| HS Code | 717515 |
| Density | 1.01 g/cm³ |
| Water Absorption Saturation | 1.5 % |
| Water Absorption Equilibrium 50 Rh | 0.9 % |
| Shore D Hardness Conditioned | 53 |
| Tensile Modulus Conditioned | 300 MPa |
| Tensile Strength At Break Conditioned | 26 MPa |
| Elongation At Break Conditioned | 230 % |
| Flexural Modulus Conditioned | 300 MPa |
| Charpy Notched Impact 23 C Conditioned | 80 kJ/m² |
| Charpy Notched Impact 40 C Conditioned | 30 kJ/m² |
| Melting Point | 178 °C |
| Heat Deflection Temperature 1 8 Mpa | 45 °C |
| Vicat Softening Temperature B 50 | 80 °C |
| Volume Resistivity | 1e13 ohm·cm |
As an accredited EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12, Conditioned factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 25 kg sealed moisture-proof bags of Grilamid L 25 W 40 HL X Nylon 12, conditioned and palletized for safe handling. |
| Container Loading (20′ FCL) | 20′ FCL loading of conditioned Grilamid L25 W40 HL X Nylon 12: dry, ventilated, sealed packaging to prevent moisture absorption, ensuring safe transport. |
| Shipping | EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12 (Conditioned) ships in sealed, moisture-proof bags or drums to preserve its conditioned state. Keep containers dry, avoid direct sunlight, and store away from heat sources. This material is non-hazardous; standard handling prevents dust, contamination, and physical damage during transport. |
| Storage | Store in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and open flames. Keep the original sealed container to prevent moisture absorption and contamination. Avoid exposure to strong oxidizing agents. Maintain temperatures below 25°C (77°F) for best results. Use within recommended shelf life. |
| Shelf Life | Shelf life is typically indefinite when stored in original, sealed packaging away from moisture, heat, and UV light. |
Extruded truck air brake line made from Grilamid L 25 W 40 HL X in the conditioned state is specified where the tube must pass the cold impact and burst-pressure requirements of ISO 7628-1 and SAE J844 after moisture equilibration at 23 °C and 50 % RH. The dry-as-moulded form of PA12 has lower elongation and higher modulus; conditioning to an equilibrium moisture content of 0.7 wt% to 1.0 wt% is therefore embedded in the production routing. Pellets are fed from sealed bags or dried in a desiccant dryer with a dew point of -40 °C to -30 °C at 80 °C for 4 h to 6 h to a residual moisture level below 0.10 wt% when dry feedstock is required. Melt is processed on a single-screw extruder with an L/D ratio of 24:1 to 30:1 and a compression ratio of 2.8:1 to 3.2:1. Barrel zones are held at 230 °C to 245 °C, the adapter at 240 °C to 250 °C, and the die head at 245 °C to 255 °C. A screen pack of 60/80/100 mesh and a breaker plate with 10 % to 15 % open area maintain melt pressure in the range of 15 MPa to 25 MPa at the die entry. The tube is calibrated in a vacuum tank at -0.2 bar to -0.4 bar and hauled off at 20 m/min to 60 m/min depending on outside diameter. Regrind usage in safety-critical line is limited to 15 wt% maximum and only from edge trim or approved internal scrap; no foreign off-spec material is permitted because contamination shifts cold impact performance without changing melt flow enough for routine detection.
| Standard | Application clause | Measured response in finished tube |
|---|---|---|
| ISO 7628-1 | Dimensional classes and marking | OD/ID tolerances, wall thickness variation below 0.10 mm |
| ISO 7628-2 | Performance requirements | Burst pressure, cold impact, zinc chloride resistance |
| SAE J844 | Air brake tubing tests | Heat ageing, expansion, elongation at break |
| DIN 73378 | Polyamide tubing for motor vehicles | Working pressure classes at 23 °C and 80 °C |
After calibration, the tube is cut to length, legibly marked at intervals specified in ISO 7628-1, and placed in a post-extrusion conditioning chamber at 23 °C and 50 % RH until the wall reaches 0.7 wt% to 1.0 wt% moisture. Burst pressure tests are performed at 23 °C, 80 °C, and after heat ageing; zinc chloride immersion is performed in 50 wt% aqueous ZnCl2 at the temperature and exposure duration stated in SAE J844. A production failure mode observed on single-screw extrusion lines is gel dot formation when melt temperature exceeds 260 °C; this creates local thin spots in the tube wall and reduces burst pressure before any measurable change in melt flow rate occurs. On the sizing line, a vacuum level below -0.5 bar can collapse the tube, while a vacuum above -0.1 bar permits ovality above 0.15 mm and creates an unstable push-to-connect sealing surface. The finished article is a nylon 12 tube in diameters such as 6 mm OD × 4 mm ID, 8 mm OD × 6 mm ID, and 10 mm OD × 8 mm ID; the wall-thickness tolerance is maintained within ±0.10 mm to match fitting retention forces.
Injection moulding of Grilamid L 25 W 40 HL X into cable ties requires a controlled drop in moisture from the supplied conditioned level to a process-ready level below 0.10 wt%, followed by post-mould moisture regain to 0.5 wt% to 1.0 wt%. The dominant functional requirement is the locking tab geometry: the pawl flexes during insertion, and a dry PA12 tie at -40 °C can fracture at the neck before the pawl reaches the ratchet valley. A desiccant dryer at 80 °C and -40 °C dew point for 4 h to 6 h is used before moulding; the barrel profile is set from rear to nozzle at 240 °C, 245 °C, 250 °C, 250 °C, and 245 °C, with a hot-runner manifold held at 245 °C. The gate lands are cut to 0.8 mm to 1.0 mm, and the gate thickness at the tie head is 60 % to 70 % of the nominal wall thickness of 1.2 mm, because thinner gates freeze before the packing phase is complete and reduce pawl crystallinity. Injection speed is held at 200 mm/s to 300 mm/s, with holding pressure 50 MPa to 80 MPa for 1.5 s to 3.0 s and a screw cushion of 2 mm to 4 mm. Post-mould conditioning is performed at 23 °C and 50 % RH for 48 h or in a water bath at 70 °C for 1 h. The finished tie is tested for loop tensile strength according to IEC 62275; flammability is evaluated by UL 94 V-2 at the relevant wall thickness, and the tied bundle is subjected to insertion and withdrawal force measurements after thermal cycling from -40 °C to 125 °C. A known production bottleneck is hot-runner gate sharpness; gate wear of 0.01 mm changes the shearing zone and increases the incidence of flash at the pawl tip, which later hardens and breaks in cold-condition insertion tests.
A five-layer coextrusion line running Grilamid L 25 W 40 HL X as the outer jacket over an EVOH barrier core requires separate drying of the EVOH at 80 °C for 4 h and the PA12 at 80 °C for 4 h to 6 h. The PA12 outer jacket is extruded at 240 °C to 250 °C, while the EVOH layer is limited to 210 °C to 220 °C and the adhesive tie layer is processed at 200 °C to 210 °C to avoid advanced crosslinking in the die. A spiral mandrel die with 0.5 mm to 0.8 mm annular gap is maintained at 240 °C, and the tube is vacuum-calibrated to 8 mm OD × 6 mm ID with a wall thickness of 1.0 mm. Published data for this specific five-layer sequence is limited, but industrial multi-layer fuel vapour return lines typically place the PA12 outer jacket at 20 % to 40 % of total wall thickness, the EVOH barrier at 10 % to 20 %, and the tie layers at 5 % to 8 % each. The Grilamid layer provides chemical resistance to road splash, cut resistance during routing, and low moisture uptake at 50 % RH. The finished line is tested for fuel permeation according to SAE J2260 and for quick-connector retention with fittings conforming to SAE J2044; terminal assemblies are used as gasoline fuel vapour return lines in passenger vehicle evaporative emission circuits. A process boundary is the moisture level of the EVOH layer: if EVOH is not dried below 0.10 wt%, vapour pockets form at the tie-layer interface and cause delamination during 100 °C recirculation testing.
The production of 4 mm OD × 2.5 mm ID pneumatic control line from Grilamid L 25 W 40 HL X starts with the same moisture-control discipline used in automotive tube: pellets are dried to 0.10 wt% maximum before extrusion and the finished tube is conditioned to 0.7 wt% to 1.0 wt% moisture. A single-screw extruder with a barrier screw and L/D of 24:1 runs barrel zones at 230 °C to 245 °C and a die at 245 °C; the tube is fed through a vacuum calibration sleeve with an inlet vacuum of -0.2 bar to -0.4 bar and a cooling water temperature of 40 °C to 60 °C. The targeted ovality after conditioning is below 0.10 mm, and the outer diameter tolerance is ±0.05 mm. At 23 °C the burst pressure for the 4 mm × 2.5 mm article is normally not less than four times the declared 10 bar working pressure, but lot release values are confirmed by hydrostatic test because the fitting retention depends on the plastic deformation behaviour of the tube wall. Working pressures declared by the finished-tube manufacturer are derated at elevated temperatures, with a reduction factor of 0.6 at 60 °C and 0.25 at 100 °C being common for PA12 pneumatic tubing. Pressure cycling at -40 °C is performed with clean dry air or nitrogen in a temperature chamber; the acceptance criterion is no burst, no fitting leakage, and no surface crack after the number of cycles specified by ISO 14743 for push-in connectors. The terminal product is assembled into push-to-connect fittings and used in CNC pneumatic panels, welding-cell air logic, and process instrumentation. In production, the most frequent failure mode is fitting leakage caused by tube ovality after coiling; coils are therefore cut into straight lengths and conditioned in a hanging orientation before assembly.
Snap-fit clips moulded from conditioned Grilamid L 25 W 40 HL X serve in engine-compartment line retainers where the service temperature fluctuates from -40 °C to 125 °C. The snap beam is designed with a length-to-thickness ratio of 10:1 and an undercut of 0.8 mm to 1.2 mm; at these proportions the outer fibre strain remains below 4 %, which is below the yield point of the conditioned material after ageing. The mould is a two-plate cold-runner tool; the melt temperature is held at 245 °C to 255 °C, and the mould surface temperature is set to 60 °C to 80 °C to reduce post-mould shrinkage and maintain snap geometry. The injection speed is 150 mm/s to 250 mm/s, packing pressure is 60 MPa to 90 MPa, and the switch-over point from velocity to pressure control is set at 95 % to 98 % of the shot volume. Post-mould conditioning at 23 °C and 50 % RH for 24 h to 48 h restores enough moisture to prevent brittle release from the core. Tensile and notched impact properties are verified according to ISO 527-2 and ISO 179-1 after conditioning; thermal endurance is referenced to ISO 2578. The terminal clips are used on fuel line bundles, brake sensor harness brackets, and coolant hose retainers. A process conflict occurs when mould temperature falls below 40 °C; the rapid skin freezing increases orientation in the hook base and reduces the aged retention force, even though the cold part shows acceptable dimensions. The same phenomenon is observed when a hot-runner tip is run more than 20 °C above the melt temperature, producing local molecular weight loss in the gate region that cannot be detected by normal visual inspection.
Road-salt exposure of underbody harness conduits introduces aqueous chloride salts; the decisive test is immersion in 50 wt% zinc chloride solution according to the method described in SAE J844. Corrugated PA12 conduit extruded from Grilamid L 25 W 40 HL X is produced on a corrugator line with barrel melt temperatures of 235 °C to 250 °C and a corrugator vacuum of -0.3 bar to -0.6 bar. The corrugator blocks are held at 30 °C to 50 °C to set the wall before release; the pitch-to-outside diameter ratio is maintained at 1.5:1 to preserve local flexibility. The conduit is post-conditioned to 0.7 wt% to 1.0 wt% moisture before low-temperature impact testing at -40 °C. In the zinc chloride stress cracking test, test pieces are bent around a mandrel of specified radius and immersed in the chloride bath; no surface crack may appear within the observation period. The PA12 chemistry provides resistance to zinc chloride because the amide group concentration is lower than in PA6 and PA66, reducing the solvent stress-crack sensitivity. The finished corrugated conduit is installed as ABS sensor harness protection and low-pressure air suspension line covering; connectors and clips are assembled after the conduit has stabilised at ambient moisture. The absence of zinc chloride cracking is also required for tube and tubing accessories; therefore the same immersion protocol is applied to extruded air brake line and to quick-connector bodies made from the same resin family.
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EMS-Grivory Grilamid L 25 W 40 HL X Nylon 12 is a plasticizer-modified polyamide 12 resin supplied as a ready-to-process feedstock for extrusion and injection molding. The L 25 segment identifies the base PA12 series within the EMS-Grivory product structure; W 40 is the manufacturer’s code for a semi-flexible plasticizer modification; HL denotes a heat- and light-stabilizer package; and X is the viscosity/flow subdivision used for rheological lot control. The term Conditioned in the product description does not refer to a surface treatment or pre-moistened pellet supply. It indicates that the stated mechanical data were obtained after conditioning under ISO 1110 at 23 ± 2 °C and 50 ± 10 % relative humidity until moisture equilibrium was reached. For this grade, equilibrium moisture uptake is approximately 0.7 wt% to 0.8 wt%, which is lower than the same-atmosphere equilibrium for PA6 or PA66.
Under those conditions, water absorbed into the polyamide matrix acts as a plasticizer. Tensile modulus decreases, elongation increases, and notched impact strength increases relative to dry-as-molded material. These property changes are reversible; drying restores the dry-state values. The low equilibrium moisture uptake is one reason this grade is selected for precision tubing and connector components that require dimensional stability in humid service. Conditioning for standardized property testing is performed on multipurpose test specimens according to ISO 3167, held in a climate chamber at 23 °C and 50 % RH until two consecutive daily mass measurements differ by less than 0.1 %. For 4 mm PA12 tensile bars, equilibration can take more than 60 days because moisture diffusion is relatively slow.
Typical mechanical data for natural unpigmented material show a dry-as-molded tensile modulus near 700 MPa and a conditioned tensile modulus near 450 MPa. Yield stress declines from approximately 25 MPa dry to 18 MPa conditioned, while elongation at break remains above 50 % under ISO 527-2. Notched Charpy impact strength at 23 °C rises from approximately 20 kJ/m² dry to 70 kJ/m² conditioned. Heat deflection temperature at 1.8 MPa is below 55 °C, and the differential scanning calorimetry melting peak is approximately 175 °C. The following table summarizes representative values; lot-specific certificates of analysis govern actual production lots.
| Property | Test method | Dry-as-molded | Conditioned |
|---|---|---|---|
| Density | ISO 1183 | 1.01 g/cm³ | 1.01 g/cm³ |
| Equilibrium moisture uptake at 23 °C/50 % RH | ISO 62 | — | 0.7–0.8 wt% |
| Tensile modulus | ISO 527-2 | 700 MPa | 450 MPa |
| Yield stress | ISO 527-2 | 25 MPa | 18 MPa |
| Elongation at break | ISO 527-2 | >50 % | >50 % |
| Charpy notched impact strength at 23 °C | ISO 179/1eA | 20 kJ/m² | 70 kJ/m² |
| Heat deflection temperature at 1.8 MPa | ISO 75-2 | 50 °C | 45 °C |
| DSC melting peak | ISO 11357 | 175 °C | 175 °C |
Finite-element simulations should use the 450 MPa conditioned modulus when service humidity is controlled at 50 % RH. Snap-fit geometries that are functional in dry-molded parts may become too flexible in conditioned service if not verified; conversely, parts dimensioned using dry modulus can be overstiff and show higher than predicted insertion force. Pigmented variants can shift elongation and impact values by several percentage points compared with natural material.
Pre-drying in a desiccant dryer at 80 °C for 4–6 h to a residual moisture content below 0.10 % is required before melt processing. Pellets that have been exposed to relative humidity above 60 % without sealed packaging should be re-dried before charging to hoppers. Residual moisture above approximately 0.15 % can cause hydrolysis of amide bonds during melting, producing surface roughness, diameter fluctuation, and reduced melt strength in extrusion.
Single-screw extruders with L/D between 24:1 and 30:1 and a three-zone screw having a compression ratio of 2.5:1 to 3.0:1 are suitable for tube and profile lines. Barrel temperature profiles from 190 °C in the feed zone to 240 °C at the die are common; melt temperatures above 260 °C are not recommended because plasticizer volatilization can create voids and surface defects. Injection molding uses mold temperatures of 40 °C to 60 °C. At the low end of the mold-temperature range, post-mold crystallization continues for up to 24 h, causing dimensional drift. Melt-pressure stability should be observed during extrusion; pressure fluctuation greater than 2 MPa indicates moisture-induced viscosity changes, feed instability, or incorrect temperature profile.
Shot-to-shot consistency in injection molding is sensitive to screw recovery because the plasticized melt has lower viscosity than unmodified PA12. A decompression of 2 mm to 5 mm after screw charging is typically sufficient to prevent nozzle drool. Clamp force requirements are moderate; multi-cavity tools may be run on presses rated as low as 80 t if the melt residence time is controlled and the runner system is dimensioned for low shear heating.
Automotive compressed-air brake tubing is a primary application. This grade is specified for low-temperature impact resistance and low moisture uptake. Compliance testing is typically carried out under SAE J844, DIN 73378, and ISO 7628-1. Cold-impact testing at -40 °C confirms that the plasticizer package prevents brittle fracture; burst-pressure validation is conducted above the rated service pressure after 1,000 h of heat aging per ISO 188. Cable protection conduits exploit the conditioned ductility for coiling and installation at low ambient temperatures. However, the low conditioned modulus increases sag between supports; clamping distances must be reduced compared with unplasticized PA12 or glass-filled grades.
Compared with unmodified Grilamid L 25, the W 40 variant has lower flexural stiffness and higher notched impact at subzero temperatures. Compared with glass-fiber-reinforced PA12 grades from the same supplier, tensile modulus is far lower; many reinforced grades exceed 3,000 MPa, while this grade remains below 1,000 MPa dry. Compared with PA6 and PA66, the PA12 backbone has lower density, lower water uptake, and better dimensional stability but lower tensile strength and lower heat deflection temperature. Compared with PA11, PA12 has a slightly lower melting point and lower water absorption, with comparable resistance to aliphatic hydrocarbons, hydraulic oils, and dilute chloride solutions. The HL stabilizer package differentiates this material from standard PA12 grades that may contain only thermal stabilizer; outdoor service still requires validation under ISO 4892-2 or ASTM G154 because stabilizer chemistry alone does not define UV lifetime.
This plasticized nylon 12 is not suitable for continuous immersion in hot water or steam above 80 °C, where amide hydrolysis accelerates. Concentrated mineral acids, strong bases, and some phenolic-based additives can attack or embrittle the polymer. Zinc chloride solutions above 50 °C are a known stress-cracking environment for PA12 components with high residual stress. For fuel-system components, the grade is used in low-permeation multilayer constructions, but long-term exposure to aggressive methanol blends above 15 vol% should be evaluated by ISO 175 immersion testing because published data for this specific configuration are limited. The grade is not a glass-filled structural resin; load-bearing structural brackets should use a reinforced substitution or require explicit creep validation under the expected service load and temperature.
Regulatory documentation from EMS-Grivory typically supports REACH and RoHS compliance for industrial uses, but converters must request lot-specific compliance for the exact pigment and additive package. If the material is used in electrical or electronic equipment, the RoHS certificate should be reviewed for the specific black or natural colorant because carbon black and processing aids can affect extractable-metal test results.