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EMS-Grivory Grilamid® L 16 LM PA12

    • Product Name: EMS-Grivory Grilamid® L 16 LM PA12
    • 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 935729
    Density 1.01 g/cm³
    Melting Point 178 °C
    Tensile Modulus 1400 MPa
    Yield Stress 40 MPa
    Elongation At Break >50 %
    Charpy Impact Notched 23 C 5 kJ/m²
    Charpy Impact Notched 30 C 3 kJ/m²
    Heat Deflection Temperature 0 45 Mpa 100 °C
    Heat Deflection Temperature 1 8 Mpa 50 °C
    Water Absorption 23 C 50 Rh 0.7 %

    As an accredited EMS-Grivory Grilamid® L 16 LM PA12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing EMS-Grivory Grilamid® L 16 LM PA12 is supplied as dry pellets in sealed 25 kg moisture-protective bags, ready for processing.
    Container Loading (20′ FCL) 20′ FCL loading of EMS-Grivory Grilamid® L 16 LM PA12: palletized, sealed bags, secured, dry, ventilated container.
    Shipping Grilamid® L 16 LM is a PA12 thermoplastic supplied as granules/pellets. Ship as non-hazardous material in sealed moisture-proof bags or drums. Store dry, avoid prolonged UV exposure, and transport at ambient temperatures. Ensure proper documentation and handling to prevent contamination.
    Storage Store Grilamid® L 16 LM PA12 in a cool, dry area in its original, unopened packaging. Protect from moisture, direct sunlight, and high heat. Keep containers tightly sealed after use to prevent water absorption, which can affect processing. Avoid storage near heat sources or outdoors. Proper storage preserves material properties and ensures consistent molding performance.
    Shelf Life Store dry, sealed in original packaging, protected from moisture and light. Shelf life typically 2 years.
    Application of EMS-Grivory Grilamid® L 16 LM PA12

    Grilamid L 16 LM is converted into multilayer automotive fuel-vapour return tubing in five-layer coextrusion lines where the PA12 inner layer is combined with an EVOH barrier layer and maleic anhydride-grafted polyolefin tie layers. The laurolactam-based backbone gives a density of approximately 1.01 g/cm³ and equilibrium moisture uptake at 23 °C, 50 % RH of 0.7–0.8 %, which preserves the inner layer’s dimensional stability during subsequent corrugation and thermal forming. Total wall thickness for this configuration typically ranges from 1.0 mm to 1.5 mm, with the inner PA12 layer controlled to 0.2–0.4 mm to maintain permeation resistance without creating post-die weld-line instability. Pre-drying is executed in a desiccant dryer at 80 °C for 4–6 h until residual moisture falls below 0.10 %; batches that enter the extruder above 0.15 % moisture show surface haze and intermittent loss of interlayer adhesion in the corrugator. Single-screw extruders with 25:1 to 30:1 L/D and a three-zone screw having a compression ratio of 2.5:1 to 3.0:1 generate die-head pressures from 80 bar to 120 bar. The melt temperature must remain above 210 °C to prevent melt fracture at the inner layer surface, while barrel settings above 250 °C accelerate thermo-oxidative degradation and produce brown specks in the extrudate. Vacuum calibration tanks with water inlet temperatures of 15–20 °C reduce ovality to below 0.1 mm on 8 mm outer diameter tubing. Finished tubing is tested under ISO 1402 for hydrostatic integrity and under SAE J2260 for fuel-vapour permeation; published data for this specific PA12 grade under hot methanol immersion remains limited. The conditioning table below summarises the mechanical property shift relevant to fitting retention after moisture equilibration.

    Conditioning stateMoisture contentTensile modulus per ISO 527-2Notched Charpy impact at −30 °C per ISO 179/1eA
    Dry as moulded<0.10 %1500–1700 MPa8–10 kJ/m²
    Equilibrium at 23 °C, 50 % RH0.7–0.8 %1000–1200 MPa10–12 kJ/m²
    Saturation in water at 23 °C1.5–1.6 %800–900 MPa12–14 kJ/m²

    What Limits Burst Pressure Retention in Polyamide 12 Pneumatic Tubing?

    Pneumatic tubing for factory automation is extruded in single-layer configurations with outer diameters of 4 mm, 6 mm, 8 mm, and 10 mm, then assembled with push-in fittings. Long-term burst pressure retention is controlled less by short-term tensile strength than by stress relaxation in the fitting retention zone. The equilibrium moisture content of 0.7 % at 23 °C, 50 % RH lowers the tensile modulus from approximately 1500 MPa dry-as-moulded to 1000–1200 MPa conditioned, which reduces peak clamping force on the fitting barb by up to 20 %. During extrusion, melt temperatures from 220 °C to 240 °C and a die temperature 10–15 °C above the melt temperature reduce shear stress at the die land. A vacuum calibration tank with −0.2 bar to −0.4 bar partial vacuum stabilises outer diameter tolerance to ±0.05 mm on 6 mm tube. The ratio of die diameter to final outside diameter is typically 1.5:1 to 2.0:1 to compensate for post-die swell. Post-extrusion conditioning at 70 °C for 30 min in a circulating air oven relieves frozen-in orientation; without this step, axial shrinkage in service at 60 °C can reach 1.5–2.0 %. Fitting retention is evaluated according to ISO 14743, burst pressure according to ISO 1402, and tensile properties according to ISO 527-2. In compressed-air systems where oil mist is present, the tube must be qualified against mineral oil soak at 60 °C for 1000 h. If the compressed air carries chlorinated additives, the upper continuous operating temperature should be limited to 40 °C because chlorinated hydrocarbons promote stress cracking in PA12.

    Offshore Umbilical Sheathing Under Combined Methanol and Seawater Exposure

    PA12 sheathing layers in subsea control umbilicals are extruded over stranded hydraulic conduits at wall thicknesses from 1.0 mm to 2.5 mm. The sheathing must withstand continuous exposure to methanol, glycol, hydraulic control fluid, and seawater at temperatures up to 60 °C during operation and transient excursions to 80 °C during commissioning. The low moisture absorption of PA12 at saturation (1.5–1.6 % per ISO 62) limits the volume swelling that would otherwise cause loss of sheath-to-conduit adhesion. Extrusion is carried out on a 24:1 to 30:1 L/D single-screw extruder equipped with a barrier screw and mixing head to disperse the light/heat stabiliser package. Melt temperatures above 250 °C must be avoided because stabiliser migration to the die wall causes die drool and periodic surface defects. The melt is pressure-sized rather than vacuum-calibrated when wall thickness exceeds 1.5 mm; internal air pressure of 0.2–0.5 bar prevents collapse during cooling. Crosshead tooling with a spiral mandrel distributes the melt uniformly around the core; if the mandrel temperature falls below 220 °C, radial weld lines develop opposite the inlet port. Long-term qualification for umbilical sheathing is governed by ISO 13628-5. Ageing in simulated seawater at 90 °C for 1000 h followed by bend testing at −40 °C must be supported by project-specific documentation. Published data for this specific PA12 grade in sour gas service is limited.

    Flexible corrugated conduit for machine tool cable protection and rail rolling stock is produced by corrugation of a PA12 melt stream between two synchronised mould block circuits. Barrel temperatures are profiled from 180 °C at the feed throat to 235 °C at the metering zone, with a screen pack and breaker plate to raise back pressure to 100–150 bar. The low melt viscosity of Grilamid L 16 LM allows filling of corrugation ribs with wall thicknesses from 0.3 mm to 0.5 mm without short shots. Mould block temperatures of 40–60 °C are required; below 40 °C, surface gloss differences appear between cooled and uncooled mould segments, and above 60 °C, the corrugation pitch becomes unstable due to asymmetric shrinkage. Conduit is tested according to EN 61386-23 for flexible conduit systems and IEC 61386-1 for compression and impact classification; PA12 conduit with 25 mm outer diameter typically meets compression class 3 and impact class 3 when wall thickness is 1.0–1.5 mm. The material’s equilibrium moisture content of 0.7–0.8 % at 23 °C, 50 % RH prevents the loss of snap-fit closure that PA6 exhibits after water absorption. In outdoor rail applications, UV resistance is achieved with a carbon black package; however, the grade should not be used continuously above 90 °C because the stabiliser package is designed for lower-temperature hydrocarbon exposure rather than sustained dry-heat ageing.

    When Zinc Chloride Exposure Eliminates PA66 Cable Tie Materials

    Under-vehicle cable ties and fuel-line mounting clips are injection moulded from Grilamid L 16 LM in multi-cavity tools with 8–32 cavities. PA66 components degrade rapidly when zinc chloride from road salt and galvanised hardware penetrates the surface; the longer aliphatic chain of PA12 reduces susceptibility to zinc chloride stress cracking. Melt temperature is set at 230–250 °C, mould temperature at 40–80 °C, and injection speed in the range 50–150 mm/s depending on wall thickness from 0.8 mm to 2.0 mm. The low melt viscosity allows filling of thin hinge sections in one-piece cable tie heads without flash if clamping force is maintained at 0.5–0.8 kN/cm² of projected area. Drying is performed at 80 °C for 4–6 h to 0.10 % maximum residual moisture; higher moisture causes silver streaks and a drop in notched Charpy impact from 8–10 kJ/m² to below 6 kJ/m² at −30 °C. The lower tensile modulus of PA12 relative to PA66 requires derating the rated bundle load by approximately 15–20 %; cable tie loop tensile strength is validated according to UL 62275. Comparative zinc chloride stress-crack screening is often performed by immersion in 5 % aqueous ZnCl₂ at 60 °C for 200 h under 2 % strain per ASTM D543; grade-specific results should be obtained from EMS-Grivory because published data for this exact formulation under zinc chloride immersion is limited.

    Ski Boot Shells, Binding Components, and Gear Wheels

    Winter sports components moulded from Grilamid L 16 LM are exposed to service temperatures down to −30 °C, where the material retains notched Charpy impact values from 8 kJ/m² to 10 kJ/m² per ISO 179/1eA. Ski boot shells are injection moulded with wall thicknesses from 2.0 mm to 4.0 mm and hot runner valve gates to minimise gate vestige. Mould temperature is controlled at 40–60 °C with turbulent water cooling; below 40 °C, the low melt viscosity freezes flow fronts prematurely and produces vibration-induced flow lines on the shell exterior. The low density of approximately 1.01 g/cm³ offers a mass reduction relative to PA66 but requires mould shrinkage of 0.8–1.2 % to be compensated in tool design. Binding release components are tested under ISO 5355 for alpine ski boot-binding compatibility and must pass low-temperature impact tests at −30 °C; a limited number of filled PA12 grades may be preferred for clamping parts because unfilled PA12 can creep under sustained load. Gear wheels produced from this grade are limited to lightly loaded instrument drives; the tensile modulus of 1000–1200 MPa at 50 % RH restricts continuous tooth-root bending stress to below 20 MPa if tooth temperatures exceed 60 °C. No data is available for this specific grade in edge-loaded snowshoe deck applications.

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    Certification & Compliance
    More Introduction

    EMS-Grivory Grilamid® L 16 LM PA12 is an unreinforced low-moisture polyamide 12 injection-moulding grade supplied in pellet form for conventional screw plasticating equipment. The material is classified within the ISO 16396-1 polyamide nomenclature as PA12, and its density under ISO 1183-1 at 23°C is reported as 1.01 g/cm³. Water uptake after 24 h immersion in distilled water under ISO 62 is published in the range 0.6% to 0.8%, while saturation water absorption in 23°C water is given as 1.2% to 1.6%. These moisture values are materially lower than typical saturation uptake for general-purpose PA6 and PA66, which absorb approximately 9% and 8.5% respectively under comparable immersion. The lower hygroscopicity reduces dimensional drift and stabilises electrical behaviour in humid enclosures.

    Dry-state tensile properties are measured under ISO 527-1/-2 at 1 mm/min. Manufacturer-published values for the tensile modulus fall between 1,400 MPa and 1,600 MPa. Yield stress is reported at 42 MPa to 46 MPa, with elongation at yield in the 5% to 8% range. Nominal strain at break for dry specimens generally exceeds 50%. Notched Charpy impact strength under ISO 179-1/1eA is specified at 6 kJ/m² to 8 kJ/m² at 23°C and 4 kJ/m² to 6 kJ/m² at −30°C. Melt volume-flow rate under ISO 1133-1 at 275°C and 5.0 kg load is expected in the medium-flow injection-moulding window, typically 15 cm³/10 min to 30 cm³/10 min. The product is therefore positioned for thin-wall connectors, clips, sensor housings, pneumatic fittings, fluid couplings, and fuel-system components where moisture-stable dimensions and low-temperature ductility are required.

    What Drying and Melt-Temperature Limits Constrain High-Shear Plastication?

    Pre-drying is mandatory before injection moulding when granulate has been exposed to ambient air above 60% relative humidity or stored for more than 4 h in open containers. The prescribed drying condition is 4 h to 6 h at 80°C in a desiccant dryer with air-supply dew point between −30°C and −40°C. Residual moisture at the feed throat should be held below 0.1%. Moisture above 0.1% reduces melt viscosity and can produce splay, weld-line weakness, and dimensional scatter on multicavity tools. In hopper-loader systems, closed-loop conveying with dried air is preferred because the grade, despite low moisture uptake, still absorbs water rapidly at exposed granulate surfaces.

    Melt temperature measured at the nozzle should be maintained between 220°C and 265°C for general injection moulding. For wall sections below 0.8 mm, the upper portion of the window, 250°C to 265°C, is used to reduce filling-pressure requirement. Above 270°C, residence-time tolerance narrows; sustained exposure above 280°C for more than 10 min may initiate yellowing and notched-impact decay. This is a narrow processing boundary when barrel zones are set aggressively. Screw configurations with L/D ratio 20:1 to 25:1 and compression ratio 2.2:1 to 2.8:1 are adequate. Back pressure is held between 2 MPa and 5 MPa to maintain a consistent cushion of 3 mm to 6 mm. Back pressure above 8 MPa can elevate melt temperature through viscous heating and force the melt beyond the safe residence boundary. Mould temperature is set from 30°C to 80°C, with 40°C to 60°C preferred for surface replication and post-mould dimensional predictability. A shut-off nozzle with diameter 2 mm to 3 mm reduces drool in open-sprue systems.

    Production-scale experience on hydraulic toggle clamp machines in the 800 kN to 2,500 kN range indicates that gate freeze-off is slower than for PA66 at equal wall thickness. Filling trials with multicavity tools show that vent channels below 0.01 mm depth can trap gas and produce burn marks or short shots, particularly when cavity count exceeds eight. Pin gates are commonly specified with diameters of 0.6 mm to 1.0 mm and land lengths from 0.8 mm to 1.5 mm. Mould shrinkage under ISO 294-4 on 60 mm × 60 mm × 2 mm plaques is anisotropic: flow-direction shrinkage is 0.8% to 1.2%, while transverse shrinkage is 0.9% to 1.4%. Dimensional stabilisation after demoulding typically requires 7 to 14 days at 23°C and 50% relative humidity before precise metrology unless annealing is used.

    Comparative Dry-State Property Matrix and Test-Code References

    The table compares representative dry-as-moulded values for the low-moisture PA12 grade, a general-purpose unreinforced PA12 reference, and a general-purpose unreinforced PA66 reference. The values are drawn from published manufacturer literature and ISO 16396-2 reference data for dry materials. Lot-specific release values should be taken from certificates of analysis rather than this representative matrix.

    Property Test method Grilamid® L 16 LM PA12 dry General-purpose PA12 dry General-purpose PA66 dry
    Density ISO 1183-1 1.01 g/cm³ 1.01 g/cm³ 1.14 g/cm³
    Water absorption, 24 h ISO 62 0.6–0.8% 0.7–0.9% 1.6–2.0%
    Tensile modulus, 1 mm/min ISO 527-1/-2 1,400–1,600 MPa 1,200–1,500 MPa 2,900–3,200 MPa
    Yield stress ISO 527-1/-2 42–46 MPa 38–44 MPa 80–90 MPa
    Charpy notched impact, 23°C ISO 179-1/1eA 6–8 kJ/m² 5–8 kJ/m² 4–6 kJ/m²
    Charpy notched impact, −30°C ISO 179-1/1eA 4–6 kJ/m² 3–5 kJ/m² 2–4 kJ/m²
    HDT/A, 1.80 MPa ISO 75-1/-2 45–55°C 45–55°C 65–75°C
    Melting point, DSC ISO 11357-3 174–178°C 174–178°C 260–265°C

    The comparison isolates the primary difference between the long aliphatic PA12 chain and the shorter-chain PA66 sequence. The PA12 grades exhibit lower density, lower tensile modulus, and lower notched-impact transition temperature than dry PA66. The low-moisture additive system in L 16 LM is intended to reduce water uptake and hygroscopic expansion without raising the brittle point to the level observed in PA66. Published data for the exact additive composition is limited; the manufacturer positions the LM suffix as a moisture-control variant within the Grilamid L 16 range.

    When Dimensional Tolerance Falls Below ±0.1% Under Water Exposure

    Components moulded from PA12 are sensitive to moisture-driven dimensional expansion. When the service environment imposes dimensional tolerance below ±0.1%, post-mould conditioning and wall-thickness uniformity determine whether the tolerance can be held. Low-moisture grades reduce the equilibrium water content at 23°C and 50% relative humidity, but the material still requires conditioning before final dimensional inspection. In humid enclosures, PA12 retains better dimensional stability than PA6 or PA66 because the hydrocarbon-rich backbone absorbs less water per unit mass. This is relevant for sealed sensor housings and electrical connectors in automotive under-bonnet locations where condensation is intermittent.

    The reduction in hygroscopic expansion is also observed as lower property shift after conditioning. Mechanical values measured after conditioning at 23°C and 50% relative humidity will show lower modulus than dry values, but the relative drop is smaller than for short-chain polyamides. The exact shift should be verified on moulded plaques under ISO 291 conditioning and ISO 527-1/-2 tensile testing. If dimensional validation is performed on dry parts immediately after moulding, field failures can occur after the part reaches equilibrium moisture content. For this reason, quality-control protocols for tight-tolerance PA12 parts commonly include a humidity chamber or desiccator stabilisation step before coordinate measuring.

    Chemical Contact Boundaries in Fuel, Coolant, and Halide Media

    The PA12 backbone provides resistance to aliphatic hydrocarbons, diesel, mineral oil, and many lubricating fluids. Fuel-system components such as quick-connect couplings and vapour-management bodies are common because the material maintains impact strength after fuel exposure and because the long-chain structure limits alcohol-induced softening relative to PA6. However, fuel blends containing aggressive aromatic solvents or methanol above 85% require specific validation. Alcohol uptake softens the matrix and reduces tensile modulus under sustained load. SAE J2260 or equivalent system-level fuel-line testing may be required for assembled fuel transport components, but the material itself is not a complete system qualification.

    Contact with hot ethylene glycol/water coolant above 80°C can cause surface attack or stress cracking when the component is under hoop stress. Zinc chloride solutions, chlorinated solvents, phenols, strong acids, and strong oxidising media are incompatible. Stress-cracking resistance in zinc chloride solution is sometimes used as a comparative PA12 quality indicator, but the test outcome depends on specimen geometry, solvent concentration, and applied strain. The material is not inherently flame-retardant; unreinforced PA12 typically carries a UL 94 classification of HB. Regulatory statements for REACH SVHC content, RoHS 2011/65/EU, and food-contact suitability under 21 CFR 177.1500 must be requested from the supplier for this specific grade, because finished-article compliance depends on migration testing with the intended food simulant and processing history.

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