retention of nominal strain at break above 10%, a value not attainable in most 30% glass fibre PA12 grades. The low-temperature impact transition is also less severe than in highly reinforced materials: Charpy notched energy at -30 °C of 5 kJ/m² is sufficient for snap arms that are loaded in bending, but not for structural housings subject to multiaxial impact.

    Fibre distribution in the moulded part is less stratified than in high-glass compounds. During injection, the 8% fibre phase migrates only weakly toward the core under fountain flow, so the skin-shell morphology remains relatively isotropic. Gate location therefore has less influence on warpage than in 30% glass-filled nylon 12, although weld lines should still be placed away from high-strain snap features.

    Pre-drying is required when pellet moisture exceeds 0.10%. A desiccant dryer with a dew point below -30 °C and a bed temperature of 80 °C for 4–6 h is the standard method; residual moisture levels of 0.05% or lower are achievable in closed-loop hoppers. Open hopper residence above 60% RH should not exceed 30 min. Excessive moisture produces splay, silver streaks, and fluctuations in melt pressure at the nozzle. Melt temperature is maintained between 230 °C and 250 °C, measured at the injection nozzle. The lower bound avoids cold slugs and unmelts in thick sections; the upper bound avoids thermal yellowing and a reduction in molecular weight. Mould temperature is controlled between 40 °C and 80 °C. At 40 °C, cycle time is shorter but post-mould flow-direction shrinkage over 24 h is higher by approximately 0.1% to 0.2%. At 80 °C, weld-line tensile strength and dimensional stability improve, but cycle time increases and ejector pin loads rise because the modulus remains higher at demoulding.

    Injection speed is set so that the average melt-front velocity is constant in thin walls below 1.5 mm. Sudden acceleration above approximately 10,000 s⁻¹ apparent shear rate at the gate can produce jetting and lower weld-line strength in glass-filled PA12. A screw with low-compression ratio between 2.2:1 and 2.8:1 and a free-flow non-return valve is adequate; the low glass content does not require the wear-resistant barrel liners specified for 30% glass fibre compounds. Gate diameter for a 2 mm wall should be at least 50% of wall thickness, and land length should be less than 1 mm to avoid free glass particles on the surface.

    When the Grade Replaces Unfilled PA12 in Snap-Fit Connectors and Harness Clips

    The substitution is justified when assembly loads require a higher flexural modulus than unfilled PA12 but the part cannot tolerate the brittle failure associated with high glass content. In connector bodies and cable harness clips, the material is commonly selected for beam-type snap arms that must open over a steel stud or bracket edge without stress whitening at -30 °C. Design calculations based on ISO 527 tensile strain at break of 15% typically use a permissible assembly strain of 6% for one-time deflection and 3% for repeated service. The friction behaviour of the PA12 matrix is also relevant: unfilled PA12 has a low coefficient of friction against steel, and the 8% glass phase does not create the abrasive wear seen with higher glass loadings in sliding clip applications.

    In fuel-line quick connectors and pneumatic fittings, the PA12 chemistry provides resistance to aliphatic hydrocarbons, diesel fuel, and zinc chloride corrosion. Dimensional change after immersion in ASTM Reference Fuel C is typically below 3% by mass for PA12 at 23 °C; published data for specific connector configurations should be verified because wall thickness and gating alter the accessible surface. Compliance validation may follow SAE J2044 for automotive quick connectors or component-level leak and pull-out tests derived from ISO 18418. The glass fibre content in LXM8 increases hoop stiffness in barbed fittings by approximately 30–40% compared with unfilled PA12, reducing retained diameter loss after prolonged clamp storage.

    Table 1 places the grade relative to unfilled PA12 and a 30% glass fibre PA12 reference. Values are dry-as-moulded typical figures compiled from publicly available datasheets; certificate values may differ by colour and processing history.

    PropertyTest methodUnitVESTAMID LXM8Unfilled PA12PA12 GF30
    DensityISO 1183g/cm³1.051.011.25
    Tensile modulusISO 527-1/-2MPa1,9001,4005,500
    Nominal strain at breakISO 527-1/-2%15>505
    Notched Charpy impact, 23 °CISO 179/1eAkJ/m²7610
    HDT A, 1.8 MPaISO 75-1/-2°C655095
    Water absorption, saturation in water at 23 °CISO 62%1.51.51.3
    Moulding shrinkage, flow directionISO 294-4%0.81.20.3

    Compared with a PA66 GF10 grade, the determining difference is not short-term stiffness but hygroscopic growth. Saturation water uptake in PA12 is 1.5% according to ISO 62, whereas unmodified PA66 and PA6 absorb approximately 8.5% and 9.5% respectively. In a connector housing with 30 mm critical width, a PA66 GF10 part may exhibit dimensional growth of 0.2–0.3% under humidity cycling, while PA12 remains below 0.1% after equilibrium moisture uptake. The same moisture resistance preserves surface insulation; surface resistivity of natural PA12 grades remains near 1×10¹⁴ Ω under IEC 60093 after standard humid ageing, though test data for the specific glass-filled grade should be obtained from the lot certificate.

    Dimensional Stability, Hydrocarbon Contact, and Surface Electrical Behaviour

    The PA12 backbone in VESTAMID LXM8 provides low equilibrium water absorption, which reduces the swelling-driven clamping force relaxation observed in polyamide 6 and polyamide 66. Moulded parts exposed to 85 °C and 85% RH for 1,000 h typically show a mass increase below 2%, although the exact value is thickness-dependent. Because the glass fibre does not absorb water, the 8% filler fraction also lowers the coefficient of hygroscopic expansion relative to unfilled PA12 by approximately 10–15%. This is a practical difference for connector shells that must maintain a press-fit over a metal collar under high-humidity engine-bay conditions.

    Hydrocarbon resistance is comparable to unfilled PA12. Swelling in aliphatic hydrocarbons is low, and continuous contact with diesel, gasoline, and mineral oils at temperatures below 80 °C does not normally require additional stabilisation. Aromatic hydrocarbons and oxygenated fuel blends with high methanol content are more aggressive; prolonged immersion testing under ISO 175 is recommended for such fluids. The electrical tracking index of PA12 is high; published comparative tracking index values for unreinforced PA12 are typically 600 V per IEC 60112, and the glass-filled grade retains good surface leakage resistance under humid conditions. However, conductive carbon black or antistatic additive packages are not part of the LXM8 designation, so the material should not be specified for static dissipative service.

    The material is supplied in natural and coloured forms; colour masterbatches can alter notched impact and moulding shrinkage. Certification for food-contact, potable-water, or medical use is application-specific and must be confirmed against the actual lot formulation. The grade is not recommended for continuous service above 120 °C in air or for hot-water piping beyond 80 °C without hydrolysis testing. If a part requires the tensile modulus of a 30% glass-filled PA12 but with lower distortion, LXM8 is not a direct replacement because its 1,900 MPa dry modulus is approximately one-third of that class. Conversely, if the specification requires an unfilled PA12 impact envelope with a higher modulus, the 8% glass content provides the stiffness increase without the sharp ductility loss present in higher-glass PA12. Incompatible melt-phase additives include strong acids and halogenated flame-retardant systems that can degrade the polyamide at processing temperatures above 250 °C.

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