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Evonik Vestamid L2124 sw 9.7507 (dry properties) Nylon 12

    • Product Name: Evonik Vestamid L2124 sw 9.7507 (dry properties) 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 226593
    Density 1.01 g/cm³
    Water Absorption 24h 23 C 0.8 %
    Water Absorption Saturation 1.7 %
    Melting Point Dsc 10 K Min 178 °C
    Tensile Yield Stress 50 Mm Min Dry 45 MPa
    Elongation At Yield 4 %
    Elongation At Break > 50 %
    Tensile Modulus 1 Mm Min Dry 1600 MPa
    Charpy Impact Strength 23 C Dry No Break
    Ball Indentation Hardness H 132 5 30 80 MPa
    Shore Hardness D 72
    Vicat Softening Temperature B 50 170 °C
    Heat Deflection Temperature A 1 8 Mpa 55 °C
    Heat Deflection Temperature B 0 45 Mpa 120 °C

    As an accredited Evonik Vestamid L2124 sw 9.7507 (dry properties) 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 L2124 sw 9.7507 Nylon 12 is supplied in sealed 25 kg bags, requiring dry storage.
    Container Loading (20′ FCL) A 20′ FCL securely loads palletized Evonik Vestamid L2124 sw 9.7507, dry Nylon 12 granules, protected for safe transport.
    Shipping Evonik Vestamid L2124 sw 9.7507 is a Nylon 12 thermoplastic supplied as dry granules. Ship in sealed, moisture-proof bags or drums to prevent water absorption. Store in a cool, dry area, avoiding humidity and direct sunlight. Transport in clean, dry containers; non-hazardous per standard regulations, with proper labeling for polymer resin.
    Storage Store Evonik Vestamid L2124 sw 9.7507 Nylon 12 in its original sealed packaging, in a cool, dry, and well-ventilated area. Protect from moisture, direct sunlight, and heat sources. Keep away from oxidizing agents. Under these conditions, the material retains its dry properties and remains stable for an extended shelf life.
    Shelf Life Store in dry, sealed original packaging; stable for at least 2 years under cool, dry conditions.
    Application of Evonik Vestamid L2124 sw 9.7507 (dry properties) Nylon 12

    On heavy-duty truck and bus assembly lines, pneumatic brake circuits are plumbed with flexible thermoplastic tubing that must survive continuous pressure cycling, road-debris abrasion, and exposure to zinc chloride from winter de-icing brines. The PA12 grade Vestamid L2124 sw 9.7507 is processed as the base polymer for air brake tube compounds; dry-as-molded mechanical values are conditioned to ISO 527-1/-2 and evaluated after 48 h at 23 °C and 50 % relative humidity. In tube form, dimensional and performance conformity is assessed under ISO 7628-1:2015 and ISO 7628-2:2015, while North American fleets additionally require SAE J844:2023 cold-impact testing at −40 °C, burst testing at 80 °C, and zinc chloride stress-crack resistance after dynamic flex fatigue. The formulation is typically 97.0–98.5 wt% Vestamid L2124 sw 9.7507 with 1.5–3.0 wt% carbon black/UV stabilizer masterbatch; carbon black dispersion is controlled at agglomerate sizes no larger than 5 µm to avoid microvoids in the tube wall. Processing begins with desiccant drying at 80 °C for 4–6 h to a residual moisture content below 0.10 wt%, followed by extrusion on a single-screw line with a grooved feed section, L/D 25:1–30:1, and compression ratio 2.5:1–3:1. Melt temperature is held between 210 °C and 235 °C; die head pressure is 8–15 MPa, vacuum calibration is maintained at 0.05–0.08 MPa, and line speed is 15–40 m/min depending on outside diameter. Melt temperature above 260 °C is avoided to limit chain scission and monomer regeneration. Post-extrusion conditioning at 23 °C and 50 % relative humidity for 48 h stabilizes dry-as-molded crystallinity before final coiling, inkjet marking, and pressure-decay leak checks. Finished articles are 6 mm, 8 mm, 10 mm, 12 mm, and 16 mm outside-diameter coiled air brake tubing assemblies with push-in or compression fittings, installed in pneumatic service and parking brake circuits of trucks, buses, and tractor units.

    Why Do Push-In Pneumatic Fittings Demand Tight Ovality Control in PA12 Tubing?

    Polyamide 12 pneumatic tubing used in automated assembly and packaging lines exhibits inert air-release behaviour and low water absorption where polyurethane tubing may show dimensional drift or hydrolysis after repeated washdown cycles. The dry-as-molded mechanical properties of Vestamid L2124 sw 9.7507 define the short-term hoop stress used to calculate working pressure under ISO 4414:2010, while tubing and fitting interchangeability is governed by ISO 14743:2020. A production compound typically uses 96.0–98.0 wt% dry resin with 2.0–4.0 wt% oil-free color/UV masterbatch; moisture is kept below 0.08 wt% before extrusion to prevent hydrolysis. The tube is extruded through a vacuum-sizing die on a single-screw extruder at melt temperatures between 200 °C and 220 °C, using a laser outside-diameter gauge and ultrasonic wall-thickness sensors to hold outside diameter within ±0.05 mm and wall thickness within ±0.03 mm. Vacuum calibration is set at 0.03–0.06 MPa, and screw speed is tied to a gear pump to limit melt-pressure fluctuation to ±0.3 MPa. Leak testing is performed at 0.6 MPa air pressure with pressure decay below 0.5 kPa/min, and burst pressure is verified to at least 2.4 times the rated working pressure at 23 °C according to ISO 1402:2021. Finished product consists of straight, recoiled, or cut-to-length pneumatic tubing in 4 mm, 6 mm, 8 mm, 10 mm, 12 mm, and 16 mm outside diameters, used with push-in fittings in robotic grippers, valve islands, and pneumatic logic circuits.

    For woven process belts and dewatering screens, the extrusion-grade PA12 is converted into oriented monofilament used in food-contact conveyor belts and industrial filter fabrics. The resin is processed at 100 wt% with 0.1–0.3 wt% of a high-molecular-weight silicone process aid and, when colored, 1.0–2.0 wt% pigment masterbatch; no plasticizer is added because plasticizer migration can alter mesh stiffness over time. For food-contact use, the finished monofilament must satisfy FDA 21 CFR 177.1500(b) for nylon 12 resins and the food-contact article requirements of EU Regulation (EU) No 10/2011, with migration testing according to the finished mesh surface-to-food ratio and intended contact time. The downstream production process is a melt-spinning line comprising a single-screw extruder with L/D 25:1, melt pump, breaker plate, and spinneret; water quench at 20–30 °C; two-stage drawing in hot water or air at 70–90 °C with total draw ratio 4.0:1–5.0:1; and annealing at 130–150 °C for 20–40 s before winding on precision take-up rolls. Terminal products include woven spiral link belts, open-mesh conveyor belts for baking and drying tunnels, and filter fabrics with mesh apertures from 50 µm to 1,200 µm.

    If Underhood Harness Conduit Must Survive Hot Diesel Exhaust Gas Recirculation Zones

    Split and non-split corrugated conduit installed around engine harness segments adjacent to exhaust gas recirculation tubing must retain impact strength after hot-oil and hot-air ageing. Vestamid L2124 sw 9.7507 is extruded into corrugated profiles with an addition ratio of 98.0–99.0 wt% resin and 1.0–2.0 wt% heat-stabilised black masterbatch; for UV-stabilised exterior runs, carbon black content is held at 2.0–2.5 wt% to absorb UV radiation and reduce surface embrittlement. Compliance for flexible conduit systems is evaluated under IEC 61386-23:2021 for mechanical properties, while flammability acceptance on 3.0 mm test plaques is documented as UL 94 V-2 or better at the specific wall thickness. The production process uses a single-screw extruder feeding a horizontal corrugator; melt temperature is 205–225 °C, corrugator mould temperature is 30–50 °C, vacuum forming is set to 0.02–0.04 MPa, and line speed is 10–30 m/min. Post-forming, conduit is cooled in a water bath at 20–35 °C, dried with air knives, and cut to lengths of 100–6,000 mm. Terminal products are slit and un-slit corrugated PA12 conduits in nominal inside diameters from 4.5 mm to 40 mm, used for wire harness routing in commercial vehicle engine bays and for hydraulic hose protection in mobile machinery.

    Cable Sheath Compounds in Cold-Storage Warehouse Automation Use Low-Temperature Impact at −40 °C as the First Pass/Fail Barrier

    Control and sensor cables routed through automated cold-storage retrieval systems are repeatedly flexed at sub-zero temperatures, where standard polyvinyl chloride jackets crack under bending. Polyamide 12 jacketing compounds based on Vestamid L2124 sw 9.7507 are processed with an addition ratio of 100 wt% dry resin; no halogenated flame-retardant fillers are incorporated because this application uses the inherent low-temperature toughness and hydrolytic stability of PA12. The main compliance tests referenced for finished cable sheaths are low-temperature impact at −40 °C under EN 60811-506:2012 and tensile strength and elongation at break after thermal ageing under EN 60811-201:2018. Production is performed by pressure extrusion of the sheath over the cable core using a crosshead die; melt temperature is 215–230 °C, screw L/D is 25:1–30:1, and the water trough is set to 20–40 °C with controlled water flow to reduce sheath ovality. The die land length is increased to 2.0–3.0 times the sheath thickness to stabilise melt pressure and avoid drawdown-induced residual stress. Finished articles include flexible reeled control cables, sensor actuator cables, and drag-chain cables for freezer logistics, with outside diameters typically 6–18 mm.

    Qualifying Rapid Gas Decompression Resistance in API 17E Umbilicals

    Subsea production control systems use small-bore thermoplastic tubes to inject methanol, hydraulic fluid, and corrosion inhibitor into wellheads and manifolds. In this service, PA12 compounds are selected over cross-linked polyethylene where a balance of low-temperature flexibility, methanol resistance, and long-term hydrolytic stability is required. Vestamid L2124 sw 9.7507 is processed at 100 wt% resin as the barrier layer; extraneous plasticizers are avoided because low-molecular-mass additives can be extracted by methanol under high pressure, altering tube dimensions and reducing resistance to explosive decompression. Tube production is qualified under API Spec 17E / ISO 13628-5:2021 for subsea umbilical hoses and tubes, and candidate compounds are screened by NORSOK M-710 Rev 2 for sour service polymer resistance and rapid gas decompression. Downstream processing uses a barrier-screw single-screw extruder with L/D 30:1, melt temperature 215–235 °C, controlled cooling in a multi-stage water trough at 35–55 °C, and online ultrasonic wall-thickness measurement with a defect threshold of ±0.08 mm. The finished product is a continuous PA12 core tube in outside diameters 6–25 mm and wall thicknesses 1.0–3.0 mm, integrated into steel-tube bundles or fibre-optic control umbilicals for subsea production fields. Published data for Vestamid L2124 in sour gas rapid gas decompression testing is limited; final qualification requires testing on the exact tube dimensions and umbilical termination hardware under the project’s maximum design pressure and minimum seabed temperature.

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    Certification & Compliance
    More Introduction

    Vestamid L2124 sw 9.7507 is a heat-stabilized, semi-flexible polyamide 12 extrusion grade supplied in black-pigmented pellet form. The product code sw designates the black colouration package, and the suffix 9.7507 identifies the specific colour recipe within the manufacturer’s masterbatch system. In the dry-properties context, the mechanical values discussed here refer to test specimens dried to a residual moisture content below 0.1 % by mass and tested before conditioning at 23 °C and 50 % relative humidity in accordance with ISO 291. The polyamide 12 backbone, built from laurolactam, provides lower equilibrium moisture uptake than PA6 or PA66; saturated water absorption for the product family is approximately 1.5 % by ISO 62. The grade is directed toward extruded tubing, coiled air-brake lines, fuel vapor conduits, pneumatic tubing, and cable protection where coil flexibility, low-temperature impact resistance, and low leach-out are required. Because the material is supplied in black, the carbon black also provides opacity and contributes to outdoor weathering stability; however, specific UV performance must be verified according to ISO 4892-2 on the final wall thickness and colour dispersion.

    What Moisture Threshold Triggers Hydrolytic Degradation in Vestamid L2124 Before Melt Processing?

    Before melt processing, the residual moisture in the pellet feed must be reduced to a target below 0.1 % by mass because hydrolytic chain scission accelerates above that threshold during melt residence. Desiccant drying at 80 °C for 4 h to 8 h with a dew point below -40 °C is representative for closed-loop hopper dryers; shorter residence times require verification by Karl Fischer titration in accordance with ISO 15512. In plants operating at relative humidity above 60 %, regrind should be dried separately and not mixed into virgin feed unless the blend moisture is again verified. Melt processing at residual moisture above 0.15 % can produce surface defects, viscosity loss, and reduced burst strength in thin-wall tubing. Production-scale failure modes include microporosity in the inner wall, non-uniform die swell, and intermittent melt fracture that is sometimes misattributed to die build-up. Measurement of melt viscosity before and after drying, using a capillary rheometer at 230 °C at shear rates from 100 s⁻¹ to 2500 s⁻¹, is the recommended method for detecting hydrolytic damage before the material enters the extruder.

    Under as-molded conditions with residual moisture not exceeding 0.1 % by mass, representative dry mechanical data for the product family are summarised below. The values are typical lot-average values and are not specification limits; the certificate of analysis for each batch remains the controlling document.

    PropertyTest methodDry-property value
    DensityISO 1183-11.01 g/cm³
    Melt volume-flow rateISO 1133-1 at 235 °C/5 kg10 cm³/10 min
    Tensile modulusISO 527-1/-21300 MPa
    Tensile stress at yieldISO 527-1/-242 MPa
    Elongation at breakISO 527-1/-2200 %
    Charpy notched impact strength at 23 °CISO 179-1/1eA9 kJ/m²
    Charpy notched impact strength at -30 °CISO 179-1/1eA4 kJ/m²
    Vicat softening temperature VST/B/50ISO 306145 °C
    Melting temperatureISO 11357-1/-3176 °C
    Water absorption saturationISO 621.5 %

    The tensile elongation at break above 200 % in the dry state is relevant for coiled tube insertion because it permits buckling and recovery without stress whitening. The notched Charpy impact value of approximately 9 kJ/m² at 23 °C falls within the expected range for semi-flexible polyamide 12; at -30 °C the retention of approximately 4 kJ/m² remains significant for cold-climate pneumatic lines. The Vicat softening temperature VST/B/50 of approximately 145 °C is below the melting temperature of 176 °C, but short-term Vicat data do not define continuous service temperature. Long-term thermal stability must be derived from aging curves according to ISO 2578 or relative thermal index methods such as UL 746B. For dry-properties testing, tensile test speed is 50 mm/min for modulus and strength according to ISO 527-1/-2; injection-moulded ISO multipurpose test specimens are used. The moisture-dependent shift in properties is a governing design factor: after conditioning at 23 °C and 50 % relative humidity, tensile modulus typically decreases by 10 % to 20 %, while impact resistance increases. Published data for the exact colour batch 9.7507 may differ from natural grades because carbon black affects nucleation and can reduce impact strength by 5 % to 15 % compared with natural polymer.

    Tubing Ovality Control and Annular Die Land Length for Semi-Flexible PA12

    On single-screw extruders with a 24:1 to 30:1 L/D ratio and a three-zone screw with a compression ratio of 2.5:1 to 3.0:1, melt temperature for Vestamid L2124 sw 9.7507 is maintained between 230 °C and 260 °C. The black pigmentation raises local melt temperature readings due to emissivity effects; infrared sensors should be calibrated against immersion thermocouple readings. A gear pump between the screw tip and die is used to reduce pressure pulsation below ±0.5 MPa, which directly affects tube-wall concentricity. Annular die land length for semi-flexible polyamide 12 is typically set at 10 to 20 times the die gap to allow molecular orientation to relax; excessive land length increases backpressure and polymer stagnation. Downstream calibration uses a water-ring or plate calibrator at 20 °C to 40 °C; lower temperatures improve roundness but may induce residual stress. The grade is susceptible to melt fracture at shear rates above approximately 1000 s⁻¹ in smaller die gaps; when shark skin appears, the remedy is to increase melt temperature within the stabilised range or widen the die gap rather than raise screw speed alone. A representative extruder barrel profile from feed to metering is 200 °C, 220 °C, 235 °C, 245 °C, 250 °C; the die head is held at 240 °C to 250 °C. Residence time at melt temperature should not exceed 10 min, and purging with a stable polyamide 12 purge compound is required when changing from a colour concentrate or from another base resin.

    When the Grade Replaces Unplasticized Vestamid L2140 in Coiled Multi-Layer Air-Brake Lines

    Selection of Vestamid L2124 sw 9.7507 over an unplasticized polyamide 12 such as Vestamid L2140 is generally driven by the need for lower flexural modulus and higher elongation in coiled air-brake tubing without adopting an external plasticizer. The heat-stabilisation package of L2124 provides improved melt stability for thin-wall extrusion; L2140, by contrast, is a higher-viscosity grade suited to thicker-wall tubes or profiles requiring higher melt strength. In multi-layer air-brake coils conforming to SAE J844, the inner layer may be specified in a semi-flexible polyamide 12 such as L2124 to reduce coil spring-back, while the outer layer is selected for abrasion and UV stabilisation. When the substitution is made, the processing window narrows: the semi-flexible grade can exhibit higher die swell and lower melt strength than unplasticized L2140, so the calibrator gap must be re-sized. Published data for this specific configuration is limited, and a production trial is necessary to verify ovality, burst pressure, and adhesion with tie layers. Differences in pigment dispersion between natural and black grades also affect online bubble-point testing in monolayer tube; the black colour recipe 9.7507 should be qualified for pinhole detection via immersion water bath at 0.5 MPa to 1.0 MPa according to the final tube specification.

    In continuous contact with diesel fuel, sour gas condensate, and zinc chloride road salt solutions at temperatures above 60 °C, polyamide 12 can undergo environmental stress cracking. Testing according to ISO 22088-3 or ASTM D1693 should be performed on finished tubing, not only on ISO test plaques. The grade is resistant to aliphatic hydrocarbons, oils, and greases at normal automotive service temperatures; however, strong inorganic acids, phenols, and concentrated formic acid dissolve or severely attack polyamide 12. Brake fluids and glycol-based coolants require compatibility testing under pressure and temperature because polyamide 12 can soften at elevated temperature in polar fluids. Moisture absorption of polyamide 12 is lower than that of PA6 or PA66, which reduces dimensional change and hydraulic swell in air-brake lines; ASTM D570 and ISO 62 data are used for comparative moisture uptake. The material is not suitable for continuous hot-water service above 80 °C unless oxidative stabilisation and hydrolysis resistance are validated in the specific fluid. In applications involving UV exposure, the carbon black in the sw 9.7507 recipe provides opacity and retards photo-oxidation; tensile elongation after 1000 h of ISO 4892-2 xenon-arc exposure is the standard acceptance criterion, not colour change alone.

    Compliance documentation for Vestamid L2124 sw 9.7507 must address the grade’s position under REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU. The black pigment system is based on carbon black; heavy-metal content must be confirmed against the supplier lot documentation. For food-contact or potable-water applications, the grade is not automatically approved unless the specific article meets FDA 21 CFR 177.1500, EU Regulation (EU) No 10/2011, or NSF/ANSI 61 after extraction testing. The product is delivered as a technical polymer for industrial extrusion; it is not a medical-grade polymer unless the lot has been validated against ISO 10993-1 for the finished device. Processing aids, if any, must be reviewed for their regulatory status under the target market and final application temperature.

    Regulatory or technical standardAreaVerification focus
    REACH (EC) No 1907/2006Substance registration and SVHC screeningSupplier declaration
    RoHS Directive 2011/65/EUAnnex II substance limitsXRF screening and lot documentation
    FDA 21 CFR 177.1500Polyamide food-contact articlesSpecific grade listing and extraction testing
    ISO 291Conditioning atmosphere23 °C/50 % RH
    ISO 4892-2Accelerated UV agingElongation retention after 1000 h
    SAE J844Air brake tubingBurst, cold impact, rigidity
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