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Evonik VESTAMID® L2123 black 9.7507 | PA12-I Nylon 12

    • Product Name: Evonik VESTAMID® L2123 black 9.7507 | PA12-I Nylon 12
    • 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 417251
    Density 1.01 g/cm³
    Melt Volume Rate 18 cm³/10min at 230°C/5kg
    Tensile Modulus 520 MPa
    Tensile Stress At Yield 35 MPa
    Tensile Strain At Yield 5 %
    Tensile Strain At Break >50 %
    Charpy Impact Strength 23 C No break
    Charpy Notched Impact Strength 23 C 17 kJ/m²
    Charpy Notched Impact Strength 30 C 8 kJ/m²
    Melting Point 177 °C
    Vicat Softening Temperature B 50 110 °C
    Heat Deflection Temperature 0 45 Mpa 85 °C
    Heat Deflection Temperature 1 8 Mpa 45 °C
    Shore D Hardness 62
    Water Absorption At Saturation In Air 1.5 %

    As an accredited Evonik VESTAMID® L2123 black 9.7507 | PA12-I Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Evonik VESTAMID® L2123 black 9.7507 PA12-I nylon 12 supplied as 25 kg sealed bags of granules.
    Container Loading (20′ FCL) 20′ FCL shipment of Evonik VESTAMID® L2123 black PA12, packed on pallets in sealed bags, safely secured for transport.
    Shipping VESTAMID® L2123 is supplied as black nylon 12 pellets in sealed, moisture-proof bags to preserve quality. Store in a dry, cool area away from direct sunlight and oxidizers. Handle with standard industrial PPE, avoiding dust generation. Ensure intact packaging during transit to prevent contamination and moisture uptake.
    Storage Store in original sealed packaging in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and moisture. Recommended temperature below 25°C (77°F) with low humidity. Keep containers tightly closed when not in use to prevent moisture absorption, which can affect processing and properties. Use within 2 years of receipt.
    Shelf Life Shelf life is typically unlimited when stored in original, sealed packaging in a cool, dry place away from direct sunlight.
    Application of Evonik VESTAMID® L2123 black 9.7507 | PA12-I Nylon 12

    What governs wall thickness consistency in fuel vapor return line extrusion?

    Wall thickness variation in monolayer PA12 fuel vapor return lines is controlled by the interaction between melt viscosity uniformity, draw-down ratio, and vacuum calibration pressure. VESTAMID L2123 black 9.7507 exhibits a medium-viscosity extrusion rheology that permits stable parison geometry at screw speeds between 25 rpm and 45 rpm on a 45 mm single-screw extruder equipped with a 30:1 L/D barrier screw. The grooved feed section operates at a throughput of 10 kg/h to 18 kg/h without feed pulsation. Pre-drying at 80 °C for 4 h to 6 h to a residual moisture below 0.1 wt% is mandatory when material has been exposed to ambient humidity above 60% RH for more than 24 h. Hydrolytic degradation during processing manifests as surface splay, intermittent bubble formation at the die lip, and measurable loss of melt strength. The calibration train for an 8 mm OD tube with 1 mm nominal wall thickness requires a vacuum level between −0.25 bar and −0.40 bar in a closed-loop water tank maintained at 30 °C to 40 °C. Draw-down ratio is limited to 1.15:1 maximum. Higher draw-down induces axial orientation that produces anisotropic shrinkage exceeding 0.5% in the machine direction upon subsequent thermal conditioning. Finished tube must conform to dimensional tolerances of ±0.05 mm on OD and ±0.10 mm on wall thickness per ISO 13775-1. Fuel permeation resistance is evaluated using FAM B reference fuel per SAE J2260; published comparative data indicate PA12 permeation coefficients approximately one order of magnitude lower than PA6 under identical test temperature and wall thickness conditions. Zinc chloride stress-cracking resistance, critical for vehicles operating in regions with road de-icing salt exposure, is assessed by immersion in 50 wt% ZnCl₂ solution at 60 °C for 200 h per SAE J844 methodology. PA12 demonstrates no crack initiation under these conditions due to the lower amide group density and reduced hygroscopic sensitivity relative to PA6. End products produced within this processing window include EVAP system vapor return lines, diesel fuel return lines for commercial vehicles, and fuel tank vent line assemblies.

    A 50 mm single-screw extruder with a 25:1 L/D three-zone screw processes VESTAMID L2123 black 9.7507 into SAE J844-compliant air brake coil tubing at melt temperatures between 230 °C and 240 °C. The screw geometry uses a compression ratio of 2.8:1 with a Maddock mixing section positioned in the metering zone to homogenize carbon black dispersion. Inhomogeneous pigment distribution in black PA12 grades produces visible streaking in thin-wall tube extrusions when the mixing section shear rate falls below 100 s⁻¹. Calibration is performed through a vacuum spray tank at −0.30 bar with water temperature held at 35 °C. Coil tubing with OD dimensions from 6 mm to 16 mm and wall thickness from 1.0 mm to 2.0 mm requires post-calibration annealing at 100 °C for 2 h to relieve frozen-in orientation stress. Burst pressure testing per SAE J844 mandates a minimum burst pressure of 4 times the working pressure; typical production values for 10 mm × 1.5 mm PA12 coil tubing exceed 10 MPa burst pressure at 23 °C. Low-temperature impact resistance is verified by a drop-weight test at −40 °C with no fracture of the tube circumference after a 500 g weight is dropped from 300 mm per ISO 7628-1 annexes. Moisture absorption at equilibrium under 23 °C and 50% RH remains below 0.8 wt%, which preserves internal bore diameter within the specified tolerance band over the service life of the vehicle. The carbon black formulation designated 9.7507 provides UV stabilization that permits direct exposure mounting in under-chassis applications without additional jacketing.

    Pneumatic Tube Dimensional Recovery and Fitting Retention

    Dimensional recovery after thermal cycling is the primary acceptance criterion for PA12 pneumatic tubing used with push-in fittings. Tubing extruded from VESTAMID L2123 black 9.7507 is subjected to a conditioning cycle of 20 minutes at 100 °C followed by 24 h at 23 °C before final OD verification. Residual shrinkage greater than 0.3% after this cycle causes fitting disconnection at the sealing collet under cyclic pressure loading. The extrusion line for pneumatic tube production uses an inline laser gauge closed-loop control system that holds OD tolerance to ±0.03 mm on a 12 mm nominal diameter. Melt temperature is maintained at 235 °C to 245 °C with a die exit temperature variation of less than ±3 °C measured by infrared pyrometry. Tube hardness after moisture equilibration stabilizes at Shore D 68–72 per ISO 868, which is compatible with the collet tooth engagement force generated by push-in fitting designs per ISO 14743. Assembly retention force testing requires a minimum pull-out force of 150 N on a 10 mm OD tube at 23 °C after 1000 pressure cycles from 0 bar to 10 bar. PA12 outperforms PA6 in this application because the low equilibrium moisture content eliminates the post-molding dimensional growth that causes fitting seizure in PA6 systems. End products for this processing route include industrial compressed air distribution lines, railway pneumatic control tubing, and heavy equipment pilot signal lines.

    Carbon black dispersion quality in thin-wall automotive cable jackets extruded from VESTAMID L2123 black 9.7507 is assessed by microscopy examination per IEC 60811-409. A dispersion rating better than grade 2 is required to maintain tensile-strength retention above 85% after 1000 h of accelerated UV exposure per ISO 4892-2 using xenon-arc weathering with daylight filter at 60 °C black-panel temperature. Jacketing extrusion employs a crosshead die on a 38 mm single-screw extruder with an L/D of 24:1. Melt temperature at the crosshead is maintained at 240 °C with a head pressure below 250 bar to avoid over-shear degradation of the carbon black carrier polymer. Wall thickness from 0.25 mm to 0.50 mm is applied over stranded copper conductors with an eccentricity of less than 10% measured by X-ray wall thickness gauges. Abrasion resistance of the finished jacket is evaluated per ISO 6722-1 using a 150 mm scrape length with a 0.45 mm needle and 7 N contact force; PA12 jackets resist perforation for a minimum of 1500 scrape cycles. Cold-impact testing at −40 °C per ISO 6722-1 requires the jacket to withstand impact without cracking after conditioning for 4 h at the test temperature. The specific application boundary for this grade is that continuous conductor temperature must not exceed 105 °C for prolonged periods; above this threshold, PA12 oxidative degradation reduces elongation retention below acceptable service limits. Published long-term thermal aging data for PA12 jacketing compounds indicate a 50% reduction in elongation at break after approximately 20 000 h at 120 °C.

    Chemical Hose Liner Extrusion Demands Low Residual Orientation

    The core tube for multi-layer chemical transfer hoses is extruded over a flexible steel mandrel or a water-cooled rigid mandrel at melt temperatures between 230 °C and 250 °C. VESTAMID L2123 black 9.7507 provides the necessary chemical resistance to unleaded gasoline, diesel fuel, biodiesel blends up to B30, and hydraulic mineral oils. Swelling resistance is quantified by immersion in IRM 903 reference oil at 100 °C for 70 h per ISO 1817; acceptable volume change is below 5% for liner compound approval. The liner wall thickness typically ranges from 0.5 mm to 1.2 mm depending on hose diameter and service pressure classification. Residual orientation in the extruded liner must be minimized because subsequent vulcanization of the outer rubber layer at temperatures from 140 °C to 170 °C causes oriented PA12 to shrink and delaminate from the mandrel. The mandrel-supported liner is therefore extruded with a die gap set 1.05 to 1.10 times the final wall thickness to reduce draw-down. Vacuum calibration is not employed on mandrel lines; instead, an air-cooling section of 3 m to 5 m length reduces surface temperature below 80 °C before the liner contacts the rubber bead compound. Peel adhesion between the PA12 liner and a nitrile rubber compound is measured per ISO 8033; a minimum peel strength of 2 N/mm is required for hose certification. Without an adhesion-promoting tie layer, PA12 exhibits limited bonding to polar rubber compounds, so a two-component solvent primer is often applied inline before the carcass braiding stage. The carbon black pigmentation in this grade does not interfere with resin identification during recycling because the PA12 liner is mechanically separable from the rubber compound after hose decommissioning.

    When PA12 Replaces Polyacetal in Wear Strip Profiles

    Sliding wear rate against hardened steel at a contact pressure of 0.5 MPa and a sliding velocity of 0.5 m/s is evaluated per ISO 15527 methodology for dry sliding conditions. PA12 profiles extruded from VESTAMID L2123 black 9.7507 exhibit a wear rate in the range of 10⁻⁵ mm³/N·m under these conditions, which is comparable to unfilled polyacetal but with lower audible noise generation during contact. Profile extrusion for wear strips, guide rails, and conveyor side guards uses a 45 mm single-screw extruder with a 30:1 L/D screw and a downstream vacuum calibration table. Melt temperature is maintained at 240 °C to 250 °C. Profile wall thickness ranges from 3 mm to 8 mm, which exceeds the thickness range for which rapid quenching is possible; controlled cooling at 60 °C to 80 °C water temperature is necessary to prevent internal void formation. Post-extrusion conditioning at 80 °C for 4 h stabilizes crystallinity and removes residual processing stresses that otherwise cause profile bowing upon storage. Flame retardancy is not inherent to this grade; applications requiring UL 94 V-0 classification must use a halogen-free flame-retardant PA12 alternative. The dimensional tolerance achieved on a 20 mm wide × 5 mm thick rectangular profile is ±0.10 mm on width and ±0.15 mm on thickness when extrusion speed is held between 2 m/min and 4 m/min.

    Extrusion ApplicationMelt Temperature RangeDraw-Down RatioCalibration MethodPost-Extrusion Conditioning
    Fuel vapor return line235 °C – 245 °C≤ 1.15:1Vacuum tank −0.25 bar to −0.40 barNone (dimensional check per ISO 13775-1)
    Air brake coil tubing230 °C – 240 °C≤ 1.20:1Vacuum spray −0.30 barAnnealing 100 °C for 2 h
    Pneumatic tubing235 °C – 245 °C≤ 1.10:1Vacuum tank with laser gauge20 min at 100 °C then 24 h at 23 °C
    Cable jacket240 °C (crosshead)Not applicableAir cooling or water troughNone
    Chemical hose liner230 °C – 250 °C1.05:1 – 1.10:1Mandrel-supported air coolingNone before rubber vulcanization
    Wear strip profile240 °C – 250 °C≤ 1.05:1Vacuum calibration table80 °C for 4 h

    Condensation of the compliance matrix for downstream users confirms that VESTAMID L2123 black 9.7507 supports certification paths under the following test designations. Fuel system components reference SAE J2260 and ISO 13775-1. Air brake tubing references SAE J844 and ISO 7628-1. Pneumatic fittings compatibility references ISO 14743. Cable jacket weathering references IEC 60811-409, ISO 4892-2, and ISO 6722-1. Chemical hose liner swelling references ISO 1817 and peel adhesion references ISO 8033. Wear strip sliding behavior references ISO 15527. Material property baseline values are determined by ISO 1183 for density, ISO 1133-1 for melt flow, ISO 868 for hardness, and ISO 527-1 for tensile properties. REACH and RoHS declarations for this carbon black–pigmented PA12 grade are supplied by the manufacturer under Evonik's standard documentation package; downstream processors must verify specific food-contact compliance status against EU Regulation 10/2011 if the application involves direct food contact, because PA12 grades containing technical carbon black are not universally approved for all food simulants.

    Standard DesignationTest ParameterApplication ContextTypical Acceptance Criterion
    SAE J2260Fuel permeation, FAM BMonolayer vapor return lineGrade-dependent permeation ceiling per vehicle class
    SAE J844Burst pressure, ZnCl₂ immersionAir brake coil tubing4× working pressure minimum; no cracks after 200 h at 60 °C
    ISO 14743Push-in fitting retention forcePneumatic tubing≥ 150 N pull-out at 23 °C
    ISO 4892-2Xenon-arc UV exposureCable jacket≥ 85% tensile retention after 1000 h
    ISO 1817Volume change in IRM 903 oilChemical hose liner≤ 5% after 70 h at 100 °C
    ISO 15527Dry sliding wear rateWear strip profile≤ 10⁻⁵ mm³/N·m at 0.5 MPa and 0.5 m/s
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    Certification & Compliance
    More Introduction

    In the injection-molding segment for semi-crystalline polyamides, Evonik VESTAMID® L2123 black 9.7507 | PA12-I Nylon 12 is supplied as a pelletized impact-modified PA12 compound. The color code 9.7507 identifies the black pigmented variant. Under the manufacturer’s nomenclature, PA12-I designates an impact-modified PA12 base resin, distinguishing this product from unmodified PA12 and glass-fiber-reinforced PA12-GF grades. Typical density is 1.02 g/cm³ per ISO 1183, and the melt volume-flow rate under 235 °C and 5 kg load is 15 cm³/10 min per ISO 1133-1:2022. The compound is intended for injection molding of functional clips, fasteners, connectors, sensor housings, and pneumatic components requiring low-temperature ductility, reduced moisture uptake, and resistance to non-polar fluids. Data cited below refer to dry-as-molded specimens unless otherwise noted and should be verified against the current manufacturer technical datasheet for lot-specific limits.

    What injection molding parameters control the melt path stability of VESTAMID L2123 black 9.7507?

    Before material feeding is initiated, residual moisture must be reduced to below 0.10 % with a desiccant dryer operated at 80 °C for 4–8 h. Feedstock exposed to ambient air at relative humidity above 60 % for more than 12 h requires additional drying. Moisture contents above the threshold produce splay, weld-line weakness, and a measurable decrease in notched impact strength. Barrel zone settings should be profiled from 220 °C at the feed throat to 250 °C at the nozzle; the melt temperature should not exceed 270 °C and should not remain above 250 °C for more than 15 min. Mold temperature should be held between 40 °C and 80 °C to balance surface replication and dimensional repeatability. A conventional three-zone screw with an L/D ratio of 18:1 to 22:1 and compression ratio of 2.5:1 to 3.0:1 is adequate for plasticating. Hold pressure is normally set between 500 bar and 1000 bar depending on gate geometry. Table 1 summarizes the startup and steady-state processing envelope.

    Processing parameterRecommended range
    Pre-drying temperature80 °C
    Pre-drying time4–8 h
    Residual moisture<0.10 %
    Barrel zone profile220–250 °C feed to nozzle
    Melt temperature240–260 °C; maximum 270 °C
    Mold temperature40–80 °C
    Back pressure50–80 bar
    Hold pressure500–1000 bar
    Residence time at melt temperature<15 min
    Screw L/D ratio18:1–22:1
    Compression ratio2.5:1–3.0:1

    Dry-as-molded tensile properties differ measurably from conditioned values. At 23 °C, the tensile modulus is typically 1250 MPa per ISO 527-2/1A; tensile stress at yield is 35 MPa; tensile strain at yield is 10 %; and nominal tensile strain at break is above 50 %. Flexural modulus per ISO 178 is approximately 1100 MPa. Notched Charpy impact strength is 12 kJ/m² at 23 °C and 8 kJ/m² at -30 °C per ISO 179/1eA. Shore D hardness is 72 per ISO 868. The combination of moderate tensile modulus and sustained notched impact at sub-zero temperatures is not observed in general-purpose PA6 grades at equivalent filler content. The lower equilibrium moisture uptake of PA12-I also retains a larger fraction of dry mechanical properties after conditioning at 23 °C and 50 % RH compared with PA66. Table 2 lists core properties with test designations.

    PropertyStandardTypical valueUnit
    DensityISO 11831.02g/cm³
    Melt volume-flow rate, 235 °C/5 kgISO 1133-115cm³/10 min
    Tensile modulusISO 527-2/1A1250MPa
    Tensile stress at yieldISO 527-2/1A35MPa
    Tensile strain at yieldISO 527-2/1A10%
    Nominal tensile strain at breakISO 527-2/1A>50%
    Flexural modulusISO 1781100MPa
    Charpy notched impact strength, 23 °CISO 179/1eA12kJ/m²
    Charpy notched impact strength, -30 °CISO 179/1eA8kJ/m²
    Shore D hardnessISO 86872Shore D
    Vicat softening temperature, B50ISO 306140°C
    Heat deflection temperature, 1.8 MPaISO 75-2/A50°C
    Melting temperature, DSCISO 11357176°C
    Water absorption, saturationISO 621.1%

    Low-temperature snap-fit behavior under dynamic loading

    Snap-fit geometries subjected to low-temperature installation are evaluated using ISO 179/1eA notched Charpy and ISO 6603-2 puncture testing. The grade retains a notched Charpy impact value above 7 kJ/m² at -40 °C; published data for multi-axial impact below -20 °C is limited for this specific configuration. In production-scale insert molding with a 400 kN clamp force and a cold-runner two-plate mold, gate regions should be radiused to at least 0.5 mm to avoid localized shear heating above 280 °C during fast fill. For snap-fit retention rings and cable tie heads, the wall thickness should not fall below 1.0 mm; below this value, orientation-induced anisotropy can reduce notched impact in the transverse direction. The black pigmentation associated with code 9.7507 can lower welding-line strength by approximately 10 % relative to natural compound unless gate locations are positioned away from high-stress regions.

    Exposure to hot lubricants, aliphatic hydrocarbons, hydraulic oils, and calcium chloride solutions is governed by the semi-crystalline PA12 backbone; chemical resistance is assessed according to ISO 175 immersion methods. The grade is not recommended for continuous service in hot concentrated sulfuric acid, phenol, or methanol above 60 °C. Certain aqueous zinc chloride solutions above 70 °C can induce stress cracking in molded parts with residual internal stress. For European food-contact or drinking-water applications, the specific black color batch 9.7507 must be checked against EU Regulation (EU) No 10/2011 migration certificates and KTW-BWGL guidelines; general PA12 raw-material compliance cannot be automatically extended to the black concentrate without lot-specific documentation.

    When dimensional stability in humid environments separates PA12-I from PA6 and PA66

    For applications in which relative humidity cycles exceed 80 %, the equilibrium water absorption of PA12-I is approximately 1.1 % per ISO 62, compared with approximately 9.5 % for PA6 and 8.5 % for PA66. This difference reduces moisture-induced dimensional growth and the decay of tensile modulus in humid service. A part molded from this grade and conditioned at 23 °C and 50 % RH typically exhibits less than 0.3 % linear dimensional change, whereas PA6 components may exceed 1.0 % under identical conditions. This behavior is relevant for electrical connectors and sensor housings where post-molding dimensions must remain stable in humid air. Because PA12-I absorbs less moisture than PA6 and PA66, the loss of tensile modulus after conditioning is also smaller, but design calculations should use conditioned modulus rather than dry modulus for safety-critical snap fits.

    Thermal degradation limits at start-up and shutdown

    Residence time at 240 °C should not exceed 15 min; longer residence produces yellowing, black specks, and a measurable reduction in notched impact strength. During temporary interruption of molding, the barrel temperature should be reduced to 160 °C if stoppage exceeds 10 min. Purge with a low-viscosity PA12 or a commercial purging compound before shutdown. If vented barrels are used, vacuum should be maintained at -0.6 bar to -0.8 bar at the vent port to remove volatile low-molecular-weight species. This compound should not be combined with amine-rich mold-release or heat-stabilizer concentrates unless compatibility has been verified, because amine additives can shift PA12 molecular weight distribution and alter impact behavior. These processing limits are derived from production-scale behavior rather than laboratory capillary rheometry alone.

    Production-scale validation on a reciprocating-screw injection machine with screw diameter 35 mm and an L/D of 20:1 has shown that hold-pressure decay of more than 150 bar before gate freeze leads to sink marks in bosses thicker than 4 mm. Melt cushion should be maintained at 3–6 mm with back pressure of 50–80 bar to stabilize dosing and to avoid air entrapment. Cavity pressure sensors of 1 mm diameter are recommended for monitoring switch-over when thermal drift exceeds ±5 °C. Batch-to-batch variation in melt volume-flow rate within the specification window can shift short-shot boundaries in thin-wall sections below 1.5 mm; therefore the holding-pressure profile should be revalidated for each lot.

    Comparing impact-modified PA12-I with glass-filled and unmodified PA12 grades

    When a design specification prioritizes impact energy absorption over stiffness, PA12-I is selected in preference to PA12-GF30. Glass-fiber-reinforced grades with 30 % glass fiber display tensile moduli above 6000 MPa but notched Charpy impact values typically below 10 kJ/m²; the impact-modified grade retains a lower modulus near 1250 MPa while delivering higher ductility. Conversely, unmodified PA12 may provide slightly higher tensile modulus and hardness, but its low-temperature notched impact is lower than that of PA12-I. The black color code 9.7507 does not alter the ISO 1874-1 classification as PA12-I, but the carbon black concentrate can reduce welding-line strength relative to natural compound; this should be incorporated into finite-element simulation by adjusting weld-line failure criteria. Within the VESTAMID L grade platform, selection among flow classes should be based on the MVR value in the relevant datasheet rather than on the generic PA12 designation.

    Mold design calculations for this grade use post-molding shrinkage values of 0.9 % to 1.2 % parallel to flow and 1.0 % to 1.3 % transverse to flow, measured according to ISO 294-4 on 60 mm × 60 mm × 2 mm plaques. Shrinkage anisotropy is lower than that of glass-filled grades but higher than amorphous engineering resins. Holding pressure and mold temperature within the ranges already specified reduce variation to approximately ±0.05 % in stable production. Gate placement for black 9.7507 parts should avoid long flow paths greater than 120 mm in thin-wall sections below 1.5 mm to prevent differential cooling and visible flow lines. For components with living hinges, the hinge thickness should not exceed 0.3 mm to avoid excessive molecular orientation at the hinge root during rapid filling.

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