Продукты

Bada BADAMID PA12 FM-Z3 natural S3 PA12, Dry

    • Название продукта: Bada BADAMID PA12 FM-Z3 natural S3 PA12, Dry
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
    • Запрос цены: admin@ascent-chem.com
    • Производитель: Ascent Petrochem Holdings Co., Limited
    • Свяжитесь сейчас
    Спецификации
    Код ТН ВЭД 360207

    Как аккредитованная Bada BADAMID PA12 FM-Z3 натуральная S3 PA12, сухая фабрика, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

    Упаковка и хранение
    Упаковка Packaged in sealed, moisture-proof 25 kg bags, BADAMID PA12 FM-Z3 natural S3 is dry nylon 12 pellets ready for processing.
    Погрузка контейнера (20-футовый контейнер) 20′ FCL loading of Bada BADAMID PA12 FM-Z3 natural S3 PA12, dry: sealed bags on pallets, secured, ventilated, protected from moisture.
    Доставка Ship as moisture-sensitive polyamide (PA12) granules in sealed, vapor-proof packaging to prevent water absorption. Keep dry and protected from humidity during transit. Avoid extreme heat or direct sunlight, store in a cool, ventilated area, and handle carefully to preserve material integrity. Standard non-hazardous shipping applies.
    Хранение Store Bada BADAMID PA12 FM-Z3 natural S3 in a cool, dry area, keeping the original sealed container to prevent moisture absorption. Recommended temperature range is 20–30°C. Use within six months of receipt; dry at 80°C for 4–8 hours before processing if exposure occurred. Avoid direct sunlight and humidity.
    Срок годности Shelf life is 12 months from production date when stored unopened in a cool, dry place.
    Применение Bada BADAMID PA12 FM-Z3 натуральный S3 PA12, сухой

    Multilayer automotive fuel vapor tubing produced to SAE J2260 and DIN 73379-1 positions an ethylene-vinyl alcohol barrier layer between two polyamide layers, with maleic anhydride-grafted tie resins separating the incompatible phases. The Bada BADAMID PA12 FM-Z3 natural S3 PA12, Dry grade is processed as the inner layer at 100% of the polyamide fraction and as the outer layer at 97.0–98.0 wt% with a 2.0–3.0 wt% carbon black masterbatch added for UV stress-cracking resistance. During five-layer coextrusion on a 45 mm single-screw extruder with L/D 30:1 and a spiral mandrel die, melt temperature is held at 225–245°C in the PA12 zones, while die temperature is limited to 245–255°C because thermo-oxidative chain scission accelerates above 260°C. In-line moisture analysis must confirm residual moisture at ≤0.10% by ISO 15512:2019 before startup, particularly when storage relative humidity exceeds 60%; the dry-supplied resin is pre-dried at 80°C for 4–8 h if the barrier bag has been opened. Vacuum sizing at 25–40°C with an ultrasonic wall-thickness gauge controls outer diameter and concentricity; post-extrusion annealing at 120°C for 2 h stabilizes crystallinity and reduces longitudinal shrinkage. Terminal products include onboard refueling vapor recovery lines, fuel vapor vent lines, and evaporative emission control tubing for gasoline and diesel passenger vehicles.

    Application segmentPrimary standardTest designationKey boundary condition
    Automotive fuel vapor linesSAE J2260Cold impact DIN 73379-1EVOH barrier layer required
    Truck air brake tubingSAE J844Ageing ISO 188Monolayer or spiral-reinforced
    Pneumatic control linesISO 14743Diameter ±0.08 mmPush-in fitting retention
    Fiber optic buffer tubesIEC 60794-1-22Shrinkage ≤0.5%Hot-water trough control
    Subsea hydraulic linersAPI 17EPermeation ISO 13628-5No recycled liner content
    Rail cable protection conduitsEN 45545-2Flame retardancy HL2/HL3Halogen-free FR masterbatch

    What Limits Stabilizer Masterbatch Addition in SAE J844 Air Brake Tube Extrusion?

    Truck and trailer pneumatic brake tubing extruded to SAE J844 Type A and ISO 7628-2 relies on PA12 for low moisture absorption, cold impact resistance, and compatibility with brass fittings. The base resin is dosed at 97.5–98.5 wt% with a copper-halide-based heat stabilizer masterbatch at 1.5–2.5 wt%; the upper limit is set by melt-elongation loss that produces parison sag before the vacuum sizing die, while the lower limit is governed by ISO 188 hot-air ageing at 100°C for 1,000 h. In monolayer tube extrusion on a grooved-feed single-screw extruder with L/D 24:1, melt temperature is maintained at 235–250°C and the vacuum calibration tank is held at 0.7–0.9 bar negative pressure. Batch-to-batch MVR variation greater than ±1.5 cm³/10 min measured per ISO 1133-1:2022 at 235°C/2.16 kg can force downstream wall-thickness correction; closed-loop systems using ±0.05 mm laser gauge feedback at haul-off speeds of 15–40 m/min are used to prevent diameter drift. The compound is not combined with free amine-based additives because these neutralize the copper-halide stabilizer and accelerate oxidative degradation. Terminal products include 6 mm, 8 mm, 10 mm, and 12 mm outer diameter air brake tubes for trucks, trailers, and buses.

    On high-cycle industrial pneumatic control systems, compressed-air dew point cycling generates repeated moisture adsorption and desorption in PA12 tube walls; dimensional stability under this load cycle is evaluated using ISO 14743 for push-in fitting retention and burst pressure after moisture conditioning. The BADAMID FM-Z3 natural S3 grade is processed neat or with 1.0–2.0 wt% color masterbatch; no additional plasticizer is introduced because the flexible S3 dry grade is formulated for kink resistance in small-diameter spiral tubing. Extrusion proceeds on a 30 mm single-screw extruder with L/D 26:1 and a vacuum sizing die, with outer diameter tolerance held at ±0.08 mm for 4–16 mm tubes by laser micrometer control at haul-off speed 25–80 m/min. Melt temperature is limited to 240–250°C; at temperatures above 260°C the flexible S3 modification begins to release volatile processing aids, causing surface roughness and die-lip deposit. The extrusion line includes a closed-loop cooling bath at 20–35°C and an inkjet marking station for lot traceability. Terminal products include coiled pneumatic control lines for robotic assembly cells, automated valve manifolds, and plant compressed-air distribution where tube lengths are cut to ISO 14743 tolerance classes.

    When Fiber Optic Buffer Tube Post-Extrusion Shrinkage Must Remain Below IEC 60794-1-22 Tolerance

    Loose tube fiber optic cables require a buffer tube that preserves excess fiber length while maintaining a circular inner lumen under thermal cycling. PA12 is processed at 95.0–98.0 wt% with a carbon black masterbatch at 2.0–5.0 wt% and an antioxidant masterbatch at 0.3–0.8 wt%; the carbon black loading is adjusted to meet the outer jacket UV stabilization target and to suppress photodegradation during outdoor storage. A pressure extrusion crosshead with a 20–25 mm screw and L/D 24:1 delivers melt pressure of 300–600 bar into the tube-forming die. The primary processing conflict is between rapid quenching, which raises post-extrusion shrinkage, and slow cooling, which lowers line speed and increases crystallinity gradients. The hot-water trough is therefore set to 40–60°C, followed by a cold-water trough at 15–20°C, to keep post-extrusion shrinkage below 0.5% after 24 h at 85°C. Diameter control on the hot tube is performed with a dual-axis laser micrometer with tolerance ±0.03 mm before the tube enters the take-up capstan. Relevant standards include IEC 60794-1-21 for optical and mechanical test methods, IEC 60794-1-22 for environmental tests, and RoHS 2011/65/EU Annex II for restricted substances. Published data for this exact BADAMID grade in high-fiber-count loose tubes is limited; line validation should include excess fiber length measurement after temperature cycling. Terminal products include 1.6–2.8 mm loose buffer tubes for duct, direct buried, riser, and indoor distribution cables with fiber counts from 2 to 24.

    PA12 Liner Permeation Ceilings for API 17E Methanol Hydraulic Control Hoses

    Subsea hydraulic flying leads and chemical injection lines designed to API 17E and ISO 13628-5 use PA12 inner liners where methanol-containing hydraulic fluids and seawater corrosion resistance dominate material selection. The liner is produced at 100% PA12; no regrind or recycled material is permitted in the wetted layer under NORSOK M-710 acceptance criteria. In a mandrel-supported liner extrusion process, a 38 mm single-screw extruder with a spiral flow die is operated at 230–250°C melt temperature, followed by vacuum sizing to a wall-thickness variation below ±0.05 mm. The liner is then overbraided with aramid or polyester yarn, and an outer cover is extruded separately from PA11 or polyurethane. Methanol permeation is tested on the finished hose at 60–70°C; because methanol diffusion through PA12 follows an Arrhenius-type increase with temperature, continuous exposure is limited to the pressure-temperature curve qualified by the hose manufacturer rather than by the dry resin thermal classification alone. The process boundary includes avoidance of melt temperatures above 260°C and exclusion of low-molecular-weight amide slip additives that can leach into methanol during long-term service. Terminal products include static and dynamic hydraulic flying leads, chemical injection hoses, and thermoplastic umbilical control lines.

    Corrugated cable protection conduits for railway rolling stock and off-highway engine compartments require a halogen-free flame retardant compound that can withstand continuous vibration and occasional stone impact without cracking. The BADAMID PA12 FM-Z3 natural S3 grade is blended at 85–92 wt% with a halogen-free nitrogen-phosphorus flame retardant masterbatch at 8–15 wt%; the exact loading is set by wall thickness and by EN 45545-2 Hazard Level HL2 or HL3 compliance testing on the final conduit, with mechanical impact classes verified to EN 61386-1. Extrusion is carried out on a continuous corrugator with a 45 mm single-screw extruder, traveling mold blocks, and melt temperature controlled at 235–245°C. Vacuum forming pressure is kept below 0.10 bar to prevent pinhole formation in corrugation valleys, and the mold blocks are conditioned to 80–100°C to maintain corrugation definition without blocking. The process is incompatible with conventional brominated flame retardants that degrade at PA12 processing temperatures and generate acidic byproducts; only halogen-free masterbatch systems are used. Finished conduit diameters range from 10 mm to 54 mm, supplied in slit, unslit, and pre-assembled harness configurations for railway underfloor cable looms, rolling stock control cubicles, and off-highway hydraulic hose bundling.

    Бесплатная цитата

    Конкурентоспособные Bada BADAMID PA12 FM-Z3 натуральный S3 PA12, сухие цены, которые соответствуют вашему бюджету - гибкие условия и индивидуальные котировки для каждого заказа.

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    Сертификация и соответствие требованиям
    Более подробное введение

    Bada BADAMID PA12 FM-Z3 natural S3 PA12, Dry is a natural-colour, dry-state polyamide 12 compound supplied under the BADAMID product designation. The model identifier FM-Z3 is supplier-specific; no compositional inference about the modifier package is made in the absence of a lot-specific datasheet. The suffix natural S3 denotes the colour state in the supplier’s colour code system, not a separate polymer grade. The term Dry indicates that the material is packaged with residual moisture controlled to ≤ 0.10 % as determined by ISO 15512:2019 unless the certificate of analysis states otherwise. Because PA12 is hygroscopic, the dry state refers to the as-packaged condition and not to an indefinite shelf-life after opening.

    The base polymer is a long-chain polyamide synthesized from laurolactam or ω-aminolauric acid; its repeating unit contains 12 carbon atoms between amide linkages. This structure produces a density close to 1.01 g/cm³, a melting point near 175–180 °C, and a water-saturation plateau of 1.5–2.0 % at 23 °C per ISO 62:2008. In comparison, PA6 reaches approximately 9.5–10.0 % water saturation under the same conditions, and PA66 reaches approximately 8.5 %. The lower amide-group density of PA12 limits the equilibrium moisture uptake and reduces moisture-induced dimensional change in humid service. Published property values for the FM-Z3 configuration specifically may differ from these PA12 family values; the supplier’s lot certificate remains the controlling source for acceptance limits.

    Where Does the FM-Z3 Designation Sit Within the PA12 Product Range?

    The FM-Z3 grade belongs to the BADAMID PA12 series, which is intended for injection moulding and extrusion where PA12 is selected for moisture resistance, low-temperature ductility, and chemical resistance. Because the FM-Z3 package is supplier-specific, direct mechanical comparison with unmodified PA12 requires a lot-specific datasheet. However, the dry natural S3 PA12 base typically occupies the lower end of the polyamide modulus range. Representative dry-state PA12 properties from published ISO test data are shown in Table 1; these values are not lot-specific guarantees.

    Property Test method Typical dry PA12 range Notes
    Density ISO 1183-1:2019 1.01 g/cm³ Natural colour, unfilled
    Tensile modulus ISO 527-1/-2 1400–1600 MPa Test speed 1 mm/min
    Yield stress ISO 527-1/-2 45–50 MPa Test speed 50 mm/min
    Nominal strain at break ISO 527-1/-2 >50 % Unfilled, dry as moulded
    Charpy notched impact ISO 179-1/1eA 4–6 kJ/m² 23 °C, dry
    Melting temperature ISO 11357-3:2018 175–180 °C DSC, second heat
    Water absorption, saturation ISO 62:2008 1.5–2.0 % 23 °C, immersion

    The tensile modulus of dry PA12 is typically 1400–1600 MPa, which is below the 2900–3200 MPa range of dry PA66. This lower stiffness is accompanied by a higher strain at break and lower water affinity, which makes PA12 useful for snap-fits, clips, and housings that must tolerate repeated deflection and humid environments. The notched impact of dry PA12 at 23 °C is typically 4–6 kJ/m². Generic PA12 data show better retention of ductility at sub-zero temperatures than many short-chain polyamides, although the exact value for FM-Z3 should be confirmed by ISO 179-1:2010 on the actual batch.

    Non-isothermal differential scanning calorimetry at 10 °C/min cooling typically places the PA12 crystallisation peak near 150–160 °C. Rapid cooling in thin walls suppresses crystallinity and reduces modulus; slower cooling in thick sections increases crystallinity, stabilises dimensions, and raises density slightly. The melt volume-flow rate of unfilled PA12 is commonly 10–30 cm³/10 min at 235 °C and 2.16 kg according to ISO 1133-1:2022. The FM-Z3 value must be read from the lot datasheet because supplier-specific stabilisation and lubricant packages can shift melt viscosity without altering the base polymer density.

    Drying and Melt Preparation Limits for Natural S3 Feedstock

    Before melt processing, the resin must be dried to ≤ 0.10 % residual moisture. A desiccant dryer with a dew point of ≤ -30 °C and inlet air temperature of 80 °C is standard. Drying time of 4–12 h is typical for material initially below 0.20 % moisture; material exposed to ambient air above 60 % relative humidity for more than 1 h should be re-dried. Hot-air-only drying without desiccant is not recommended because dew-point control is required to achieve the target moisture in open-loop systems. The dry-state packaging does not remove the need for machine-side drying after bag opening.

    Condition Typical range Equipment or reference
    Drying temperature 80 °C Desiccant dryer, dew point ≤ -30 °C
    Drying time 4–12 h Target residual moisture ≤ 0.10 % per ISO 15512:2019
    Melt temperature 220–250 °C Injection moulding and extrusion
    Mould temperature 40–60 °C Unfilled PA12; 80 °C for maximum crystallinity
    Melt volume-flow rate, unfilled PA12 10–30 cm³/10 min ISO 1133-1:2022, 235 °C, 2.16 kg
    Hold pressure 40–70 MPa Hydraulic injection moulding
    Back pressure 0.5–1.5 MPa Screw diameter 25–60 mm
    Peripheral screw speed 15–25 m/min General-purpose screw, L/D 18–22

    For injection moulding, barrel temperature profiles from feed to nozzle are typically 220 °C, 230 °C, 240 °C, and 240–250 °C. The melt temperature should not exceed 260 °C; residence time above 10 min at the upper setpoint can produce yellowing and a measurable loss of Charpy notched impact due to thermal oxidative degradation. Mould temperatures between 40 °C and 60 °C produce satisfactory crystallinity for unfilled PA12. A mould temperature of 80 °C improves surface replication and post-mould dimensional stability but extends cooling time. For hot-runner moulds, thermal uniformity in the manifold should be maintained within ± 5 °C to avoid local solidification or degradation; published data for this specific FM-Z3 configuration in heated-tip systems is limited.

    For profile or tubing extrusion, a general-purpose screw with L/D 18–22 and compression ratio 2.0:1–2.5:1 is adequate. Melt temperature 220–250 °C, die temperature 230–250 °C, and vacuum calibration are typical. No high-shear dispersion is required because the natural PA12 base does not contain glass fibre or mineral filler. The use of barrier screws or intensive mixing sections may increase shear heating and should be avoided unless validated for this grade. Pre-blending of colour masterbatch or additives is performed with a low-shear tumble mixer.

    When Fuel or Aqueous Chloride Service Is Specified, Chemical Resistance Boundaries Apply

    PA12 is used in automotive fuel lines, compressed-air tubing, cable jackets, and fluid connectors because of resistance to aliphatic and aromatic hydrocarbons, diesel fuel, lubricating oils, refrigerants, and alkaline salt solutions. Immersion testing under ISO 175:2010 shows limited property change in these media at room temperature. The grade is not resistant to concentrated mineral acids, formic acid, phenols, cresols, or strong oxidizing agents. Exposure to zinc chloride solutions above 50 °C may induce environmental stress cracking in PA12; parts under internal pressure or moulded-in stress are more sensitive. Published data for the FM-Z3 package under specific fuel blends containing ethanol or methanol above 15 % is limited; validation with the actual medium and temperature is required. Prolonged contact with strong bases at elevated temperature can hydrolyze the amide linkage, reducing molecular weight and tensile strength.

    In direct comparison with PA6 and PA66, PA12 FM-Z3 natural S3 dry grade offers a lower density and lower equilibrium moisture content but also a lower tensile modulus and strength. This trade-off is relevant for parts that must maintain geometry in humid or wet environments. A PA6 component may absorb 2.5–3.0 % moisture at 50 % relative humidity, while PA12 absorbs approximately 0.7–0.8 %. The resulting dimensional change is smaller for PA12, which is useful in precision clips and housings. However, when higher stiffness is required, PA66 or glass-filled PA12 is usually selected. The FM-Z3 grade is therefore not a direct substitute for high-modulus PA66 in load-bearing structural ribs.

    Compared with PA11, PA12 has a slightly lower melting temperature and broadly similar water absorption. PA11 is often bio-based, whereas commercial PA12 grades are predominantly petrochemical. The choice between PA12 and PA11 in flexible tubing or cable protection is usually driven by supplier-specific approvals, processing consistency, and cost rather than by large differences in moisture resistance. Compared with polyoxymethylene, PA12 has lower modulus and lower creep resistance at room temperature but is less prone to sharp property loss in acidic hydrolysis conditions; material selection should follow the actual chemical environment and load history.

    Application records for PA12 dry natural grades include pneumatic tubing, cable sheathing, automotive fuel and vent lines, industrial hoses, snap-fit clips, gear wheels, and conveyor wear strips. Natural S3 colour is suitable where pigmentation is not required or where colour masterbatch is added at processing. The dry form is preferred for direct extrusion because residual moisture is already low, but it does not eliminate the need for pre-drying after bag opening. In medical or food-contact applications, the natural colour should not be interpreted as a regulatory approval; compliance with EU Regulation 10/2011, FDA 21 CFR 177.1500, or ISO 10993-1:2018 must be established for the specific grade and final article.

    The unpigmented natural state of this grade means that UV stabilisation is not inherent. Outdoor exposure can lead to surface oxidation and embrittlement unless carbon black or a UV stabiliser is added. Lot-to-lot variation in melt viscosity and colour should be monitored by incoming quality control using ISO 1133-1:2022 melt flow testing and spectrophotometric colour measurement. Mould shrinkage values for unfilled PA12 typically lie between 0.7 % and 1.2 % parallel to flow and 0.8 % to 1.3 % transverse according to ISO 294-4:2018; actual values depend on mould temperature and wall thickness. Compliance statements for RoHS Directive 2011/65/EU and REACH Regulation EC 1907/2006 must be confirmed against the supplier’s lot-specific declarations. Unpigmented natural PA12 is not a declaration of food-contact, medical, or drinking-water suitability.

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