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EMS-Grivory Grilamid XE 4076 black 9992 PA12-I

    • Название продукта: EMS-Grivory Grilamid XE 4076 black 9992 PA12-I
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
    • Запрос цены: admin@ascent-chem.com
    • Производитель: Ascent Petrochem Holdings Co., Limited
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    Спецификации
    Код ТН ВЭД 636639

    Как аккредитованный завод EMS-Grivory Grilamid XE 4076 black 9992 PA12-I, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

    Упаковка и хранение
    Упаковка Grilamid XE 4076 black 9992 PA12-I is supplied as granules in a sealed 25 kg moisture-resistant bag, ready for processing.
    Погрузка контейнера (20-футовый контейнер) Loaded as 20′ FCL: 25 kg bags on pallets, shrink-wrapped, ensuring secure transport of Grilamid XE 4076 PA12-I.
    Доставка EMS-Grivory Grilamid XE 4076 black 9992 is a PA12-I thermoplastic supplied as moisture-resistant pellets. Ship in sealed, dry containers to prevent moisture absorption. Keep away from heat, sparks, and incompatible oxidizing agents. Standard non-hazardous freight applies, though avoid excessive pressure or puncture. Store in a cool, ventilated area.
    Хранение Store Grilamid XE 4076 black 9992 in its original, unopened packaging in a cool, dry, well-ventilated area. Keep tightly sealed to prevent moisture absorption, and protect from direct sunlight, UV radiation, and heat sources. Ideal storage temperature is below 30°C. Under these conditions, shelf life is typically two years.
    Срок годности Grilamid XE 4076 PA12-I has a 2-year shelf life if kept sealed, dry, and away from heat and UV in original packaging.
    Применение EMS-Grivory Grilamid XE 4076 черный 9992 PA12-I

    In heavy-duty truck pneumatic braking circuits, XE 4076 black 9992 is processed into coil-formed harness conduit for service temperatures down to −40 °C. The PA12-I modification replaces unmodified PA12 where notch sensitivity under stone strike and clamp abrasion has produced field failures in cold-climate fleet corridors. Extrusion on a single-screw barrier screw with L/D 30:1 is standard; barrel zones are maintained from 200 °C at the feed throat to 245 °C in the metering section, with die head temperature held at 235 °C. Desiccant drying at 80 °C for 4 h to 6 h reduces residual moisture to below 0.10 wt%, and the dried granules are conveyed by dried-air lines to avoid rehydration above 60% RH. Wall thickness is controlled relative to outside diameter at a ratio between 0.10:1 and 0.14:1; for a typical 12 mm outside diameter tube, this yields 1.2 mm to 1.6 mm walls. Vacuum sizing at −0.2 bar to −0.5 bar and haul-off at 15 m/min to 35 m/min hold ovality below 0.15 mm. Regrind from edge trim is limited to 20 wt% of dried scrap in protective conduit but is excluded from safety-critical brake lines. Terminal products include tractor-to-trailer air brake spiral assemblies, cab tilt cylinder supply tubes, and suspension leveling valve lines. When ISO 7628-1:2015 is invoked, burst pressure, cold-impact, and heat-aging evidence is retained for lot traceability. DIN 74324 dimensional classes are used for fitting interchange. Processing limits observed on line include melt fracture below 210 °C and die swell acceleration above 250 °C; head pressure is therefore held between 100 bar and 180 bar by screw speed adjustment within 30 rpm to 60 rpm.

    Processing variableTube extrusionInjection molding
    Desiccant drying80 °C, 4 h to 6 h to <0.10 wt% moisture80 °C, 4 h to 6 h to <0.10 wt% moisture
    Melt temperature window210 °C to 250 °C220 °C to 250 °C
    Tool temperatureCooling water 10 °C to 20 °C; sizing sleeve 15 °C to 25 °CMold 40 °C to 80 °C
    Pressure limitsHead pressure 100 bar to 180 barHold pressure 60 MPa to 90 MPa
    Screw speed / back pressure30 rpm to 60 rpmScrew speed 60 rpm to 120 rpm; back pressure 5 bar to 15 bar

    Why Does High-Viscosity PA12-I Shift Melt Pressure in Corrugated Electrical Conduit Tooling?

    Flexible cable protection conduit in rail and machine-tool installations is corrugated from XE 4076 black 9992 when low-temperature impact and abrasion tolerance are specified. The melt-pressure signature diverges from unmodified PA12 because the impact-modified high-viscosity matrix retains higher zero-shear viscosity; this may raise head pressure by 15% to 30% at equivalent screw speed in grooved-feed extruders with L/D 30:1. The corrugator is set to a blow ratio between 1.8:1 and 2.4:1, while the corrugation depth-to-root-wall thickness ratio is held between 1.5:1 and 2.0:1 to maintain crush resistance without splitting at the root. Melt temperature is clamped between 220 °C and 245 °C; below 220 °C the elastomeric phase can generate flow segregation, and above 245 °C black 9992 carbon black dispersion may produce surface pitting. The die lip gap is set to 0.5 mm to 0.8 mm, with mold vacuum at −0.3 bar to −0.7 bar in the corrugator blocks. Terminal products include underfloor rail cable conduits and heavy machine-tool drag-chain protection. Compliance follows EN 61386-1:2008 for conduit systems, and when EN 45545-2:2020 is required, full-system testing is performed because published data for this specific black PA12-I corrugated geometry is limited. Regrind ratios are held at or below 15 wt% to limit gel accumulation at the screen pack, which is configured with 60/80/120 mesh layers. Batch-to-batch variation in melt flow is controlled by accepting lots only with melt-volume-flow rate measured under ISO 1133-1:2022 within supplier-agreed limits. On-line ultrasonic wall monitoring detects thinning at corrugation roots below 0.20 mm and triggers vacuum trim adjustment.

    For factory automation air distribution blocks and tube-to-port adapters, pneumatic push-in fitting bodies are molded from XE 4076 black 9992. In injection molding, the material is plasticated at 225 °C to 250 °C with mold temperature 60 °C to 80 °C. The gate is sized to a gate-to-wall-thickness ratio between 0.6:1 and 0.8:1 to prevent jetting; edge gates are preferred over tunnel gates to reduce shear heating of the impact modifier. Hold pressure is set from 60 MPa to 90 MPa until gate freeze, with decompression after plasticating of 3 mm to 5 mm to avoid drool at the nozzle. The screw cushion is maintained at 3 mm to 5 mm. Tooling uses P20 steel with cooling circuits to maintain cavity temperature uniformity within ±5 °C. Terminal products include release rings, collet housings, and end caps for push-in connectors. Dimensional acceptance follows ISO 14743:2004 or the buyer-specified equivalent for pneumatic fittings. The black 9992 color package based on carbon black is documented under RoHS Directive 2011/65/EU by the fabricator, and the resin does not intentionally contain halogenated flame retardants. In production, cracking at insertion barbs is observed when mold temperature falls below 50 °C, and sticking is observed above 85 °C; this boundary defines the processing window. Parts are conditioned at 23 °C and 50% RH for 24 h before insertion-force testing because dry-as-molded PA12 can bind on metal collet teeth. Batch-to-batch viscosity differences are managed by monitoring melt-volume-flow rate under ISO 1133-1:2022 and adjusting injection speed between 30 mm/s and 60 mm/s.

    Battery Pack Interconnection Clip Geometries Molded from XE 4076 black 9992

    In electric vehicle battery pack wiring systems, impact-modified PA12-I is used for snap-fit clips that retain voltage-sense harnesses and busbar cables. The material is dried to 0.08 wt% moisture or lower and molded in a hot-runner multi-cavity tool with valve gates. Melt temperature is limited to 240 °C to 250 °C because black 9992 disperses uniformly only when the melt is fully wetted. Mold temperature is set at 70 °C to 80 °C. Snap-fit return-arm wall thickness is held between 1.0 mm and 1.6 mm, with a length-to-thickness ratio of 3:1 to 5:1 to keep flexural strain within the grade’s ductile range. Gate placement is located away from the neutral axis to prevent stress whitening at the snap-fit root. Terminal products include module-to-busbar retention clips, cable cleats, and edge-protection brackets. Electrical insulation is evaluated according to IEC 62631-3-1:2016 for volume resistivity, although published data for this specific configuration is limited; converter-level testing is therefore required for clearance and creepage distances. Flammability is typically assessed at the final part level because PA12-I without flame retardants is classified under UL 94 HB at 0.8 mm thickness. RoHS Directive 2011/65/EU and REACH Candidate List screenings are part of batch documentation. To avoid warpage in clip arrays, the tool uses sequential valve gating and packing pressure decay from 80 MPa to 40 MPa over 2 s. Production scrap is limited to 10 wt% regrind in non-safety retention parts. In-process checks use a go/no-go insertion force fixture calibrated to 15 N to 45 N because climatic humidity shifts PA12 dimensions by less than 0.3% but enough to alter fit.

    Quick-release pneumatic coupling sockets are molded from XE 4076 black 9992 where repeated snap engagement at sub-zero warehouse temperatures causes thread boss cracking in POM or unmodified PA12 parts. Molding uses a two-plate tool with a tunnel gate; drying follows the same 80 °C schedule. The thread boss outer-to-inner diameter ratio is maintained at 1.4:1 to 1.6:1. Terminal product is the socket body in compressed-air quick-release couplings. Dimensional fits follow ISO 6150:2018 for pneumatic quick-action couplings. Compliance is limited to RoHS Directive 2011/65/EU and the fabricator’s standard industrial substance list; no food-contact or medical claim is implied. Batch-to-batch lot acceptance includes an impact test at −30 °C using ISO 179-1/1eA notched Charpy, with ductile failure required. If mold temperature drops below 50 °C, the thread root develops stress cracks after insertion torque, and this is controlled by raising tool temperature to 65 °C before restart. Cold runner sprue and runner regrind is not blended into socket bodies because the thread boss is a high-stress area, and minor viscosity shifts affect torque retention.

    When Fuel Vapor Return Lines Are Coextruded with EVOH Barrier Layers

    In gasoline and flex-fuel passenger-vehicle vapor management, multi-layer return lines can use XE 4076 black 9992 as the outer layer where PA12 is specified for low-temperature mechanical behavior and the EVOH core provides hydrocarbon barrier. Coextrusion is conducted on a multi-layer line with a spiral mandrel die; the outer PA12-I layer occupies 45 wt% to 60 wt% of total wall, the EVOH barrier 5 wt% to 10 wt%, and the tie layers 5 wt% to 10 wt%, with the balance an inner PA12 conductive or neat layer depending on fuel system anti-static requirements. Melt temperatures are set at 210 °C for EVOH, 235 °C for tie resin, and 240 °C for XE 4076 black 9992. Interfacial instability occurs when the outer layer viscosity falls below the EVOH layer; the high-viscosity PA12-I modification helps stabilize the interface at a line speed between 10 m/min and 30 m/min. Terminal products include low-permeation vapor return lines and tank vent lines for gasoline and flex-fuel passenger vehicles. Permeation compliance is evaluated under SAE J2260 for fuel lines, requiring total hydrocarbon emission below the fleet-average limits adopted by CARB LEV II and Euro 6 evaporation standards; the barrier layer, not the PA12-I outer layer, is the main control parameter. Dimensional tolerances follow SAE J2045 for automotive tubing. Regrind from coextruded trim is not fed into the barrier layer and is limited to 15 wt% in the outer layer only when sorted by layer. Published data for this specific grade in SAE J2260 multi-layer constructions is limited; fuel-system suppliers therefore perform subassembly permeation testing on each lot. The black 9992 outer layer is UV-stabilized in the pigment package, but underbody exposure still requires additional evaluation if the line is mounted without shielding.

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    Сертификация и соответствие требованиям
    Более подробное введение
    EMS-Grivory Grilamid XE 4076 black 9992 PA12-I is an unfilled impact-modified polyamide 12 compound supplied in the black 9992 colour code. The PA12-I designation follows ISO 1043-1 conventions: PA12 identifies the base polymer and I indicates impact modification. The material is a two-phase system in which a dispersed elastomer phase is present in a semicrystalline PA12 matrix. The black 9992 reference is a supplier-specific colour designation, customarily associated with carbon-black pigmentation. Published supplier data place the dry as-moulded density at 1.01 g/cm³ when tested to ISO 1183-1. The grade is normally converted by injection moulding and tube or profile extrusion. Table 1 summarises the dry as-moulded mechanical and thermal property set used to distinguish the material from unmodified PA12, glass-reinforced PA12, and PA6 impact-modified compounds.
    PropertyTest standardDry as-moulded typical valueUnit
    DensityISO 1183-11.01g/cm³
    Melt volume-flow rate at 275°C/5 kgISO 1133-115–25cm³/10 min
    Tensile modulusISO 527-1/-2350MPa
    Tensile stress at yieldISO 527-1/-216MPa
    Nominal strain at breakISO 527-1/-2>50%
    Charpy notched impact strength at 23°CISO 179-1/1eA25kJ/m²
    Charpy notched impact strength at −30°CISO 179-1/1eA9kJ/m²
    Melting temperature, DSCISO 11357-3175°C
    Vicat softening temperature A/50ISO 306138°C
    Water absorption, saturation at 23°CISO 621.2%

    Values are typical for dry as-moulded specimens and are not specification limits. Conditioned values after moisture saturation differ; the supplier’s conditioned dataset should be requested for design at room-temperature humid conditions.

    Mechanical and thermal thresholds shift with absorbed moisture

    Under ISO 62 water absorption at saturation is approximately 1.2%. The PA12 backbone absorbs less moisture than PA6 or PA66 because amide groups are separated by a long aliphatic repeat unit. This lower equilibrium moisture reduces the dry-to-conditioned modulus shift relative to short-chain polyamides. Nevertheless, the impact-modified grade still undergoes property changes when wet: tensile modulus falls from the dry typical value of 350 MPa toward 190–250 MPa, and notched Charpy values at 23°C often move from 25 kJ/m² to no-break behaviour. The transition is reversible after re-drying; however, regrind stored at more than 60% RH must be re-dried to below 0.10% residual moisture before processing. Melt hydrolysis caused by residual moisture reduces molecular weight and creates surface roughness in extruded tube. On a single-screw extruder with a grooved feed section and L/D 30 vented screw, the moisture-removal section is exhausted at approximately −200 mbar; if the vent flow is compromised, steam streaks appear at melt temperatures above 240°C.

    Before melt processing, the granulate is dried in a desiccant dryer at 80°C for 4–8 h, with a dew point below −30°C, until residual moisture is below 0.10%. Material exposed to ambient relative humidity above 60% RH or stored in open bins requires re-drying even if the original bag was sealed. In injection moulding, barrel profiles typically rise from 220°C at the feed zone to 260°C at the nozzle, with melt temperature held between 240°C and 270°C. Mould temperatures of 20–100°C are used; the lower end favours cycle-time reduction and the upper end improves crystallinity and dimensional stability. Injection speed is set to avoid gas traps in thick sections, and holding pressure is profiled because the unfilled impact-modified melt exhibits different compressibility than glass-filled PA12. On a twin-screw compounding line, specific mechanical energy input is lower than for glass-filled PA12, and screw elements that generate excessive shear should be avoided to preserve the elastomer particle size. For tube extrusion, melt temperatures of 230–250°C and vacuum calibration are typical, but the exact calibration vacuum depends on tube diameter and wall thickness. Coextrusion with PA12 tie layers or barrier layers is possible when the melt streams are kept within 10°C of one another. Published data for this specific configuration at line speeds above 100 m/min is limited, so lot-specific validation is required.

    What Distinguishes PA12-I from Unmodified PA12 and Glass-Reinforced Grades?

    Unmodified PA12 grades are available with higher dry tensile modulus and lower room-temperature notched impact. A standard PA12 extrusion grade may show a dry tensile modulus near 1,400 MPa, a yield stress near 40 MPa, and a notched Charpy impact at 23°C below 5 kJ/m² in dry articles. In the impact-modified PA12-I system, the elastomer phase reduces modulus to the 350 MPa typical range and raises impact to 25 kJ/m² at 23°C. Glass-fibre-reinforced PA12 grades, in contrast, increase dry tensile modulus to 3,000–6,000 MPa and reduce elongation at break below 5%, which is unfavourable for snap-fit geometries and cable conduits that must flex. The unfilled impact-modified grade also produces lower abrasion of adjacent polymer surfaces and better colour uniformity than black glass-filled compounds. Compared with PA11, this grade has a similar low-moisture paraffinic backbone but a lower melting temperature. Compared with PA612, the PA12 system generally provides lower density and, in impact-modified form, improved low-temperature toughness. These comparisons are material-class generalisations and must be checked against the specific grade’s datasheet for critical dimensions.

    The chemical resistance profile of this grade is governed primarily by the PA12 matrix. The material is resistant to aliphatic hydrocarbons, oils, greases, salt solutions, and diesel fuel. The paraffinic backbone provides better zinc chloride stress-cracking resistance than PA6, which is relevant for underhood connectors exposed to road salt. The impact-modifier phase reduces resistance to concentrated acids and polar solvents relative to unmodified PA12. The material is unsuitable for prolonged contact with concentrated sulfuric acid, nitric acid, chlorinated solvents, and high-peroxide environments. At temperatures above 60°C, continuous contact with hot water or glycol-water mixtures can accelerate hydrolysis, especially when the material was processed with residual moisture above 0.15%. Fuel blends containing methanol or ethanol above 15% by volume may increase permeability and should be evaluated by immersion testing to ISO 175 or SAE J2260. In monolayer PA12 tubing, fuel permeation is controlled by the amorphous fraction and the elastomer phase; the impact modifier tends to increase permeation relative to unmodified PA12 by a measurable but modest amount. Therefore, fuel lines with strict evaporative emission limits often use multilayer constructions with EVOH or fluoropolymer barrier layers. This grade serves as a flexible outer or inner layer rather than as the sole barrier layer. Published data for this specific black 9992 configuration in biodiesel blends is limited, and component validation to an OEM standard is required.

    When Black 9992 Pigmentation and Impact Modification Are Combined

    Black 9992 is the EMS colour code for the black-pigmented grade, customarily based on carbon black. The pigmentation is not solely cosmetic; it provides UV screening and improves weathering relative to natural or light-coloured PA12. Outdoor applications such as cable protection conduits, exterior fasteners, and pneumatic lines exposed under vehicle bodies use the black formulation. In natural PA12, UV radiation causes chain scission and surface chalking; the black pigment masks yellowing and reduces crack initiation during weathering cycles to ISO 4892-2. The impact-modified PA12-I phase remains the dominant source of low-temperature ductility; the black pigment does not raise modulus to the level of glass reinforcement. However, carbon black dispersion affects notched impact and pressure rise during extrusion. Poor dispersion can produce black specks in thin-walled tube and local variations in impact properties. Production experience on injection-moulded cable clips shows that nozzle temperatures below 240°C increase cavity-to-cavity variation and short shots in thin sections, while nozzle temperatures above 270°C accelerate pigment agglomeration and generate brown streaks. The black 9992 grade is therefore processed in a narrow thermal window with residence times limited to the supplier’s recommended maximum.

    Reference standard or requirementTypical application or test relevance
    ISO 1183-1Density classification for unfilled impact-modified PA12
    ISO 527-1/-2Tensile modulus, yield stress, and elongation data
    ISO 179-1/1eANotched Charpy impact at 23°C and −30°C
    ISO 306/A50Vicat softening temperature
    ISO 11357-3Melting temperature by differential scanning calorimetry
    ISO 1133-1Melt volume-flow rate at 275°C/5 kg
    DIN 73378Polyamide tubing for automotive systems
    SAE J844Air brake tubing
    UL 94 HBFlame class at 1.6 mm
    RoHS 2011/65/EURestricted substances in electrical and electronic equipment
    REACH SVHCCandidate-list substance declaration

    Specifications for this grade in fuel-tube and air-brake applications commonly require lot-specific tensile and impact evidence, dimensional stability after annealing, and absence of surface defects in extrusion. The material is not recommended for continuous service above 100°C because oxidative aging of the impact-modifier phase reduces low-temperature toughness. In applications requiring continuous exposure to hot glycol-water mixtures, alternative heat-stabilized or unmodified PA12 grades may be more suitable.

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