| HS Code | 119219 |
| Density 23 C | 1.01 g/cm³ |
| Melting Point Dsc | 168 °C |
| Vicat Softening Temperature B50 | 100 °C |
| Shore D Hardness | 40 |
| Tensile Strength At Break | 40 MPa |
| Elongation At Break | >400 % |
| Flexural Modulus | 350 MPa |
| Charpy Notched Impact Strength 23 C | No break |
| Water Absorption Saturation | 1.2 % |
| Melt Volume Rate 230 C 2 16 Kg | 30 cm³/10 min |
| Heat Deflection Temperature 0 45 Mpa | 70 °C |
| Glass Transition Temperature | -50 °C |
As an accredited Evonik Vestamid E40-S3 Heat & Light Stabilized Nylon 12/PEBA Elastomer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Vestamid E40-S3 supplied as pellets in moisture-resistant 25 kg bags, packaged on pallets. Heat & light stabilized nylon 12/PEBA elastomer. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Evonik Vestamid E40-S3 Nylon 12/PEBA elastomer, heat/light stabilized, properly secured and sealed for transport. |
| Shipping | Ship Evonik Vestamid E40-S3 as heat- and light-stabilized nylon 12/PEBA elastomer pellets. Non-hazardous polymer supplied in sealed, moisture-proof bags or drums. Store dry, away from direct sunlight and high temperatures. Standard dry freight transport is suitable; no special dangerous-goods declarations required. Handle with care to prevent bag damage. |
| Storage | Store Evonik Vestamid E40-S3 in its original, sealed container in a cool, dry area away from direct sunlight, heat, and moisture. Avoid exposure to UV radiation and contaminants. Keep the packaging tightly closed when not in use. Under these conditions, shelf life is typically maintained for several years. |
| Shelf Life | Store in original sealed packaging, cool, dry conditions. Shelf life is typically 2 years from date of manufacture. |
Evonik Vestamid E40-S3 is a polyether block amide (PEBA) comprising nylon 12 hard segments and polyether soft segments, supplied in heat- and light-stabilized form. Nominal hardness is 40 Shore D per ISO 868. Residual moisture must be verified before melt processing because the resin reabsorbs atmospheric moisture rapidly above 60% relative humidity. The downstream tracks below are presented with process windows and compliance anchors typical of industrial equipment for this hardness class; supplier certificate-of-analysis values and component-specific qualification remain release-limiting.
Extrusion of multi-lumen catheter shaft segments from neat E40-S3 begins with desiccant drying at 80°C for 4–6 h to a residual moisture level below 0.10 wt%, confirmed by ISO 15512. The line uses a 25–30 L/D single-screw extruder with a barrier screw, 2.5:1 compression ratio, 400/400/200 mesh screen pack, and a gear melt pump. Barrel temperatures ramp from 180°C in the feed section to 220–230°C at the metering section; the die is held at 225°C. Melt pump pressure is controlled within 5–10 MPa to hold outer diameter tolerance at ±0.03 mm after vacuum calibration. Tube draw-down ratio is set between 2:1 and 4:1; tip land length is kept at 0.5–1.0 mm to prevent spiral melt fracture at high wall shear rates. Screen pack pressure rise above 15 MPa over its service life indicates gel accumulation and requires line shutdown before die plate replacement.
After the vacuum tank at 15–25°C, the tubing passes through an annealing stage at 60–80°C for 2 h to reduce frozen-in molecular orientation and improve dimensional stability after coil packaging. Multi-layer catheters may co-extrude a higher-durometer nylon 12 liner with an E40-S3 outer jacket in a spiral mandrel die; interlayer melt-temperature variation is limited to 5°C to avoid interface waviness. Radiopaque shafts are compounded with 20–30 wt% barium sulfate masterbatch, which changes rheological behaviour; published rheological data for this filled configuration are limited, so a capillary viscosity sweep under ISO 11443 at 100 s⁻¹ and 1000 s⁻¹ is required before lock-in of melt pump settings.
Finished catheter shaft components are evaluated under ISO 10993-1:2018 risk-based biocompatibility. The test programme typically includes cytotoxicity per ISO 10993-5:2009, sensitization per ISO 10993-10:2010, and chemical characterization per ISO 10993-18:2020. Moisture above 0.10 wt% in the hopper, or condensation on chilled vacuum tanks, creates bubble defects and intermittent surface roughness that cannot be reworked after coiling. The terminal product category includes outer jackets of diagnostic guide catheters and guide-extension catheter shafts where flexural modulus must remain stable after repeated traversing through tortuous vessel anatomy.
Injection moulding of sprint-spike plates and football boot sole plates from E40-S3 is carried out on a 600–1,200 kN clamp press with a 20–25 mm screw, 18–20 L/D general-purpose screw, and a check-ring non-return valve. Drying is performed at 80°C for 4 h to 0.10 wt% maximum moisture. Nozzle melt temperature is held between 225°C and 245°C; mould temperature is 30–50°C; holding pressure is 40–60 MPa. Gate sizing follows a rheological fingerprint generated on a capillary rheometer per ISO 11443 using a 1 mm die with 16:1 L/D at 230°C. Screw recovery time is kept below 18 s because longer residence time at higher barrel set points increases yellowness and gate drool in multi-cavity tools. In high-cavity moulds, nozzle temperature variation across ±5°C shifts fill viscosity sufficiently to move weld-line placement; hot runner controllers are therefore tuned within ±2°C per manifold zone.
The main processing constraint is regrind re-introduction. Production specifications cap regrind at 20 wt%, with a maximum allowable regrind of 25 wt% only after lot-by-lot testing. Yellowness index is measured per ASTM E313-20; weld-line tensile strength is measured on 2 mm plaques according to ISO 527-2 type 5A. Above 25 wt% regrind, batch-to-batch moisture variation and consumed stabilization in the regrind fraction reduce weld-line performance and increase splay defect rate. Actual field data for this specific grade are limited, so moulders calibrate the regrind ceiling by running a design-of-experiments matrix with 0 wt%, 10 wt%, and 20 wt% regrind at a fixed cavity pressure profile.
Finished plate sections are 1.5–3.0 mm thick. Gate vestiges are placed on the medial or lateral non-flexing zones of the plate, not on the forefoot flex grooves, because gate stresses and weld lines reduce crack-initiation resistance under repeated flex cycles. Hot runner thermal gate tips are operated at 210–230°C; cold sprue bushes are avoided because degraded material at the sprue boundary can create visible streaking in translucent plates. The terminal product is a structural footwear component, not a foam midsole; its function depends on low-temperature flexibility and flexural fatigue resistance rather than solely on Shore hardness.
In heavy-truck air brake and suspension pilot-control tubing, E40-S3 is extruded on a 25–30 L/D single-screw line with a 2.5:1 compression barrier screw, 200/400 mesh screen pack, and gear melt pump. The barrel profile is set from 185°C to 220–235°C; the die is held 5–8°C below the metering zone to raise melt strength before vacuum calibration. Tube outside diameter is controlled to ±0.10 mm for 4–12 mm OD and wall thickness from 0.5–2.0 mm. Line speeds between 20 m/min and 60 m/min are used with a triple-axis laser gauge; vacuum calibration pressure is held at −30 kPa to −60 kPa gauge to avoid bore chatter in the soft tube.
Formulation for black tubing uses 2–3 wt% PA12-carrier carbon black masterbatch to maintain UV resistance; non-black colours are limited to 3 wt% of a carrier-compatible concentrate. Lubricant masterbatches are not added because low-molecular-weight lubricants migrate to the tube bore and reduce push-to-connect fitting retention. Process limitations are set by melt fracture at high output. If the extruder is run above 60 m/min on 4 mm OD tubing, sharkskin on the outer surface appears and is controlled by raising die temperature by 5°C or reducing line speed.
Finished tube assemblies are tested under SAE J844 for non-metallic air brake tubing and DIN 73378 where polyamide tube-to-fitting geometry is specified. Terminal products include tractor air brake lines, cab tilt pilot lines, and suspension control tubes that operate through repeated thermal cycling from −40°C to 100°C. The heat-stabilized package of E40-S3 is relevant in this track because tube bundles routed near the engine compartment must resist surface embrittlement after prolonged dry-heat exposure.
Soft-touch overmoulding of E40-S3 onto nylon 12 surfaces is executed on a two-shot rotary-platen press or an insert-loading injection moulding cell, usually at 1,000–1,500 kN clamp force. The nylon 12 substrate is demoulded, plasma-cleaned, and preheated by infrared lamps to 80–100°C before the second shot. The PEBA melt temperature is maintained at 230–240°C, and the interfacial melt-temperature differential is held at 10–15°C during the first 0.5–1.0 s of injection. Fill velocity is 60–100 mm/s; holding pressure is 20–40 MPa for an overmoulded wall thickness of 1.2–2.5 mm. Gate location is critical because jetting into deep rib areas can create folded flow fronts and visible weld lines in the soft layer.
The material is processed neat, with no adhesion promoter or primer, because the nylon 12 hard segments of E40-S3 are chemically compatible with the nylon 12 substrate. Silicone-based mould release used on the substrate is limited to ≤0.5 wt% in the substrate resin; higher levels suppress interlayer diffusion and lower peel strength. Interlayer adhesion is derived from chain interdiffusion, not from enthalpy of mixing alone. Published data for this exact material combination are limited, so destructive adhesion testing of the first five shots after each mould cleaning is used to establish the in-house control limit. A peel coupon with overmoulded lap geometry is pulled at 50 mm/min using an ISO 527-2 tensile machine configuration; crack propagation at the interface before substrate yielding is cause for hard-stop.
Terminal products include hand-held power tool housings and portable diagnostic device enclosures where the E40-S3 layer functions as a chemical-resistant soft grip. The tool is vented with 0.02–0.04 mm land vents to avoid gas burning at the end of fill. The main incompatibility in this track is any external amine-containing cleaning agent left on the substrate; it reduces bond consistency and should be removed by plasma or isopropanol wipe before overmoulding.
Snowshoe binding plates and torsion straps are injection-moulded from E40-S3 at a melt temperature of 220–240°C, mould temperature of 40–60°C, and holding pressure of 30–50 MPa. The resin is pre-dried at 80°C for 4 h; regrind is capped at 15 wt% because low-temperature impact performance is more sensitive to accumulated heat history than standard tensile properties. Colour masterbatch with a PA12 carrier is added at 2–4 wt%. Polyolefin-based carrier masterbatch is excluded because it creates discrete low-molecular-weight domains at weld lines and reduces cold impact resistance.
Gate placement is arranged so that weld lines lie outside the main flexural hinge path. Moulded ribs are thickened to 2.0–3.5 mm at the binding pivot because the low flexural modulus of E40-S3 requires section enlargement to limit strain concentrations. Notched impact testing per ISO 180 is performed at −30°C; flexural modulus is measured per ISO 178. Accelerated weathering is conducted per ISO 4892-2 using xenon-arc exposure; colour shift is measured per ASTM E313-20. Thin tabs below 1.5 mm are at greater risk of surface embrittlement after 500 h xenon exposure because of the high surface-to-volume ratio.
Published data for this specific snowshoe binding geometry are limited. Outdoor field testing under combined mechanical load and UV exposure is required because xenon testing alone cannot reproduce the simultaneous flexural cycling and ultraviolet dose in alpine use. The terminal product is a load-transferring binding plate that must survive repeated cold flexing without cracking at the pivot points; design review uses creep data per ISO 899-1 and excludes continuous stresses above the validated linear viscoelastic limit of the material.
Chill-roll film casting of E40-S3 for footwear laminating interlayers and fabric bonding webs is run on a 25–30 L/D single-screw extruder feeding a flexible-lip sheet die of 250–600 mm width. Drying at 80°C for 4 h to 0.10 wt% residual moisture is mandatory; free water in the melt produces bubble defects and irregular gauge bands at the chill roll. Melt temperature is held at 220–235°C; die gap is 0.6–1.0 mm; air gap is 5–15 mm; chill roll temperature is 10–30°C. Film thickness between 50 µm and 150 µm is produced by adjusting roll speed and die gap, not by machine-direction stretching, to keep residual orientation low for later thermoforming and lamination.
Anti-blocking is introduced as 0.5–1.0 wt% silica masterbatch only when winding on uncoated paper cores; untreated film has a high blocking tendency because of the low Shore hardness and low glass transition of the polyether soft segment. Colour masterbatch with a polyamide carrier is added at 2–5 wt% when the film must match sportswear upper colours. Winding tension is kept below 0.2 N/mm² to avoid film blocking and core crushing under long storage times. Colour shift is measured per ASTM E313-20 after 240 h of QUV exposure under ASTM G154.
Compliance for industrial film is documented under REACH Regulation (EC) No 1907/2006; if the film is specified for food-contact laminating structures, the nylon 12 portion is evaluated under FDA 21 CFR 177.1500. Terminal products include breathable laminating interlayers, toe-counter films, and fabric bonding webs that require low-temperature flexural endurance without cracking at crease lines. This film track rejects melt temperatures above 235°C because higher residence time at the die lip promotes yellowing and gel formation in the light-stabilized formulation.
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Evonik Vestamid E40-S3 Heat & Light Stabilized Nylon 12/PEBA Elastomer is a polyether block amide formed from polyamide 12 hard segments and polyether soft segments. The commercial model E40-S3 encodes two distinctions: the Shore D hardness class of 40 per ISO 868 and the S3 heat and light stabilization package. The material is not a nylon 12 homopolymer and is not a plasticized polyamide; the low hardness derives from covalently bound polyether blocks, which reduces dependence on migratory plasticizers. Typical density is 1.01 g/cm³ under ISO 1183-1. Water absorption at saturation is 1.2% under ISO 62. Melting point, determined by differential scanning calorimetry per ISO 11357-3, is published at 166 °C. This combination places E40-S3 in the low-modulus segment of polyamide 12 elastomers, with tensile modulus typically in the range 80 MPa to 100 MPa under ISO 527-1/-2 and elongation at break above 300%. These values are routine screening data, not substitutes for application-specific certificates.
Polyamide 12-polyether block amides are susceptible to two degradation routes that differ in mechanism. The first is thermo-oxidative degradation in the melt, in which oxygen attacks the polyether soft segments and radicals abstract hydrogen from the PA12 backbone. This reduces melt viscosity, shifts melt volume-flow rate upward, and produces discoloration and gel particles. The second is photo-oxidative degradation during outdoor exposure, in which ultraviolet light generates radicals at surface layers and causes chain scission, cracking, and loss of elongation at break. The S3 package is intended to interrupt both routes through heat stabilizers that deactivate peroxy radicals and light stabilizers—commonly of the hindered amine light stabilizer class in polyamide elastomer formulations—that quench radical chain reactions. Exact stabilizer chemistry is not disclosed in the public grade data sheet. The result is a longer stable melt residence time and better retention of mechanical properties after weathering than a non-stabilized PA12 elastomer. Quantitative xenon arc retention data under ISO 4892-2 are not consistently published for E40-S3 across regional datasheets; weathering qualification should therefore require grade-specific exposure data from the supplier or independent testing.
The effect of stabilization is not limited to UV exposure. In extrusion of flexible tubing, the melt spends extended time in the die; a non-stabilized PEBA can show progressive viscosity loss and inferior weld-line strength. With S3 stabilization, the melt-volume-flow drift during a 30-minute dwell test can be lower, although published values for E40-S3 under this test are limited. The practical field observation is that stabilization reduces batch-to-batch variation in visible surface finish when recycled sprues or edge trim are reintroduced at controlled levels. Processing trials should nevertheless monitor melt-volume-flow rate under ISO 1133-1 because stabilizer consumption is cumulative and cannot be inferred from pellet color alone.
Pre-drying is a gate condition for melt processing. Pellets should be dried to a residual moisture target below 0.05% by weight. A desiccant dryer operating at 80 °C for 4 h to 6 h with a dew point of -40 °C is typical; shorter tray drying may be ineffective above 60% relative humidity. Moisture levels above 0.10% can produce splay, bubbles, and loss of melt strength because water hydrolyzes the polyether blocks at processing temperatures. In single-screw extrusion, polymer melt temperature is usually profiled from 170 °C in the feed zone to 210 °C at the metering zone. Extruders with L/D ratios between 24:1 and 30:1 and low-shear barrier screws are preferred; high compression ratios above 3.0:1 can increase melt temperature above 230 °C and consume the S3 stabilization package prematurely. Injection molding for Shore D 40 PEBA is generally performed at melt temperatures of 190 °C to 220 °C and mold temperatures of 20 °C to 60 °C. Lower mold temperatures shorten cycle time but raise frozen-in orientation and anisotropic shrinkage; higher mold temperatures improve surface replication and dimensional stability at the cost of longer demolding. Back pressure is commonly held below 5 MPa to reduce shear heating. Shot volume should be kept between 30% and 70% of barrel capacity to avoid excessive residence time distribution. These values reflect standard PA12 elastomer processing guidance; the current supplier processing bulletin for E40-S3 should be used for final setup.
Processing conflicts arise because the lower hardness of E40-S3 corresponds to a lower melt viscosity than that of semi-crystalline PA12 homopolymers, but the polyether segments also reduce thermal stability. The usable production window is bounded at the low end by high melt viscosity causing short shots or poor weld lines, and at the upper end by thermal degradation above 230 °C. The critical variable is temperature–time integral, not peak set temperature alone. A machine with a large barrel relative to shot weight and a long runner system can degrade material even when barrel set points are inside the recommended range. On production-scale injection molding machines with clamp force below 1,000 kN, the remedy for intermittent splay is not always increased melt temperature; it may require reduction in screw recovery speed, a larger gate, or a shorter hot-runner path. In coextrusion where E40-S3 is used as a soft outer layer over a rigid PA12 or rigid PEBA substrate, melt temperature uniformity across the die is more important than absolute set point. A die temperature variation of ±5 °C can cause layer thickness nonuniformity and poor interlayer adhesion. Published data for this specific configuration are limited, but similar PA12/PEBA structures indicate that a temperature gradient across the die must be mapped with surface thermocouples before adjusting screw speed. Drying interruptions and line stops longer than 15 min should trigger a purge because stagnant melt at 220 °C degrades even with S3 stabilization. The melt rheology of E40-S3 is shear-thinning; melt viscosity decreases with increasing shear rate. Processing simulations use capillary rheometry per ISO 11443 at 200 °C and 220 °C. A common production issue is that viscosity data from a melt flow index test under ISO 1133-1 cannot distinguish subtle thermal degradation because the test is a single-point measurement. Therefore incoming inspection should combine melt volume-flow rate with moisture content and, if possible, capillary viscosity at 100 s⁻¹ and 1,000 s⁻¹. Published data for E40-S3 at these exact shear rates is limited to supplier lot reports. That does not preclude process control; it simply means quality limits should be established from qualified production lots rather than literature values.
Post-mold shrinkage of semi-crystalline PEBA continues as crystallization progresses. For E40-S3, the low PA12 hard-segment content reduces shrinkage relative to homopolymer PA12. Typical mold shrinkage values for PA12 elastomers with Shore D 40 are in the range 0.5% to 1.2% depending on thickness, mold temperature, and flow orientation; dimensional acceptance should be verified after 24 h at 23 °C and 50% relative humidity. Post-mold annealing at 60 °C for 2 h can stabilize semicrystalline morphology, but published E40-S3-specific shrinkage curves are limited. Below the PA12 glass-transition temperature, the polyether phase retains segmental mobility. Differential scanning calorimetry may show a soft-phase glass transition below -40 °C; this contributes to impact resistance in cold environments. Low-temperature brittleness of PA12 elastomers is commonly assessed by ISO 812 or by Charpy impact at -40 °C; published values for E40-S3 are frequently summarized as no break, but the absence of a reported numeric means the end-user should request the complete lot test certificate. Hardness stability after heat aging is also sensitively dependent on the S3 package; a non-stabilized PEBA with the same Shore D 40 would lose elongation at break more rapidly in air below 120 °C.
The primary difference from unmodified nylon 12 is morphology. Semi-crystalline PA12 homopolymers have Shore D hardness near 72, tensile modulus above 1,000 MPa, and lower elongation at break under ISO 527. E40-S3 has Shore D 40, tensile modulus below 100 MPa, and higher low-temperature flexibility. The trade-off is reduced creep resistance, lower tensile strength, and higher gas permeability. Compared to higher-hardness PEBA grades, E40-S3 offers lower flexural stiffness but requires thicker sections to carry the same load. Compared to thermoplastic polyurethanes with similar Shore D hardness, E40-S3 has lower density and a different water-absorption profile; TPU substitution is not direct because ISO 868, ISO 527, and ISO 34-1 tear strength values do not capture dynamic wet-environment behavior. The grade should be evaluated against the exact comparative candidate under the same specimen preparation and conditioning protocols.
| Property | Method | Typical Value |
|---|---|---|
| Density | ISO 1183-1 | 1.01 g/cm³ |
| Hardness | ISO 868 | 40 Shore D |
| Tensile modulus | ISO 527-1/-2 | 80–100 MPa |
| Tensile stress at break | ISO 527-1/-2 | 30–35 MPa |
| Elongation at break | ISO 527-1/-2 | >300 % |
| Melting point | ISO 11357-3 | 166 °C |
| Water absorption, saturation | ISO 62 | 1.2 % |
Application contexts listed in Evonik technical literature include flexible pneumatic tubing, cable sheathing, sports shoe components, ski boot soft segments, and seals. In these markets, the Shore D 40 hardness and PA12-based chemistry are relevant because final parts must combine flexibility with chemical resistance and low-density construction. For tubing, the end-use qualification typically includes dimensional stability under pressure cycling, burst pressure testing according to the relevant product standard, and tensile property retention after air aging under ISO 188 or equivalent. For cable sheathing, abrasion resistance and low-temperature impact are evaluated according to the cable-specific IEC or national standard, with ISO 179-1 or ISO 180 used for notched or unnotched impact screening. For medical or food-contact use, E40-S3 does not automatically carry ISO 10993 certification, USP Class VI status, or compliance with Commission Regulation (EU) No 10/2011; such status must be confirmed with the supplier for the specific grade, colorant package, and conversion conditions. Regulatory documentation under REACH Regulation (EC) No 1907/2006 Article 33 and RoHS Directive 2011/65/EU Annex II should be obtained from the supplier certificate for the lot supplied. Published data for this specific configuration is limited in the public domain; material substitution and qualification should be based on current grade data sheets.
At the market-compliance level, the material must be integrated into the final article's risk assessment. For electrical and electronic equipment within the scope of RoHS Directive 2011/65/EU, Annex II restricts lead, mercury, cadmium, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers. For cadmium the threshold is 0.01% by weight in homogeneous material; for other restricted substances it is 0.1%. REACH Regulation (EC) No 1907/2006 Article 33 imposes communication duties for candidate-list SVHCs above 0.1%. The S3 stabilizer package may include substances that are not listed; however, a supplier letter of compliance should be obtained for the exact product code and color. For food-contact use, nylon 12 may be evaluated under FDA 21 CFR 177.1500, but elastomeric block copolymers with polyether segments are not automatically covered; Commission Regulation (EU) No 10/2011 requires specific migration testing of the final article. Without these documents, a generic data sheet is insufficient for market entry.