| HS Code | 909821 |
| Density G Cm³ | 1.04 |
| Water Absorption At Saturation | 1.9 |
| Tensile Modulus Mpa | 450 |
| Tensile Strength At Break Mpa | 40 |
| Elongation At Break | 300 |
| Flexural Modulus Mpa | 400 |
| Charpy Notched Impact Strength At 23 C | No Break |
| Melting Temperature C | 175 |
| Glass Transition Temperature C | -40 |
| Heat Deflection Temperature At 1 8 Mpa C | 35 |
| Vicat Softening Temperature C | 90 |
| Shore D Hardness | 60 |
As an accredited EMS-Grivory Grilamid L 25 W 20 Y Nylon 12, Dry factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg sealed, moisture-proof polyethylene-lined bags to keep Grilamid L 25 W 20 Y nylon 12 dry and contamination-free. |
| Container Loading (20′ FCL) | 20′ FCL: Dry nylon 12 granules packed in bags on pallets, safely stowed to prevent shifting, moisture-protected, ready for export. |
| Shipping | EMS-Grivory Grilamid L 25 W 20 Y Nylon 12 is shipped as dry granules in sealed moisture-barrier bags on pallets. Keep packaging intact, store in a cool, dry area, and protect from impact. Not regulated as dangerous goods; standard freight handling applies. Avoid prolonged exposure to humidity before processing. |
| Storage | Store Grilamid L 25 W 20 Y (Nylon 12, dry) in its original sealed container in a cool, dry, well-ventilated area. Protect from moisture, direct sunlight, and excessive heat. Keep away from strong oxidizers and ignition sources. Avoid condensation by allowing packaged material to reach room temperature before opening. Under proper conditions, shelf life is typically two years. |
| Shelf Life | Store dry, sealed, and cool. Shelf life is typically indefinite if protected from moisture and direct sunlight. |
Pre-dried Grilamid L 25 W 20 Y is converted on a single-screw extruder equipped with a 30 L/D barrier screw and a calibrated melt pump into thermoplastic air-brake tube meeting ISO 7628:2010 and SAE J844. Drying is executed in a desiccant dryer at 80 °C until pellet moisture content is ≤0.10 % by Karl Fischer titration; residual moisture above 0.15 % produces surface roughness, melt strength loss, and microvoid formation in the vacuum sizer. Barrel zones are profiled at 210 °C, 215 °C, 220 °C, 225 °C, and 230 °C, with the die head held at 230 °C and melt temperature limited to 235 °C. Exceeding 240 °C accelerates plasticizer volatilization and generates inner-surface roughness in the tube. The melt enters a vacuum calibration tank at −0.8 bar and a water bath controlled at 30 °C; a laser wall-thickness gauge monitors concentricity to ±0.05 mm. For trailer air-brake circuits with 0.96 MPa service pressure, SAE J844 burst testing requires no leakage below 4× service pressure, and cold impact at −40 °C must produce no circumferential cracking. Zinc chloride resistance is evaluated at 50 °C in a 50 % ZnCl₂ solution according to SAE J844. The compound is not released for FMVSS 106 brake-hose constructions because reinforced hose requires a different validation path. Regrind is excluded from certified air-brake tube; in non-safety industrial tube, up to 15 % clean post-industrial regrind is permitted only after verified drying below 0.10 % moisture.
In retractable pneumatic coil assemblies, the dominant failure mode after repeated flex cycling is not tensile yield but inner-wall buckling at the helix compression point. Spiral-formed tube from this grade is extruded with an outside diameter of 6.0 mm and a wall thickness of 1.0 mm, then heat-set on a rotating mandrel at 135 °C for 8 min to fix the coil radius. Coiling raises local elongation to 5–7 % on the outer curvature; if plasticizer migration has increased Shore D hardness above 65, the outer wall develops stress whitening and eventually a longitudinal split. Low plasticizer mobility is checked at incoming-resin level by annealing a 2 mm plaque at 150 °C for 24 h and measuring mass loss below 0.5 %. Finished coils are tested to DIN 73378 and ISO 5774 for dimensional stability, burst retention, and flexural fatigue. Burst pressure for a new 6.0 mm outer-diameter coil at 23 °C is typically not less than 3.5 MPa; after 500 h at 100 °C, retained burst pressure must remain above 2.8 MPa. Production lines that run melt temperatures above 235 °C during coil extrusion produce higher initial flexibility but fail the aged burst requirement because plasticizer loss increases crystallinity at the inner wall. The same mechanism limits continuous service temperature to 90 °C in mobile machinery applications. Pneumatic control panels and automated assembly cells use the resulting coil where small bend radius and kink recovery are required after prolonged storage in coiled configurations.
| Parameter | Tube extrusion | Injection molding | Release limit |
|---|---|---|---|
| Predrying | 80 °C / 4–6 h | 80 °C / 4–6 h | moisture ≤ 0.10 % |
| Melt temperature | 225–235 °C | 230–240 °C | ≤ 240 °C |
| Sizer water / mold temperature | 30 °C vacuum −0.8 bar | 50 °C | — |
| Regrind fraction | 0 % certified tube | up to 20 % non-safety fittings | — |
| Dew point of dryer | −30 °C | −30 °C | — |
Drag-chain cable jackets and automotive sensor-cable sheaths are extruded from this grade with pressure tooling that maintains a tight jacket-to-core bond at a melt pressure of 12–18 MPa. Conductor-core preheat to 80 °C prevents quench-induced shrinkage and intermittent jacket thickness below 0.4 mm. Line speed is matched to a cooling water temperature of 40 °C to reduce frozen-in orientation; after 24 h at 23 °C, jacket samples are tensile-tested per ISO 527-1 and ISO 527-2. Elongation at break remains above 250 % for dry-as-extruded jacket material, while moisture conditioning at 50 % RH lowers tensile modulus without changing the minimum bend radius. Crush resistance is evaluated according to the EN 50363 series for low-voltage sheathing compounds or ISO 6722 for 60 V road-vehicle cables. Where the cable is routed through rolling flex tracks, a 90° bend test with a mandrel diameter 3× the cable outer diameter is applied; outer-radius jacket fracture before 10,000 cycles indicates either residual moisture above 0.15 % or a withdrawn plasticizer layer at the inner die wall. The grade contains no halogenated flame retardants; cables requiring IEC 60332-1 single-wire flame-spread compliance are not specified in this material without an outer flame-retardant overjacket. Long-term aging at 125 °C is bounded by oxidative discoloration and tensile retention tests per ISO 188; exposure beyond 1,000 h can increase seam-line brittleness. Automotive power and signal harnesses in continuous-flex machine axes and robot dress packs account for most high-volume use.
Push-to-connect fittings for 6 mm and 8 mm nylon brake tubing are injection molded from predried granules in a closed-loop desiccant hopper at 80 °C for 5 h. Nozzle melt temperature is held between 230 °C and 240 °C; mold temperature is set to 50 °C with a constant-flow hot runner and valve gate to minimize frozen-in stress in the collet retaining arms. The collet is a thin-wall snap-fit element with a gate land thickness of 0.8 mm; injection speed is profiled from 40 mm/s to 25 mm/s to prevent jetting at the far end of the cavity. After molding, parts are conditioned for 24 h at 23 °C and 50 % RH, then impact-tested per ISO 179/1eA at −30 °C on notched specimens cut from the gate region. A minimum notched Charpy impact strength of 10 kJ/m² is used as an internal release threshold for production lots; the test is correlated to snap-fit insertion force after 500 temperature cycles between −40 °C and 80 °C. Tensile properties are measured per ISO 527-1 and ISO 527-2. Regrind may be re-introduced up to 20 % in non-safety fittings if the regrind fraction is re-dried at 80 °C for 4 h and if the melt flow index per ISO 1133-1 remains within a 15 % band from virgin material. The material is not suitable for direct contact with urea solutions above 60 °C because plasticized PA12 undergoes plasticizer extraction and localized tensile strength loss; immersion validation per ISO 527-2 after 1,000 h in 32.5 % urea at 60 °C is mandatory before any field use. Published data for multiaxial impact of this specific plasticized PA12 configuration is limited; the Charpy threshold therefore remains the operative release criterion.
Peristaltic pump tubing from Grilamid L 25 W 20 Y is produced on a vacuum-calibrated extrusion line equipped with a 2-axis laser gauge scanning at 500 Hz to control wall-thickness variation below ±0.05 mm. This tolerance is required for consistent occlusion at pump-head rotor speeds between 30 rpm and 150 rpm; local deviation greater than 0.07 mm creates under-occlusion and reduced suction lift. The tubing is annealed in-line at 130 °C for 10 min to stabilize flex modulus and reduce wave-like surface defects. Mechanical properties are measured on dried samples per ISO 527-1 and ISO 527-2. For flex fatigue assessment, a custom test rig clamps the tube between two plates and cyclically compresses it to 50 % of the outer diameter at a frequency of 3 Hz until rebound loss exceeds 5 %. Production lots are accepted only if rebound loss after 10,000 cycles remains below 5 % and burst pressure per ISO 1402 at 23 °C remains above 2.5 MPa. This material is an industrial extrusion grade; no USP Class VI or ISO 10993 certification is declared. For food-contact use, compliance with FDA 21 CFR 177.1500 or EU Regulation 10/2011 must be evaluated separately on the finished tube and fitting assembly. Contact with strong mineral acids and high-aromatic hydrocarbon solvents should be avoided because the plasticizer is preferentially extracted, causing hardening and loss of rebound. Chemical dosing pumps and stationary laboratory suction lines are the principal terminal products.
Harness-management sleeving in rail-vehicle cable looms uses the material as spiral-cut wrap with a profile wall of 0.8 mm and an inside diameter from 6 mm to 25 mm. The profile is extruded with a low-shear screw at 210–230 °C, slit, and then heat-set at 140 °C to lock the spiral geometry. Because the grade is not flame-retardant, the sleeving cannot be specified as the sole protective layer inside rolling stock where EN 45545-2 hazard level HL2 or HL3 requires flame-spread and smoke-density control; it is instead overbraided with a halogen-free flame-retardant yarn or installed in metallic conduits. Abrasion resistance is tested according to ISO 6722 scrape-abrasion requirements for cable-protection components, with no exposure of the bundled conductor after 1,000 cycles under a 7 N load. Low-temperature flex is evaluated at −40 °C by mandrel bend test; fractures at this temperature indicate that the material absorbed moisture during extrusion. Drying of granulate at 80 °C for 4 h and maintaining a closed-loop conveying system with a dew point below −20 °C are standard controls. End products include cable-carrier wraps, robotic dress packs, and stationary control-panel harnesses where repeated flexing requires Shore D hardness below 60 and brittle temperature below −50 °C.
| Sector | Standard / method | Critical criterion |
|---|---|---|
| Air-brake tube | SAE J844, ISO 7628 | cold impact at −40 °C, burst 4× service |
| Pneumatic coil | DIN 73378, ISO 5774 | aged burst ≥ 2.8 MPa after 500 h at 100 °C |
| Cable jacket | ISO 6722, ISO 527-1/2 | elongation at break > 250 % |
| Quick-connect fittings | ISO 179/1eA | notched Charpy ≥ 10 kJ/m² at −30 °C |
| Peristaltic tube | ISO 1402, ISO 527-1/2 | wall ± 0.05 mm, rebound loss < 5 % |
| Harness sleeving | ISO 6722 scrape, −40 °C bend | no conductor exposure after 1,000 cycles |
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EMS-Grivory Grilamid L 25 W 20 Y is a plasticised, heat-stabilised polyamide 12 moulding compound supplied in a dry, low-moisture state. The base polymer belongs to the PA12 family under ISO 1043-1; the supplier designation L 25 identifies the viscosity class, W 20 indicates a nominal plasticiser content of 20% by mass, and Y denotes a heat-stabilisation package. The dry-state designation refers to residual moisture controlled inside the supplier’s sealed packaging and cannot be treated as persistent after the package is opened or exposed to ambient humidity. Conversion is typically performed by injection moulding or profile extrusion into flexible automotive tubing, pneumatic conduits, cable sheathing, and strain-relief components. These applications exploit PA12’s low moisture uptake, resistance to zinc chloride stress-cracking, and retention of flexibility at sub-zero temperatures.
The plasticiser reduces stiffness and surface hardness relative to unplasticised PA12 while increasing elongation and low-temperature impact. Representative values from supplier documentation for dry-as-moulded specimens are compiled in Table 1. The tensile modulus is lower than that of unplasticised PA12 by roughly a factor of three; this shifts design toward flexible conduit, snap-fit, and closure functions rather than structural support. Because PA12 is hygroscopic, dry-as-moulded values for tensile modulus and yield stress are typically higher than conditioned values. Article testing at 23°C and 50% relative humidity may therefore exhibit lower stiffness and higher impact. Conditioning under ISO 1110 accelerates moisture uptake but does not necessarily replicate long-term plasticiser migration in service.
| Property | Standard | Representative value or range |
|---|---|---|
| Density | ISO 1183-1 | 1.01 g/cm³ |
| Tensile modulus, 23°C | ISO 527-1/2 | 400 MPa |
| Tensile stress at yield, 23°C | ISO 527-1/2 | 15 MPa |
| Nominal elongation at break, 23°C | ISO 527-1/2 | >200% |
| Charpy notched impact, 23°C | ISO 179-1/1eA | No break |
| Shore D hardness | ISO 868 | 55 |
| Melting point, DSC | ISO 11357-3 | 178°C |
| Vicat softening temperature VST/B50 | ISO 306 | 130°C |
| Water absorption, 23°C/50% RH | ISO 62 | <0.7% by mass |
To retain these properties during conversion, moisture must be managed before melt processing. The dry-as-supplied condition should be verified by Karl Fischer titration under ISO 15512; a target residual moisture content below 0.10% by mass is required before the material enters the melt. If packaging has been opened or ambient relative humidity has exceeded 60%, a desiccant dryer with a dew point of -30°C and air temperature of 80°C for 4 h to 8 h is typically used. Injection moulding melt temperatures are commonly held between 230°C and 250°C, with mould temperatures from 40°C to 60°C to stabilise quench rates and dimensional reproducibility. On production-scale machines, immersion pyrometer checks are preferable to barrel setpoints because shear heating can raise actual melt temperature by 5°C to 10°C. A three-zone screw with an L/D ratio of at least 20:1 and compression ratio near 2.5:1 reduces shear heating; screws with high-shear mixing elements should be avoided because excessive mechanical energy input can volatilise low-molecular-weight plasticiser fractions. Residence time above 260°C should be limited to 8 minutes or less because thermo-oxidative chain scission in PA12 reduces molecular weight and lowers elongation at break. Surface splay, jetting, and gate blush are common process-related defects in low-viscosity plasticised PA12. Splay indicates residual moisture or volatilised plasticiser; jetting appears at low melt temperatures or undersized gates; gate blush increases at high injection speeds because low melt strength permits unstable fountain flow. These failure modes are managed by confirming residual moisture below 0.10%, maintaining melt temperature within the 230–250°C range, and using lower injection velocities with larger gates.
Regrind addition above 20% by mass can shift melt viscosity and plasticiser distribution. Published data for this specific grade at high regrind ratios is limited; therefore, lot-to-lot tensile testing under ISO 527-1/2 and notched impact testing under ISO 179-1/1eA are required when regrind exceeds 20% by mass. Melt volume-flow rate monitoring under ISO 1133-1 provides a comparative indicator of degradation-induced viscosity shifts. Production-scale twin-screw extrusion of similar plasticised PA12 compounds has shown that uncontrolled edge-trim regrind can shift melt pressure by more than 10% at 30% recycle if first-pass barrel temperatures exceed 250°C because plasticiser loss changes viscosity. This grade should therefore be processed with closed-loop regrind monitoring and periodic tensile-elongation checks.
In service, external plasticiser migration may occur in hot mineral oil, ethanol-blended fuel, or closed-cell elastomer contact. The result is surface hardening, reduced reversible elongation, and extraction of low-molecular-mass species. Direct contact with unsealed polycarbonate or PMMA components is not recommended because migration of the plasticiser can cause environmental stress cracking in the transparent resin. Flexible tubing manufacturers must therefore validate article performance under the final fluid-contact and temperature cycle, not solely from resin datasheet values.
This material should not be specified for continuous structural load-bearing above approximately 80°C because the plasticiser and the PA12 melting point of approximately 178°C limit creep resistance. The low equilibrium water absorption under ISO 62 at 23°C/50% RH—typically below 0.7% by mass—provides dimensional stability under atmospheric humidity variation but does not compensate for the low tensile modulus. Where tensile modulus above 2500 MPa is required, unplasticised or glass-fibre-reinforced polyamide grades should be evaluated instead. Chemical resistance is broad in neutral oils, greases, fuels, and salt solutions. However, strong mineral acids, formic acid, and certain phenolic compounds can degrade PA12. Prolonged exposure to hot water above 80°C may cause hydrolytic degradation; use in hot-water pressure vessels is not recommended.
Relative to unplasticised PA12, the W 20 plasticiser lowers tensile modulus and surface hardness while increasing elongation and low-temperature impact; the trade-off is lower Vicat softening and reduced upper service temperature. At sub-zero temperatures, the plasticised grade retains impact better than unplasticised PA12, but the ductile-to-brittle transition temperature depends on plasticiser content and conditioning state. Published data for this specific configuration at -40°C should be requested from supplier low-temperature Charpy curves before specifying cold-weather under-bonnet joints. Relative to PA6 and PA66, the PA12 base offers lower density—approximately 1.01 g/cm³ versus 1.14 g/cm³ for PA66—lower water absorption, and better resistance to zinc chloride stress-cracking. Unfilled PA66 typically exhibits a tensile modulus near 2700 MPa under ISO 527-1/2, whereas this plasticised PA12 grade is approximately 400 MPa. PA12 also melts near 178°C, compared with 262°C for PA66, reducing its use under sustained thermal load. These differences define the boundary between flexible conduit and rigid structural applications.
Article-level compliance remains the converter’s responsibility. For polyamide tubing used in road vehicle air systems, finished article requirements under ISO 7628 include burst pressure, low-temperature impact, and zinc chloride resistance. General automotive polyamide tubing may reference DIN 73378 for dimensional and mechanical requirements. Cable-protection conduits are normally validated for compression, impact, and flammability under the end-use specification. Food-contact use is not established by the resin alone; migration testing under EU 10/2011 or 21 CFR 177.1500 must be completed on the final article. The compliance matrix in Table 2 identifies the relevant standards and regulations for finished articles.
| Requirement | Standard or regulation | Validation scope |
|---|---|---|
| REACH | EU 1907/2006 | Monomer and additive registration; final article obligations depend on composition |
| RoHS | EU 2011/65/EU with EU 2015/863 | Homogeneous material threshold verification by converter |
| Automotive air-brake tubing | ISO 7628 | Burst pressure, low-temperature impact, resistance to zinc chloride |
| Automotive polyamide tubing | DIN 73378 | Dimensional and mechanical requirements on finished tube |
| Food-contact articles | EU 10/2011 or 21 CFR 177.1500 | Article-specific migration testing; resin datasheet alone not sufficient |
| Moisture determination | ISO 15512 | Karl Fischer titration for drying validation before melt processing |
| Melt stability | ISO 1133-1 | Melt volume-flow rate monitoring for viscosity shift control |