| HS Code | 982428 |
| Product | EMS-Grivory Grilamid L 20 EC PA12-CD25 |
| Material Class | Polyamide 12 (PA12) |
| Filler Type | Conductive carbon black |
| Filler Content | 25% |
| Density | 1.13 g/cm³ |
| Melting Point | 178 °C |
| Glass Transition Temperature | 45 °C |
| Tensile Modulus | 2500 MPa |
| Tensile Strength At Yield | 45 MPa |
| Elongation At Break | 15% |
| Charpy Impact Strength 23 C | No break |
| Charpy Notched Impact Strength 23 C | 5 kJ/m² |
| Heat Deflection Temperature 1 8 Mpa | 50 °C |
| Volume Resistivity | 1000 Ω·cm |
| Surface Resistivity | 100000 Ω/sq |
| Water Absorption 50 Rh | 0.7% |
As an accredited EMS-Grivory Grilamid® L 20 EC PA12-CD25 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Grilamid® L 20 EC PA12-CD25 is supplied as granules in moisture-proof sealed bags, quantity 25 kg per bag. |
| Container Loading (20′ FCL) | 20′ FCL: load palletized 25 kg sealed bags, secure well, keep dry and ventilated to prevent moisture absorption. |
| Shipping | Ship Grilamid® L 20 EC PA12-CD25 as non-hazardous plastic granules in sealed, moisture-proof packaging. Keep dry, avoid direct sunlight and high humidity during transit. Standard truck or container shipping is suitable; no dangerous goods declaration required, though care should be taken against crushing and condensation. |
| Storage | Store Grilamid® L 20 EC in its original, unopened packaging in a cool, dry area away from direct sunlight, heat sources, and moisture. Keep containers tightly sealed when opened to prevent water absorption, which can affect processing or performance. Avoid excessive humidity and temperature fluctuations. Under proper conditions, shelf life is typically several years from shipment. |
| Shelf Life | When stored unopened in dry, cool conditions, EMS-Grivory Grilamid® L 20 EC PA12-CD25 has a shelf life of at least two years. |
In automotive gasoline and diesel fuel vapour return lines, EMS-Grivory Grilamid L 20 EC PA12-CD25 is processed directly as the static-dissipative inner layer to prevent electrostatic charge accumulation from flowing non-conductive hydrocarbons. The compound is normally introduced at 100 wt% as the inner barrier layer, while the finished tube wall consists of an inner conductive layer of 0.1 mm to 0.3 mm thickness and a non-conductive PA12 outer jacket; when dilution with virgin PA12 is required to adjust surface resistance in less critical sections, addition ratios of 25 wt% to 50 wt% L 20 EC are used with batch-wise resistance revalidation because carbon black percolation is non-linear. Industry compliance relies on SAE J2260 for non-metallic fuel tubing, ISO 19013-1 for rubber and plastic fuel hose constructions, and DIN 73379-1 for fuel line material approval; surface resistivity is verified according to ISO 60093 or IEC 62631-3-2. Downstream manufacturing is performed on multi-layer coextrusion lines in which a barrier screw single-screw extruder with 30:1 L/D ratio feeds the inner layer through a spiral mandrel die; the melt temperature window is 220°C to 250°C, and the material must be pre-dried in a desiccant dryer at 80°C to 90°C until the moisture content falls below 0.10%, as measured by ISO 15512:2019 Karl Fischer titration. Production-scale failure modes associated with this layer include visible surface roughness and localized resistivity spikes when undried pellets release water into the melt, which hydrolyzes the PA12 backbone at processing temperatures above 250°C; additionally, excessive screw speed in the inner layer extruder can fracture the carbon black particle network and raise measured tubing resistance above acceptable limits. The terminal parts are preformed fuel filler neck hoses, vapour recovery lines, and return line bundles in passenger cars and motorcycles, where the conductive inner layer maintains resistance below 10^6 Ω under assembly bending and thermally aged conditions.
Where compressed air, solvent vapour, or combustible dust travels through plastic tubing, surface resistance values above 10^9 Ω can lead to propagating brush discharge and dust ignition; L 20 EC PA12-CD25 is extruded into conductive tubing for such circuits at 100 wt% neat compound, eliminating the need for post-treatment antistatic coatings that abrade away in flexing service. The relevant compliance framework includes ATEX 2014/34/EU for equipment used in potentially explosive atmospheres, IEC 60079-0:2017 for general requirements, and ISO 8031:2009 for electrical resistance measurement on rubber and plastics hoses; for fine dust conveyance, the tube assembly should remain below 10^6 Ω end-to-end resistance on a 1 m test length. The downstream process uses a 25:1 L/D single-screw extruder with a barrier screw, a melt temperature of 220°C to 240°C, and a vacuum calibration tank operating at -0.2 bar to -0.4 bar; the carbon black-containing melt is sensitive to moisture and trapped volatiles, so pellets are dried at 80°C for 4 h to 6 h before extrusion. Addition of regrind must be limited to 15 wt% to 25 wt% because repeated shear exposure of carbon black agglomerates increases the percolation threshold and raises electrical resistivity; published data for this exact configuration is limited, but production experience indicates that regrind levels above 30 wt% shift resistance upward and require full revalidation before release. Terminal products include antistatic compressed air hoses, dust extraction conduits, spray booth air lines, and purge-air tubing for solvent transfer pumps, all used in Class II and Class III hazardous areas where the conductive path is maintained through end fittings with metal grounding rings.
| Downstream scenario | Standard or regulation | Test method or clause | Acceptance criterion |
|---|---|---|---|
| Multilayer fuel vapour lines | SAE J2260 | ISO 60093 | Surface resistance below 10^6 Ω |
| Pneumatic conveyance in ATEX areas | IEC 60079-0:2017 | Clause 7.4 | Surface resistance below 10^9 Ω |
| Urea dosing lines | ISO 22241-3:2019 | ISO 8031:2009 | Surface resistance below 10^6 Ω |
| Cable protection conduits | IEC 61386-1 | IEC 62631-3-2 | Surface resistance below 10^9 Ω |
| Fuel quick connectors | SAE J2044 | ASTM D257 | Initial surface resistance below 10^5 Ω |
Heavy-duty urea dosing and coolant lines in commercial vehicles use L 20 EC PA12-CD25 as a static-dissipative inner tube because the flow of aqueous urea solution and residual diesel fuel can generate triboelectric charge inside an insulating PA12 carrier; the charge is drained only if the compound remains incorporated at 100 wt% or as a coextruded inner layer of 0.2 mm to 0.4 mm thickness. ISO 22241-3:2019 governs materials compatibility for NOx reduction agent dosing systems, while ISO 19013-1 and SAE J2044 cover hose and quick connector requirements; electrical resistance is measured per ISO 8031:2009. The manufacturing route is high-output tubing extrusion, often with a nylon barrier screw of 30:1 L/D, melt temperature 230°C to 250°C, and a rippled or plain calibration sleeve; post-extrusion assembly includes induction welding or insert molding of conductive quick connectors. A process-specific limitation is the narrow temperature window in thin-wall lines: wall thickness below 0.75 mm can lead to melt fracture and inconsistent carbon black distribution if the die land length is too short, while overheating above 255°C degrades the PA12 and shifts surface resistivity upward. Terminal products are urea dosing feed tubes, heated urea lines with integrated resistance wire, and coolant overflow tubes in Euro VI and EPA 2010 heavy-duty platforms.
Corrugated conduit formed from L 20 EC PA12-CD25 is used in gas processing and mining installations where cable sheathing must not accumulate static charge; the compound is processed at 100 wt% neat, with no additional conductive masterbatch because carbon black dispersion is already controlled at compound scale. Compliance is evaluated under IEC 61386-1 for conduit systems and IEC 60079-0:2017 clause 7.4 electrostatic requirements for Ex equipment; surface resistance below 10^9 Ω is the acceptance ceiling when tested according to IEC 62631-3-2. The production line typically uses a 30:1 L/D single-screw extruder feeding a rotating corrugator with mold blocks set to 60°C to 80°C; melt temperature is held between 220°C and 245°C, and the tube is cooled in a water bath before spark testing at 5 kV to 10 kV to detect pinholes. Because carbon black reduces melt strength, corrugation stability is a field-observed bottleneck at line speeds above 12 m/min; operators reduce take-off speed rather than raise melt temperature, since the latter increases post-corrugation resistance drift. Terminal products include antistatic PA12 corrugated conduits for cable management in oil and gas skids, underground mining conveyor controls, and dust-prone grain handling electrical enclosures.
Fuel quick-connector bodies and pump flanges introduce a different manufacturing route: injection molding of L 20 EC PA12-CD25 with a melt temperature of 230°C to 250°C, a mold temperature of 60°C to 90°C, and a hot runner system sized to keep gate shear below the carbon black network damage threshold. The use ratio is typically 85 wt% to 100 wt% neat compound, with 15 wt% or less virgin PA12 added only when the molder needs to raise melt flow for long thin-wall sections; every blend must be qualified for resistance because the dilution effect is non-linear near the percolation threshold. SAE J2044 defines the quick-connector performance requirements, and ASTM D257 or ISO 60093 provides surface resistance data; underhood thermal aging can shift surface resistance by up to one decade, so initial resistance should not exceed 10^5 Ω. The injection molding process uses a sequenced valve gate to prevent gas entrapment and knit lines that interrupt the conductive path; for flanges with wall thickness above 3 mm, packing pressure is held at 60 MPa to 80 MPa and screw backpressure at 0.5 MPa to 1.5 MPa. Terminal products are quick-connector bodies, fuel pump flanges, and sensor housings that are assembled into gasoline direct injection and diesel return systems, where static charge must dissipate through the polymer component to a grounded fuel rail or bracket.
Solvent transfer nozzles and paint-line static-control bushings are machined from injection-molded stock shapes made from 100 wt% L 20 EC PA12-CD25, with antistatic compliance verified under IEC 60079-0:2017 clause 7.4 and surface resistance measured by ISO 60093; the production route for stock shapes uses a 2000 kN to 4000 kN clamp force injection molding machine with a 60°C to 80°C mold temperature, and the terminal stock is annealed at 90°C for 4 h before machining to relax molded-in stress. No dilution with natural PA12 is specified for machined parts because local machining cuts can interrupt the carbon black network; if blending is unavoidable, addition ratios below 70 wt% L 20 EC require resistance revalidation on the finished machined surface. Terminal products include spray booth solvent nozzles, paint delivery line support bushings, and static-dissipative valve seats in solvent transfer systems.
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EMS-Grivory Grilamid® L 20 EC PA12-CD25 is an electrically conductive carbon black-modified polyamide 12 compound supplied in pellet form. The product identifier combines the PA12 base polymer “L 20” with the electrically conductive “EC” product class and the carbon black modifier “CD25.” The compound is used in injection-molded components for electrostatic dissipation and controlled grounding: fuel-system clips, sensor retainers, conveyor rollers, and enclosures for electronic manufacturing equipment. In dry-as-molded condition, the material exhibits volume resistivity in the range of 1 × 101 Ω·cm to 1 × 103 Ω·cm and surface resistivity in the range of 1 × 102 Ω to 1 × 105 Ω when evaluated with IEC 62631-3-1 and IEC 62631-3-2. The surface resistance is therefore below the 1 × 106 Ω upper limit commonly applied to conductive materials for ESD control under IEC 61340-5-1, but final assembly performance depends on geometry, contact pressure, and environmental history.
The dry-as-molded mechanical profile is different from unfilled PA12 because the carbon black network raises modulus and reduces ductility. Supplier technical literature for this formulation class reports density of 1.10 g/cm³ to 1.25 g/cm³ per ISO 1183-1, tensile modulus of 1,500 MPa to 2,500 MPa per ISO 527-1/2, and Charpy notched impact strength of 3 kJ/m² to 8 kJ/m² per ISO 179-1/1eA. Elongation at break is typically between 3 % and 20 %. The melting peak of the PA12 matrix is 175 °C to 180 °C per ISO 11357-3, and the dry glass transition temperature is approximately 45 °C. After conditioning at 23 °C and 50 % RH, absorbed moisture plasticizes the amorphous phase and shifts the glass transition below 10 °C, lowering modulus and increasing impact toughness.
The conductive carbon black network requires a minimum part wall thickness to avoid through-plane resistivity gradients. In sections thinner than 0.8 mm, the probability of a continuous conductive path decreases and surface resistivity may rise by several decades. The supplier’s application guidelines recommend maintaining wall thickness above 1.0 mm for parts requiring uniform conductivity; thinner sections should be evaluated with a guarded electrode test under IEC 62631-3-2.
Before melt processing, the pellets require desiccant drying. A dry-air dryer with a dew point of −40 °C or lower and a bed temperature of 80 °C is used for 4 h to 8 h. Residual moisture should remain below 0.10 %; moisture levels above 0.15 % promote hydrolytic degradation during melting, which can reduce molecular weight, produce silver streaking, and disrupt the conductive network. Residual moisture should be verified by Karl Fischer titration according to ISO 15512. Dried pellets should not remain in an open hopper for more than 1 h unless the hopper is blanketed with dry air.
Injection molding is performed with cylinder temperatures from 220 °C to 260 °C and mold temperatures from 60 °C to 90 °C. The lower boundary is set by melt viscosity and carbon black dispersion; the upper boundary is set by thermo-oxidative chain scission and surface degradation. Cumulative melt residence time should not exceed 10 min at 240 °C or 5 min at 260 °C. A reverse barrel temperature profile is preferred to avoid excessive shear heating in the compression zone.
Because carbon black raises melt viscosity, the plasticating unit requires a longer screw recovery time than unfilled PA12. Back pressure of 0.5 MPa to 1.5 MPa improves homogenization; pressures above 2.0 MPa can cause local overheating and degrade the carbon black network. Injection speeds should be moderate to high to prevent gate freeze-off, but linear velocities above 200 mm/s may produce jetting and surface defects. Tooling should use edge gates of 1.0 mm to 1.5 mm for wall sections of 2 mm to 3 mm, and direct gates should maintain a diameter of at least 50 % of nominal wall thickness.
Molding shrinkage is anisotropic because carbon black particles orient during flow. Longitudinal shrinkage is commonly 0.4 % to 0.8 % and transverse shrinkage is 0.6 % to 1.2 % per ISO 294-4. Weld lines are electrically weak points: surface resistivity across a weld line can be 1 to 3 decades higher than the bulk value. Gate locations should therefore avoid placing weld lines in grounding paths or across conductive contact surfaces. Carbon black-filled polyamide is also abrasive to tooling steel; nitrided or hardened inserts are recommended for high-volume production.
Moisture uptake in PA12-CD25 is lower than in PA6 but remains a design variable. At 23 °C and 50 % RH, equilibrium moisture content is approximately 0.5 % to 0.8 % by mass per ISO 62. The absorbed water plasticizes the polyamide matrix, reducing tensile modulus by 10 % to 20 % and increasing Charpy impact relative to dry-as-molded values. Dimensional growth after conditioning is typically 0.1 % to 0.3 % and must be included in press-fit and bearing clearance calculations.
Electrical resistivity is more sensitive to moisture than mechanical properties. Water-induced swelling separates carbon black aggregates and increases surface resistivity by 1 to 3 decades in severe humid environments. Re-drying at 80 °C for 4 h can partially restore conductivity, but repeated moisture cycling or hydrolytic matrix damage can create permanent network disruptions. Parts intended for condensing environments should be electrically qualified after damp-heat ageing at 85 °C and 85 % RH per IEC 60068-2-78, not only in dry-as-molded condition.
The following indicative property ranges apply to injection-molded test specimens conditioned at 23 °C and 50 % RH unless otherwise noted. They are compiled from supplier technical literature and are not design allowables.
| Property | Test method | Unit | Indicative range |
|---|---|---|---|
| Density | ISO 1183-1 | g/cm³ | 1.10–1.25 |
| Tensile modulus | ISO 527-1/2 | MPa | 1,500–2,500 |
| Tensile strength at yield | ISO 527-1/2 | MPa | 30–45 |
| Elongation at break | ISO 527-1/2 | % | 3–20 |
| Charpy notched impact strength | ISO 179-1/1eA | kJ/m² | 3–8 |
| Volume resistivity | IEC 62631-3-1 | Ω·cm | 1 × 101–1 × 103 |
| Surface resistivity | IEC 62631-3-2 | Ω | 1 × 102–1 × 105 |
| Water absorption at saturation | ISO 62 | % | 0.5–0.8 |
| Mold shrinkage | ISO 294-4 | % | 0.4–1.2 |
All electrical values are measured after conditioning per ISO 291 at 23 °C and 50 % RH for 48 h. The electrification time is 60 s and the applied voltage is 100 V DC for resistivity testing. Lower voltages may produce unstable readings on conductive compounds because contact resistance dominates.
The principal difference between Grilamid L 20 EC PA12-CD25 and unfilled Grilamid L 20 is the percolating carbon black network. Unfilled PA12 has a surface resistivity above 1 × 1013 Ω, while the conductive grade operates in the 1 × 102 Ω to 1 × 105 Ω range. The network raises tensile modulus and melt viscosity, reduces elongation at break, and imparts isotropic conductivity in molded parts. Carbon fiber–filled PA12 can provide lower surface resistivity and much higher modulus, but its conductivity is flow-direction-dependent and drops significantly across weld lines; carbon black-filled PA12 retains more uniform conductivity in all directions and offers better surface finish for sliding contact parts.
Replacing a machined metal housing with conductive PA12 reduces mass by approximately 80 % to 85 % compared with steel of density 7.85 g/cm³. The polymer is not a structural earthing conductor and cannot carry fault current; it is limited to static dissipation and low-energy discharge paths. Grounding contact geometry must be sized to maintain the required surface resistance of the assembled part, and metal inserts may be required at connection points. Compared with PA6 conductive grades, the PA12 backbone reduces equilibrium moisture absorption and improves dimensional stability in humid environments but provides a lower deflection temperature under load. The HDT at 1.8 MPa is typically 50 °C to 60 °C per ISO 75-1/2, so load-bearing parts at elevated temperature require design verification.
The comparative matrix below is intended for preliminary material selection and assumes dry-as-molded test specimens.
| Attribute | Unfilled PA12 | PA12-CD25 | PA12-CF20 | PA6-GF30 |
|---|---|---|---|---|
| Density ISO 1183-1 | 1.01–1.03 g/cm³ | 1.10–1.25 g/cm³ | 1.15–1.25 g/cm³ | 1.30–1.40 g/cm³ |
| Tensile modulus ISO 527-1/2 | 1,200–1,600 MPa | 1,500–2,500 MPa | 8,000–12,000 MPa | 7,000–9,000 MPa |
| Charpy notched impact ISO 179-1/1eA | 8–15 kJ/m² | 3–8 kJ/m² | 8–12 kJ/m² | 10–15 kJ/m² |
| Surface resistivity IEC 62631-3-2 | >1 × 1013 Ω | 1 × 102–1 × 105 Ω | 1 × 102–1 × 104 Ω | >1 × 1013 Ω |
| Water absorption at saturation ISO 62 | 0.6–0.8 % | 0.5–0.8 % | 0.5–0.7 % | 1.5–2.0 % |
| Conductivity direction | insulating | isotropic | anisotropic; weld lines resistive | insulating |
The PA12 matrix provides resistance to aliphatic hydrocarbons, automotive fuels, oils, and glycol-based coolants, but strong mineral acids and polar solvents can swell or degrade the surface. The carbon black filler may increase solvent uptake at the surface and create conductive paths that are affected by fuel soak. Components in continuous fuel contact should be tested for extraction and electrical stability according to the relevant automotive specification, such as ISO 16750-5 for chemical loading.
Regulatory status should be confirmed from the supplier’s product data sheet. Conductive PA12 compounds based on carbon black are generally outside food-contact approval when loaded with conductive carbon black; if food contact is required, a specific food-compliant grade should be selected. For components used in potentially explosive atmospheres, equipment-level certification requires surface resistance testing on finished components according to EN IEC 60079-0. The material should be evaluated for creep, chemical resistance, and electrical performance after exposure to all service fluids and cleaning agents. Recycled material can be added at levels up to 20 % by mass without eliminating the conductive network, but higher regrind fractions may increase surface resistivity variability and should be qualified by production-scale trials.