| HS Code | 905837 |
| Density | 1.23 g/cm³ |
| Water Absorption At Saturation | 1.5% |
| Tensile Modulus Dry | 9500 MPa |
| Tensile Strength At Break Dry | 150 MPa |
| Elongation At Break Dry | 3% |
| Flexural Modulus Dry | 8500 MPa |
| Flexural Strength Dry | 200 MPa |
| Charpy Impact Strength Notched Dry 23 C | 13 kJ/m² |
| Melting Point | 178 °C |
| Heat Deflection Temperature 0 45 Mpa | 175 °C |
| Heat Deflection Temperature 1 80 Mpa | 170 °C |
| Volume Resistivity | 1.0E13 Ohm·cm |
As an accredited EMS-Grivory Grilamid LV-3A H Nylon 12, 30% Glass Fiber Filled, Dry factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packed in 25 kg sealed, moisture-proof bags to maintain dryness and protect the 30% glass-filled Nylon 12 granules. |
| Container Loading (20′ FCL) | 20′ FCL container loading of dry Grilamid LV-3A H nylon 12 pellets, 30% glass fiber filled, palletized in sealed bags. |
| Shipping | Ship as non-hazardous dry granules in sealed, moisture-barrier bags or drums. Protect from humidity and direct sunlight. Avoid excessive heat and mechanical damage. Store upright, keep dry, and use proper lifting equipment for bulk containers. No special transport restrictions; standard protective gloves and dust masks recommended during handling. |
| Storage | Store in a cool, dry area in sealed, original containers to prevent moisture absorption, as the nylon is hygroscopic. Avoid exposure to high humidity, direct sunlight, and temperatures above 25°C (77°F). Keep away from incompatible materials. Properly sealed storage maintains dryness and ensures optimal processing performance. |
| Shelf Life | Shelf life is approximately two years when stored sealed, dry, and cool in original packaging away from moisture. |
Processing of Grilamid LV-3A H, a 30% glass fiber reinforced polyamide 12, requires pre-drying to below 0.10% residual moisture by weight before any melt processing. In desiccant dry-air systems, an inlet air dew point of −30°C to −40°C and a bed temperature of 80°C for 4–8 h are used when sealed packaging has been opened or when ambient relative humidity exceeds 60%. Residual moisture above 0.10% produces splay, weak weld lines, and hydrolysis-related viscosity reduction in the melt phase. The dry condition is the reference state for the mechanical values cited below.
In multi-layer fuel line systems, rigid quick-connect bodies, retainer clips, and flange adapters are injection-molded from Grilamid LV-3A H because the 30% glass fiber loading shifts the dry-as-molded tensile modulus into the 7,000–8,500 MPa band under ISO 527-1/-2, while the PA12 backbone holds equilibrium moisture uptake below 0.8% at 23°C and 50% RH per ISO 62. The practical result is a smaller post-molding dimensional swell than PA66-GF30 parts exposed to the same fuel vapor and humidity environment. Tooling for quick connectors typically uses two to four core pulls and a direct sprue or hot-tip gate on a non-visible flange. Wall sections between 0.8 mm and 2.0 mm demand a melt temperature of 240–260°C and a mold temperature of 80–100°C; lower mold temperatures produce a frozen skin layer that freezes glass fibers at the surface and increases surface roughness. At the knit-line confluence around the tube bore, fiber orientation becomes random, and mechanical strength is controlled by the matrix. Weld-line tensile values in glass-filled PA12 connectors commonly fall to 40–50% of non-weld reference values measured under ISO 527-1/-2; published data for this exact grade and gate geometry is limited, so pilot tool trials with three to five gate positions are required. Pressure integrity is verified by air decay testing at 5 bar with a 0.5 cm³/min leak threshold, while pull-off and insertion force limits are set through OEM-specific variants of SAE J2044.
Pneumatic valve islands and manifolds convert a single air supply into multiple controlled circuits; the manifold block is molded with internal galleries and fitted with cartridge valves or spool valves. In glass-reinforced PA12, the limiting parameter is not short-term tensile strength but long-term oxidative aging at the 80–100°C continuous air supply boundary. The heat-stabilized formulation of Grilamid LV-3A H is intended to resist thermal oxidation, but the usable upper bound must be validated by retention of notched Charpy impact after aging. A typical production floor test sequence involves aging specimens at 120°C for 500 h and comparing notched Charpy impact under ISO 179-1/1eA; failures often appear first at the sprue-to-cavity transition where fiber orientation is most anisotropic. Manifold bodies operate at 6–10 bar supply pressure with solenoid pilot valves cycling at 3–5 Hz; pressure impulse testing is conducted at 1×106 cycles from 0 bar to 10 bar at 80°C on a test stand fitted with a piezo-resistive pressure transducer. If the transducer detects a pressure drop greater than 0.1 bar/s during the closed-valve phase, the cavity is rejected. The mold should be fitted with sequential valve gates to move the weld line away from the cartridge-valve seat; an unmelted glass bundle at the seat produces chatter marks and outer diameter run-out above 0.05 mm. Published component-level data for this grade in pneumatic manifold duty is limited, and acceptance testing is typically performed on five consecutively molded shots per cavity.
In commercial vehicle air-brake circuits, push-in fittings are exposed to road spray containing zinc chloride and calcium chloride deicing brines. If the material specification excludes hot zinc chloride immersion, PA12-GF30 is selected over PA66-GF30 because PA12 absorbs less road salt solution and retains a higher fraction of its dry notched Charpy impact at −40°C. Test programs for such fittings commonly follow the nylon tubing requirements of SAE J844 for the mating tube, while the fitting itself is subjected to 1×106 pressure cycles from 0 bar to 10 bar at 80°C. Annealing of molded fitting bodies at 120°C for 2–4 h after molding increases crystallinity and reduces internal residual stress, which improves resistance to salt-spray cracking. The main limitation is not heat but chemical degradation on continuous exposure to zinc chloride solutions above 60°C; published long-term data for this specific grade in concentrated road salt is limited, and field validation through 24 weeks of cyclic salt spray is mandatory. Threaded and push-in features are molded with collapsible cores rather than machined after molding, because machining removes the glass-rich skin and exposes the core layer to stress-corrosion attack. The acceptable leak rate after pressure cycling is typically set at 1 cm³/min at 7 bar using a volumetric leak test.
Diaphragm metering pumps for hydrocarbon additives and water-glycol mixtures use a molded pump head and internal wet-end components that must maintain insert-to-seal concentricity through dry-out and re-wetting cycles. In Grilamid LV-3A H, the combined effect of 30% glass fiber and the low-moisture PA12 matrix reduces the post-molding dimensional shift between dry-as-molded and service equilibrium. Seal groove diameters are held to IT8 or tighter using injection-compression molding or a two-stage packing profile; a short initial fill to 95–98% of cavity volume followed by a low-speed packing phase reduces jetting around ceramic or PTFE insert pins. Weld lines are positioned away from the seal-mounting plane by sequential valve gating. If the weld line crosses the O-ring groove at an included angle below 30°, helium leak rates have exceeded 1×10-6 mbar·L/s in prototype trials, although the threshold depends on groove surface finish and insert temperature. The material is not recommended for continuous immersion in strong mineral acids or oxidizing bleach solutions; for hydrocarbon and glycol service up to 80°C, the wet-end housing has been qualified using 1,000 h pressure-aging tests at 6 bar and 70°C.
| Standard / Directive | Test or specification area | Application relevance |
|---|---|---|
| ISO 527-1/-2 | Tensile properties, test speed 5 mm/min | Dry-as-molded modulus for connector and manifold body design |
| ISO 179-1/1eA | Notched Charpy impact | Low-temperature fitting toughness and aged-part acceptance |
| ISO 75-1/-2 | HDT under 1.8 MPa | Charge-air cooler caps and hot manifold housings |
| ISO 1183 | Density | Mass creep and part weight audit |
| ISO 62 | Water absorption | Dimensional change relative to PA66-GF30 |
| SAE J844 | Nylon air brake tubing | Reference for mating truck air-brake fittings |
| REACH Regulation (EC) No 1907/2006 | Substance registration and SVHC screening | EU market compliance verification |
| RoHS Directive 2011/65/EU | Restricted substances in homogeneous materials | Lead, mercury, cadmium, hexavalent chromium, PBB, PBDE limits |
Charge-air cooler end caps and inlet/outlet adapters molded from Grilamid LV-3A H are exposed to hot compressed air on the boost side and under-hood radiant heat. The glass fiber reinforcement raises the heat deflection temperature under 1.8 MPa into the 150–170°C range when measured by ISO 75-1/-2, but continuous under-hood operation above 120°C still requires thermal oxidation screening. Fiber emergence at the sealing face is controlled by running mold temperatures above 100°C and by using a cooled sprue bushing to prevent gate blush. Burst testing of prototype end caps is performed hydrostatically at 5–7 bar and 120°C with the part submerged in coolant; the failure mode in short-shot regions is typically a brittle split along the glass-fiber flow boundary. Published data for this specific part configuration is limited, so each tool iteration must be validated by cycling between −40°C and 140°C for 500 cycles before production approval.
Dry-running actuator gear trains and cam followers in textile and packaging machinery are candidate applications for Grilamid LV-3A H where PA66-GF30 tooth profiles show wide backlash changes due to moisture absorption. The material’s lower moisture uptake under 23°C/50% RH conditions translates to a narrower backlash drift across seasons in non-climate-controlled plants. Gear teeth are molded with a full-round or trapezoidal gate at the hub, and the cavity is packed at 60–80 MPa hydraulic holding pressure to minimize sink at the root diameter. Tooth flank failures after 1×106 load cycles are typically abrasive wear and not bending fatigue; adding external lubrication or selecting a polished cavity surface reduces fiber pull-out at the tooth tip. The grade is not a substitute for machined metal gears in high-load power-transmission stages, because the short-glass reinforcement does not provide the tooth root fatigue margins of carbon-fiber filled PEEK or metal gear steels. Published data for this exact grade in gear testing under ISO 6336 is limited, so replacement of metal gears must be validated at target torque and cycle count.
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EMS-Grivory Grilamid LV-3A H is a heat-stabilized polyamide 12 injection-molding resin reinforced with 30% glass fiber by weight. The designation LV identifies a long-fiber pultrusion route that preserves fiber length during pelletization, while H denotes the stabilizer package intended for prolonged hot-air and hot-fluid exposure. Under ISO 1043-1:2011 the material is designated PA12-GF30. The “Dry” condition in supplier documentation refers to the dry-as-molded test state, not to a permanently moisture-free supply condition; mechanical values are generated on specimens with residual moisture below 0.05 wt% rather than after standard laboratory conditioning at 23 °C and 50% relative humidity.
Pre-drying is required when ambient relative humidity exceeds 60%, because polyamide 12 pellets absorb surface moisture rapidly under plant-floor conditions. A dehumidified-air dryer set at 80 °C for 4 h to 8 h is standard practice; the hopper should maintain a dew point of -30 °C or lower. Moisture at the feed throat should be verified with a Karl Fischer titrator or calibrated moisture analyzer and kept below 0.06 wt%. Drying temperatures above 90 °C should be avoided because prolonged exposure can degrade the heat-stabilization package and discolor the pellets without materially improving drying rate.
Barrel settings from 230 °C to 270 °C are typical, with nozzle melt temperature not exceeding 280 °C. The practical processing window is narrow at the upper boundary because long-glass fiber raises melt viscosity and reduces thermal conductivity, slowing screw recovery and increasing residence time at the barrel wall. On a 35 mm three-zone screw mounted in an 800 kN hydraulic molding machine, a rear-zone setting near 230 °C and a nozzle setting near 260 °C is commonly used to balance fiber attrition against fill pressure. Melt cushion should be held between 3 mm and 6 mm. A larger cushion extends residence time and breaks fibers, while a smaller cushion transfers shot-weight variation to the cavity.
Mold temperature should be maintained at 60 °C to 100 °C. For structural parts with tight post-mold shrinkage limits, 80 °C is frequently selected. Shrinkage is anisotropic in long-glass polyamide 12. Under ISO 294-4, typical flow-direction shrinkage is 0.1% to 0.3%, while transverse shrinkage is 0.4% to 0.6%. Multi-cavity tools with unbalanced runners should be avoided where possible because flow-distance differences alter fiber orientation and therefore part dimensions and impact behavior.
Mechanical data generated under ISO 527-1/-2:2012 on dry specimens indicate a tensile modulus near 9.2 GPa, tensile strength at break near 140 MPa, and elongation at break of 4%. These values are orientation-dependent; gated tensile plaques show higher stiffness along the fiber direction and lower transverse ductility. At knit lines, glass-fiber reinforcement does not bridge the weld effectively, so design calculations should apply a flow-direction tensile-strength derating factor of approximately 0.7. Notched Charpy impact measured under ISO 179-1/1eA:2010 is strongly influenced by gate location, fiber length, and moisture state; the producer’s published value for a standard edge-gated specimen should be consulted rather than using unnotched data as a substitute.
| Property | Test method | Typical value |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.23 g/cm³ |
| Water absorption, saturation | ISO 62:2008 | 1.1% |
| Tensile modulus, dry | ISO 527-1/-2:2012 | 9.2 GPa |
| Tensile strength at break, dry | ISO 527-1/-2:2012 | 140 MPa |
| Elongation at break, dry | ISO 527-1/-2:2012 | 4% |
| Melting temperature | ISO 11357-3:2018 | 178 °C |
The selection of PA12-GF30 over short-glass PA66-GF30 is often driven by the saturation moisture difference. PA66-GF30 can absorb 5.5% to 6.0% water at saturation, whereas Grilamid LV-3A H is specified at 1.1% water absorption under ISO 62:2008. The result is a smaller conditioned tensile-modulus shift and reduced moisture-induced dimensional growth in snap-fit retainers, bearing journals, and electrical housings. The coefficient of linear thermal expansion in the flow direction is typically in the range of 30 µm/m·K to 40 µm/m·K, with higher values in the transverse direction. Published comparative data for the specific fiber orientation of this grade remain limited, but the low saturation moisture uptake is the primary dimensional-stability argument in humid service.
Low-temperature performance is also distinct from glass-reinforced PA66. Polyamide 12 has a lower glass transition than PA66, which preserves more ductile character below -20 °C. Long-glass reinforcement increases modulus without introducing the sub-zero brittleness often observed in high-modulus short-glass systems. This combination is relevant for cable clips, cold-side automotive fasteners, and pneumatic fittings that are assembled in outdoor environments.
Chopped-strand PA12 compounds frequently exhibit a post-molding mean fiber length below 0.3 mm. The pultruded long-glass route used for LV-3A H retains longer fiber bundles in the pellet and improves the fraction of fibers exceeding 1 mm after injection molding. The longer fiber network deforms by fiber pull-out and bridging during crack extension, increasing the energy absorbed per unit fractured area at the same nominal glass loading. The trade-off is rheological: LV-3A H requires higher injection pressure and has lower apparent melt flow than a short-glass PA12 of identical glass content. Cold-runner gates should have a land length below 1 mm and a diameter of at least 0.8 mm; hot-runner channels should be at least 3 mm in diameter. Narrow restrictions shear the fiber bundles and erase the impact advantage.
Applications are concentrated in structural clips, fluid connectors, cable-management brackets, pneumatic valve bodies, and under-hood retainers where cyclic mechanical load, road salt, and temperature cycling coexist. The material is not intended for flexible living hinges, thin-walled flexible closures, or low-modulus sealing features; unreinforced PA12 has a tensile modulus near 1.5 GPa, while LV-3A H is approximately five times stiffer in the dry state.
Calcium chloride and sodium chloride road-salt solutions stress polyamide components by promoting plasticization, hydrolysis, and metal-ion interactions at the amide group. PA12 contains fewer amide bonds per unit chain length than PA66, giving a reduced hydrolysis rate and improved resistance to zinc chloride and calcium chloride stress cracking. Grilamid LV-3A H is therefore applied to underbody fasteners, sensor brackets, and brake-system clips that encounter de-icing salts. The heat-stabilized package also supports continuous dry-heat exposure in structural parts, but it is not a universal replacement for hydrolysis-stabilized PA66 in ethylene glycol service above 120 °C. Long-term coolant-immersion parts require OEM-specific chemical-resistance protocols or stress-rupture testing under ISO 22088-3 before substitution.
Batch release should record glass-fiber content by ash analysis under ISO 3451-1 and moisture content at the hopper inlet. Post-industrial regrind addition is commonly limited to 25% by weight in non-appearance parts; higher regrind fractions reduce fiber length and increase shot-to-shot viscosity variation. Regrind should be homogenized with virgin pellets before drying, and the ratio should not exceed 1:3 unless the molder has qualified the specific part through dimensional capability studies. Food-contact or drinking-water suitability must be confirmed for the finished article under FDA 21 CFR 177.1500 or EU 10/2011; the base polyamide 12 designation alone is not sufficient for compliance. Flammability classification under UL 94 is thickness- and color-dependent and must be established from the material certificate for the final molded part. Avoid long-term contact with concentrated sulfuric acid, strong oxidizing acids, and phenol-based fluids at elevated temperature, because these media can swell and stress-crack polyamide 12 systems.