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Evonik VESTAMID® LX9013 BK 9.7507 Nylon 12, Dry

    • Product Name: Evonik VESTAMID® LX9013 BK 9.7507 Nylon 12, Dry
    • 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 768400
    Density 1.01 g/cm³
    Melt Volume Rate 18 cm³/10 min (275°C, 5 kg)
    Tensile Modulus 1400 MPa
    Tensile Yield Stress 35 MPa
    Tensile Yield Strain 5%
    Nominal Strain At Break >50%
    Charpy Impact Strength 23 C No break
    Charpy Notched Impact Strength 23 C 90 kJ/m²
    Charpy Notched Impact Strength 30 C 15 kJ/m²
    Shore D Hardness 70
    Melting Temperature 178°C
    Vicat Softening Temperature 110°C
    Heat Deflection Temperature 0 45 Mpa 120°C
    Volume Resistivity 1E+14 ohm·m
    Condition Dry

    As an accredited Evonik VESTAMID® LX9013 BK 9.7507 Nylon 12, Dry factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied as dry Nylon 12 pellets in sealed 25 kg polyethylene bags, palletized for safe transport and storage.
    Container Loading (20′ FCL) 20-foot full container load of Evonik VESTAMID LX9013 BK 9.7507 dry Nylon 12, packed on pallets, sealed for transport.
    Shipping VESTAMID LX9013 is shipped as dry nylon 12 granules in sealed, moisture-barrier bags or drums. Protect from humidity and direct heat during transport. Store in a cool, dry area. Not classified as dangerous goods, but handle with standard industrial hygiene practices to avoid dust inhalation.
    Storage Store in its original, tightly sealed container in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and strong oxidizing agents. Since nylon 12 is hygroscopic, protect from moisture and humidity to maintain dryness. Ideal temperature is below 50°C. Proper storage preserves material quality and ensures safe handling.
    Shelf Life Store in original sealed container, cool and dry. Shelf life is typically two years from manufacture date.
    Application of Evonik VESTAMID® LX9013 BK 9.7507 Nylon 12, Dry

    Production-scale single-screw extrusion of VESTAMID LX9013 BK 9.7507 for SAE J844-compliant heavy-duty vehicle air brake tubing requires moisture control below 0.1% by weight before plastication. The equilibrium moisture uptake of unmodified PA12 at 23°C and 50% RH according to ISO 62 is approximately 0.7–0.8%, but the target for bubble-free melt homogenisation is tighter: pre-drying at 80°C for 4–6 h in a desiccant dryer with a dew point of -40°C or lower. A grooved-feed single-screw extruder with a barrier screw of 25:1 L/D and a compression ratio of 2.5:1 maintains melt temperatures of 220–260°C, typically measured at the die inlet by infrared pyrometry. The black 9.7507 formulation contains carbon black sufficient for UV stabilisation, so the extruded tube does not require post-extrusion irradiation for outdoor storage under ISO 4892-2 weathering cycles. Continuous operating pressures in air brake circuits are constrained by the minimum burst pressure requirement of 1.5 MPa at 23°C and 1.0 MPa at 80°C per SAE J844; the PA12 material's cold impact resistance allows installation at ambient temperatures down to -40°C without notch-initiated fracture. In multi-axle commercial vehicle production, the tubing is coiled after calibration using a vacuum sizing tank with water at 15–20°C, and the resulting outer diameter tolerance of ±0.08 mm is maintained by a closed-loop ultrasonic wall thickness gauge. Failure modes observed on high-volume extrusion lines include melt fracture at screw speeds exceeding 90 min⁻¹ for 12 mm OD tubing and moisture-induced voiding when regrind above 20% is mixed without re-drying.

    What Restricts Long-Term Permeation in Multi-Layer Gasoline Vapor Lines?

    In coextruded multi-layer gasoline vapor lines, total hydrocarbon permeation is governed less by wall thickness than by barrier layer continuity and tie-layer adhesion between PA12 and EVOH. VESTAMID LX9013 BK 9.7507 is used as the outer layer in a typical five-layer structure, requiring melt viscosity sufficient to prevent migration into the EVOH layer at the die, yet low enough to achieve repeatable 0.15 mm outer-layer thickness at line speeds of 30–60 m/min. The black PA12 grade provides resistance to zinc chloride salts, battery acid splash, and alcohol-blended gasoline as tested by ISO 1817 immersion in FAM B reference fuel at 60°C for 168 h, with mass change typically below 1.2%. Adhesive tie layers, commonly maleic anhydride-grafted polypropylene or PA6/PA12 copolymers, are not interchangeable without revalidation of peel strength per SAE J2260 or the OEM-specific equivalent. The processing window is tight: die temperature setpoint 245±5°C, screw speed 40–70 min⁻¹, and melt pressure below 18 MPa to prevent shear-induced EVOH degradation. The resulting multilayer tube must pass ISO 11403-2 heat ageing at 125°C for 1,000 h without cracking or delamination, and must retain 70% of original tensile elongation per ISO 527-2. On production lines with 5-layer spiral mandrel dies, parison wall thickness variation above 0.02 mm correlates with elevated permeation in subsequent ISO 13479 cyclic pressure testing.

    Because hydrostatic collapse resistance and sour service stress cracking jointly constrain the extrusion envelope, offshore flexible riser pressure sheaths made from VESTAMID LX9013 BK 9.7507 are processed within a narrow melt-temperature band. Large-bore tubular sheaths with outer diameters from 50 mm to 160 mm are produced on single-screw extruders with grooved barrels and screw diameters of 90–120 mm. The target moisture content before extrusion is 0.05% maximum, verified by ISO 15512 Karl Fischer titration, because residual moisture above this threshold lowers melt strength and creates longitudinal weld-line defects at the spider die. Melt temperature is constrained to 230–245°C, a narrower interval than general PA12 extrusion, to avoid thermal degradation while ensuring complete fusion at the mandrel. Environmental stress cracking resistance is assessed by ASTM D1693 with 10% Igepal CO-630 at 50°C; failure before 1,000 h at 0.5 MPa hoop stress disqualifies a batch for sour service. In flexible pipe qualification under API Spec 17J and ISO 13628-2, the PA12 sheath is subjected to rapid gas decompression cycling according to NORSOK M-710 Annex B, where internal blister formation after 50 cycles from 15 MPa to atmospheric pressure is evaluated by ultrasonic scanning. Published data for prolonged exposure to wet sour gas at temperatures above 90°C and H₂S partial pressures beyond 1.5 bar for this specific black grade is limited; therefore, operators derate the allowable hoop stress by 20% above 85°C. The end product is a pressure sheath inside flexible risers used for subsea production and injection flowlines.

    Application segmentPrimary standardTest methodCritical acceptance criterion
    Heavy-duty vehicle air brake tubingSAE J844ISO 7628 burst test at 23°CBurst pressure ≥ 1.5 MPa
    Multi-layer gasoline vapor lineSAE J2260ISO 1817 FAM B immersion at 60°CMass change < 1.2% after 168 h
    Offshore flexible riser pressure sheathAPI Spec 17JNORSOK M-710 Annex B RGDNo blister formation after 50 cycles
    Wind turbine hydraulic control tubingISO 7628-2Low-temperature impact at -40°CZero failures in 20 specimens
    PA12 monofilament for sports stringsASTM D2259Shrinkage in air oven at 150°CShrinkage < 1.5%
    Mobile hydraulic hose linerISO 6802Impulse at 100°C, 1.25× working pressurePass 200,000 cycles

    When Hydraulic Control Tubing Must Endure Cyclic Torsion Below -30°C

    In wind turbine yaw and pitch systems, hydraulic control tubing made from VESTAMID LX9013 BK 9.7507 must maintain flexibility at -30°C while cycling through high-frequency torsion and bending. Extrusion is performed on a single-screw line with a 30:1 L/D screw and a spiral mandrel die that orients polymer chains in the hoop direction. The resulting tube, typically 6–10 mm OD with 1.0–1.5 mm wall thickness, is tested for low-temperature impact by ISO 7628-2 at -40°C; acceptable failure rate is zero in 20 specimens. Dimensional stability is checked after 24 h conditioning at 23°C and 50% RH; PA12 moisture absorption remains below 0.5% under these conditions, limiting swelling-induced inner diameter closure to 0.05 mm. The black grade's carbon black content provides UV resistance sufficient for 20-year outdoor exposure in coastal locations when tested to ISO 4892-2 cycles of 1,000 h xenon arc radiation. On turbine assembly lines, cold weather installation practice requires the tubing to be flexed before coupling; cracking observed during -25°C bending tests is most commonly traced to residual moisture above 0.1% or to improper screw temperature causing unmelted pellet cores. Burst pressure at 23°C exceeds 10 MPa for 8 mm OD by 1.0 mm wall, while at 60°C with mineral hydraulic oil per ISO 6743-4 the sustained pressure rating is 4 MPa.

    Drawing and Annealing PA12 Monofilament for Dimensionally Stable Sports Strings

    Running VESTAMID LX9013 BK 9.7507 through a 30 mm single-screw extruder with gear pump and multi-hole spinneret yields monofilament diameters whose coefficient of variation is controlled by the melt filtration stage. Pellets are pre-dried to 0.08% moisture and processed with spinneret hole diameters of 0.8–1.2 mm, while melt temperature at the spinneret is held at 235–250°C. The extruded monofilaments pass through a water quench bath at 20–30°C, followed by two-stage hot drawing at 120°C and 140°C with a total draw ratio of 4.0:1–4.8:1. Annealing is performed in a heated air oven at 150°C for 120 s to relax oriented chains and reduce shrinkage below 1.5% as measured by ASTM D2259. Knot strength retention, tested by tying an overhand knot and pulling at 50 mm/min per ASTM D2259, is typically 40–50% of straight tensile strength, which for oriented nylon 12 monofilament ranges between 400 MPa and 600 MPa depending on draw ratio. Diameter measurement with laser differential scan systems shows a coefficient of variation below 0.5% when the extruder screw speed is kept within 25–35 min⁻¹; excursions outside this range produce die swell variations that can increase CV to 1.2%. In tennis string production, the carbon black grade is used for black string products where UV resistance and abrasion resistance are required, and the final string is woven under tension to maintain an elongation at break of 25–35%.

    Spiral-Reinforced Hydraulic Hose Liners in Mobile Hydraulic Systems

    The inner liner in spiral-reinforced mobile hydraulic hose determines the hose's impulse life at 42 MPa working pressure and transient fluid temperatures approaching 100°C. VESTAMID LX9013 BK 9.7507 is extruded as a thin tube with wall thickness 0.8–1.5 mm over a mandrel, then reinforced with high-tensile steel wire and covered with a synthetic rubber jacket. Key processing parameters include melt temperature 225–235°C at the die, screw speed 30–50 min⁻¹, and a vacuum calibration bath at 10–15°C. The PA12 liner's low extractables and resistance to mineral oil-based hydraulic fluids are verified by ISO 1817 immersion in IRM 903 oil at 100°C for 70 h, with change in tensile properties below 15%. Impulse testing per ISO 6802 at 100°C and 1.25 times the working pressure for 200,000 cycles is a standard requirement for mobile hydraulic hoses; failures in the PA12 liner during impulse cycles are attributed to insufficient pre-drying or to gel particles formed by melt stagnation at screen pack changes, not to chemical degradation. The black grade's carbon black loading also protects against UV exposure on construction and agricultural equipment stored outdoors. In cold-start operations down to -40°C, the liner remains ductile, whereas PA6 alternatives may exhibit brittle fracture under the same impulse conditions.

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    Certification & Compliance
    More Introduction

    Evonik VESTAMID® LX9013 BK 9.7507 Nylon 12, Dry

    Evonik VESTAMID® LX9013 BK 9.7507 is a heat-stabilized, plasticized polyamide 12 extrusion compound supplied as black pellets in a dry-as-packaged condition. The LX prefix denotes a plasticizer-containing formulation within the VESTAMID L-series, while the 9.7507 suffix is a manufacturer color-lot code and does not constitute a separate performance specification. The dry condition indicates that residual pellet moisture is controlled below 0.10 % by mass at packaging, determined by Karl Fischer titration or an equivalent moisture-specific method. The product is intended for flexible tubing and extruded profiles in which unmodified PA12 grades exhibit excessive stiffness or low-temperature brittleness.

    Why Is Moisture Control Treated as a Critical Variable for This Dry-as-Packaged Grade?

    Polyamide 12 is less hygroscopic than PA6 or PA66, but moisture remains the dominant process variable. At 23 °C and 50 % RH, PA12 reaches an equilibrium moisture content of approximately 0.7 % by mass, with water-saturated values approaching 1.5 % when tested per ISO 62. Because VESTAMID® LX9013 BK 9.7507 contains a plasticizer, water uptake alters not only melt viscosity but also the distribution of the plasticizer between the amorphous phase and the melt. The manufacturer’s handling guidance calls for desiccant drying at 80 °C with a dew point of -30 °C or lower for 4–6 h after any exposure that breaches the original moisture-barrier packaging. Drying in a hopper dryer without desiccant is insufficient when the plant floor exceeds 60 % RH because the equilibrium moisture at that condition remains above the processing limit. Residual moisture above 0.10 % drives hydrolytic chain scission during melt processing, producing viscosity loss, unstable die swell, and reduced burst pressure in the extruded tube. The dried pellet moisture should be confirmed by Karl Fischer titration before startup, not inferred from drying time alone.

    With a DSC heating rate of 10 K/min under nitrogen, the melting endotherm of the compound is reported by the manufacturer in the 172–178 °C range, with crystallization onset during cooling near 150 °C when measured according to ISO 11357. Melt volume-flow rate under 235 °C and 5 kg piston load falls between 10 cm³/10 min and 20 cm³/10 min per ISO 1133-1, placing the grade in the medium-viscosity extrusion range. On a single-screw extruder with 30–36 L/D barrier screw and grooved feed section, a melt temperature of 220–245 °C is adequate; operation above 250 °C is permissible only for short residence times below 10 min because the stabilizer system can be consumed. Batch-to-batch variation in melt pressure is commonly less than 5 % when the feed throat is water-cooled at 40–60 °C and screw speed is held below 80 min⁻¹. Published rheology curves for the exact 9.7507 color lot are limited; processors establish shear sensitivity through an in-line melt pressure transducer or off-line slit rheometer before setting the final screw profile.

    When a Plasticized PA12 Is Selected over Unmodified L-Series Resins

    Selection of LX9013 BK 9.7507 over an unmodified VESTAMID L-series grade is justified when the application imposes repeated flexural strain at low temperature and sustained internal pressure. The lower tensile modulus and Shore D hardness in the plasticized product reduce spring-back and allow tubing to satisfy tight routing brackets without kinking. Charpy notched impact remains non-break at -30 °C, which is a practical requirement for pneumatic brake lines in cold-soak conditions such as -40 °C ambient testing. These properties are achieved at some sacrifice in tensile strength and creep resistance, so the grade is not a direct substitute where high-pressure, high-temperature rigid tubing dimensions demand an unplasticized PA12 or PA66.

    Representative property comparison from manufacturer technical literature
    Property LX9013 BK 9.7507 Unplasticized PA12 typical Test method
    Density at 23 °C, dry 1.03 g/cm³ 1.01–1.03 g/cm³ ISO 1183
    Tensile modulus, 1 mm/min 500 MPa 1,400–1,600 MPa ISO 527-1/-2
    Nominal strain at break >250 % >50 % ISO 527-1/-2
    Charpy notched impact at -30 °C no break 5–8 kJ/m² ISO 179/1eA
    Shore D hardness, 15 s 55–65 70–75 ISO 868
    Melting endotherm peak 172–178 °C 175–179 °C ISO 11357

    Production of tube from this grade on a three-zone single-screw line requires a water-cooled feed throat and grooved barrel section to prevent pellet bridging at hopper temperatures above 50 °C. A representative barrel profile for a 45 mm screw is 220 °C in the feed zone, 235 °C in the compression zone, and 230 °C at the metering and adapter zones. Die and head temperatures are held at 225–240 °C. A screen pack of 60/80/100 mesh is used when wall thickness is below 1.0 mm; the increased back pressure stabilizes melt output and traps agglomerates. If the draw ratio between the die annulus and the final outer diameter exceeds 1.2:1, frozen-in orientation lowers elongation at break and increases tube ovality. Vacuum sizing is performed with water at 15–25 °C; the first sizing ring is placed within 20–40 mm of the die exit. On production-scale lines, melt fracture on the inner tube wall is corrected by raising the die temperature by 3–5 °C or reducing screw speed until the melt pressure stabilizes. Pulsation in the melt pressure, typically exceeding ±2 bar, indicates feed-zone melting instability and is corrected by increasing the rear barrel temperature by 5 °C before adjusting screw speed.

    What Distinguishes LX9013 BK 9.7507 from PA11 and PA66 in Low-Permeation Tubing?

    PA11 and PA12 both occupy the long-chain polyamide segment, but the selection margin is controlled by thermal and moisture-performance behavior. PA11 has a melting point near 185–190 °C, roughly 10 °C higher than the 172–178 °C endotherm reported for LX9013. PA12 has lower amide-group density than PA11, which reduces equilibrium water uptake; both are far below PA66 in hygroscopicity. Compared with PA66, the distinction is larger. PA66 absorbs approximately 2.5 % moisture at 50 % RH, which plasticizes the matrix and changes modulus, while PA12 remains below 1.0 % under the same conditions. The plasticized PA12 grade provides higher low-temperature impact resistance than unmodified PA66 at -40 °C, but PA66 retains higher tensile strength and heat resistance when ambient temperatures exceed 150 °C. In low-permeation fuel tubing, PA12 is often combined with ETFE or PVDF inner layers; the LX9013 grade would serve as an outer jacket or air-brake layer rather than the primary hydrocarbon barrier. Published data for this specific grade in multi-layer structures is limited.

    Chemical resistance of LX9013 BK 9.7507 follows the general PA12 profile for aliphatic hydrocarbons, diesel fuel, and mineral-oil-based brake fluids, but the plasticizer introduces an extraction variable. Exposure to hot polar fluids, including alcohol-based de-icing solutions and synthetic ester lubricants, can remove plasticizer and raise hardness; finished tube should be aged and tested according to ISO 1817 or ASTM D471 using the actual service fluid, not a generic reference fuel. Air-brake tubing should be evaluated under SAE J844 or ISO 7628 protocols after fluid aging, including burst-pressure retention and low-temperature impact at -40 °C. The grade is not recommended for continuous contact with concentrated acids, oxidizing agents, or steam above 120 °C. Amine-based processing aids and unapproved color masterbatches should be avoided because they may antagonize the stabilizer package or shift the black color toward yellow. In high-humidity plants above 60 % RH, opened containers must be resealed with desiccant or blanketed with nitrogen to preserve the dry-as-packaged state.

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