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EMS-Grivory Grilamid L 25 W 20 Nylon 12, Conditioned

    • Product Name: EMS-Grivory Grilamid L 25 W 20 Nylon 12, Conditioned
    • 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 426897
    Density 1.01 g/cm³
    Tensile Strength 50 MPa
    Elongation At Break 50%
    Flexural Modulus 1200 MPa
    Charpy Impact Strength 23 C No break
    Melting Point 178 °C
    Heat Deflection Temperature 1 80 Mpa 50 °C
    Water Absorption 24h 23 C 1.5%
    Vicat Softening Temperature B 50 170 °C
    Volume Resistivity 1.0E+11 Ω·cm

    As an accredited EMS-Grivory Grilamid L 25 W 20 Nylon 12, Conditioned factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in sealed, moisture-proof 25 kg bags, conditioned for optimal processing, ensuring consistent quality and protection from humidity.
    Container Loading (20′ FCL) 20′ FCL: Grilamid L25W20 Nylon 12 conditioned granules packed in sealed bags on pallets, securely loaded, moisture-protected.
    Shipping Ship EMS-Grivory Grilamid L 25 W 20 (conditioned nylon 12) in sealed, moisture-proof containers to preserve its equilibrium moisture content. Protect from direct sunlight, extreme heat, and mechanical contamination. Store below 50°C, keep dry, and handle with clean equipment to maintain product integrity during transit.
    Storage Store in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep the original, tightly sealed container to prevent moisture absorption and contamination. Avoid high humidity and temperature extremes. Under these conditions, the conditioned Nylon 12 resin will remain usable within its designated shelf life.
    Shelf Life Shelf life is indefinite when stored in sealed, dry conditions away from UV light and heat.
    Application of EMS-Grivory Grilamid L 25 W 20 Nylon 12, Conditioned

    Equilibrium moisture uptake in Grilamid L 25 W 20, conditioned per ISO 1110 at 23 °C/50 % RH, establishes the downstream reference state for property declarations. In this state the 20 wt% plasticizer package and absorbed water act together to reduce flexural modulus and increase elongation at break relative to dry-as-molded material. For heavy-duty air brake tubing, the pellet is fed as 100 % virgin material with no external plasticizer addition. A 45 mm single-screw extruder with a barrier screw of L/D 30:1 and a 3:1 compression ratio is run with feed, compression, and metering temperatures of 190 °C, 205 °C, and 215 °C. The die head is held at 210 °C. Barrel residence time is limited to 4 min to avoid plasticizer volatilization. A vacuum calibration sleeve applies -0.04 MPa to -0.06 MPa; the two-stage water bath is held at 15 °C and 20 °C. The draw ratio is limited to 1.05:1 to 1.15:1. Wall-thickness eccentricity is logged by a laser gauge with 0.005 mm resolution and maintained below 0.05 mm on an 8.0 mm outside diameter tube. The cut lengths are assembled with brass compression fittings into pneumatic circuits tested to SAE J844. Post-extrusion conditioning at 23 °C/50 % RH for 48 h restores the equilibrium moisture state before final burst and elongation testing.

    Process variableAir brake tubingCable sheathingRailway pneumatic line
    Melt temperature190–215 °C195–220 °C185–205 °C
    Residual moisture before extrusion≤0.10 %≤0.10 %≤0.08 %
    Screw L/D ratio30:130:128:1
    Draw ratio1.05–1.15not applicable1.03–1.08
    Primary reference methodSAE J844ISO 527-1:2019ISO 179-1/1eA

    Can a 20 wt% plasticizer package survive continuous-flex cable carrier service without jaw-box exudation?

    Continuous-flex cable jackets in storage and retrieval shuttles require a balance of abrasion resistance and low-temperature flex endurance. The conditioned grade enters a 60 mm single-screw extruder with a 3.5:1 compression ratio screw and a pressure crosshead die. Barrel temperatures are set from 195 °C to 220 °C; screw speed is limited to 35 min⁻¹ to 55 min⁻¹ to avoid shear heating. The jacket formulation uses 97.5 wt% virgin pellet and 2.5 wt% carbon black masterbatch. Regrind from the same production lot is limited to 15 wt%. The water trough is segmented with the first 2 m at 40 °C and the next 4 m at 15 °C. In-line ultrasonic wall monitoring flags any deviation outside ±0.05 mm. The terminated cable is then placed in a customer-specific flex fixture at a bend radius of 7.5 times cable outer diameter and cycled for 5 × 10⁶ cycles. Published data for this specific grade in that fixture is limited; qualification is therefore based on the customer's dynamic test protocol. The conditioned moisture together with the 20 wt% plasticizer package suppresses stress whitening at the neutral bend axis, which is the primary visual rejection criterion.

    Railway pneumatic control lines in low-temperature switching yards

    Railway pneumatic control lines for switching yard actuators route pressurized air across exposed concrete channels. In this segment, cold impact at -40 °C is tested according to ISO 179-1/1eA. The material is processed as 100 % virgin pellets; regrind is not permitted because lot-to-lot variability in Charpy impact test results creates acceptance risk. A vented 50 mm single-screw extruder with L/D 28:1 is used, and the vent is connected to a vacuum pump at -0.08 MPa to strip residual moisture and monomer. Melt temperature is held between 185 °C and 205 °C; sustained operation above 210 °C produces a visible plasticizer haze on the tube surface. The calibration die has a 12 mm land length and a 10.0 mm outside diameter. A draw ratio of 1.05:1 is applied between die exit and puller. In-line laser micrometry with 0.005 mm resolution logs ovality. The finished coil is assembled with push-to-connect fittings. When the line is routed through rolling-stock interiors, fire performance under EN 45545-2 must be confirmed separately; published data for this specific formulation is limited. The conditioned moisture state is acceptance-relevant for the -40 °C impact margin because dry-as-molded material exhibits higher notch sensitivity when tested to ISO 179-1/1eA.

    Injection-molded strain relief grommets for industrial sensor cables are produced from the same conditioned pellet using an 80-tonne clamping force injection molding machine with a 3-zone general purpose screw. Barrel temperatures from rear to nozzle are 190 °C, 200 °C, and 210 °C; mold temperature is held at 30 °C. The pellet is dried to ≤0.10 % residual moisture in a desiccant dryer with a -30 °C dew point. The molded part is a flexible cable entry grommet with a wall section of 2.0 mm and integrated strain relief ribs. A 100 % virgin formulation avoids the viscosity shift caused by contaminated regrind; hot runner tips are kept below 215 °C to prevent plasticizer degradation at the gate. Mold shrinkage is characterized according to ISO 294-4. The grommet is subjected to pull-out force testing on a tensile tester at 50 mm/min; acceptance is defined by the connector manufacturer. Installation trials at 0 °C after 4 h soak are used to confirm that the conditioned state permits assembly without cracking, which is not guaranteed by dry-as-molded material with the same geometry.

    When spiral wrap extrusion uses melt temperature as a plasticizer migration control variable

    Spiral wrap sleeves for agricultural machinery harness protection are produced by profile extrusion through a spiral die at melt temperatures between 185 °C and 205 °C. The formulation is 100 % virgin Grilamid L 25 W 20; no regrind is used when the sleeve must retain its spiral pitch after 72 h of thermal exposure at 80 °C. A UV-stabilized partner grade is preferred for outdoor installations; if a masterbatch is required, addition is capped at 2.0 wt%. The extruder is a 45 mm single-screw machine with a 25:1 L/D ratio. The profile passes through a water bath at 12 °C and is wound continuously. Post-extrusion annealing at 80 °C for 2 h reduces spiral pitch relaxation. The terminal sleeve is evaluated for tensile modulus of the spiral profile according to ISO 527-1:2019. Plasticizer migration is checked by weight loss after 24 h at 80 °C under airflow; the acceptance limit is set by the harness maker's project specification. Melt temperature remains the primary control variable because plasticizer loss at the die lip produces pitch distortion and surface tack in the wound coil.

    Subsea methanol injection control lines require low water uptake and methanol resistance over years of service. The conditioned starting state is not the long-term service state; after immersion in seawater at 23 °C, water absorption in polyamide 12 typically reaches an equilibrium measured by ISO 62. Grilamid L 25 W 20 is extruded as a 6.0 mm outside diameter tube with 1.0 mm wall thickness using a 50 mm single-screw extruder at melt temperature 190 °C–210 °C. The tube is spooled under controlled tension and pressure-tested at 1.5 times design working pressure. Compliance with API 17E for subsea umbilical hose requires additional qualification; published data for this plasticized grade under API 17E is limited. The terminal assembly is an armored methanol injection line bundled into a steel-tube umbilical. Plasticizer extraction in methanol service remains a lifetime-limiting mechanism; a limit of 40 °C continuous service is imposed unless specific extraction data from the manufacturer is available. This boundary prevents thermal acceleration of plasticizer leaching beyond the design basis.

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    Certification & Compliance
    More Introduction

    At 23 °C and 50 % relative humidity, EMS-Grivory Grilamid L 25 W 20 Nylon 12 reaches an equilibrium moisture content of approximately 0.7 % by mass in the conditioned state, as defined by ISO 291 and accelerated conditioning protocols under ISO 1110. The product is a plasticised, low-viscosity polyamide 12 (PA12) compound, designated as PA12 under ISO 1043-1:2011, with a semi-crystalline aliphatic backbone and a density of 1.02 g/cm³ when tested to ISO 1183-1:2019. Published datasheet values include a melting endotherm peak of 174 °C under ISO 11357-3:2018 and a melt volume-flow rate of 20 cm³/10 min at 275 °C and 5 kg load under ISO 1133-1:2022. The conditioned state reduces tensile modulus and yield stress while increasing notched Charpy impact toughness relative to dry-as-moulded specimens.

    Tensile testing to ISO 527-2:2012 reports a tensile modulus of 700 MPa, a yield stress of 27 MPa, and a nominal strain at break above 50 % for conditioned specimens. Dry-as-moulded values are approximately 1000 MPa tensile modulus and 32 MPa yield stress. Charpy notched impact strength under ISO 179-1/1eA:2010 increases from a dry value of 7 kJ/m² to a conditioned value of 40 kJ/m² at 23 °C, while Charpy unnotched specimens do not fail under the same test conditions. Shore D hardness measured to ISO 868:2003 falls in the 55–60 range for conditioned specimens. Water absorption at saturation under ISO 62:2008 is approximately 1.4 %, with the 0.7 % equilibrium value at 50 % RH being the defining moisture condition for the conditioned data set.

    PropertyTest methodUnitDry-as-mouldedConditioned
    DensityISO 1183-1:2019g/cm³1.021.02
    Tensile modulusISO 527-2:2012MPa1000700
    Yield stressISO 527-2:2012MPa3227
    Nominal strain at breakISO 527-2:2012%>50>50
    Charpy notched impact, 23 °CISO 179-1/1eA:2010kJ/m²740
    Charpy unnotched impact, 23 °CISO 179-1/1eU:2010kJ/m²No breakNo break
    Shore D hardnessISO 868:20035855
    Water contentISO 15512:2019%0.070.7

    What Processing Limits Exist for Low-Viscosity Plasticised PA12?

    Injection moulding and extrusion units processing Grilamid L 25 W 20 must remove the conditioning moisture before melting. Although the conditioned state is advantageous for solid-state toughness, the moisture content of 0.7 % must be lowered to below 0.10 % before melt processing to prevent hydrolytic degradation and surface splay. Desiccant drying at 80 °C for 4–6 h in a dry-air dryer with a dew point below -30 °C is typical. Residence time at melt temperatures above 250 °C should not exceed 10 min because prolonged exposure volatilises the plasticiser and shifts the viscosity upward. Machine barrel profiles from hopper to nozzle are set between 200 °C and 250 °C, with nozzle and hot-runner temperatures held at or below 260 °C. Mould temperatures are typically 40–80 °C; higher mould temperatures above 80 °C increase crystallinity and can reduce impact toughness due to larger spherulite formation. Screw geometry on conventional three-zone screws uses an L/D ratio from 18:1 to 25:1 and a compression ratio of 2.0:1 to 2.5:1. Back pressure is kept below 0.7 MPa hydraulic to limit shear heating in the low-viscosity melt.

    On a 30 mm single-screw extruder with L/D 24:1, cylinder temperatures are typically set from 200 °C in the feed zone to 230 °C in the metering zone, with a breaker plate and screen pack of 60/80/100 mesh. The conditioned moisture must still be removed by pre-drying; vented barrels are not a substitute. Melt pressure at the die is usually limited to 15 MPa because the plasticised PA12 has lower viscosity than unplasticised PA12, and excessive pressure indicates insufficient melt temperature or excessive die restriction.

    Processing parameterSettingNotes
    Pre-drying temperature and time80 °C, 4–6 hDesiccant dryer, dew point -30 °C or lower, target moisture <0.10 %
    Melt temperature, injection moulding220–250 °CNozzle ≤260 °C
    Mould temperature40–80 °CHigher mould temperatures reduce impact due to crystallinity
    Screw L/D ratio18:1–25:1Compression ratio 2.0:1–2.5:1
    Residence time above 250 °C<10 minPlasticiser volatilisation risk
    Extrusion melt temperature200–240 °CDie pressure limit 15 MPa
    Back pressure, hydraulic0.3–0.7 MPaLimits shear heating in low-viscosity melt
    Regrind level≤30 %Virgin blend, dried, free of oil and contamination

    Published data for automotive fuel and vapour line applications show that the conditioned compound is evaluated for low-temperature flexibility and resistance to zinc chloride stress cracking. The grade is often processed into corrugated tubing and quick connectors using ISO 19013-1 and SAE J844 as dimensional and performance references. Fuel permeation is governed by SAE J2260 for multi-layer fuel line constructions, where PA12 is typically combined with polyolefin or fluoropolymer barrier layers. The low moisture uptake of PA12, approximately 0.7 % at 50 % RH, reduces dimensional change compared with PA6 and PA66 in under-hood humidity cycles.

    Electrical cable sheathing and pneumatic tubing applications use the plasticised PA12 because the conditioned Charpy notched impact of 40 kJ/m² supports installation at low temperature. Processing on 45 mm single-screw extruders commonly requires melt temperatures between 200 °C and 240 °C; melt temperatures above 250 °C produce visible surface defects from plasticiser volatilisation. Chemical resistance to aliphatic hydrocarbons, diesel fuel, lubricants, and dilute salt solutions is a further factor. Immersion testing according to ISO 175:2010 typically shows mass change below 1.5 % after 28 d at 23 °C in reference fuel C. Published data for this specific configuration is limited for hot chlorinated solvents and strong acids; such media should be excluded without component validation. At relative humidity above 60 %, pre-drying before melt processing is mandatory because the material quickly returns to conditioned moisture levels.

    When Grilamid L 25 W 20 Replaces PA6, PA66, POM or TPU

    When a design replaces PA6 or PA66 with Grilamid L 25 W 20, the first measurable difference is moisture uptake: PA6 reaches about 2.7 % water at 50 % RH, and PA66 about 2.5 %, compared with 0.7 % for PA12 under ISO 62:2008. This gives PA12 better dimensional stability and more stable dielectric properties, but the lower glass transition temperature of PA12, near 45 °C, means creep and stiffness must be checked under continuous load at temperatures above 60 °C.

    Compared with unplasticised PA12 grades, the plasticised L 25 W 20 exhibits a conditioned tensile modulus of 700 MPa, whereas unplasticised PA12 typically shows 1100–1300 MPa under the same conditioning. The plasticised grade therefore suits snap-fit, flexible conduit, and cable sheathing geometries but is less suitable for load-bearing structural brackets. Against polyoxymethylene, Grilamid L 25 W 20 has approximately 28 % lower density at 1.02 g/cm³ versus 1.41 g/cm³ and higher notched impact toughness, but lower modulus and creep resistance. POM is specified for precision gears where dimensional stability under load is critical; PA12 is specified for low-temperature impact and chemical resistance to fuels and zinc chloride.

    Against thermoplastic polyurethane elastomers, the PA12 grade has higher modulus but lower elastic recovery. TPU may show tensile moduli of 20–200 MPa, whereas conditioned Grilamid L 25 W 20 is 700 MPa. TPU offers high abrasion resistance and elongation, while PA12 offers lower moisture absorption, better chemical resistance to oils and fuels, and more stable processing at melt temperatures of 220–250 °C. Compared with PA11, the PA12 backbone has lower amide density and slightly lower water absorption, although both are used in automotive pneumatic tubing and fuel line components. For applications requiring automotive fuel line performance, the material is evaluated under SAE J2260 and SAE J844; these specifications prescribe low-temperature impact, burst pressure, and extraction limits that vary by OEM drawing.

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