| HS Code | 960140 |
| Material | Polyamide 12 (PA12) / Nylon 12 |
| Color | Black |
| Density | 1.08 g/cm³ |
| Melting Point | 178 °C |
| Tensile Modulus | 2200 MPa |
| Tensile Strength At Yield | 43 MPa |
| Elongation At Break | 25 % |
| Flexural Modulus | 1900 MPa |
| Charpy Notched Impact Strength 23 C | 30 kJ/m² |
| Surface Resistivity | 1.0E5 Ω/sq |
| Volume Resistivity | 1.0E6 Ω·cm |
| Heat Deflection Temperature 1 8 Mpa | 60 °C |
| Moisture Absorption 24h 23 C | 0.2 % |
| Water Absorption At Saturation | 0.7 % |
As an accredited Evonik Vestamid L-R3-EI Antistatic, Black, Electrically Conductive Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Supplied as black electrically conductive nylon 12 pellets in sealed 25 kg bags, antistatic grade, ensuring safe handling and storage. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): 20′ FCL container of Evonik Vestamid L-R3-EI Antistatic Black Electrically Conductive Nylon 12, securely packed for export. |
| Shipping | Ship as sealed, moisture-proof polyethylene-lined bags or fiber drums to prevent humidity absorption. This conductive nylon 12 is non-hazardous but static-sensitive; use grounded or anti-static packaging, avoid dust formation, and store in a cool, dry area away from direct sunlight. Standard freight handling applies. |
| Storage | Store Evonik Vestamid L-R3-EI in its original, sealed container in a cool, dry, well-ventilated area. Keep away from heat, open flames, and ignition sources. Protect from moisture and direct sunlight; avoid temperatures above 50°C. Ensure containers remain tightly closed to prevent contamination and degradation. |
| Shelf Life | Shelf life is typically 2 years from delivery if stored unopened, cool, and dry, away from moisture and light. |
Carried out as the innermost electrostatic dissipative layer in multi-layer automotive fuel tubing, Vestamid L-R3-EI addresses the charge accumulation generated by high-velocity fuel flow through non-conductive polymer layers. The construction is governed by SAE J2260 for non-metallic fuel system tubing, SAE J1645 for electrostatic charge mitigation, and vehicle manufacturer specifications derived from evaporative emission requirements under CARB and EPA frameworks. In this application, the conductive inner layer is processed at 100 wt% as supplied; no additional carbon black masterbatch, ionic antistat, or conductive fibre is introduced at the converter because the conductive network is already formed in the pellet. Dilution with unreinforced PA12 is not permitted in the inner layer, and coextruded trim regrind may be fed into the outer cover layer at 10 wt%–20 wt% only if the inner layer remains continuous. The finished product types include multi-layer fuel filler necks, vapour return lines, tank vent valve connectors, and quick-connect fuel line assemblies.
Multi-layer coextrusion is performed on five-layer lines with barrier screws and L/D ratios of 25:1–33:1, using vented barrels at a vacuum below -0.08 MPa. The conductive PA12 stream is maintained at a melt temperature of 250–270°C, whereas the EVOH barrier is kept at 210–230°C; the temperature delta of up to 40 K prevents EVOH degradation while avoiding over-dispersion of carbon black in the PA12 matrix. The inner layer thickness must remain sufficient to create a continuous grounding path to the quick-connect fitting; if weld lines or folds interrupt the layer, the assembly fails the SAE J1645 continuity check. Pre-drying at 80°C for 4–6 h to <0.10 wt% moisture is required before extrusion because residual moisture above this threshold causes surface pitting and localised non-conductivity. Published grade-specific dilution curves for this exact multi-layer configuration are limited; converters must confirm resistance after assembly because tube bending and fitting swaging introduce mechanical strain in the conductive inner wall.
Process failure is most commonly observed at corrugation echoes or tube bends when the inner layer thickness falls below the continuous conductive minimum. In flexural testing at -40°C under SAE J2260 or OEM-specific low-temperature impact methods, microcracks can propagate from the corrugation roots if the conductive inner layer is too thick relative to the tube outer diameter; carbon black increases notch sensitivity compared with unfilled plasticized PA12. The layer distribution is therefore governed by a balance between electrical continuity and bending strain: the inner layer must remain uninterrupted, while the outer layers carry the bulk of the flexural stress. This balance becomes critical in fuel filler neck tubes with tight bend radii, where the inner layer can delaminate at the adhesive tie resin if the tie-layer melt temperature falls below the resin supplier's minimum. Published component-level validation data for this exact grade in all vehicle-specific corrugation geometries is limited, and pre-production trials are required.
Flexible pneumatic hoses used in Zone 1 and Zone 2 areas must dissipate charge from both inner and outer surfaces; the relevant compliance framework includes ISO 80079-36:2016 for non-electrical equipment in explosive atmospheres and IEC TS 60079-32-1 for electrostatic hazard control. The conductive bore is produced from 100 wt% Vestamid L-R3-EI; regrind from edge trim may be inserted into a non-conductive cover or an intermediate layer at up to 15 wt%, but not into the bore, because reprocessing history disrupts the carbon black network and can lift surface resistance above the 10^9 Ω threshold used in IEC TS 60079-32-1 for preventing propagating brush discharges. For grounded components, resistance to earth below 10^6 Ω is maintained by embedding a copper drain wire or by a conductive coupling strip that contacts the bore at fitting ends.
The low resistance of the liner requires permanent grounding; a floating hose with conductive liner but without grounded couplings can transfer charge from an isolated conductor more rapidly than a static-dissipative material, creating an ignition risk under certain conditions. Extrusion uses a crosshead die on a vented single-screw extruder with a grooved feed section; melt temperature is held at 250–270°C, and the tube is cooled through a vacuum calibration tank with a grounded mandrel or downstream earthed brush. A corrugator is used to form the finished hose profile, with wall thickness typically 0.5–1.5 mm. Operational failure includes die blockage from carbon black degradation if melt temperature exceeds 270°C or residence time exceeds 10 min; purging with unreinforced PA12 without disassembly of conductive tooling is not recommended because it can leave insulating polymer at the bore surface. The product is not classified as flame-retardant; where mining or ATEX machinery requires V-0 behaviour or low smoke, a separate flame-retardant jacket must be coextruded or the specified grade must be re-evaluated. Terminal product types include ATEX-rated compressed air hoses, dust extraction ducts, solvent vapour extraction hoses, and powder conveying pipes.
In semiconductor and PCB handling, charge decay from ±1000 V to ±100 V within 0.1 s is a common acceptance window, and surface resistance class is evaluated according to IEC 61340-2-3:2016. ANSI/ESD S20.20-2021 and IEC 61340-5-1:2016 define the ESD control programme requirements, while ANSI/ESD STM11.11 is used for surface resistance verification on flat plaques. Vestamid L-R3-EI is processed at 100 wt% by injection molding or by sheet extrusion followed by vacuum thermoforming; mold temperatures are kept at 40–80°C and pack pressure is limited because carbon black can align near the gate and shift local surface resistance. Release agents are not used because they form an insulating skin that masks the conductive surface; demolding is achieved through draft angles and mould release geometry. PA12 moisture uptake at 23°C and 50% RH is about 0.7 wt%, lower than PA6 or PA66, which reduces dimensional shift in dry cleanrooms where relative humidity can fall below 10% RH. For injection molded trays, valve-gated hot runners produce more uniform resistance than cold edge gates; weld lines must be positioned away from grounding pads because a weld line crossing the grounding area can elevate measured resistance even when the bulk part is conductive. The conductive compound is chosen only where rapid charge removal to ground is required; it is not used for high-resistance static-dissipative packaging that limits discharge current to a sensitive device. Parts produced in this category include semiconductor wafer cassettes, PCB racks, display panel carriers, and hard disk drive trays.
| Application | Standard or test method | Resistance requirement |
|---|---|---|
| Automotive fuel system | SAE J1645 | normally < 10^6 Ω to ground |
| ATEX non-conductive parts | IEC TS 60079-32-1 | surface resistance < 10^9 Ω for brush discharge control |
| ESD packaging | IEC 61340-2-3, ANSI/ESD STM11.11 | 10^4 Ω–10^11 Ω depending class |
| Conveyor belts | ISO 284:2012 | ≤ 3 × 10^8 Ω |
| Chemical hoses | ISO 8031:2020, EN 12115 | continuity often ≤ 10^6 Ω/m |
Gravure press rollers, solvent laminating idlers, and ATEX-rated conveyor rollers expose the polymer surface to methyl ethyl ketone, ethyl acetate, and toluene while requiring the roller cover to bleed static to ground. The relevant compliance framework includes NFPA 77:2019 for static electricity control and ISO 284:2012 for electrical conductivity of conveyor belts; where the roller operates in an ATEX-classified solvent zone, the equipment-level requirements of ISO 80079-36:2016 also apply. The roll cover is injection molded or extruded from 100 wt% Vestamid L-R3-EI and is not diluted with unfilled PA12 because the conductive threshold of the cover must remain below the 3 × 10^8 Ω limit of ISO 284:2012. Overmolding onto steel cores requires core preheating to reduce differential shrinkage; a universal core temperature is not specified because it depends on roll diameter and wall thickness, but mold material selection must account for the carbon black compound’s abrasive character. The failure mode observed with this design is interfacial cracking caused by differential shrinkage between the conductive PA12 cover and the steel core; helical grooves in the core or a thin adhesive primer are used when published-process tests show crack propagation after thermal cycling. Because the compound’s solvent resistance prevents swell-induced softening in ketone and ester environments, the main operational boundary is frictional heating: continuous surface temperatures above 80°C should be evaluated by long-term creep testing under load.
Cover thickness is a critical process variable: thicker covers reduce interfacial shrinkage stress but increase surface temperature under continuous line speed because the polymer’s lower thermal conductivity restricts heat dissipation. Roller manufacturers therefore balance cover thickness against line speed, grounding path design, and solvent exposure. In dry sliding contact, the compound is not a replacement for metal rollers where very low friction torque is required; bearing load capacity must be verified separately because the antistatic property does not improve load-bearing performance. Parts produced from this process include gravure printing press rollers, solvent laminating idler rolls, ATEX-rated conveyor rollers, and cleanroom transfer rollers.
The lining of chemical transfer hoses is extruded at 100 wt% from Vestamid L-R3-EI, and no additional conductive additive is needed. The electrical continuity between end couplings is verified according to ISO 8031:2020, while EN 12115:2021 governs the construction and marking of hose assemblies for chemical transfer. When continuous conductivity is specified, the resistance between couplings is frequently limited to ≤ 10^6 Ω/m; the exact value depends on the purchaser’s specification and the chemical group being handled. Mandrel-supported crosshead extrusion at a melt temperature of 250–270°C is followed by spiral winding of steel wire or polyester yarn and then cover extrusion; because Vestamid L-R3-EI is thermoplastic, no vulcanization step is required, which reduces thermal history compared with rubber hose linings. Pre-drying at 80°C for 4–6 h to <0.10 wt% moisture is critical because residual moisture produces microporosity and local conductivity loss in the inner liner. At storage or processing ambient relative humidity above 60% RH, sealed containers and a dry-air hopper are required to prevent rapid moisture pickup. Regrind from cover trim or rejected hose ends is not allowed in the liner; it may be reused in the cover at up to 15 wt% only after verification that the cover retains its specified conductivity or non-conductivity. Grade-specific published data for liner dilution with virgin PA12 in multi-layer chemical hoses is limited, so liner-layer conversion trials should measure resistance after coupling swaging and after a minimum 48 h conditioning at 23°C and 50% RH according to ISO 8031:2020.
Chemical compatibility under EN 12115:2021 is medium-specific and must be revalidated after any change in process temperature or impurity content. A PA12 liner can lose low-molecular-mass additives in hot ester or ketone immersion; the resulting stiffening or shrinkage changes the contact pressure between the liner and the electrical coupling and may shift the measured resistance. Coupling attachment by swaging or bolted flanges must provide a defined metal-to-liner contact ring; an intermittent contact point can create a local hot spot during static discharge. The outer cover in a conductive hose specification is often left non-conductive to prevent external current if the hose runs near live conductors; this is a deliberate design choice controlled by material selection rather than by the liner compound. Completed hoses are tested for resistance on the production line before marking according to EN 12115:2021. Converted article types include chemical transfer hoses, solvent discharge hoses, powder conveying hoses, and vapour recovery tubes.
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Evonik Vestamid L-R3-EI Antistatic, Black, Electrically Conductive Nylon 12 is a carbon-black-filled polyamide 12 compound supplied as black pellets for injection moulding and profile or sheet extrusion. The product combines the polyamide 12 backbone with a conductive carbon-black network that reduces electrical resistance relative to unfilled Vestamid L grades. The material is specified where electrostatic charge must be dissipated from polymer parts, including fuel-system accessories, pneumatic conveying components, electronic packaging, and enclosures in potentially explosive atmospheres. Current manufacturer documentation should govern final design values, but publicly available technical data for this grade class places density near 1.04 g/cm³ according to ISO 1183-1 and tensile modulus near 1500 MPa according to ISO 527-1/-2. Electrical surface-resistance values are geometry-dependent and are measured by IEC 62631-3-2 or IEC 60093. The material is not a substitute for system-level electrostatic risk assessment; the final moulded part must meet the resistance-to-earth and charge-decay requirements of the application specification.
The principal difference is the percolating carbon-black network. Unfilled PA12 commonly shows surface resistance above 10^13 Ω, whereas the conductive filler network in L-R3-EI lowers the surface resistance into the antistatic-to-conductive band. The exact measured value depends on skin morphology, gate location, wall thickness, filler orientation, and moisture content. Parts with high shear at the mould surface can be more conductive at the frozen skin than in the core. The carbon-black structure increases melt viscosity and shear sensitivity, and it reduces weld-line strength relative to unfilled grades. Compared with carbon-black-filled PA6, the PA12 matrix gives lower saturated water uptake, generally below 1.5%, which limits dimensional change and moisture-driven conductivity drift. Compared with semi-aromatic polyamides or glass-filled grades, the continuous-use temperature ceiling is lower. The product therefore occupies a defined niche: moderate conductivity with PA12 chemical resistance and low-temperature toughness, not a replacement for high-modulus or thermally stabilised compounds.
Pre-drying is required when the moisture content of the granules exceeds 0.1% by weight. Drying in a desiccant-air dryer at 80°C to 85°C for 4–6 hours with a supply-air dew point of -30°C or lower is a practical production envelope. Residual moisture above 0.15% at melt temperature hydrolyses the polyamide backbone, producing surface splay, increased mould deposit, and loss of impact strength. Barrel-temperature profiles in injection moulding commonly range from 230°C to 270°C from rear zone to nozzle, with mould temperatures between 40°C and 80°C. High back pressure and high screw speed can over-shear the carbon-black network and reduce conductivity; a medium screw speed and back pressure below 15 bar are frequent starting conditions. Melt residence time should remain below 10 minutes at the upper end of the temperature interval because thermal degradation of the carbon-black/PA12 interface can destabilise surface-resistance reproducibility. On a twin-screw reprocessing line with an L/D 40:1 vented barrel, regrind from conductive parts can be re-compounded, but the addition ratio must be validated by measuring surface resistance at the same gate location of the moulded plaque over at least three consecutive shots.
Melt rheology of conductive PA12 differs from unfilled PA12 in two measurable ways: the shear-thinning exponent is steeper and the extensional viscosity at high deformation rates can be lower because filler aggregates orient under elongational flow. Capillary rheometry at 240°C commonly shows that the addition of carbon black reduces the melt volume-flow rate by 20–50% relative to an unfilled PA12 of similar molecular weight. In practice, a thin-wall mould with a flow length exceeding 300:1 can experience short shots or high-pressure alarms on a standard injection unit. The processing window can be extended by increasing melt temperature within the permitted range, but the resulting lower viscosity is partly offset by a risk of carbon-black network breakdown. Mould-filling simulations require a corrected viscosity model; using an unfilled PA12 database will under-predict injection pressure by more than 15%.
Surface-resistance measurements on conductive PA12 parts are influenced by electrode geometry, contact pressure, and conditioning. Measurement according to IEC 62631-3-2 using strip or ring electrodes should be performed after conditioning at 23°C and 50% RH for at least 48 hours. Thin-wall sections may record lower surface resistance than thick-walled sections because the shear-induced skin confines a higher proportion of oriented conductive filler. In applications intended for potentially explosive atmospheres, non-metallic enclosures are commonly required to maintain surface resistance below 1.0 × 10^9 Ω under EN IEC 60079-0 or ISO 80079-36; however, the material alone cannot certify a final assembly. Grounding continuity across joints, inserts, and gaskets must be verified at the product level. Field failures observed in production applications include localised static accumulation at weld lines where the conductive network has been disrupted by flow-front collision. Mould-flow simulation should therefore be used before tool construction to move weld lines away from the shortest path to earth or from solvent-wiped surfaces.
| Property / response | Test method | Unfilled PA12 | Carbon-black-filled conductive PA12 class |
|---|---|---|---|
| Density | ISO 1183-1 | 1.01–1.03 g/cm³ | 1.04–1.08 g/cm³ |
| Surface resistance | IEC 60093 | typically >10^13 Ω | 10^4–10^9 Ω depending on moulding |
| Tensile modulus | ISO 527-1/-2 | 1100–1500 MPa | 1400–1800 MPa |
| Water absorption at saturation | ISO 62 | 1.1–1.5% | 1.1–1.4% |
| Charpy notched impact at 23°C | ISO 179-1/1eA | 6–15 kJ/m² | 5–10 kJ/m² |
| Thermal melting endotherm | ISO 11357-3 | 175–180°C | 175–180°C |
The ranges are indicative for the compound class and must not replace the current Evonik datasheet or part-specific measurement. Product-specific values can shift with lot-to-lot carbon-black dispersion and final moisture condition.
PA12 absorbs less water than short-chain or mid-chain polyamides at equilibrium. This characteristic is important in antistatic components because water absorption is not required to achieve conductivity. In carbon-black-filled PA12, conductivity remains largely electronic after desorption at 80°C, whereas antistatic PA6 based on hygroscopic additives may become insulating under dry conditions. Nevertheless, dimensional change between dry-as-moulded and conditioned states can still reach 0.5–0.7% in unreinforced PA12, so bearing fits and snap-fit deflections must be designed with clearance studies. Parts exposed to 23°C and 50% RH reach stabilisation only after several days; measurement of surface resistance before that point can produce unstable readings.
When regrind is re-introduced at levels above 20% by weight, the cumulative shear and thermal history can break down the carbon-black network and produce batch-to-batch variance in surface resistance. In multi-cavity tools with unbalanced runner systems, cavity-to-cavity resistance differences of more than one decade are observed in field production, particularly when filling is pressure-limited. Weld-line sections in carbon-black-filled PA12 may retain only 50–70% of the bulk strength of the same material, so weld lines should be positioned in low-stress regions or eliminated through sequential valve gating. Laser transmission welding is usually impractical for black conductive grades because carbon black absorbs the infrared or near-infrared laser radiation and can create surface porosity; hot-plate welding, ultrasonic joining, or mechanical interlocking are more consistent production routes. Colour changes in L-R3-EI are constrained by the black filler; a non-black conductive variant is not part of the standard L-R3-EI product line, and colour masterbatches can dilute the conductive network and must be avoided unless the supplier has specifically qualified them.
Resistance mapping of plaques moulded from L-R3-EI reveals spatial variation between the gate and the end of flow. The gate region often shows higher skin orientation and can give lower resistance readings, while the end-of-fill region may show higher resistance due to filler orientation perpendicular to the measurement direction. For process capability studies, a nine-point grid across an ISO A5 plaque with a square electrode gap of 25 mm is more informative than a single centre-point measurement. The standard deviation between these points can approach 0.5 decades in unfavourable gating designs, which is unacceptable for some ESD specifications. Tooling engineers should therefore gate at a low-shear location and avoid abrupt thickness steps that create jetting or weld-line formation.
Vestamid L-R3-EI retains the chemical resistance of PA12 to aliphatic hydrocarbons, diesel fuel, lubricating oils, and many neutral salt solutions. Chemical exposure testing should follow ISO 175 for mass and dimensional change after immersion, but conductivity must be re-measured after drying because fuel absorption can plasticise the amorphous phase and change the tunnelling-gap distribution between carbon-black aggregates. Strong oxidising acids, concentrated formic acid, hot phenol, and polar solvents above 60°C are not recommended. Alcohol-blended fuels can shift surface resistance through plasticisation or extraction of low-molecular-weight additives; published multi-batch data for conductive PA12 in high-percentage ethanol fuel is limited, so OEM-specific validation is mandatory. The carbon-black filler does not function as a broad-spectrum UV stabiliser. Outdoor components require an additional UV-protective layer or compounding with UV additives because PA12 exposed to long-wavelength UV can undergo oxidative degradation with surface chalking and a rise in surface resistance.
In pneumatic conveying of powders and pellets, conductive PA12 pipes, elbows, and receiver bodies can provide charge dissipation when the resistance to earth across the assembly remains below 10^6 Ω and all isolated conductive elements are bonded. For fuel filter housings, the material is used to avoid a separate metal grounding tab and to create a uniform electrically conductive body; however, the material cannot achieve the very low resistance of metallic shielding, and it is not specified where surface resistance below 10^2 Ω is mandatory. In ESD-protected equipment, component carriers and handling trays made from L-R3-EI can be tested for charge decay from 1000 V to 100 V according to IEC 61340-2-1; a requirement below 2 seconds is typical but must be confirmed on the final moulded part, not on a polished surface only. Each application must verify grounding-path durability after thermal cycling, impact, and chemical ageing because surface resistance can shift by more than one decade after those exposures.
Compared with permanently conductive polyamide grades containing metal fibres, L-R3-EI does not create equivalent electromagnetic shielding effectiveness because its conductivity is in the dissipative range. It is generally selected for electrostatic discharge avoidance rather than EMI/RFI attenuation. Compared with carbon-black-filled polypropylene, the PA12 matrix provides improved heat resistance and chemical resistance but at higher material cost and higher moisture sensitivity. Compared with stainless steel grounding strips and metallic inserts, the polymer reduces component count and can be moulded into complex geometries, but it cannot provide comparable mechanical stiffness or resistance to abrasion under high-velocity particulate flow. These trade-offs define the operational boundaries of the grade.
| Evaluation area | Standard / regulation | Material-level vs system-level |
|---|---|---|
| Electrical surface resistance | IEC 62631-3-2, IEC 60093 | Material/component test |
| Electrostatic discharge packaging | IEC 61340-5-1, IEC 61340-2-1 | Component/system test |
| Explosive atmosphere constraints | EN IEC 60079-0, ISO 80079-36 | System certification |
| Chemical immersion effects | ISO 175 | Material coupon test |
| RoHS | EU 2011/65/EU as amended | Product documentation |
| REACH SVHC | EC 1907/2006 | Supplier statement |
| Food-contact suitability | FDA 21 CFR or specific migration test | Finished article, not generic material |
Processing aids, external lubricants, or antistatic topical coatings should not be applied to L-R3-EI without validation because they can mask or disrupt the conductive filler network. The product should not be blended with amine-based additives or certain halogenated flame retardants that can react with the polyamide at melt temperature. Moisture-conditioned parts can show lower mechanical stiffness; if the application requires dimensional stability under humidity changes, the design should use ribs and gussets rather than increasing wall thickness, because thicker sections prolong cooling time and make surface resistance less uniform. Injection-moulding trials on a production machine with 600–1200 kN clamp force and a screw diameter matched to shot volume will provide more reliable processing data than small laboratory moulding machines due to the shear sensitivity of the conductive network.