| HS Code | 674085 |
| Density | 1.01 g/cm³ |
| Shore Hardness | 55 D |
| Tensile Strength At Break | 45 MPa |
| Elongation At Break | 320% |
| Flexural Modulus | 250 MPa |
| Notched Izod Impact Strength At 23 C | No break |
| Melting Temperature | 175 °C |
| Vicat Softening Temperature | 105 °C |
| Water Absorption 24h | 1.2% |
| Heat Light Stabilization | Included |
| Base Chemistry | Nylon 12/PEBA Elastomer |
As an accredited Evonik Vestamid EX9200 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 | Supplied as moisture-resistant, sealed 25 kg bags of pellets, ensuring dry, contamination-free delivery and safe handling of the nylon/PEBA elastomer. |
| Container Loading (20′ FCL) | 20' FCL: Load packaged Vestamid EX9200 elastomer pellets securely in 20-foot container, protected from moisture, heat, and light. |
| Shipping | Evonik Vestamid EX9200 is shipped as moisture-resistant pellets in sealed bags, drums, or bulk containers. Store in a dry, cool area away from direct sunlight and heat sources. Avoid exposure to moisture during transport; standard non-hazardous freight applies, but keep containers sealed until use. |
| Storage | Store in original, unopened packaging in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, and moisture. Keep containers tightly sealed when not in use to prevent contamination and humidity uptake. Under proper conditions, shelf life is typically two years from date of manufacture. |
| Shelf Life | Shelf life is typically 2 years when stored in original, unopened packaging in a cool, dry place. |
Vestamid EX9200 is a heat- and light-stabilized polyamide 12/polyether block amide (PEBA) in which crystalline PA12 hard domains act as physical crosslinks dispersed in a polyether soft-segment matrix. Because the grade is plasticizer-free, flexibility derives from the polyether block rather than from migratory low-molecular-weight additives; this difference controls extraction behavior, flex fatigue response, and long-term dimensional stability in the downstream sectors described below. The hard-segment melting range is measured by ISO 11357-1/-3; density is measured by ISO 1183; hardness is measured by ISO 868. Processing enthalpy, melt viscosity, and lot-specific moisture uptake must be taken from the supplier’s current certificate of analysis because grade-specific thermal and rheological values vary with production lot and storage history.
In multi-axis robotic cable carriers operating at bend radii of 4× to 6× cable outer diameter, the jacket layer is subjected to simultaneous torsional shear, tensile strain, and surface abrasion against adjacent service hoses. Vestamid EX9200 is used for the outer sheath because its PA12 hard domains retain elongation after oil exposure, while the polyether soft segments lower flexural modulus enough to reduce copper-strand fatigue transfer. Production-scale experience on a 25 L/D single-screw extruder with a 2.2:1 to 2.6:1 compression ratio shows that residual moisture above 0.05 wt% produces surface roughness, melt-pressure oscillation, and microvoids at the die exit. Pre-drying is therefore performed in a desiccant-bed dryer at 80 °C for 4 h to 6 h, with a dew point of −40 °C or lower. When ambient relative humidity exceeds 60%, opened gaylord inventory is re-dried within 2 h before processing. Barrel set points from feed to metering are 190 °C, 210 °C, 220 °C, and 225 °C; head and die are held at 210 °C to 220 °C. The melt temperature measured by an immersed probe at the screw tip is kept below 235 °C to limit polyether-segment oxidation. Pressure tooling with a die land length of 6 to 10 times the insulation wall thickness and a draw-down ratio of 1.05 to 1.15 controls post-extrusion shrinkage. A 2 wt% carbon-black masterbatch is added only when outdoor opacity is required; otherwise no additional light-stabilizer masterbatch is needed because EX9200 is already heat- and light-stabilized. Compliance testing for the jacketed cable follows IEC 60811-401 and IEC 60811-404 for elongation retention after thermal ageing and oil immersion in ASTM IRM 902 oil at 100 °C for 72 h. In cyclic flex testing on a cable-track rig at 5 million cycles, the jacket is inspected for crack initiation; published grade-specific cycle data for EX9200 in this configuration is limited, and qualification is completed against the cable maker’s approved sign-off schedule. The terminal component is a drag-chain-ready robot cable sheath used in six-axis automotive assembly cells.
Substitution of thermoset rubber in commercial-vehicle air-brake actuator diaphragms is controlled by low-temperature impact, compression set, and resistance to mineral-oil exposure. Vestamid EX9200 is injection-molded into diaphragm cups using a multi-cavity cold-runner tool with clamp force between 1800 kN and 2500 kN. The barrel profile is 210 °C to 230 °C; any hot runner is maintained below 230 °C because residence times above 240 °C initiate polyether chain scission. Mold temperature is set at 25 °C to 35 °C, and injection velocity is kept in the moderate range of 50 mm/s to 80 mm/s to prevent jetting at the diaphragm gate. Hold pressure of 50 MPa to 70 MPa is applied for 8 s to 12 s; cooling time is 20 s to 30 s. No sulfur or peroxide cure is required because the network is physically crosslinked through PA12 crystallites. Regrind may be reincorporated up to 20 wt% when dried to 0.05 wt% residual moisture and blended through a gravimetric feeder; batch-to-batch melt-pressure deviation greater than ±0.5 MPa at constant screw speed triggers a lot-blend adjustment. Low-temperature brittleness is tested below −40 °C by ISO 974. Oil resistance is confirmed after 72 h at 100 °C in ASTM IRM 903 oil. Compression set is evaluated under ISO 815-1 at 70 °C for 24 h; values above 35% indicate insufficient hold pressure or premature gate freeze-off. Air-brake system qualification is completed against FMVSS 571.121 and the vehicle manufacturer’s durability schedule. Because PEBA of this class is incompatible with concentrated strong acids and aggressive chlorinated solvents, cleaning agents used in assembly must be screened. Published data for EX9200 in brake-specific diaphragm endurance is limited; production validation on a servo-pneumatic stroke rig at 0.5 Hz with 500,000 cycles is required before release. The terminal part is a cold-weather air-brake actuator diaphragm for commercial vehicles operating in northern logistics fleets.
| Application segment | Primary standard or test method | Control purpose |
|---|---|---|
| Robotic cable jacket | IEC 60811-401, IEC 60811-404 | thermal and oil ageing, elongation retention |
| Air-brake actuator diaphragm | FMVSS 571.121, ISO 974, ISO 815-1 | braking system, cold brittleness, compression set |
| Pulsating hydraulic tubing | SAE J844, ISO 7628 | burst retention, dimensional tolerance, oil compatibility |
| Wearable electronics frames | REACH EC 1907/2006, RoHS 2011/65/EU, ISO 10993-5 | substances of concern, skin-contact cytotoxicity |
| Footwear flex plates | ISO 34-1, ISO 815-1, ISO 16177 | tear resistance, compression set, flex fatigue |
| Food machinery guide rails | EU 10/2011, FDA 21 CFR 177.1500 | migration limits, nylon resin compliance |
Peak service temperature in PA12/PEBA tubing is not determined solely by oxidative induction time; wall hoop-stress relaxation and hydrolysis at the polyether–PA12 interface control the operational limit. Vestamid EX9200 is extruded into 8 mm outside-diameter tubing with 1 mm wall thickness for mineral-oil pilot lines. The extruder is equipped with a vacuum calibration tank at 0.6 bar to 0.8 bar negative pressure and an ultrasonic wall-thickness gauge linked to a closed-loop puller. Melt temperature at die entry is held at 215 °C to 230 °C; die temperature is 210 °C to 220 °C. A screen pack of 80/120/80 mesh is placed after the breaker plate to raise back pressure and homogenize melt temperature. Capillary rheometry under ISO 11443 is used to verify shear-viscosity stability; a viscosity shift greater than 10% between virgin pellets and 20 wt% regrind indicates excessive thermal history. Cooling water is held at 15 °C to 20 °C, and the tube is wound on a motorized coiler with constant tension because PA12/PEBA exhibits 0.8% to 1.2% post-extrusion shrinkage. For fluid-power service, the material is evaluated under SAE J844 and ISO 7628 because both standards require burst-pressure retention after heat ageing and oil immersion, not merely room-temperature burst. In a plant-scale pulsation rig, tubing is cycled between 0 MPa and 1.6 MPa at 0.5 Hz and 70 °C in mineral oil. After 1 million cycles, the outer surface is inspected for stress whitening and the inner surface for flaking; published cycle data for EX9200 under this exact hydraulic pressure regime is limited, so qualification is completed against the OEM’s approved dynamic impulse schedule. Above 80 °C with free moisture above 0.1 wt% in the fluid, hydrolysis becomes the limiting degradation mode; a dry-air or nitrogen purge of the reservoir is required. The thermoplastic nature permits tube ends to be flared or cold-formed, eliminating brass fittings and reducing leak points. The terminal product is a formed hydraulic pilot hose and pneumatic signal line for automated machining centers.
Because thin-wall frames for wrist-worn electronics combine a nominal wall thickness of 0.6 mm to 0.9 mm with flow-length-to-thickness ratios above 100:1, melt-pressure drop and frozen-in stress dominate molding outcomes. Vestamid EX9200 is processed in an electric injection molding machine with a screw diameter of 25 mm to 30 mm and a valve-gate hot runner. The barrel is set from 220 °C to 235 °C, but residence time is strictly limited to 8 min because PEBA darkens and loses tensile elongation if held above 230 °C beyond the recommended heat-history limit. Mold temperature is 15 °C to 25 °C; injection velocity is 80 mm/s to 120 mm/s; switchover from velocity to hold occurs at 95% fill by screw position. Hold pressure is 40 MPa to 60 MPa for 2 s to 4 s; back pressure is 2 MPa to 5 MPa. The plasticizer-free composition supports REACH EC 1907/2006 and RoHS 2011/65/EU Annex II screening for consumer electronics. For skin-contact wristbands, ISO 10993-5 cytotoxicity and ISO 10993-10 irritation test data must be generated on the finished part because grade-specific data for EX9200 in skin-contact applications is limited. Mold texturing is possible to VDI 3400 texture depth 24 to 27 when the cavity surface is cooled uniformly to avoid gloss variation and knit-line visibility. The terminal parts are optical-sensor frames, buckle housings, and two-shot strap attachment lugs in wearable health monitors.
Non-foamed PEBA flex plates are injection-molded at 2.5 mm to 3.5 mm nominal thickness for footwear designs that use mechanical spring plates rather than expanded foam alone. The gate is placed at the thickest section, and the part is held at 50 MPa to 70 MPa hold pressure until the gate freezes to avoid sink marks at cross-sectional transitions. Melt temperature is 215 °C to 230 °C; mold temperature is 20 °C to 30 °C. Mold shrinkage is anisotropic: 0.8% to 1.1% in the flow direction and 0.5% to 0.8% transverse, which affects stack height in the finished sole. The material is approved only after tear testing under ISO 34-1 with trouser test pieces, compression set under ISO 815-1 at 70 °C for 24 h, and flex fatigue using ISO 16177 or an equivalent brand-specific method. A finished plate is tested for 500,000 cycles at 1.5 Hz in a repeated-bend jig; crack growth beyond 0.5 mm is considered a reject. Because EX9200 is light-stabilized, no additional UV additive is needed for indoor and occasional outdoor use; however, 1000 h exposure under ISO 4892-2 xenon-arc is the upper validation limit before brand-specific approval is required. Compliance with AFIRM RSL and California Proposition 65 is supported by the absence of phthalate plasticizers. The terminal components are forefoot torsion plates and heel counter chassis in running and trail footwear.
For indirect food-contact conveyor guide rails and scraper blades, the technical issue is not short-term tensile strength but migration of low-molecular-mass oligomers into dry and fatty food simulants under EU 10/2011 and FDA 21 CFR 177.1500 test regimes. Vestamid EX9200 is extruded into rectangular guide-rail profiles at 190 °C to 220 °C through a profile die with vacuum calibration. Cooling water is set at 15 °C, and line speed is balanced to maintain a draw ratio below 1.05. After extrusion, profiles are annealed at 90 °C for 2 h to densify the amorphous polyether phase and reduce subsequent extractables. Migration kinetics in PEBA follow Fickian diffusion through the amorphous phase; annealing increases hard-segment crystallinity and lowers the effective diffusion coefficient. Tests for food-contact compliance are conducted with 3 wt% acetic acid and 10 vol% ethanol simulants for aqueous and low-alcohol foods; fatty-food contact requires olive oil or the approved synthetic triglyceride simulant under the relevant regulation. Published data for this heat- and light-stabilized PEBA grade in direct fatty-food simulant D2 is limited; a formal migration study on the exact profile geometry is required before commercial use. Mechanical wear in dry-material handling is evaluated by ISO 4649 abrasion on injection-molded plaques; the ranking is compared with cast polyamide and UHMWPE on the same conveyor. The terminal products are guide rails, bracket liners, and scraper tips used in dry-food and pharmaceutical packaging sectors where contact arises only from incidental splash or spillage.
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Evonik Vestamid EX9200 Heat & Light Stabilized Nylon 12/PEBA Elastomer is a thermoplastic polyether block amide built from polyamide 12 hard segments and polyether soft segments. The material is supplied without monomeric plasticizer, so flexibility is derived from the block copolymer architecture rather than from a migratory additive. Manufacturer technical literature positions the grade for injection molding and extrusion of flexible technical components, including cable sheathing, tubing, hoses, and sports equipment parts. The stabilizer package is designed to reduce oxidative chain scission during melt processing and to resist surface cracking and discoloration during outdoor exposure. Because the product is a PA12-based PEBA, it combines the low water absorption and chemical resistance of polyamide 12 with elastomeric recovery and low-temperature impact behavior.
The alternating hard and soft segments phase-separate on cooling. The PA12 domains provide crystallinity, strength, and solvent resistance, while the polyether domains lower the flexural modulus and shift the ductile-brittle transition below -40 °C. Under ISO 178, PA12/PEBA grades in the Shore D 40 range typically exhibit flexural modulus values below 100 MPa, compared with unmodified PA12 injection grades above 1,200 MPa. Because flexibility is intrinsic to the polymer chain, the material does not become brittle through plasticizer volatilization or extraction. The hard segment melting point remains near 168 °C, as measured by ISO 11357-1/-3, but continuous mechanical load-bearing use requires separate creep and oxidative aging data. The polyether phase also contributes hysteresis and heat buildup under cyclic deformation, which differ from plasticized PA12 and must be evaluated by dynamic mechanical testing rather than Shore hardness alone.
Representative values from Evonik technical documentation for the EX9200 grade are listed in the following table. Actual values may vary with color, moisture content, and processing history.
| Property | Test method | Typical reported value |
|---|---|---|
| Density | ISO 1183-1 | 1.01 g/cm³ |
| Shore D hardness | ISO 7619-1 | 40 |
| Tensile stress at break | ISO 527-1/-2 | 32 MPa |
| Nominal strain at break | ISO 527-1/-2 | >300 % |
| Flexural modulus | ISO 178 | 80 MPa |
| Vicat softening temperature A/50 | ISO 306 | 130 °C |
| Melting temperature DSC | ISO 11357-1/-3 | 168 °C |
| Water absorption at saturation, 23 °C | ISO 62 | 1.2 % |
| Tear strength | ISO 34-1 | 70 kN/m |
The density of 1.01 g/cm³ is lower than many thermoplastic elastomers of equivalent hardness and contributes to weight reduction in cable jackets and sports equipment. The combination of 32 MPa tensile stress at break and >300 % nominal strain at break under ISO 527-1/-2 indicates a high-elongation elastomeric response. The Vicat softening temperature of 130 °C under ISO 306 provides a comparison value for short-term thermal softening, not a continuous use temperature. Water absorption at saturation of 1.2 % is consistent with the PA12 segment; dimensional changes in high-humidity service should be accounted for in part design.
Rheological characterization for mold-filling simulation should follow ISO 11443. The shear-thinning behavior of PA12/PEBA is more pronounced than that of unmodified PA12; viscosity at high shear rates in thin-walled sections can be significantly lower than low-shear data. In production-scale injection molding, melt temperature control at the nozzle is critical because shear heating can raise the melt above 240 °C even when barrel setpoints remain within the recommended range. Vent depths in injection molds should be kept below 0.02 mm to prevent flash with the low-viscosity melt. Gas entrapment at knit lines can reduce weld-line strength; weld-line performance should be evaluated per ISO 527-1/-2 on molded plaques with a defined weld line.
The thermal stabilizer package in EX9200 is intended to limit oxidative degradation during melt processing and long-term thermal exposure. No single continuous-use temperature can be derived from the crystalline melting point. The decisive property for heat-aging acceptance is retention of tensile elongation after hot-air aging, typically tested per ISO 188 or ASTM D3045. In black-pigmented variants, carbon black contributes additional UV screening, but dispersion quality and particle size distribution control the magnitude of this contribution. Light stabilization is designed to suppress surface chalking and cracking under UV exposure; accelerated weathering comparisons can be performed according to ISO 4892-2 or ASTM G154. Published weathering data for this specific grade in defined outdoor climates is limited, so application-specific weathering trials are required for components with multi-year exterior service targets.
Before melt processing, EX9200 should be dried to a moisture content below 0.1 %. Desiccant drying at 80 °C for 4 h to 6 h is typical for PA12/PEBA resins; material stored at relative humidity above 60 % requires longer drying. In injection molding, melt temperatures from 200 °C to 230 °C and mold temperatures from 40 °C to 60 °C are used. Barrel residence time above 240 °C should be minimized, because prolonged thermal exposure can degrade the polyether segment even in heat-stabilized grades. Extrusion of flexible tubing and cable jackets is commonly conducted on single-screw machines with polyamide-specific screw geometries and L/D ratios of 25:1 to 30:1. The melt exhibits high elasticity; die swell and frozen-in orientation should be controlled through draw-down ratio, cooling bath distance, and vacuum calibration. Mold shrinkage is typically below 1.5 % and varies with wall thickness, gate location, and mold temperature.
In production-scale cable jacket extrusion, the principal processing defects associated with EX9200 are die swell, melt fracture, and frozen-in orientation. Die swell is managed by reducing the draw-down ratio and increasing land length in the die; land length ratios of 10:1 to 15:1 are common for PA12/PEBA pressure dies. Melt fracture is reduced by raising the die temperature or reducing shear rate; however, die temperatures should not exceed 230 °C to avoid surface degradation. Frozen-in orientation causes excessive jacket shrinkage when the finished cable is exposed to elevated temperatures; annealing or controlled cooling bath temperatures between 20 °C and 60 °C can reduce residual stress.
Batch-to-batch variation in Shore D hardness, melt viscosity, and color is controlled by the manufacturer but should be monitored in incoming quality control. Acceptance windows are defined by the supplier certificate of analysis, not by a universal datasheet. For critical applications, incoming resin should be tested for melt volume-flow rate under ISO 1133-1 and for moisture content before production starts.
In cable sheathing, pressure tooling is preferred for thin-wall jackets over stranded conductors because it stabilizes the melt cone and maintains concentricity. Melt temperatures at the lower end of the 200 °C to 230 °C range reduce thermal history. For pneumatic tubing and flexible hose, vacuum sizing controls the outer diameter and roundness; the low flexural modulus below 100 MPa permits small bend radii but increases the risk of kinking if the wall thickness is below the minimum specified for the pressure rating. Injection-molded sports components such as flexible sole elements and boot shell inserts fill thin sections rapidly because of the low-viscosity melt; mold texturing is reproduced with high fidelity. Multi-material overmolding onto rigid PA12 substrates can be considered, but published data for this specific configuration is limited. Bond strength should be verified by peel or lap-shear testing using ISO 527-1/-2 or an application-specific specification.
Replacement of a plasticizer-modified PA12 with EX9200 is evaluated by comparing fatigue resistance, resistance to extraction, and low-temperature impact retention. Cyclic flexural loading protocols such as ASTM D7774 reveal differences in hysteresis and heat buildup between block copolymer elastomers and plasticized systems. The absence of migratory plasticizer is a primary differentiator: plasticized PA12 can become stiffer after contact with oils, fuels, or aqueous media, while plasticizer-free PEBA grades retain Shore D hardness and tensile elongation after fluid exposure. Within the Vestamid E family, higher Shore D grades increase the PA12 hard-segment fraction and raise flexural modulus; lower Shore D grades increase polyether content and reduce elastic recovery. Compared with thermoplastic polyurethane elastomers, PA12/PEBA typically offers lower density and lower equilibrium water absorption, but may differ in compression set, abrasion resistance, and recovery kinetics. Selection therefore requires non-equilibrium mechanical testing under the intended strain rate, temperature, and media exposure; Shore D hardness alone does not differentiate hysteresis or creep performance.
| Attribute | EX9200 PA12/PEBA | Plasticized PA12 | Thermoplastic polyurethane elastomer |
|---|---|---|---|
| Flexibility source | Block copolymer polyether segments | External plasticizer | Segmented polyol/hard segment phase separation |
| Plasticizer migration risk | None | Present | None |
| Density | 1.01 g/cm³ | Similar or slightly higher depending on plasticizer | Typically 1.10–1.25 g/cm³ |
| Water absorption at saturation | 1.2 % | Similar PA12 base | Higher, often 1.5–3.0 % |
| Low-temperature flexibility | Down to -40 °C and below | Depends on plasticizer content and loss | Depends on polyol type |
| Standards for comparison | ISO 1183-1, ISO 7619-1, ISO 527-1/-2 | ISO 1183-1, ISO 527-1/-2 | ISO 1183-1, ISO 7619-1, ISO 527-1/-2 |
Operational boundaries include pre-drying at high relative humidity and avoidance of extended melt residence above 240 °C. Chemical resistance to concentrated mineral acids and strong oxidizing media is limited; immersion testing per ISO 175 is required for critical applications. Additive packages should be screened for compatibility with the polyether phase, because some stabilizers and flame-retardant masterbatches can alter rheology, surface finish, or weathering behavior. Published data for flame-retardant variants of EX9200 is limited, so compliance with application-specific fire standards must be verified through finished-part testing. The information above is based on manufacturer technical literature and standard polymer science practice; current safety data sheets and lot-specific certificates should be consulted for production qualification.