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Evonik VESTAMID® LX9123 NC Nylon 12, 4% Glass Fiber Reinforced

    • Product Name: Evonik VESTAMID® LX9123 NC Nylon 12, 4% 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 817262
    Density 1.03 g/cm³
    Melting Temperature 178 °C
    Glass Transition Temperature 50 °C
    Tensile Modulus 1900 MPa
    Yield Stress 45 MPa
    Elongation At Break 50 %
    Charpy Impact Strength 23 C 80 kJ/m²
    Charpy Notched Impact Strength 23 C 6 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 85 °C
    Heat Deflection Temperature 1 8 Mpa 45 °C
    Water Absorption Saturation 1.5 %

    As an accredited Evonik VESTAMID® LX9123 NC 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 & Storage
    Packing Supplied as grey granules in 25 kg moisture-protective, vacuum-sealed paper bags on pallets. Quantity: 25 kg per bag.
    Container Loading (20′ FCL) 20' FCL of Evonik VESTAMID LX9123 NC Nylon 12, 4% glass fiber reinforced, securely packed in standard export packaging.
    Shipping Evonik VESTAMID® LX9123 NC Nylon 12 (4% glass fiber reinforced) ships as solid pellets in sealed moisture-barrier bags or drums. Protect from humidity, direct sunlight, and excessive heat during transport. No hazardous goods classification; standard dry, ventilated freight conditions apply. Keep packaging intact to prevent contamination and moisture uptake.
    Storage Store VESTAMID® LX9123 NC 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, which can degrade the material. Under recommended conditions, shelf life is typically 2 years from date of manufacture.
    Shelf Life Store in original sealed packaging, cool and dry. Shelf life is typically two years from date of manufacture.
    Application of Evonik VESTAMID® LX9123 NC Nylon 12, 4% Glass Fiber Reinforced

    In commercial vehicle compressed-air brake lines, the 4 wt% short glass fiber reinforcement in VESTAMID LX9123 NC limits circumferential creep under the pressure pulse loads imposed between -40°C and 100°C. Qualification for this segment is not generic; tube assemblies are checked against SAE J844-2022 for non-metallic air brake tubing and against DIN 73378 where European vehicle parc requirements apply. Tensile yield and elongation after ageing are evaluated according to ISO 527-2, and heat ageing is performed in forced-air ovens at 100°C for 168 h followed by burst pressure measurement at 23°C and 100°C. Because the grade already contains 4 wt% glass fiber, the processing formulation is not a compounded addition at the converter; the dried pellet is metered neat, with regrind limited to 20 wt% of the same grade and only after the ground material has been re-dried to 0.10% moisture. If laser marking is specified, a PA12-based colour masterbatch is added at 1.5 wt% to 2.0 wt%, not more, to avoid shifting the fiber-to-matrix ratio and local melt viscosity.

    The dominant production route is single-screw extrusion on a barrier screw with L/D 30:1, followed by gear-pump assisted melt delivery to a spiral mandrel die. Feed throat temperature is maintained at 60°C to 80°C; barrel zones are profiled from 210°C to 240°C; die head is held at 225°C to 235°C. Melt temperature at the die entry is typically 238°C to 245°C. The tube is sized through a vacuum calibration tank with water at 20°C to 40°C, then passed through a laser micrometer loop that controls outside diameter to ±0.05 mm. Closed-loop gauge data are used to adjust internal air pressure and haul-off speed, because diameter drift in the first 2 h of continuous operation is a known batch-to-batch variance when ambient humidity exceeds 60%. Finished goods from this process are coiled air brake tubes in 6 mm, 8 mm, 10 mm, and 12 mm outside diameters with wall thickness between 1.0 mm and 1.3 mm, cut lengths for chassis installation, and factory-swaged tube assemblies with brass or composite push-to-connect fittings. Marking must remain legible after abrasion testing in SAE J844-2022 and must identify tubing type, nominal outside diameter, and date of manufacture. The 4 wt% glass content increases burst pressure retention at 100°C; however, it also narrows the allowable bending radius at -40°C, so routing design should not rely on unfilled PA12 bend radii.

    How Does 4 wt% Glass Fiber Alter Burst Pressure in Aqueous Urea Dosing Lines?

    The fluid in selective catalytic reduction circuits, a 32.5 wt% aqueous urea solution with a freezing point near -11°C, imposes a combination of hydrolytic exposure, thermal cycling, and low-temperature freeze pressure that unfilled polyamide 12 does not always survive after long field service. The fluid-contact layer is used as 100% VESTAMID LX9123 NC, not as a dry blend with unfilled PA12; any regrind is limited to 15 wt% and is segregated to the outer layer of two-layer tubing because inner-layer hydrolysis resistance must remain at the virgin pellet baseline. Compliance is assessed under ISO 22241-3:2019 for diesel exhaust fluid handling compatibility and ISO 16750-4 for temperature, vibration, and chemical load conditions on the vehicle. The glass reinforcement is already fixed at 4 wt% in the supplied pellet, so converters do not alter the fiber concentration; the operating window is instead controlled through melt temperature and residence time. Production uses a two-extruder coextrusion line with 25 mm and 35 mm single-screw units, each at L/D 28:1. The inner layer is extruded at 230°C to 240°C, while the outer layer is run 10°C to 15°C lower to limit back diffusion of plasticizer from an outer polyamide alloy. Vacuum calibration is followed by a post-sizing annealing bath at 130°C for 60 sec to reduce frozen-in stress from the glass fibers; this step has a measurable effect on burst pressure retention after thermal cycling from -40°C to 85°C. In-line inspection includes laser wall-thickness measurement, spark testing at 10 kV, and burst testing of one specimen per 1,000 m production lot. Terminal products are 6 mm to 12 mm OD urea supply and return tubes, heated lines with co-extruded conductor channels, and hose assemblies with quick connectors per SAE J2044-2022. The glass-reinforced grade is suitable for line lengths where hoop strength must be maintained after 1,000 h continuous exposure to 80°C diesel exhaust fluid; published data for this specific configuration above 90°C is limited, and OEM qualification tests should be repeated if the dosing system exceeds 85°C at the tank return.

    Subsea Umbilical Liners and Methanol Injection Tube Requirements

    Subsea production control umbilicals use thermoplastic liners that must survive long-term exposure to methanol, scale inhibitor, and hydrate inhibitor fluids at hydrostatic pressures that can exceed 10,000 psi (690 bar) in deepwater fields. Material qualification follows API 17E for subsea production control umbilical specification and ISO 13628-5 for subsea control systems. Additional compatibility screening is performed under ISO 23936-1 for non-metallic materials in sour hydrocarbon service. The liner is produced from 100 wt% virgin VESTAMID LX9123 NC; no post-industrial regrind is permitted in the pressure-containing layer, and only virgin pellet from sealed moisture-barrier bags is introduced into the hopper. The extrusion line is built around a 45 mm single-screw machine with L/D 30:1, a vacuum vent at -0.8 bar, and a gear pump that holds die pressure to a tolerance of ±0.5 MPa. Melt temperature is maintained at 235°C to 245°C, below the thermal degradation threshold of 260°C. Tube wall thickness control is set to ±0.03 mm over 6.35 mm (1/4 in) and 9.53 mm (3/8 in) outside diameter configurations. After calibration, the liner passes through a 100% high-voltage pinhole test at 15 kV and a 0.2 MPa nitrogen leak test before spooling. Finished downstream products are subsea hydraulic control lines, methanol injection lines, scale inhibitor injection lines, and gas lift injection hoses supplied as thermoplastic hose bundles with steel or textile reinforcement. The 4 wt% glass fiber increases axial stiffness, which reduces radial growth under cyclic pressure but also demands a larger minimum bend radius than unfilled PA12; spooling geometry on installation vessels must account for bend radii above 10 times the tube outside diameter. For sour wet service above 60°C, published data for this specific configuration is limited and qualification to ISO 23936-1 Annex B is required.

    When Fuel Vapour Return Tubing Must Meet CARB LEV III Permeation Limits

    Light-duty gasoline fuel vapour return lines are constrained by evaporative emission limits set through CARB LEV III and federal 40 CFR Part 86. The tube construction is tested to SAE J2260-2019 for non-metallic fuel system tubing and SAE J2044-2022 for quick connector compatibility. Permeation measurements are reported using the OEM-specified method defined in the SAE J2260 qualification plan. In the three-layer structure, the centre barrier layer is 100 wt% VESTAMID LX9123 NC; the 4 wt% glass content remains in the pellet, and no filler is added by the converter. Impact-modified PA12 outer layers are combined through maleic anhydride-grafted tie resins; the barrier layer accounts for 30% to 40% of the total wall thickness. The barrier layer is coextruded on a three-layer die with inner and outer melt streams at 220°C, and the centre LX9123 NC layer at 235°C. Gravimetric feeders hold layer ratios within ±1.0 wt%; the line is equipped with ultrasonic wall-thickness sensors after the vacuum tank, and a corrugator is inserted when the finished line must follow routing bends with radius under 50 mm. The tube is leak-tested at 0.2 MPa and dried to 0.10% moisture before assembly. Pre-drying of pellets at 80°C for 4–6 h in a desiccant dryer to a dew point of -40°C is mandatory, because residual moisture in the barrier layer reduces melt strength and creates longitudinal weld-line porosity at the mandrel ports. Terminal products include EVAP canister-to-tank vapour tubes, fuel filler neck recirculation assemblies, ORVR vent hoses, and carbon canister purge lines with outside diameters from 8 mm to 16 mm. These parts are supplied to OEM and Tier 1 fuel system integrators as pre-formed harnesses with brazed or quick-connect endforms. The 4 wt% glass reinforcement improves cold burst strength, but at -40°C the formed section should be subjected to a notched burst check because glass fiber alignment at the inner radius can reduce local elongation relative to straight tube.

    Across CNC machining centres and packaging lines, dry-lubricated pneumatic control bundles are specified where mineral oil mist is prohibited. The 4 wt% glass fiber content in VESTAMID LX9123 NC provides dimensional stability for push-to-connect fittings under cyclic pressure from 0.3 MPa to 1.0 MPa, but the resin is not processed as a simple unfilled PA12 substitute; the fiber orientation generated during tube sizing directly influences fitting retention and burst scatter. System-level compliance follows ISO 4414:2010 for pneumatic fluid power, while tube pressure validation is performed according to ISO 1402:2021 and fitting compatibility is verified with ISO 14743:2020. The tube is run as 100 wt% VESTAMID LX9123 NC; a carbon black masterbatch with PA12 carrier is metered at 2.5 wt% to 3.0 wt% where UV stabilization is required for exterior runs, and silicone-free external lubricant is not used because it detracts from push-in fitting retention. Regrind from start-up scrap is capped at 25 wt% after separation of fines below 0.5 mm. Production is performed on a 30 mm single-screw extruder with L/D 28:1, a melt temperature of 235°C, and vacuum calibration that sets outside diameter to ±0.04 mm. After extrusion, coils are conditioned at 23°C and 50% relative humidity for 24 h to stabilize moisture-dependent dimensions before final length measurement. Terminal products are 4 mm to 16 mm OD pneumatic control tubes, retractable coils, multi-tube bundles with polyurethane outer jackets, and colour-coded air supply lines for automated assembly stations. The maximum continuous service temperature in dry compressed air is limited to 80°C; at -40°C, tubes must be pre-bent with a larger radius than unfilled PA12 because low-temperature notched impact is reduced by the glass fiber.

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    Certification & Compliance
    More Introduction

    Evonik VESTAMID® LX9123 NC is a natural-color polyamide 12 (PA12) compound containing 4% glass fiber by mass. The pelletized grade is intended for injection molding and extrusion of profiles, tubing, and technical components requiring a balance of dimensional stability, chemical resistance, and low-temperature impact. The PA12 backbone is polymerized from laurolactam, giving a lower amide-group density than PA6 or PA66. According to ISO 1043-1, the material is designated PA12-GF4. The 4% fiber level reduces mold shrinkage relative to unfilled PA12 without imposing the anisotropic shrinkage and surface roughness associated with glass-fiber loadings above 10–15%.

    Published typical values for this grade include a density of 1.03 g/cm³ under ISO 1183, a dry-as-molded tensile modulus of approximately 1,000–1,200 MPa under ISO 527-1/-2, a Charpy notched impact strength at 23 °C of 7–10 kJ/m² under ISO 179-1/1eA, and a melting peak of 176–180 °C under ISO 11357-1/-3. These values are lot averages and not specification limits; current lot-specific certificates of analysis should be consulted before tool design or part qualification.

    What Distinguishes the PA12 Backbone from Short-Chain Polyamides?

    The laurolactam-based repeat unit places eleven methylene groups between amide linkages, whereas PA6 and PA66 contain five or fewer methylene segments between polar groups. This lower amide-group concentration limits hydrogen-bonding sites for water. Under ISO 1110 accelerated conditioning at 23 °C and 50% relative humidity, PA12 typically reaches 0.7–0.9% moisture absorption, compared with 2.5–3.0% for PA6 and 2.0–2.5% for PA66. Water saturation values under ISO 62 show an even wider gap, with PA12 near 1.0–1.4% and short-chain polyamides above 8%. The practical consequence is that post-molding dimensional change and property drift in humid service are smaller for LX9123 NC than for glass-reinforced PA6 or PA66 grades.

    The lower amide density also reduces susceptibility to hydrolysis in hot-water and steam environments and to stress-cracking agents such as zinc chloride. The glass transition of PA12 is lower than that of PA66, typically near 45 °C versus 60–70 °C, contributing to ductile response at sub-zero temperatures measured by ISO 179-1/1eA Charpy impact testing.

    Mechanical Property Shifts at 4% Glass-Fiber Loading

    The following table summarizes the dry-as-molded property envelope published for VESTAMID® LX9123 NC. The values are typical rounded ranges and should not be used as release limits.

    Typical dry-as-molded property profile of VESTAMID® LX9123 NC
    PropertyTest methodTypical value
    DensityISO 11831.03 g/cm³
    Tensile modulusISO 527-1/-21,000–1,200 MPa
    Tensile stress at yieldISO 527-1/-228–32 MPa
    Tensile strain at yieldISO 527-1/-24–6%
    Charpy notched impact strength, 23 °CISO 179-1/1eA7–10 kJ/m²
    Charpy notched impact strength, -30 °CISO 179-1/1eA5–7 kJ/m²
    Vicat softening temperature, 50 NISO 306168–172 °C
    Melting temperatureISO 11357-1/-3176–180 °C
    Water absorption, saturation in water 23 °CISO 621.0–1.4%
    Mold shrinkage, flow directionISO 294-40.4–0.7%

    The 4% glass fiber content modifies the semi-crystalline PA12 matrix by reducing mold shrinkage to 0.4–0.7% under ISO 294-4 and raising creep resistance under sustained load when evaluated by ISO 899-1. Notched impact strength is lower than that of unfilled PA12 because the glass fibers act as stress concentrators; however, the PA12 matrix retains sufficient ductility for snap-fit assemblies and cold impact service. Tensile modulus remains below that of structural glass-filled grades, which positions this material for components requiring moderate rigidity rather than load-bearing stiffness.

    When Melt Processing Conditions Depart from the Recommended Envelope

    Pre-drying is mandatory after storage at relative humidity above 60% or whenever the original moisture-barrier package has been open for more than a few hours. Residual moisture above 0.10% before plastication causes hydrolytic chain scission at melt temperature, producing splay, viscosity reduction, and lower impact strength in molded parts. A desiccant dryer with a dew point at or below -40 °C is required; a hot-air hopper dryer cannot reliably achieve the target moisture content.

    Typical starting conditions for injection molding and extrusion of VESTAMID® LX9123 NC
    ParameterStarting condition
    Pre-drying temperature80 °C
    Pre-drying time4–6 h in desiccant dryer
    Residual moisture target<0.10%
    Melt temperature220–250 °C
    Mold temperature30–80 °C
    Maximum melt temperature270 °C with short residence time
    Screw L/D ratio20–25
    Compression ratio2.5–3.0

    The recommended melt-temperature window of 220–250 °C balances fiber wet-out and melt stability. Melt temperatures above 270 °C accelerate thermal-oxidative degradation, visible as yellowing and a loss of notched impact strength under ISO 179-1/1eA. Residence time in the barrel should not exceed 10 min; production machines with accumulation times outside this range should use lower melt temperatures and smaller shot capacity. Mold temperatures from 30–80 °C control crystallization rate and part dimensions. Variations greater than ±5 °C across the cavity can create differential shrinkage and fiber orientation, increasing warpage in flat parts.

    On production-scale injection molding machines, batch-to-batch variation in glass-fiber sizing or pellet moisture can shift melt viscosity and fiber-orientation pattern. A moisture analyzer or Karl Fischer titration should be used to verify pellet moisture before the first run after warehouse storage. Molding trials have shown that inadequate fiber wet-out produces surface roughness and lower notched impact near knit lines. Raising melt temperature within the 220–250 °C envelope and increasing screw back pressure can improve fiber dispersion, but excessive back pressure raises shear heating and can push melt temperature above 270 °C. Mold-filling simulations require measured viscosity data from capillary rheometry under ISO 11443 and thermal conductivity from ISO 22007-2, not generic PA12 data, to capture the effect of 4% glass fiber on flow length.

    For extrusion, single-screw equipment with L/D 20–25 and a compression ratio of 2.5–3.0 is typically used. Vacuum venting reduces volatiles and prevents internal void formation. Injection pressures commonly fall between 60–100 MPa for technical parts of moderate wall thickness; actual settings depend on gate size, flow length, and wall section. Screw and barrel wear is accelerated by glass fiber, particularly at compression-zone clearances below the equipment manufacturer minimum.

    Hydraulic and pneumatic tubing made from LX9123 NC is evaluated under ISO 7628 for low-temperature flexibility and burst strength after fuel and oil conditioning. The 4% fiber level increases hoop-stress retention relative to unfilled PA12 after fuel conditioning at 60 °C for 1,000 h when tested according to ISO 1817. However, published long-term hot-fuel aging data for this specific configuration are limited; part-level testing on the finished assembly remains necessary. Other production applications include industrial cable sheathing, connectors, clips, and fluid-handling components where dimensional stability after moisture conditioning is a primary requirement.

    Chemical Resistance and Permeation Behavior in Hydrocarbon Service

    PA12 exhibits resistance to many aliphatic hydrocarbons, oils, greases, fuels, and saline solutions. Performance under chemical exposure is assessed by ISO 1817 for tensile and mass change after immersion. The low amide-group density gives PA12 better resistance to zinc chloride stress-cracking than PA6 or PA66; this property is relevant for under-hood and road-salt applications. The 4% glass fiber reduces fuel and gas permeation by creating a more tortuous diffusion path through the polymer matrix. Permeation coefficients are measured under SAE J2659 for fuel systems or ISO 15105-1 for gas transmission. The reduction is moderate compared with fluoropolymer barrier layers or EVOH layers used in multilayer fuel line architectures.

    The grade is not recommended for continuous exposure to strong acids, oxidizing media, phenols, or high-pressure steam, because these environments hydrolyze or oxidize the polyamide backbone. For hot-water contact, the maximum continuous service temperature must be established by testing of the finished component under the intended stress state, because hoop stress and part design strongly influence hydrolysis rate.

    Do Not Select the 4% Glass Level Where Maximum Rigidity Is Required

    The 4% fiber content is intended for moderate stiffening, shrinkage control, and improved dimensional stability under humidity. It is not a structural replacement for glass-filled PA66 or 30% glass-fiber PA12. Published tensile modulus for LX9123 NC is approximately 1,000–1,200 MPa under ISO 527-1/-2, while 30% glass-fiber PA12 compounds commonly exceed 5,000 MPa under the same method. The lower fiber level preserves surface appearance, reduces anisotropic shrinkage, and lowers machine-tool wear compared with high-glass compounds, but it sacrifices stiffness and creep modulus.

    Compared with unfilled PA12, the 4% glass compound reduces mold shrinkage and can improve dimensional stability in large flat parts, but the fiber addition lowers notched impact strength. Typical Charpy notched impact values for LX9123 NC are 7–10 kJ/m² at 23 °C under ISO 179-1/1eA, whereas unfilled PA12 grades often range from 10–20 kJ/m² depending on moisture state and molecular weight. In applications where cold impact or high elongation is critical, unfilled or elastomer-modified PA12 should be evaluated.

    For compliance documentation, the grade is covered under the European REACH Regulation (EC No 1907/2006), the RoHS Directive 2011/65/EU, and may be used in food-contact articles if the finished component complies with EU 10/2011 and FDA 21 CFR 177.1500 as applicable to nylon resins. Electrical and electronic applications require verification against application-specific flammability standards such as UL 94. Material certifications should be requested from the manufacturer for the specific lot, because additive batches and fiber sizing can shift processing behavior and final mechanical values within the published typical range.

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