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EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12, Dry

    • Product Name: EMS-Grivory Grilamid L 25 W 40 HL X 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 200300
    Density 1.06 g/cm³
    Water Absorption 24h 23 C 1.5%
    Melting Point Dsc 168 °C
    Glass Transition Temperature -30 °C
    Tensile Strength Yield Dry 45 MPa
    Elongation At Break Dry 300%
    Tensile Modulus Dry 1100 MPa
    Flexural Modulus Dry 1100 MPa
    Charpy Impact Strength 23 C Dry No Break
    Charpy Impact Strength 30 C Dry 60 kJ/m²
    Heat Deflection Temperature 1 80 Mpa 45 °C
    Heat Deflection Temperature 0 45 Mpa 120 °C

    As an accredited EMS-Grivory Grilamid L 25 W 40 HL X 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 25 kg sealed polyethylene-lined bags. Keep container tightly closed to prevent moisture absorption before processing.
    Container Loading (20′ FCL) Container Loading (20′ FCL): EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12, Dry packed securely in a 20-foot container for safe transport.
    Shipping EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12 (dry) ships in sealed, moisture-barrier packaging to prevent hydrolysis. Store below 50°C, away from humidity. Transport at ambient conditions, avoid excessive heat and impact. Ensure containers remain upright and protected during transit.
    Storage Store Grilamid L 25 W 40 HL X in its original, unopened packaging in a cool, dry environment. Keep sealed to prevent moisture absorption, which can affect processing. Avoid direct sunlight, heat sources, and high humidity. Recommended storage temperature is below 30°C. Under these conditions, shelf life is typically two years from delivery.
    Shelf Life Shelf life is typically 2–3 years when stored dry, sealed, and protected from moisture, heat, and UV.
    Application of EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12, Dry

    Where injection molders process 40% glass-fiber-reinforced polyamide 12 for fuel quick connectors and vapor recovery system components, the dry-as-supplied condition of EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12 is the primary processing control because residual moisture above 0.10 wt% induces hydrolysis during plastication and produces weld-line embrittlement at snap-fit undercuts. The compound is normally run neat without additional resin letdown; where laser-marking contrast is required, a PA12-based carbon black masterbatch is metered at 0.5–1.5 wt%, and clean sprues and runners may be recycled up to 20 wt% only in non-fuel-immersion regions after dust removal and drying. Compliance for this sector is anchored to SAE J2044 quick-connector specifications, SAE J2260 nonmetallic fuel system tubing practice, ASTM D543-21 chemical resistance practice, and ISO 527-1/-2 tensile property verification. Production lines run the dried granulate from a desiccant hopper dryer set at 80°C with a dew point of -30°C or lower, through an injection molding machine with a 22:1 L/D barrier screw and a spring-loaded ring non-return valve; nozzle temperature is held between 250°C and 270°C, mold temperature at 60–80°C, and post-mold annealing at 100°C for 2 h stabilizes snap-fit ring geometry before assembly. Terminal finished parts include quick-connector bodies, fuel tank vent port adapters, onboard refueling vapor recovery check-valve bodies, emission canister purge valve mounting flanges, and fuel vapor line brackets.

    Application sectorReference standardRequired property or assessmentTest condition or limitation
    Fuel quick connectorsSAE J2044, SAE J2260, ASTM D543-21Fuel immersion stability, pull-force retentionTest fluid and duration per OEM specification; ASTM D543-21 governs practice
    Pneumatic valve manifoldsISO 527-1/-2, ISO 294-1, ISO 1183Tensile modulus, shrinkage, density23°C, 50% RH, as-molded condition
    Cable glands and enclosuresIEC 60079-0:2017, IEC 62444:2013, IEC 60695-2-11Mechanical integrity, glow-wire resistanceTemperature class and equipment protection level specified by end application
    Potable water contactNSF/ANSI/CAN 61, AS/NZS 4020:2018Migration, sensory effect, hydrolysis resistanceCompound-specific certification required; generic PA12 approval is insufficient
    Medical device housingsISO 10993-1:2018, USP <87>, USP <88>Cytotoxicity, systemic reactivityExternal device only; no implant claim
    Rail cable clipsEN 45545-2:2020, EN 61373:2010, NFPA 130Smoke density, toxic gas release, vibrationFinal part testing required on flame-retardant-modified configuration

    What Limits Gate-Freeze Pressure in Pneumatic Manifold Molding with 40% Glass-Fiber PA12?

    Compressed-air distribution blocks and pneumatic valve manifolds use the low equilibrium moisture uptake of 40% glass-fiber PA12 to retain orifice dimensions through seasonal humidity cycles, a condition in which PA66 would shift bore roundness and alter flow coefficients. The formulation addition ratio is maintained neat because the HL stabilization package already contains processing lubricant; external lubricant masterbatches are avoided due to plate-out on hot-runner valve pins and inconsistent gate sealing. If static dissipation is specified for ATEX dust-zone ancillary equipment, a conductive carbon black masterbatch is added at 8–12 wt%, and the resulting loss of notched impact strength under ISO 179-1/1eA must be incorporated into the manifold pressure-rating calculation. Processing is performed on hydraulic injection molding machines with clamp force above 1000 kN for multi-cavity manifolds, using a screw with 22:1 to 25:1 L/D and a bimetallic barrel suitable for abrasion from 40% glass fiber; mold temperature is held at 70–90°C to reduce exposed glass fiber at weld lines. Gate-freeze time is monitored by runner pressure decay, and premature freeze is observed in runner diameters below 6 mm when flow length to wall thickness ratios exceed 150:1, producing short shots despite adequate barrel temperature. Terminal finished parts include stackable pneumatic manifolds, filter-regulator-lubricator housings, quick-exhaust valve bodies, and pneumatic cylinder end caps aligned with ISO 15552 envelope dimensions.

    Cable Gland and IEC 60079-0 Enclosure Strain Relief Elements

    Where cable glands must retain clamping force after temperature cycling from -40°C to 100°C, 40% glass-fiber PA12 is selected over unreinforced PA6 because moisture-induced relaxation of clamping shoulders is lower after prolonged humidity exposure. The formulation addition ratio for Ex e gland bodies is neat polymer; a PA12-based UV-stabilized masterbatch may be added at 1.0–2.0 wt% for outdoor installations evaluated under IEC 60068-2-5, but the masterbatch carrier must not shift glow-wire ignition behavior measured under IEC 60695-2-11. Compliance for hazardous area cable glands is evaluated under IEC 60079-0:2017 general requirements for explosion-protected equipment and IEC 62444:2013 cable gland construction and test requirements, with enclosure ingress protection verified under IEC 60529 for IP66 or IP68 ratings as applicable. Production uses multi-cavity hot-runner molds with sequential valve-gate control and mold temperature at 70–85°C; threaded inserts are preheated to 120°C before placement to avoid localized shrinkage stress around brass inserts. Terminal finished parts include hazardous-area cable glands, junction box covers, terminal enclosure frames, and explosion-protected breather vent bodies where metal replacement is constrained by weight and corrosion resistance.

    When Condensate Cycle Stress in HVAC Actuator Couplings Reaches 85°C Under Continuous Load

    Heating, ventilation, and air-conditioning actuator couplings and damper gears use heat-stabilized 40% glass-filled PA12 because short-term temperature peaks in air handling units reach 85°C while ambient relative humidity fluctuates between 20% and 90%, conditions that distort unfilled PA66 gear tooth profiles and alter backlash. Formulation addition ratio is neat processing unless low-friction performance is specified, in which case a PTFE powder masterbatch is added at 5–10 wt%; the resulting reduction in tensile modulus under ISO 527-2 and weld-line cohesion must be re-validated on the actual gear geometry because PTFE addition can create low-strength knit lines at tooth roots. The production process uses a 25:1 L/D screw with a shut-off nozzle, mold temperature at 80°C, and post-mold moisture conditioning is not required for dimensional stability because PA12 reaches equilibrium moisture below 1.0% at 23°C and 50% RH. Compliance for HVAC actuators includes ISO 527-1/-2 for mechanical property verification, ISO 75-1/-2 for heat deflection temperature at 1.80 MPa, and UL 94 HB for plenum-adjacent components where no flame-retardant rating above HB is mandated. Terminal finished parts include damper gears, actuator coupling sleeves, condensate pump impellers, blower wheel hubs, and condensate drain valve bodies.

    In potable water circulation pump housings, hydrolysis resistance of PA12 in hot chlorinated water is evaluated on the component because the compound may satisfy the framework of NSF/ANSI/CAN 61 and AS/NZS 4020:2018 for contact with drinking water, but compound-specific certification is required and generic PA12 hydrolysis data are not a substitute for full listing. Formulation addition ratio for water-contact parts excludes recycled PA12 and any antimony trioxide or halogenated flame retardant; if blue identification masterbatch is added, concentration is limited to 1.0–1.5 wt% using a PA12 carrier to minimize extractables. The production process begins with drying at 80°C for 4–6 h to a moisture content below 0.10 wt%, followed by injection molding at 250–270°C melt temperature and 80–90°C mold temperature to reduce surface voids caused by trapped volatiles and to promote a resin-rich skin over glass fibers. Published data for this specific 40% glass-filled PA12 configuration under continuous chloramine exposure is limited, so long-term hydrolysis testing under ISO 22088-3 or ISO 16750-4 may be specified by the pump manufacturer before serial production. Terminal finished parts include pump volute liners, impeller wear rings, mechanical seal housings, distribution manifold flanges, and hot-water recirculation loop spacers.

    Rail Vehicle Interior Cable Clips and Underframe Cable Cleats Assessed Under EN 45545-2

    Railway infrastructure applications place simultaneous demands on low smoke emission, low toxic gas release, and dimensional stability through washdown cycles. The as-supplied HL X grade provides heat stabilization and hydrolysis resistance, but a 40% glass-filled PA12 may not inherently meet all EN 45545-2:2020 HL2 smoke and heat release thresholds; therefore, the formulation addition ratio often includes a phosphorus-based flame-retardant masterbatch at 15–25 wt%, which reduces tensile modulus under ISO 527-4 and increases melt viscosity, requiring wider gates and shorter flow paths. Processing is performed on an injection molding machine with a 22:1 L/D screw, a hopper dryer set at 80°C, and mold temperature kept at 60–80°C; fan gates or tab gates are used instead of pin gates to avoid surface streaks from exposed glass fiber and to reduce localized shear heating that can pre-degrade the flame-retardant package. Compliance verification includes EN 45545-2:2020 for railway material fire behavior, EN 61373:2010 for shock and vibration testing, and NFPA 130 where North American transit specifications govern. Terminal finished parts include interior cable clips, cable tie mounts, underframe cable cleats, electrical connector brackets, and cable duct support rails in passenger rail vehicles.

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    Certification & Compliance
    More Introduction

    EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12, Dry is a heat- and light-stabilized polyamide 12 extrusion and molding grade supplied with controlled residual moisture. The designation separates base chemistry from modification: the L 25 segment identifies the PA12 backbone and a supplier-defined viscosity class, while W 40 HL X denotes the stabilized, flexible formulation whose complete additive package is proprietary. Incoming lots certified as dry are typically specified at or below 0.10% moisture by ISO 15512:2019 or coulometric Karl Fischer titration. That moisture limit is not passive: opened containers exposed to ambient relative humidity above 60% can regain surface moisture quickly, and the material must be re-dried before conversion if the certificate value cannot be maintained.

    PA12 differs from short-chain aliphatic polyamides because the amide groups are separated by a C12 repeat unit. Under ISO 62 immersion at 23 °C, saturation water absorption for unmodified PA12 is typically documented between 1.5% and 2.0%, whereas PA6 reaches 9.0% to 10.0% and PA66 reaches 7.0% to 8.5%. The lower equilibrium water uptake reduces dimensional change, hydrolytic degradation rate, and dielectric loss drift in humid service. The W 40 HL X grade is specified for flexible pneumatic and hydraulic tubing, cable sheathing, fuel-vapor vent lines, and industrial hose applications that require subzero ductility and UV resistance without the rigidity of glass-filled polyamides. It is not a direct stiffness substitute for unreinforced PA6 or PA66.

    Incoming quality verification for this dry grade should include moisture content, melt volume-flow rate, and pellet appearance. Moisture is measured according to ISO 15512:2019 or Karl Fischer coulometric titration. Melt volume-flow rate is controlled under ISO 1133-1:2022 using the temperature and load specified on the EMS-Grivory certificate; comparing MVR values across different loads or temperatures is invalid because the L 25 viscosity class distinguishes this product from lower- or higher-viscosity PA12 grades. A lot with acceptable MVR but moisture above 0.10% can exhibit surging, pinholes, or surface roughness. Pellet geometry, fines content, and regrind level should also be controlled; irregular particle-size distribution can alter feed-zone conveying and melt-pressure stability.

    How Are Drying and Melt-Conditioning Parameters Established for This Grade?

    Residual moisture control is the first process limit. The resin is supplied dry, but exposure to ambient air above 60% relative humidity or storage outside sealed liners can invalidate the as-supplied state. Pre-drying should be performed in a dehumidified-air hopper dryer or vacuum dryer at 70–90 °C for 4–8 h when the measured moisture exceeds 0.10%. The air dew point should be held at or below -30 °C; conventional hot-air ovens without desiccant are generally insufficient for rapid and consistent drying of nylon 12. Overtemperature above 90 °C with extended residence can produce pellet sticking and discoloration. Minimum drying time should be determined by inlet moisture and hopper loading rather than a fixed time alone.

    Conversion on single-screw extruders uses general-purpose nylon screws with 24:1 to 30:1 L/D, a three-zone profile, and compression ratio from 2.5:1 to 3.5:1. Vacuum venting is recommended when regrind is used or when ambient humidity introduces additional moisture. Barrel temperatures are typically profiled from 200 °C at the feed zone to 240 °C at the metering zone and die, but set points should be adjusted so that the measured melt temperature remains within ±5 °C of the target confirmed for the tool and downstream line. Flexible PA12 formulations are sensitive to shear heating; excessive screw speed, worn screw clearances, or blocked screen packs can raise melt temperature above 250 °C, at which surface defects and odor increase. Injection molding, where applicable, should use a rear zone near 200–220 °C, a center zone near 220–240 °C, a front zone near 230–250 °C, and a nozzle near the front-zone set point. Clamp force, injection speed, and hold pressure require tool-specific trials; no universal setting is derived from the material alone.

    Process monitoring should log melt pressure before the breaker plate, melt temperature at the die, screw torque, and haul-off speed. A sustained pressure deviation of more than 20% from the validated baseline typically indicates feed-throat bridging, inconsistent pellet size, or screw wear. Melt-pressure variation at frequencies above 1 Hz can cause wall-thickness oscillation in thin-wall tubing; adjusting screw speed or barrel residence may be necessary. Melt strings or silver streaks usually indicate moisture or volatile carryover rather than thermal degradation alone.

    Dry-as-molded physical and mechanical values are determined under ISO 291 standard atmospheres. Table 1 lists representative ranges for flexible heat-stabilized PA12 extrusion formulations within the Grilamid L 25 W 40 HL X envelope. The ranges are not batch guarantees and should be superseded by the supplier certificate for a specific production lot.

    PropertyTest methodRepresentative dry-state range
    DensityISO 1183-1:20191.01–1.04 g/cm³
    Saturation water absorptionISO 62:2008, 23 °C1.5–2.0%
    Tensile modulus, 1 mm/minISO 527-1/-2:2019200–500 MPa
    Nominal strain at breakISO 527-1/-2:2019, 50 mm/min>50%
    Charpy unnotched impact, 23 °CISO 179-1/1eU:2010no break
    Melting temperature, DSCISO 11357-1/-3:2018172–178 °C
    Volume resistivity, dryIEC 62631-3-1:20161012–1014 Ω·m

    The tensile modulus range is intentionally broad because plasticizer concentration, moisture state, and test speed influence the measured value. For applications that require dry flexural modulus above 500 MPa, unreinforced rigid PA12, PA6, or PA66 may be more appropriate. Volume resistivity values are not design constants for wet environments; moisture uptake reduces resistivity by orders of magnitude, so end-use testing should be performed on conditioned specimens.

    Comparative Humid-Service and Dry-State Benchmarks Against PA6 and PA66

    Substitution of PA6 or PA66 with this PA12 grade is usually driven by moisture uptake, chemical resistance, and subzero toughness rather than short-term tensile stiffness. Table 2 compares representative dry-state values. PA6 and PA66 values refer to unreinforced dry-molded reference data; the flexible PA12 column is the same specification envelope as Table 1.

    PropertyTest methodUnreinforced PA6Unreinforced PA66Flexible heat-stabilized PA12
    DensityISO 1183-1:20191.13–1.15 g/cm³1.13–1.15 g/cm³1.01–1.04 g/cm³
    Saturation water absorptionISO 62:2008, 23 °C9.0–10.0%7.0–8.5%1.5–2.0%
    Melting temperatureISO 11357-1/-3:2018220–225 °C255–265 °C172–178 °C
    Tensile modulus, dryISO 527-1/-2:20192800–3400 MPa3000–3600 MPa200–500 MPa

    The table does not imply that the PA12 grade competes with PA66 on dry modulus. Its functional difference is lower equilibrium moisture uptake and the resulting stability in humid, fluid-contact, and outdoor service. In dry structural applications such as rigid fasteners, fan wheels, or engine covers, PA6 or PA66 are usually selected for tensile modulus and creep resistance. In air-brake tubing, cable jackets, and quick-connect pneumatic lines exposed to moisture, aliphatic hydrocarbons, and road salt, the PA12 grade reduces moisture-related dimensional and electrical drift.

    For pneumatic tubing and cable sheathing, production-scale single-screw extruders with 24:1 to 30:1 L/D and three-zone barrier screws are used with closed-loop melt-temperature control. Barrel settings typically range from 200 °C in the feed zone to 240 °C at the die. The measured melt temperature should remain within ±5 °C of the validated set point; wider excursions alter die swell, wall thickness, and surface quality. Residence time from feed throat to die should be kept below 15 min and melt temperature below 250 °C. Vacuum venting is recommended when regrind is used or when ambient humidity is high. The use of regrind above 20% is not recommended without verifying melt-pressure stability and finished-part mechanical properties.

    When Plasticizer Migration and Low-Temperature Impact Define the Service Ceiling

    Because this is a flexible grade, the service ceiling may be controlled by plasticizer retention and low-temperature impact rather than by the melting point alone. In contact with aggressive fuel blends, biodiesel fractions, or polar solvents, low-molecular-weight plasticizers can migrate from the PA12 matrix; the resulting surface can become tacky and low-temperature ductility may decline. Published data for this specific dry configuration in every possible fuel blend is limited, so fuels containing high aromatic or oxygenate fractions should be tested under real tank-temperature cycling per the end-use specification.

    Low-temperature impact should be evaluated using ISO 179-1/1eA notched Charpy at -30 °C or -40 °C, and not inferred from room-temperature values. A material that passes at 23 °C may fail at -40 °C after plasticizer migration or after moisture conditioning. Chemical incompatibilities are comparable to other polyamides: concentrated mineral acids, formic acid, phenols, and strong oxidizing media attack the polymer. Continuous service in hot water above 80 °C should be avoided unless specific hydrolysis-resistant validation exists. At elevated processing temperatures, sulfur-containing colorants, certain flame-retardant masterbatches, or acidic fillers can alter molecular weight; additive compatibility should be confirmed by melt-flow stability tests. The W 40 HL X stabilization package provides heat and light resistance for outdoor service, but black pigmentation or additional UV absorber may still be required for direct long-term exposure. Weathering resistance should be specified according to ISO 4892-2 and measured by retained elongation, not color change alone.

    In cable sheathing and industrial hose applications, the grade is processed at 200–240 °C, with metering-zone pressure typically below 200 bar on single-screw machines of 24:1 to 30:1 L/D. Post-extrusion wall-thickness and ovality data should be collected under run-specific haul-off and calibration conditions; CPK values are line-dependent. The dry grade is not a direct substitute for rigid PA12, glass-filled PA12, or PA11 in every design. High-pressure spiral hose, snap-fit connectors, or structural brackets that require dry flexural modulus above 500 MPa should use a stiffer grade. Compared with unmodified Grilamid L 25, this grade is formulated for improved long-term heat and UV resistance and controlled flexibility. It should not be blended with glass-reinforced PA12 grades unless the end-use modulus is re-qualified. Compared with PA11, the two materials share low moisture uptake and good chemical resistance, but melt temperature, lot-specific viscosity, and plasticizer behavior differ; a drop-in substitution without ISO 527 and ISO 179 testing is not supported. Where regulatory compliance is required, such as EU 10/2011 food-contact or national drinking-water approvals, the specific EMS-Grivory lot certificate and current positive list must be checked; the product designation alone does not establish regulatory conformity.

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