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Evonik VESTAMID L2141 BK 9.750 Nylon 12, Conditioned

    • Product Name: Evonik VESTAMID L2141 BK 9.750 Nylon 12, Conditioned
    • 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 417511
    Density 1.01 g/cm³
    Water Absorption 24h 23 C 0.25 %
    Melting Temperature Dsc 178 °C
    Glass Transition Temperature 45 °C
    Tensile Modulus Conditioned 900 MPa
    Yield Stress Conditioned 40 MPa
    Elongation At Yield Conditioned 5 %
    Elongation At Break Conditioned >50 %
    Charpy Impact Strength Conditioned 23 C No break
    Charpy Notched Impact Strength Conditioned 23 C 80 kJ/m²
    Shore D Hardness Conditioned 55
    Heat Deflection Temperature 1 80 Mpa 50 °C

    As an accredited Evonik VESTAMID L2141 BK 9.750 Nylon 12, Conditioned factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 25 kg sealed, moisture-proof bags to preserve the conditioned Nylon 12 pellets.
    Container Loading (20′ FCL) 20′ FCL container loading: palletized, secure, dry, moisture-protected packaging of Evonik VESTAMID L2141 BK 9.750 Nylon 12, Conditioned.
    Shipping Evonik VESTAMID L2141 BK 9.750 Nylon 12, Conditioned, ships as non-hazardous plastic pellets. Protect from moisture and direct sunlight; use sealed, dry containers. Store below 25°C in ventilated area. Avoid dust accumulation and static ignition. Standard freight handling applies with no special transport classification required.
    Storage Store VESTAMID L2141 BK 9.750 in its original, tightly sealed container in a cool, dry area. Protect from direct sunlight, heat sources, and humidity to prevent moisture absorption and property changes. Maintain temperatures below 40°C and avoid condensation. Use within the recommended shelf life, and reseal immediately after withdrawal to preserve conditioned state.
    Shelf Life Store in original unopened packaging, cool and dry. Shelf life is typically two years from date of manufacture.
    Application of Evonik VESTAMID L2141 BK 9.750 Nylon 12, Conditioned

    Gasoline-direct-injection fuel vapor vent lines are coextruded with a polyamide 12 inner and outer carrier layer based on L2141 BK 9.750 at outer diameters from 6.0 mm to 10.0 mm; the inner layer is coupled to an EVOH barrier layer through a maleic anhydride-grafted polyolefin tie resin. The conditioned granulate is dried in a desiccant hopper dryer to ≤0.10% water content by ISO 15512:2019 and then adjusted to 0.15–0.25% absorbed moisture before extrusion. Stable moisture content prevents melt-pressure oscillation in the die head; on a 45 mm single-screw extruder with 25:1 L/D, the adapter pressure transducer records a band of ±0.5 MPa during 80–120 rpm screw rotation when barrel temperatures rise from 190 °C in the feed zone to 230 °C in the metering zone. The outer layer moisture after water-bath vacuum calibration at 10 °C is allowed to recover to 0.20–0.30% over 48–96 h at 23 °C and 50% RH before terminal assembly. This recovery step is critical for crimp retention on steel quick connectors after thermal aging at 125 °C for 720 h; dry PA12 outer jackets can develop radial stress cracks under crimp compression at −20 °C. Permeation control follows SAE J1737 and the specific vehicle evaporative emission budget; the EVOH barrier corrects PA12 hydrocarbon loss while PA12 supplies impact and chemical resistance against salt, methanol, and zinc chloride road spray. Dimensional drift after 500 h immersion in Fuel C is monitored by a bend fixture holding the line at 3× OD minimum bend radius; inner-bend diameter reduction must not exceed 2.0% or the quick connector O-ring seal loses interference. Published data for this specific grade under cyclical methanol-blended Fuel C exposure at 60 °C is limited, so qualified production runs include a 1,000 h post-extrusion permeation and crack-resistance audit before tooling release.

    What Keeps SAE J844 Air Brake Tube Burst Pressure Stable after 125 °C Heat Aging?

    For SAE J844 air brake tubing in commercial trucks, L2141 BK 9.750 is extruded through a vacuum-calibrated die with 12.0 mm outer diameter and 0.6 mm die gap at line speeds between 20 m/min and 40 m/min, depending on wall thickness from 1.5 mm to 2.0 mm. Processing at melt temperatures above 250 °C causes surface oxidation blush on black tubing; the upper die-head setting is limited to 245 °C, with metering zones held at 230–240 °C. Conditioned feedstock at 0.20% moisture maintains stable melt-bubble formation in the water-quench tank and reduces the frequency of internal voids detected by ultrasonic scanning. Burst-pressure retention is tracked before and after hot-oil immersion for 168 h at 125 °C; production control charts use the heat-aged burst value as the critical quality characteristic. The final tube also undergoes low-temperature kink testing at −40 °C on a 300 mm mandrel after conditioning. Production failures at this point commonly trace to residual moisture in the wall center above 0.30%, which creates steam-generated microvoids during extrusion, or to inadequate homogenization causing crystalline density gradients. Between-coil burst-pressure variation within a single production shift has been observed at ±0.4 MPa when conditioning and screw speed are held constant; wider variation usually indicates worn barrel sections or poor feed-throat water-jacket temperature control. The material aligns with the international counterpart ISO 7628-2 dimensional and performance criteria when the same conditioning schedule is applied before coiling.

    Application nodeNormative baseConditioned-grade monitoring parameter
    Monolayer air brake tubeSAE J844 / ISO 7628-2Burst after 168 h at 125 °C; kink at −40 °C
    Multilayer vapor vent lineSAE J1737Permeation after 1,000 h Fuel C exposure; crimp retention
    Offshore dynamic cable sheathIEC 60840:2020Elongation after 1,000 h at 100 °C; cold bend at −35 °C

    In offshore dynamic power cable service, the black weather-stabilized PA12 sheath is extruded over the outer semiconductive bedding layer of cables with conductor cross-sections from 95 mm² to 630 mm² at line speeds below 8 m/min to hold eccentricity under 5%. The sheath layer is drawn down to 2.0–3.5 mm through a crosshead fed by a 90 mm single-screw extruder with 24:1 L/D and water-cooled trough segmentation. Tension control at the caterpillar is maintained between 0.2 N/mm² and 0.5 N/mm² of sheath cross-section; higher tension during cooling induces residual stress at the inner interface and increases the probability of longitudinal splits during factory cold bend tests at −35 °C. Conditioned L2141 reduces melt-temperature fluctuation to ±2 °C through the metering section, which stabilizes elongation-at-break after 1,000 h at 100 °C in forced-air ovens as required for cable sheath qualification under IEC 60840:2020. The pellet moisture level also affects screw-induced friction; if dried granulate is processed without conditioning, melt pressure at the breaker plate can drift by more than 1.5 MPa over a 6 h production run, producing visible surging in the outer diameter. Operators monitor in-process density at 1.01 g/cm³ ±0.005 g/cm³ as a void check, because black PA12 with dispersed carbon black can mask small discontinuities under optical inspection. At cable drum load-out, the sheath must withstand a 180° bend over a mandrel of 15× OD at −35 °C without cracks; this test is repeated after a heat cycle simulating deck burial under tropical sun. Published data for long-term marine aging of this specialty black PA12 grade under continuous 60 °C seawater head exposure is limited, so offshore projects segregate accelerated aging data by cable design and require full-scale bending fatigue trials.

    When a Corrugated Pneumatic Conduit Runs at 0.8 MPa and −40 °C

    If the die gap for a 12.7 mm outer diameter corrugated pneumatic conduit is set below 0.65 mm, conditioned melt is stretched too quickly across the corrugation chambers and the inner radius wall can thin below 1.0 mm under vacuum shaping at −30 kPa. L2141 BK 9.750 at 0.20% absorbed moisture retains adequate melt strength for continuous corrugation while allowing the finished conduit to pass 2.0 MPa hydrostatic proof testing at 23 °C without stress whitening or fitting leakage. Cyclic flex testing on production validation coupons is run at −40 °C for 500,000 cycles at a travel radius of 1.5× OD; the part is considered failed if the inner corrugation root displays a craze longer than 3.0 mm. The notched Izod impact after moisture conditioning is the controlling property in this envelope; dry as-molded conduit can lose more than 40% of cold impact resistance by ISO 180/A, which manifests as freight damage in unheated trailers. Drying and conditioning schedules therefore mirror the fuel-line sequence: 80 °C for 6 h to reach ≤0.10% moisture by ISO 15512:2019, then an external moisture cabinet set to 40 °C and 80% RH for 4 h to restore surface moisture before the material enters the hopper. Vacuum calibration blocks with silicone rubber sizing rings are used because PA12 sticks to polished steel at melt temperatures above 235 °C; stearate migration from the grade reduces frictional resistance in the corrugator tunnel. This grade is not recommended for conduits continuously exposed to 120 °C air under simultaneous external stress, as oxidative embrittlement exceeds the long-term service envelope for an aliphatic polyamide; published data for this specific configuration above 100 °C under mechanical load is limited.

    Moisture Uptake Kinetics in Conditioned L2141 BK 9.750 and Dimensional Recovery

    Moisture conditioning of L2141 BK 9.750 from the dry-as-extruded state to 0.20–0.30% absorbed water follows Fickian diffusion behavior with a diffusion coefficient on the order of 1×10⁻¹² m²/s at 23 °C; a 2.0 mm wall section reaches 80% of equilibrium after approximately 48 h at 50% RH. The absorbed water reduces tensile modulus by 20–25% relative to dry values while increasing elongation at yield; this shift is reversible upon re-drying but must be accounted for in fitting insertion-force calculations. Dimensional recovery occurs as the absorbed water relaxes process-induced orientation; tubing lengths cut immediately after extrusion shrink 0.3–0.6% in the machine direction after conditioning, requiring length compensation before cut-to-length packaging. Melt processing conditions that leave high crystallinity at the outer surface reduce moisture diffusion into the core; rapid water-bath quenching below 20 °C increases amorphous content and shortens the conditioning interval. Hot-air post-annealing at 90 °C for 2 h on final tube reduces subsequent shrinkage but yields slightly lower low-temperature flexibility compared with water-conditioned parts. The black pigment dispersion is validated by filter-screen retention of ≤0.5% on 25 µm screens; the color package does not measurably alter water-uptake kinetics. Conditioned material stored in moisture-tight containers for more than 30 days at 30 °C should be re-verified by ISO 15512:2019 before use because surface moisture can redistribute unevenly and produce visible surface streaks at the die exit.

    Because coolant-resistant nylon tubing in heavy-duty diesel engine compartments is exposed to hot ethylene glycol/water mixtures at 95 °C and intermittent chloride-bearing road deicing brines, extruders select L2141 BK 9.750 for the outer jacket of coolant overflow lines up to 16 mm outer diameter. The inner elastomer carries the coolant pressure, while the PA12 jacket prevents abrasion at bracket clips and offers melt-sealable ends for quick connectors. Conditioning the jacket to 0.20% moisture before installation improves ductility when connectors are swaged at −10 °C; dry PA12 can crack at the swaging shoulder under tool compression. Processors operate barrel profiles from 220 °C at the feed transition to 245 °C at the die head, with the die temperature held 5 °C below the final barrel zone to prevent surface sharkskin at line speeds above 25 m/min. A gear pump after the screw stabilizes head pressure at 10–15 MPa, reducing surging in the crosshead and delivering ±0.03 mm outer-diameter variation across 8 h production runs. Adhesion between the jacket and elastomer is mechanical; an aqueous adhesion promoter is not required when the assembly is cross-cut at 30° intervals and cold-impact tested under ISO 16750-4 at −40 °C. The grade is acceptable for service in hot-glycol exposure but not for continuous direct immersion in pure methanol or aggressive brake fluid at elevated temperature; published data for those specific fluid environments with this grade is limited.

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    Certification & Compliance
    More Introduction

    Evonik VESTAMID L2141 BK 9.750 Nylon 12, Conditioned is a black-pigmented, heat-stabilized polyamide 12 compound based on polylaurolactam. The L2141 designation identifies a medium-viscosity grade within the VESTAMID L-series; BK 9.750 denotes the carbon-black pigment preparation and not a filler percentage or reinforcement level. The term “Conditioned” refers to solid-state moisture equilibration at 23 °C and 50 % relative humidity in accordance with ISO 291, rather than an annealing treatment. In the conditioned state the polymer contains an equilibrium moisture fraction that reduces tensile stiffness and increases notched impact toughness relative to dry-as-moulded data. Because the repeat unit of PA12 contains one amide group per 12-carbon mer, the equilibrium moisture uptake is lower than that of shorter-chain polyamides PA6 and PA66.

    Typical industrial applications for this material include thin-wall pneumatic tubing, cable-protection conduits, corrugated automotive line sheathing, and injection-moulded clips or fluid-routing connectors. The combination of low density near 1.01 g/cm³ determined by ISO 1183-1, low equilibrium moisture uptake, and resistance to aliphatic hydrocarbons and zinc chloride solutions positions the grade in vehicle underbody systems where road-salt stress cracking and dimensional stability are design constraints. Hydrocarbon and stress-cracking resistance are screened according to ISO 175 and ISO 22088-2, with constant-strain exposure in 50 % aqueous ZnCl₂ at 23 °C used as a comparative laboratory condition. In monolayer tube extrusion, a single-screw extruder with an L/D ratio of 25:1 to 30:1, a barrier screw, and a screen pack of 200 µm or coarser is typical. Melt temperatures from 220 °C to 240 °C at the adapter are used; the upper limit is set by oxidative degradation rather than by melting or motor torque.

    Mechanical Property Shift After Conditioning to 23 °C / 50 % RH

    The dry-to-conditioned shift is a reversible plasticization effect, not a permanent molecular-weight change. Absorbed water hydrogen-bonds at amide sites, increasing chain mobility, reducing tensile modulus, and raising notched impact strength. The following values are representative for unfilled black PA12 of the L2141 type and are not a substitute for lot-specific certificates.

    Representative dry versus conditioned data for VESTAMID L2141 BK 9.750. Certificate values take precedence for specification purposes.
    PropertyTest methodDry as-mouldedConditioned 23 °C / 50 % RH
    DensityISO 1183-11.01 g/cm³1.01 g/cm³
    Tensile modulusISO 527-2/1A/501500 MPa1100 MPa
    Yield stressISO 527-2/1A/5045 MPa40 MPa
    Nominal strain at breakISO 527-2/1A/50>50 %>50 %
    Charpy notched impact at 23 °CISO 179-1/1eA5 kJ/m²10 kJ/m²
    Charpy notched impact at −30 °CISO 179-1/1eA5 kJ/m²6 kJ/m²
    Melting temperatureISO 11357-3176 °C176 °C
    Equilibrium moisture contentISO 62≤0.10 %0.70 %

    The conditioned property shift is not a permanent material change; redrying returns the tensile modulus toward the dry value. Dimensional change from moisture absorption is smaller in PA12 than in PA6 or PA66, but it is not zero. Linear expansion from dry to equilibrium at 23 °C and 50 % RH is commonly estimated in the order of 0.1–0.2 % for PA12, while PA6 and PA66 can exceed 0.4–0.6 %. Interference fits and snap-fit interlocks should therefore be evaluated with conditioned dimensions rather than as-moulded dimensions.

    What Distinguishes This Black PA12 from PA6 and PA66 in Wet Service?

    The structural basis is amide-group density. PA12 carries a longer aliphatic sequence between amide linkages than PA6 or PA66; therefore the equilibrium moisture content at 23 °C and 50 % RH is lower. In humid service, the difference is measurable by ISO 62: PA12 absorbs approximately 0.7 % moisture, whereas unfilled PA6 absorbs approximately 2.8 % and PA66 approximately 2.5 %. Saturation in water at 23 °C is approximately 1.5 % for PA12, compared with 9.5 % for PA6 and 8.5 % for PA66. The lower uptake reduces hygroscopic swell, hydrolysis-related property loss, and glass-transition suppression in humid environments. PA12 also has a density approximately 11 % lower than PA66.

    Comparative moisture and thermal data for unfilled heat-stabilized polyamides. Values are representative published data, not lot specifications.
    PropertyTest methodPA12 L2141PA6PA66
    DensityISO 1183-11.01 g/cm³1.13 g/cm³1.14 g/cm³
    Equilibrium moisture at 23 °C / 50 % RHISO 620.7 %2.8 %2.5 %
    Saturation water absorption at 23 °CISO 621.5 %9.5 %8.5 %
    Melting temperatureISO 11357-3176 °C220 °C260 °C
    Heat deflection temperature at 1.8 MPaISO 75-1/-2<60 °C65 °C70 °C

    Chemical stress-cracking resistance is a further differentiator. PA12 is specified where road-salt solutions, anhydrous aliphatic hydrocarbons, and high-pressure hydraulic oils are present; short-chain polyamides are more susceptible to zinc chloride-induced cracking. In constant-strain screening per ISO 22088-2, PA12 compounds generally show longer time to crack or no cracking within the observation period, whereas unfilled PA66 can develop surface cracks within hours under identical strain. This distinction is relevant in fuel-line clips, pneumatic brake tubing, and cable conduits exposed to de-icing salts. The trade-off is thermal: unfilled PA12 has a lower heat deflection temperature under load than PA66, so sustained exposure to underhood temperatures above 120 °C should not be assigned without component validation.

    On a production extrusion line, the moisture content of incoming pellets must be distinguished from the conditioned service state. VESTAMID L2141 BK 9.750 may be supplied with controlled residual moisture for packaging, but melt processing requires low moisture to avoid hydrolysis. A desiccant-dryer setpoint of 80 °C for 4–6 h is standard guidance when pellet moisture exceeds 0.10 % by mass; residual moisture is verified by ISO 15512 or Karl Fischer titration. Pellets that have absorbed ambient moisture and are fed directly can produce silver streaks, screw slip, and molecular-weight loss at the melt. For corrugated conduit tooling, the melt-temperature control window is typically ±10 °C around the target; excursions above 250 °C initiate carbon-black-catalysed oxidation and dark surface defects. A melt thermocouple inside the adapter is therefore preferred over barrel set-point control alone.

    The melt volume-flow rate of the base resin is controlled in the medium-viscosity range by ISO 1133-1; typical measurement conditions for PA12 are 235 °C with a 5 kg load. Because black pigment increases viscosity slightly relative to natural material, lot-to-lot MVR can shift by 1–3 cm³/10 min depending on the carbon-black masterbatch dilution. In extrusion, the shift appears as a change in melt pressure at constant screw speed. Closed-loop melt-pressure control is recommended when the same tool is used alternately for natural and black L-series products. In 24 h production of pneumatic tubing with 15 mm outside diameter and 1.5 mm wall, the principal failure modes are melt fracture at excessive output and die-lip carbon buildup. Melt fracture is avoided by raising melt temperature to 240 °C or reducing shear rate through die land length; die-lip carbon buildup is controlled by keeping the die surface below 230 °C and using purge compound between colour changes.

    When the Conditioned State Becomes the Critical Design Baseline

    For snap-fit connectors and press-fit tubing, dry-as-moulded tensile modulus can produce an overly stiff design that relaxes after moisture uptake. The conditioned modulus is approximately 27 % lower than the dry modulus for this PA12 type and should be used for finite-element analysis and after-mould shrinkage assessment. Because the equilibrium moisture content of PA12 is reached slowly in thick sections, a part may enter service dry and then absorb moisture over days to weeks. The transient produces a continuous increase in impact resistance and a reduction in flexural modulus. If dimensional stability is the primary requirement, the lower moisture uptake of PA12 compared with PA6 or PA66 keeps swell and stress relaxation smaller, but mating-metal clearances should still accommodate the calculated hygroscopic expansion.

    The glass-transition temperature of dry PA12 is reported in the range 35–55 °C depending on measurement method. After conditioning, absorbed water depresses the glass-transition temperature by several degrees. This contributes to higher notched impact toughness and greater chain mobility. Because the equilibrium moisture content is lower than in PA6 and PA66, the plasticization effect is limited. In dynamic mechanical analysis at 1 Hz, the conditioned grade may exhibit a loss-modulus maximum shifted downward by 5–15 °C relative to the dry state. Designers should use the conditioned tan δ response when evaluating vibration-damping or low-temperature ductility.

    Within the VESTAMID L-series, L2141 BK 9.750 occupies the medium-viscosity extrusion and injection-moulding range. Compared with a high-viscosity PA12 extrusion type, it provides lower melt pressure and higher melt volume-flow rate for thin walls; compared with a low-viscosity injection grade, it retains enough melt strength for uniform tube wall thickness and corrugated profiles. The black colourant package differentiates it from natural or white L-series materials by providing carbon-black-based ultraviolet screening and a different surface appearance. It is not a glass-fibre-reinforced or mineral-filled compound; therefore tensile modulus remains below 2 GPa, and moulding shrinkage is closer to that of an unfilled semicrystalline PA12.

    Operational boundaries include avoiding continuous contact with strong mineral acids, phenols, and oxidising media at elevated temperature. The black compound is not a conductive grade; it remains electrically insulating unless a separate conductive carbon-black variant is specified. Ultraviolet resistance is improved by the black pigment package relative to natural PA12, but long-term exposure to combined UV, heat, and road salts still requires end-use validation under ISO 4892-2 or outdoor weathering protocols. Food-contact suitability should not be inferred without a current manufacturer statement referencing EC 10/2011 or FDA 21 CFR 177.1500, because colourants and processing aids can alter the regulatory status of the finished article.

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