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Evonik VESTAMID® E47-S1 Nylon 12 Elastomer

    • Product Name: Evonik VESTAMID® E47-S1 Nylon 12 Elastomer
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 421665
    Density 1.02 g/cm³
    Melting Point 168 °C
    Shore Hardness 47 Shore D
    Tensile Strength At Break 35 MPa
    Elongation At Break 400 %
    Flexural Modulus 180 MPa
    Charpy Impact Strength Notched 23 C No break
    Charpy Impact Strength Notched 40 C No break
    Water Absorption 24 H 23 C 0.4 %
    Vicat Softening Temperature 115 °C
    Glass Transition Temperature -40 °C

    As an accredited Evonik VESTAMID® E47-S1 Nylon 12 Elastomer factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied as moisture-resistant sealed 25 kg bags of nylon 12 elastomer pellets, ensuring safe, easy handling and storage.
    Container Loading (20′ FCL) 20′ FCL: VESTAMID® E47-S1 Nylon 12 Elastomer loaded in moisture-protective packaging, securely palletized, ventilated, and containerized for safe transit.
    Shipping VESTAMID® E47-S1 Nylon 12 Elastomer ships as non-hazardous material in sealed moisture-proof bags on pallets, protected from damage and contamination. Keep dry, out of direct sunlight, and below 50°C. Standard truck, rail, or sea freight is suitable, with careful handling to prevent bag punctures and product contamination.
    Storage Store VESTAMID® E47-S1 in its original, sealed packaging in a cool, dry place, away from direct sunlight, heat sources, and high humidity. Since nylon 12 absorbs moisture, keep containers tightly closed to prevent water uptake, which can affect processing and performance. Under proper conditions, shelf life is typically two years.
    Shelf Life Shelf life is typically 2 years from manufacture when stored sealed, cool, and dry in original packaging.
    Application of Evonik VESTAMID® E47-S1 Nylon 12 Elastomer
    In heavy-duty commercial vehicle air brake systems, VESTAMID® E47-S1 is converted into straight and coiled tubing with outside diameters from 6 mm to 12 mm and wall thicknesses from 1.0 mm to 2.0 mm. The nylon 12 elastomer grade is selected because the polyether soft segments retain flexibility at temperatures down to −40 °C, while the PA12 hard segments limit dimensional change in humid compressed-air environments. Drying prior to extrusion is carried out in a desiccant dryer at 80 °C for 4 h to 6 h until the moisture content is below 0.10% by weight. Processors using single-screw extruders with L/D ratios from 24:1 to 30:1 and compression ratios between 2.5:1 and 3:1 typically set barrel temperatures from 210 °C to 240 °C, with the die head at 230 °C to 250 °C. The tube is calibrated in a vacuum tank maintained at 15 °C to 25 °C, and the haul-off speed is matched to extruder output to control outside diameter and ovality. A typical carbon black masterbatch addition is 2 wt% to 3 wt% of a 40% carbon black concentrate in a PA12 carrier, producing a final carbon black content of approximately 0.8 wt% to 1.2 wt% for UV stabilization. No external plasticizer is used because flexibility is built into the block copolymer structure. Compliance for coiled air brake tubing is evaluated under SAE J844 or DIN 73378, depending on the market, and the material is assessed for low-temperature impact, burst pressure retention after heat aging, and resistance to compressor oil condensate. The terminal product is a pre-formed or straight air brake line that must withstand repeated pressure cycling in tractor-trailer combinations.

    What Kink Radius and Post-Sterilization Hardness Shift Are Observed in Thin-Wall Catheter Shafts?

    Thin-wall catheter shafts produced from E47-S1 require a controlled extrusion line because the grade does not contain a migrating plasticizer, and the soft segment crystallinity contributes to kink radius. Drying is performed at 80 °C for 4 h to 6 h to a moisture level below 0.10%, using a desiccant dryer with a dew point of −40 °C or lower. The polymer is processed on a single-screw extruder with an L/D ratio of 24:1 to 25:1, a compression ratio between 2.5:1 and 3.0:1, and a barrier screw recommended for semi-crystalline block copolymers. Barrel temperatures from feed to metering zone are set between 210 °C and 235 °C, while the die and adapter are held at 225 °C to 240 °C. Thin-wall tubing with outside diameters from 1 mm to 3 mm and wall thicknesses from 0.15 mm to 0.50 mm is achievable, but the draw ratio between die land and final tube should be kept below 5:1; higher draw ratios increase orientation and may create a kink-prone anisotropy in the finished shaft. Vacuum calibration is carried out with water at 30 °C to 45 °C rather than chilled water, because rapid cooling of thin walls tends to suppress crystallinity and produce uncontrolled post-extrusion shrinkage. The resulting tubing is cut to length and assembled into diagnostic catheters, delivery sheaths, and fluid administration sets.For medical applications, the grade is not automatically medical-grade; compliance is established under ISO 10993-1 with cytotoxicity per ISO 10993-5 and, where required, hemocompatibility per ISO 10993-4. The limiting factor for gamma sterilization is not hardness but elongation retention; irradiation above 25 kGy can reduce elongation at break by more than 10% depending on dose rate, temperature, and wall thickness, so terminal sterilization is often validated using ethylene oxide at 45 °C to 55 °C with relative humidity of 60% to 70% for 2 h to 4 h, followed by forced aeration. If radiopacity is required, barium sulfate is compounded at 20 wt% to 30 wt%; the addition increases melt viscosity, narrows the processing window, and raises the Shore D hardness by approximately 1 to 3 points under ISO 868. Published data for this specific configuration is limited; the shift is compound-dependent. Assemblies are then tested for kink radius by wrapping around mandrels of decreasing diameter and for post-sterilization dimensional stability by measuring lumen diameter and shaft length before and after the sterilization cycle.In automated assembly machinery, flexible pneumatic control lines and robot dress-pack conduits are produced from E47-S1 because the material is exposed to repeated bending and occasional contact with cutting fluids. A stable formulation is 100 parts by weight of dried resin with 2 wt% of a PA12-based carbon black masterbatch for outdoor UV resistance; for indoor use, the masterbatch is omitted or replaced with a non-black pigment at 0.5 wt% to 1.0 wt%, provided the pigment carrier does not reduce burst strength. The melt is processed on a 24:1 L/D single-screw extruder with a general-purpose nylon screw, with barrel temperatures from 215 °C to 235 °C and a die temperature from 225 °C to 240 °C. Tube dimensions in this sector commonly range from 4 mm to 8 mm outside diameter with wall thicknesses from 0.75 mm to 1.5 mm. The extrudate is cooled in a water bath at 20 °C, dried, and cut into straight lengths or wound onto spools. Performance is checked by burst tests at 23 °C and flex fatigue tests under a defined bend radius, typically 6 to 10 times the outside diameter, according to internal plant standards or ISO 14743. Compliance with EU REACH Regulation 1907/2006 and RoHS Directive 2011/65/EU applies when the product is sold in Europe; a supplier declaration is required for SVHC content. The resulting product is used as spiral or straight pneumatic tubing in CNC machines, packaging lines, and automotive plants.
    Regulatory and test references by application segment
    Downstream segmentMaterial claim assessedReference standard or test method
    Automotive air brake tubingLow-temperature impact, heat-aged burst retentionSAE J844, DIN 73378
    Medical catheter shaftCytotoxicity, hemocompatibility where requiredISO 10993-1, ISO 10993-5, ISO 10993-4
    Industrial pneumatic lineBurst strength, flex fatigue, SVHC absenceISO 14743, REACH 1907/2006, RoHS 2011/65/EU
    Ski boot insertNotched Charpy at −30 °C, Shore D hardnessISO 179-1/1eA, ISO 868
    Cable jacketFlame spread where required, abrasion, elongationIEC 60332-1-2, UL 1581 if specified
    Handheld overmoldComparative tracking index, insulation resistance where covering charged partsIEC 60112, IEC 60093

    When Cold Impact Strength Governs Injection-Molded Ski Boot Shell Inserts

    Injection-molded components in winter sports equipment use E47-S1 where a Shore D hardness of 47 under ISO 868 is desired with low-temperature impact resistance. The material is dried to below 0.10% moisture and injected at melt temperatures from 230 °C to 260 °C. Mold temperature is maintained between 30 °C and 60 °C, because lower mold temperatures can produce frozen-in stress in thick-to-thin transitions. A processing regrind ratio of up to 15 wt% is permitted if the regrind is dry and free of contamination; higher levels raise the risk of black specks and reduce notched impact. Notched Charpy impact testing under ISO 179-1/1eA at −30 °C is used to qualify incoming lots and molded test plaques. The terminal components include ski boot flex inserts, snowboard binding highbacks, and heel pads, where the flexural modulus is matched to the shell rigidity by varying wall thickness rather than by adding plasticizer.
    Start-point processing parameters by conversion route
    Conversion routeDrying conditionMelt or die temperatureTooling or cooling condition
    Thin-wall medical tube extrusion80 °C, 4–6 h, moisture <0.10%Barrel 210–235 °C, die 225–240 °CVacuum water 30–45 °C, draw ratio <5:1
    Pneumatic tubing extrusion80 °C, moisture <0.10%Barrel 215–235 °C, die 225–240 °CWater bath 20 °C
    Sports injection molding80 °C, moisture <0.10%Melt 230–260 °CMold 30–60 °C
    Overmolding80 °C, moisture <0.10%Melt 220–240 °CMold 40–60 °C, vent depth 0.02–0.04 mm
    For cable jackets used in robotic dress packs, sensor cables, and offshore instrumentation, E47-S1 is pressure-extruded over twisted conductors. Melt temperature is held at 220 °C to 250 °C, and the screw L/D ratio is 24:1 to 30:1 with a compression ratio of 2.5:1. Jacket wall thickness is normally 0.5 mm to 1.5 mm. Carbon black concentration in the jacket is typically 2 wt% to 3 wt% of a 40% concentrate to meet outdoor UV exposure, and the moisture content is controlled below 0.10% before processing. Under ISO 62 at 23 °C and 50% RH, PA12-based elastomers typically absorb below 1.5% moisture by weight, which supports insulation resistance in humid environments compared with nylon 6 or nylon 66 alternatives. Abrasion resistance is evaluated by a pin-on-disc method or cable-specific cyclic abrasion procedures, and torsion resistance is tested by repeated bending over a radius of 5 to 8 times the cable outside diameter. The neat grade is not flame-retarded; where IEC 60332-1-2 flame spread performance is specified, a flame-retardant masterbatch is required, and the resulting elongation and cold flexibility must be revalidated. The terminal product is a flexible cable connector, robot dress pack, or marine instrumentation harness.

    Overmolding of Handheld Industrial Device Housings with Shore D 47 Soft-Touch Zones

    Handheld industrial scanners and power tool housings are overmolded with E47-S1 to provide a chemical-resistant grip surface without a soft-touch coating that can wear. The rigid substrate is molded first, often from PC/ABS or a filled polyamide, and then transferred to a second injection unit. The elastomer is processed at melt temperatures from 220 °C to 240 °C with mold temperatures from 40 °C to 60 °C. Bond strength is dominated by substrate surface temperature and melt contact time; cavities with vent depths of 0.02 mm to 0.04 mm reduce gas trapping at the interface. A typical formulation is 100 parts by weight of dried resin with 0.5 wt% to 1.0 wt% color masterbatch; regrind is normally limited to 10 wt% because overmolding requires consistent fill speed. The finished housing is tested for peel adhesion by a 90° peel fixture and for chemical resistance by immersion in common industrial hand sanitizers and cutting oils at 23 °C for 24 h. Electrical safety creepage distances in the rigid substrate are not altered by the overmold if the soft material is kept outside the creepage path; if the overmolded layer covers a charged terminal, comparative tracking index and insulation resistance must be evaluated under IEC 60112 and IEC 60093. The terminal components are barcode scanner housings, pressure-washer handles, and portable measuring instruments.
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    Certification & Compliance
    More Introduction

    VESTAMID® E47-S1 is supplied as an unfilled, plasticiser-free polyether block amide (PEBA) resin in which polyamide 12 forms the semi-crystalline hard segment and polyether forms the elastomeric soft segment. The product nomenclature identifies the nominal Shore D durometer target of 47 when measured on an injection-moulded plaque according to ISO 868. As a nylon 12 elastomer, it is not an externally plasticised compound and therefore does not exhibit the progressive surface tack, squeeze-out, or plasticiser migration associated with flexible PVC or monomeric plasticiser systems. Manufacturer-published typical property data for dry-as-moulded specimens conditioned at 23 °C and 50 % relative humidity are summarised below.

    PropertyTypical ValueTest Method
    Shore D hardness47ISO 868
    Density1.02 g/cm³ISO 1183-1
    Flexural modulus210 MPaISO 178
    Tensile stress at break44 MPaISO 527-1/-2
    Tensile strain at break>350 %ISO 527-1/-2
    Charpy notched impact at 23 °Cno breakISO 179-1/1eA
    Melting temperature168 °CISO 11357-3
    Vicat softening temperature A/50130 °CISO 306
    Water absorption at saturation1.3 %ISO 62

    The combination of density at 1.02 g/cm³ and flexural modulus at 210 MPa is significantly below the stiffness of polyamide 12 homopolymer grades, while the dry, non-migrating surface remains functional under repeated flexural loading. At subzero temperatures, the polyether soft block retains segmental mobility; dynamic mechanical analysis of comparable PEBA chemistries places the soft-segment glass transition below -40 °C, although published data for this specific grade in complex part geometry is limited. Moisture saturation of 1.3 % according to ISO 62 indicates that absorbed water acts as a mild plasticiser, reducing hardness and increasing elongation at equilibrium. This moisture response must be incorporated into dimensional tolerance stacks and hot-wet service evaluations rather than treated as a simple surface condition.

    What Conversion Parameters Minimise Gate Splay and Freeze-Off in Thin-Wall Components?

    Pre-drying represents the first conversion control for VESTAMID® E47-S1. Incoming pellets should be dried in a dehumidifying dryer with a dew point no higher than -40 °C at 80 °C for 4 h to 6 h to reduce residual moisture below 0.10 % by weight. Moisture above 0.15 % hydrolyses the PA12 hard block during plastication; the resulting melt pressure drop at the nozzle, surface splay, and reduction in notched impact strength are observed on production-scale injection moulding machines fitting 35 mm general-purpose screws with L/D 22. Melt temperatures measured at the nozzle should remain between 210 °C and 250 °C. Prolonged residence time above 280 °C causes oxidation of the polyether soft segment and a shift toward higher yellowness index.

    Mould temperatures of 20 °C to 60 °C are used, with the upper half of the range applied to wall sections below 1.5 mm to delay premature gate freeze. Representative processing windows on a 30 mm screw include injection velocities of 100 mm/s to 250 mm/s, hydraulic holding pressure of 40 MPa to 60 MPa, back pressure of 5 MPa to 10 MPa, and screw speed of 60 min⁻¹ to 100 min⁻¹. Because E47-S1 has lower viscosity than semi-crystalline PA12 homopolymer at equivalent melt temperature, transfer from existing PA12 settings frequently produces overpacking and mould flash. A gate-seal study should therefore be performed to determine holding time; the lower melt viscosity also reduces cushion stability if screw recovery is short. In thin-wall connectors and snap-fit housings, freeze-off at the gate is the primary constraint, not melt temperature at the front zone.

    For melt extrusion of tubing and cable sheathing, a single-screw extruder with L/D 24 to 30, a barrier screw with compression ratio 2.5:1 to 3.0:1, and breaker-plate screen packs of 40/60/80 mesh is suitable. Melt temperature at the adapter should not exceed 250 °C for extended campaigns, because the polyether segment is the thermolabile portion of the block copolymer. Batch-to-batch viscosity deviation on a 25 mm instrumented extruder is typically controlled within 5 % when incoming pellet moisture and regrind ratio are held constant. Regrind addition up to 20 % does not produce meaningful hardness shift in dry-blend operation, but higher levels alter shear heating and should be validated with melt flow rate measurement according to ISO 1133-1.

    In cable sheathing and pneumatic tubing, the absence of external plasticiser becomes operationally significant. Plasticised PVC and externally plasticised flexible nylon compounds can exhibit surface migration that contaminates connector contacts or reduces flexibility after thermal ageing. Because VESTAMID® E47-S1 obtains its 47 Shore D hardness from block architecture rather than additive plasticisation, extractable content remains low. Converters should nevertheless verify specific global migration against (EU) 10/2011 or 21 CFR 177.1500 when food-contact or potable-water certifications are required for the finished article, because processing residues and regrind history affect final compliance. For hydraulic and pneumatic tube applications, the PA12 block imparts resistance to aliphatic hydrocarbons, greases, and zinc-free hydraulic fluids, while the polyether block reduces flexural modulus for tighter minimum bend radius. Long-term fluid exposure should be evaluated by volume and mass change according to ISO 175, since chlorinated hydrocarbons, ketones, and strong polar solvents cause measurable swelling. The material is suitable for co-extrusion with PA12 and polyamide-based tie layers, provided the adapter temperature remains below 250 °C to avoid degradation between layers.

    Sports footwear sole units and ski boot components injection-moulded from E47-S1 are normally gated at the thickest article section. The low flexural modulus allows articulation zones to flex without stress whitening. Cyclic flexural loading at 23 °C should be evaluated by flexural fatigue methods rather than tensile data alone, because the strain field in a sole unit involves bending and recovery rather than uniaxial extension. In two-shot moulding with rigid PA12 or thermoplastic polyurethane substrates, melt temperature mismatch should be kept within 20 °C at the interface to avoid freezing before bond formation. Where texturing is required, higher mould temperatures within the 40 °C to 60 °C range improve grain replication without producing polyether degradation.

    Comparative Shore Hardness and Flexural Modulus Across the VESTAMID E Family

    Grade selection within the VESTAMID E family is governed by Shore D hardness. VESTAMID E40-S1 carries a Shore D hardness of 40 according to ISO 868, placing it below E47-S1 for snap-fit retention and bending stiffness. VESTAMID E55-S1 carries a Shore D hardness of 55, giving higher flexural modulus and better resistance to buckling in thin-wall profiles, but with reduced low-temperature elasticity relative to E47-S1. VESTAMID E62-S1, at Shore D 62, approaches lower-stiffness PA12 homopolymer behaviour while retaining elastic recovery. The hardness progression is not linear in modulus; a durometer increase from 47 to 55 produces a proportionally larger gain in bending resistance than the raw durometer spread suggests. Finite element analysis for snap-fit designs should therefore use a secant modulus at the intended design strain rather than the initial flexural modulus of 210 MPa.

    Compared with polyamide 12 homopolymer, VESTAMID® E47-S1 is substantially more compliant. PA12 homopolymer grades typically exhibit flexural modulus in the range of 1,300 MPa to 1,500 MPa, roughly an order of magnitude above E47-S1. This difference is critical for snap-fit and living-hinge applications; the homopolymer provides rigidity and dimensional stability, while E47-S1 supplies recovery after bending and lower stress concentration on adjoining features. When replacing PA12 homopolymer with E47-S1, wall stock should not be reduced without evaluating creep modulus at the service temperature according to ISO 899-1, because the lower initial modulus does not imply equivalent long-term deformation resistance under load.

    Unlike plasticised nylon 12 compounds that achieve flexibility through external plasticisers, E47-S1 retains flexibility through covalent bonding between PA12 hard blocks and polyether soft blocks. This structural difference reduces plasticiser loss during thermal ageing and eliminates interfacial bloom at elevated humidity. However, the polyether block is more oxidatively sensitive than PA12 alone, so hot-air ageing resistance is not equivalent to unplasticised PA12 homopolymer. The product should not be regarded as a direct drop-in for PA12 homopolymer in under-hood automotive lines where continuous dry heat above 125 °C is encountered.

    When E47-S1 Replaces Plasticised PVC in Seals and Flexible Mandrel Hoses

    When E47-S1 is specified for dynamic seals, diaphragms, or flexible mandrel hoses, the service boundary is set by hysteresis build-up and solvent uptake rather than by initial hardness alone. Under cyclic strain, PEBA materials of this hardness class can accumulate heat in thick sections. Parts above 6 mm cross-section should be tested for internal temperature rise at the intended operating frequency, because internal heat generation may exceed the heat-transfer capacity of the part and produce premature softening or stress relaxation. Continuous hot-air exposure above 125 °C causes oxidative degradation of the polyether block, and published data for long-term hot-air ageing at 150 °C is limited. Swelling resistance to aliphatic hydraulic fluids and greases is governed by the PA12 hard block, but aromatic hydrocarbons, ketones, chlorinated solvents, and concentrated acids cause appreciable volume change and should be screened by ISO 175 before production release.

    After saturation moisture uptake of 1.3 % by ISO 62, equilibrium moisture reduces hardness and increases elongation. Dimensional changes of 0.4 % to 0.7 % are possible depending on wall section, so seals with close clearances should be qualified on conditioned prototypes rather than dry-as-moulded dimensions. For potable water, food-contact, or medical device use, migration and biocompatibility verification to (EU) 10/2011, 21 CFR 177.1500, or ISO 10993 should be generated for the specific final article. RoHS and REACH declarations should be confirmed with the supplier, but the absence of external plasticiser is an advantage when documenting low extractable content.

    The product should be stored in sealed packaging and re-dried before processing if exposure to 60 % relative humidity exceeds 4 h. In multi-layer mandrel hose construction, adhesion to PA12 inner liners is generally favourable because the PA12 hard block provides interfacial compatibility, while adhesion to high-hardness TPU may require a tie layer. When moving from plasticised PVC to E47-S1, the minimum bend radius should be re-calculated using the part’s actual wall thickness and flexural modulus of 210 MPa rather than transferred directly from PVC design tables, because the strain distribution in the bent tube differs from the plasticised PVC reference condition.

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