| HS Code | 898643 |
| Density | 1.01 g/cm³ |
| Melting Point | 178 °C |
| Water Absorption Saturation | 1.5% |
| Tensile Strength At Yield | 45 MPa |
| Elongation At Break | >200% |
| Flexural Modulus | 1100 MPa |
| Charpy Impact Strength Notched | 12 kJ/m² |
| Shore D Hardness | 75 |
| Vicat Softening Temperature | 170 °C |
| Mold Shrinkage | 1.0-1.5% |
| Processing Temperature Range | 230-260 °C |
| Mold Temperature Range | 40-80 °C |
As an accredited Evonik Vestamid L2170 Nylon 12 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Evonik Vestamid L2170 Nylon 12 is packaged as moisture-protected granules in 25 kg sealed polyethylene-lined paper bags. |
| Container Loading (20′ FCL) | 20′ FCL loading: 18 pallets, approx. 720 bags of Evonik Vestamid L2170 Nylon 12, safely secured and ventilated. |
| Shipping | Evonik Vestamid L2170 Nylon 12 ships as a non-hazardous thermoplastic granulate. It is packed in sealed moisture-proof bags and shipped dry to prevent moisture absorption. Transport is via standard freight, truck, or sea cargo, with no dangerous goods declaration required under normal conditions. |
| Storage | Store Evonik Vestamid L2170 Nylon 12 in its original, unopened packaging in a cool, dry, well-ventilated area. Keep away from direct sunlight, heat sources, and moisture, as nylon absorbs humidity. Maintain moderate temperatures and reseal containers tightly after use to prevent contamination and ensure consistent processing performance. |
| Shelf Life | Shelf life is typically 2 years when stored unopened in original, dry packaging, protected from moisture and heat. |
In automotive EVAP and diesel tank vent line co-extrusion, Vestamid L2170 is used as the inner and outer polyamide layers in multi-layer tubing where an ethylene-vinyl alcohol (EVOH) core supplies the hydrocarbon permeation barrier. A typical SAE J2260 low-permeation tube construction uses inner PA12 at 0.10 mm, maleic anhydride-grafted polyolefin tie layer at 0.10 mm, EVOH barrier at 0.10 mm, second tie layer at 0.10 mm, and outer PA12 at 0.60 mm, yielding a 1.00 mm nominal wall. The layer configuration is chosen because EVOH alone lacks zinc chloride resistance and low-temperature impact strength, while Vestamid L2170 alone permits excessive Fuel C permeation. The co-extrusion line is specified with barrier screws and a 30:1 length-to-diameter ratio; the PA12 melt temperature is held at 230–240 °C, the tie resin at 200–220 °C, and the EVOH at 210–230 °C. The overlapping thermal window between 220 °C and 230 °C is a processing constraint because departure above this band initiates EVOH gelling and pinhole formation, while lower temperatures produce interfacial melt fracture. Melt temperature is verified by infrared thermocouple at the die entry, and line speeds of 20–40 m/min are used for 8 mm outside diameter tubing. After vacuum sizing and water quenching at 15–20 °C, the tube is tested for permeation at 40 °C with Fuel C under SAE J2260, with an acceptance ceiling of 15 g/m²·day after 30 days. Low-temperature impact resistance is verified by ISO 11403-3 at −40 °C. Edge trim regrind is restricted to a maximum 20 wt% in the outer PA12 layer because higher recycled content reduces tensile elongation at break below the 200% requirement of ISO 527-2 for press-fit connector retention. Terminal products include fuel tank vent lines, EVAP canister tubing, and diesel fuel feed lines exposed to road salt, where zinc chloride stress cracking resistance is required.
| Functional layer | Proportion of wall thickness | Melt temperature window | Function |
|---|---|---|---|
| Inner PA12 | 10% | 230–240 °C | Fuel contact and low-temperature impact |
| Tie layer | 10% | 200–220 °C | Adhesion to EVOH |
| EVOH barrier | 10% | 210–230 °C | Hydrocarbon permeation barrier |
| Tie layer | 10% | 200–220 °C | Adhesion |
| Outer PA12 | 60% | 230–240 °C | Zinc chloride resistance and abrasion resistance |
For truck air brake tubing and industrial pneumatic control lines, Vestamid L2170 is extruded into unreinforced tube with outside diameters from 6 mm to 16 mm and wall thicknesses from 1.0 mm to 1.5 mm. A wall thickness below 1.0 mm is not recommended under SAE J844 Type A service because long-duration cyclic bend loading at elevated line pressure causes inner-wall buckling and microcrack initiation at the tube inside radius. The extrusion process uses a grooved feed zone and a 30:1 single-screw extruder with vacuum venting at −0.08 MPa; melt temperature is controlled at 220–240 °C, and screw speed is limited to 40–80 min⁻¹. Post-extrusion crystallisation is stabilised by annealing at 80 °C for 4 h before coiling. A weathering package is added as a 2 wt% carbon black masterbatch, and a UV stabiliser masterbatch is used at 2–4 wt% depending on outdoor exposure in desert service. Burst pressure is evaluated after conditioning at 60 °C and 80 °C in air per ISO 7628-1, while SAE J844 governs low-temperature impact at −40 °C and resistance to zinc chloride. The operational boundary includes continuous exposure to phosphate ester hydraulic fluids above 60 °C, where amide hydrolysis can reduce molecular weight; the material is not recommended for polyglycol-based brake fluids because plasticiser extraction causes inner-wall softening. Terminal products include coiled air brake tubing, suspension leveling lines, and push-in fitting tube ends, where the softening temperature and kink resistance are more relevant than modulus retention at high temperature.
In unbonded flexible risers and flowlines, Vestamid L2170 is extruded as a pressure sheath or anti-wear layer over an interlocked steel carcass. The grade is selected because its equilibrium water absorption under ISO 62 is approximately 0.7% at 23 °C and 50% relative humidity, lower than PA6 and PA66, which reduces dimensional change in wet annulus conditions. Extrusion is performed on a 28:1 single-screw extruder with a barrier screw at a melt temperature of 220–235 °C; wall thickness tolerance is held to ±0.15 mm on a nominal 5 mm sheath. The main ageing mechanism is hydrolysis of the amide linkage, accelerated by free water with pH below 4.0 and by methanol concentrations above 20 vol% used for hydrate inhibition. The service envelope is restricted to a maximum continuous operating temperature of 60 °C in the annulus under wet conditions and 70 °C for dry hydrocarbon service; higher temperatures reduce time to 50% elongation loss below the design life. Batch-to-batch degradation is monitored by solution viscosity number in sulfuric acid using ISO 307, with an acceptance window of 180–210 mL/g; values below 170 mL/g indicate hydrolytic chain scission. A minimum pressure sheath thickness of 4.0 mm is specified for a 6-inch internal diameter pipe to meet 20-year design life under API 17J and ISO 13628-2. Qualification testing to API 17J Annex B is required for each project, and published data for this specific Vestamid L2170 configuration under high H₂S partial pressures above 0.1 bar remains limited; therefore project-specific sour gas ageing tests are mandatory. Terminal products include subsea water injection lines, gas lift risers, and jumper hoses where the annulus is vented to atmospheric pressure.
In medical catheter shaft extrusion, Vestamid L2170 is processed into single-lumen and multi-lumen tubing with outside diameters from 0.8 mm to 4.0 mm and wall thicknesses down to 0.1 mm. A 20 mm single-screw extruder with a 24:1 length-to-diameter ratio and melt pump is used, operating at a melt temperature of 225–245 °C. Draw-down ratio is maintained between 2.0 and 4.0, and draw ratio balance is held at 1.0–1.2 to prevent lumen collapse. Quenching is performed in a 25 °C water bath, followed by vacuum annealing at 80 °C for 4 h to stabilise crystallinity and reduce post-sterilisation shrinkage. Biocompatibility is assessed under ISO 10993-1 with cytotoxicity by ISO 10993-5 and sensitisation by ISO 10993-10; the material is commonly used in short-term patient-contact applications rather than permanent implants. Because Vestamid L2170 is plasticised, extraction testing under ISO 10993-12 uses both polar and non-polar media to quantify plasticiser migration. Ethylene oxide sterilisation is preferred over steam autoclaving because repeated steam exposure above 121 °C causes amide hydrolysis and a burst strength reduction of 10–20% after 50 cycles. Radiation sterilisation above 25 kGy can induce oxidative embrittlement; if irradiation is unavoidable, the absorbed dose is limited to below 25 kGy and packaging vacuum is specified below 50 kPa. Barium sulfate radiopacifier is added at 20–30 wt% because higher loadings reduce tensile elongation below the flexibility threshold required by ISO 10555-1 for intravascular catheter shafts. Terminal products include infusion tubing, endoscopic instrument lumens, and catheter shaft bodies where kink resistance at body temperature is required.
| Application sector | Compliance standard | Test condition | Threshold |
|---|---|---|---|
| Automotive fuel vapour tubing | SAE J2260 | 40 °C Fuel C, 30 days | ≤ 15 g/m²·day |
| Pneumatic air brake tubing | SAE J844 / ISO 7628-1 | −40 °C impact and 60 °C burst | No crack, safety factor 4:1 |
| Medical short-term contact | ISO 10993-5 / ISO 10993-10 | Extract dilution | ≥ grade 2 |
| Offshore flexible pipe | API 17J / ISO 13628-2 | Wet annulus ageing | 20-year design life |
For flexible industrial control cables and truck ABS/EBS harness jackets, Vestamid L2170 is extruded as a protective outer sheath with a wall thickness of 0.3–1.0 mm. The cable jacket is applied by pressure extrusion through a crosshead die, with melt temperature held at 230–250 °C, screw speed at 20–40 min⁻¹, and line speed up to 80 m/min. Pre-drying at 80 °C for 4–6 h to residual moisture below 0.1% by ISO 15512 is mandatory because higher moisture creates surface voids and rough jacket surfaces at elevated line speeds. Adhesion to the inner insulation is controlled by a release layer or by using a pressure die with a draw-down ratio below 1.5 to permit stripping without damaging the conductor insulation. Abrasion resistance is verified under ISO 6722-1 for road vehicle low-tension cables; the jacket is also subjected to thermal ageing at 125 °C for 3000 h, with retention of tensile elongation above 50% as the acceptance criterion. Continuous flex service requires a minimum bend radius of 10 times cable outer diameter; tighter bending generates compressive buckling of the inner radius and shortens jacket fatigue life. The material should not be used in continuous contact with strong mineral acids or phenol-based solvents because plasticiser migration and surface attack reduce abrasion resistance. Terminal products include robotic drag chain cables, truck trailer ABS/EBS cables, and industrial sensor leads where fluoropolymer replacement is driven by lower density and easier processing, not by chemical inertness.
Injection moulding of Vestamid L2170 for industrial snap-fit components and protective housings uses a barrel temperature profile of 210–230 °C, a mould surface temperature of 40–80 °C, and an injection pressure of 60–100 MPa. Because the grade is a high-viscosity PA12, screw back pressure is limited to 0.5–1.0 MPa to avoid excessive shear heating; cycle times for a 2 mm-thick part typically fall between 25 s and 35 s. Pre-drying at 80 °C for 4–8 h to moisture below 0.1% is required, and melt cushion is maintained at 3–5 mm to stabilise holding pressure. Shrinkage after 24 h is specified by ISO 294-4 at 0.8–1.2% in the flow direction and 1.0–1.4% transverse. Living hinges are not recommended because the plasticiser lowers creep resistance; hinge thickness below 0.3 mm fails after approximately 10 000 flexural cycles in production trials. Impact strength is verified by ISO 179-1/1eA at −30 °C, and tensile properties by ISO 527-2. Terminal products include pneumatic push-in fittings, cable glands, and sports eyewear frames where cold impact resistance at −30 °C is required and weight reduction relative to brass or steel is a design variable.
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Evonik Vestamid L2170 is a polyamide 12 extrusion resin supplied as a natural-colour, plasticizer-free granulate. The polymer is obtained from ω-laurolactam and contains twelve methylene groups between amide linkages, giving the backbone a more paraffinic character than short-chain polyamides. Published product data list density at 1.01 g/cm³ (ISO 1183-1), melting temperature at 176–178°C (ISO 11357-3), and Shore D hardness near 70–75 (ISO 868). Because the amide-group density is lower than in PA6 or PA66, equilibrium water absorption is lower; PA12 saturates near 1.5% by mass (ISO 62) at 23°C, while PA6 and PA66 commonly reach 9–10% and 7–9%, respectively. The glass transition temperature is in the 40–50°C range (ISO 11357-2), and the crystallization temperature on cooling is typically between 150°C and 155°C (ISO 11357-3). These properties position L2170 for tube, profile, and monofilament extrusion rather than thin-wall injection moulding.
The grade is distinguished from impact-modified PA12 compounds by the absence of elastomeric or maleic anhydride-grafted modifier domains; low-temperature toughness is instead dependent on the inherent chain mobility of the semicrystalline PA12 matrix. Notched Charpy impact strength for this viscosity class is commonly published near 5–6 kJ/m² at 23°C and remains similar at −30°C (ISO 179-1/1eA). Tensile modulus is approximately 1600 MPa dry (ISO 527-1/-2), with yield strain near 5% and nominal elongation at break above 50%. These values are typical for plasticizer-free PA12 extrusion grades and are best used for relative material selection rather than as guaranteed minima.
Water uptake in polyamides occurs primarily at hydrogen-bonded amide groups. In L2170, one amide carbonyl is present per 12 methylene units, compared with one per 6 in PA6 or one per 6 in PA66. The lower concentration of strongly polar sites reduces both the equilibrium water mass fraction and the associated dimensional expansion. Under ISO 62 immersion at 23°C, PA12 reaches saturation at approximately 1.5%; PA6 and PA66 can exceed 9% and 7%, respectively. The practical consequence is that extruded tube made from L2170 changes diameter less in high-humidity or wet service than equivalent PA6/PA66 tube. Water also acts as a plasticizer; because the maximum absorbed water fraction is lower, the dry-to-wet modulus shift is smaller. Coefficients of linear thermal expansion for PA12 are commonly reported near 1.0–1.2×10⁻⁴ K⁻¹ (ISO 11359-2) in the flow direction; dimensional changes due to water absorption can be comparable to thermal expansion, so moisture uptake control is operationally important. In humid service, the low water absorption also reduces hydrolysis of the amide linkage, which is an advantage in hot wet applications where short-chain polyamides can undergo strength loss.
On a commercial single-screw extrusion line with a grooved feed bushing, 25:1 to 30:1 L/D, and a barrier mixing screw, L2170 is processed with barrel profile settings of 200°C in the feed section increasing to 230–240°C in the metering zone. Melt temperature is measured at the breaker plate with an immersion thermocouple and maintained between 220°C and 250°C for tube and profile outputs. A gear melt pump is commonly installed between the extruder and die to reduce pressure pulsation; screen packs of 20/40/60 mesh are used where fine filtration is required. The feedstock is dried in a dry-air dryer at 80°C for 4–6 hours to a residual moisture level below 0.1% before any processing at melt temperature. Residual moisture above that threshold produces surface splay and hydrolysis-induced viscosity loss. Sustained melt temperatures above 260°C promote thermal oxidation and gel formation, so temperature interlocks on the die zones are set accordingly. Under prolonged melt hold-up above 260°C, oxidation at the methylene groups adjacent to nitrogen leads to discolouration and a drop in relative viscosity; this is detected as a shift in melt pressure at constant screw speed.
For outside diameters of 4–16 mm, tube lines typically use a vacuum calibration tank with water temperature controlled between 20°C and 40°C. The extrudate enters a dry calibration sleeve where the outer surface is fixed before the crystallization front reaches the interior. Since the crystallization temperature is approximately 150–155°C, calibration and vacuum sizing must occur within the first cooling stages. The high melt viscosity relative to injection-moulding PA12 grades reduces sag in free-form profiles and improves retention of wall thickness in large-diameter tube. Haul-off ratio is balanced between 1.05:1 and 1.20:1 to limit anisotropic orientation; excessive draw can increase longitudinal strength while reducing hoop strength and dimensional stability. For thick sections above 20 mm outside diameter, internal air pressure and controlled cooling are used to prevent voiding and sink marks. In monofilament production, the melt is extruded through a single-hole spinneret into a water quench bath maintained at 20–30°C and then drawn over heated godets at 100–140°C. Draw ratios in the range of 3:1 to 5:1 are typical for orienting the crystal lamellae and increasing tensile strength; published data for this specific configuration is limited, but commercial PA12 monofilament lines operate with similar process settings.
In compressed-air brake tubing for commercial vehicles, line-equipment testing is commonly referenced to ISO 7628 or SAE J844, which specify dimensional, burst-pressure, cold-impact, zinc chloride, and chemical-resistance requirements. Polyamide 12 grades such as L2170 are selected for plasticizer-free tube because plasticizer migration in semi-rigid systems can alter bore diameter and low-temperature flexibility. The resin resists stress-cracking in zinc chloride solution, which is a known failure mode for some short-chain polyamides; this property is evaluated by immersion of stressed tube specimens under the applicable standard. In hydraulic and lubrication lines, the paraffinic backbone limits swelling in mineral oils and greases; compatibility is assessed by mass and dimension change after immersion under ISO 175. Published data for this specific configuration is limited to standard immersion results rather than long-term field exposures. Flexible cable conduits and spiral wrap extruded from L2170 exploit the low-temperature impact response; notched Charpy values at −30°C remain near 5–6 kJ/m² (ISO 179-1/1eA), allowing coiled installation in cold environments without fracture.
Plasticized PA12 grades contain internal or external plasticizers that reduce melt viscosity and hardness. L2170 is plasticizer-free and displays higher melt viscosity at a given shear rate; extrusion line pressure at the die can be 10–20% higher for the same output when replacing a heavily plasticized grade. Die-head temperature may need to be increased by 10–20°C to restore equivalent throughput, but must remain below the 260°C degradation threshold. Without mobile plasticizer, surface tack is lower and frictional properties in tube and cable sheathing are governed by the base resin. Compared with PA11, the melting temperature of PA12 is approximately 10 K lower and equilibrium water absorption is slightly lower; both polymers share similar low-temperature impact characteristics. PA12 is therefore often preferred when lower processing temperatures are required or when dimensional stability in humid conditions is the dominant selection criterion. Relative to lower-viscosity injection-moulding grades within the same chemistry family, L2170 is not recommended for thin-wall mould filling below 1 mm because its higher viscosity produces excessive fill pressure and may require mould temperatures above 100°C; the grade is better suited to constant cross-section extrusion where high melt strength is an advantage.
Inventory must be stored in sealed containers when the plant humidity exceeds 70% relative humidity. If bulk bags are opened for more than 4 hours in humid air, pre-drying time should be extended to 8 hours at 80°C. Regrind use is limited to 30% by mass unless the melt quality is verified by pressure-viscosity monitoring; incompatible polymer contamination, especially polyolefin dust, can cause delamination and surface defects. Additive packages should be reviewed for compatibility; strongly alkaline or acidic process aids can alter crystallization kinetics and destabilize vacuum calibration. Regulatory status for food-contact or potable-water service must be confirmed against current FDA 21 CFR 177.1500 or EU 10/2011 declarations, because base resin compliance does not transfer automatically to converted articles.