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Asahi Kasei S.O.E.™ SEBS S1613

    • Product Name: Asahi Kasei S.O.E.™ SEBS S1613
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 576278
    Product Name Asahi Kasei S.O.E.™ SEBS S1613
    Manufacturer Asahi Kasei Corporation
    Polymer Type SEBS (styrene-ethylene-butylene-styrene block copolymer)
    Styrene Content 30 wt%
    Density 0.91 g/cm³
    Melt Flow Rate 3.0 g/10 min (230 °C, 2.16 kg)
    Shore A Hardness 60
    Tensile Strength 27 MPa
    Elongation At Break 600%
    Modulus At 300pct Elongation 4.0 MPa
    Tear Strength 30 kN/m
    Compression Set 40% (70 °C, 22 h)

    As an accredited Asahi Kasei S.O.E.™ SEBS S1613 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Asahi Kasei S.O.E. SEBS S1613 is supplied in 20 kg net multiwall paper bags, typically palletized for industrial shipment.
    Container Loading (20′ FCL) Typical 20′ FCL loading for Asahi Kasei S.O.E.™ SEBS S1613: 20 pallets × 40 × 25 kg bags, totaling 20,000 kg net.
    Shipping Asahi Kasei S.O.E.™ SEBS S1613 is supplied as solid thermoplastic elastomer pellets in moisture-barrier bags or octabins. Ship at ambient temperature in dry, clean, sealed containers; avoid heat, sunlight, and moisture. It is generally non-hazardous for transport; follow the SDS and local regulations.
    Storage Store Asahi Kasei S.O.E.™ SEBS S1613 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep in original, tightly closed containers on pallets to prevent contamination and dust. Avoid prolonged UV exposure and contact with strong oxidizers or solvents; use first-in, first-out stock rotation.
    Shelf Life Shelf life is typically 24 months when stored unopened in original packaging in a cool, dry place.
    Application of Asahi Kasei S.O.E.™ SEBS S1613

    Thermoplastic Olefin Skins for Low-Gloss Interior Components

    Automotive interior compound development for soft-touch, low-gloss instrument panel surfaces uses S.O.E.™ SEBS S1613 as a styrenic modifier dispersed in a polypropylene impact copolymer at 20–45 phr, with white mineral oil added at 10–30 phr to control Shore A hardness in the 55–75 range measured under ISO 868:2003. Compliance screening for this segment refers to REACH Regulation (EC) No 1907/2006, RoHS 2011/65/EU with Annex II restricted substances, and interior flammability requirements under FMVSS 302 or ISO 3795:1989 at a horizontal burn rate not exceeding 100 mm/min. The compound is manufactured on a co-rotating twin-screw extruder with L/D 44:1, barrel sections maintained at 180–220°C, screw speed 300–500 rpm, and pelletized through a strand die with water-ring cutting. Oil is injected downstream of the melting zone to prevent screw slippage when free oil exceeds 25 phr; production lines show torque fluctuation when the oil is added too early. The final injection moulding step runs at 190–230°C with mould temperatures of 30–60°C and clamp force of 1,500–3,000 kN; flow marks and gate blush become measurable when S1613 loading exceeds 35 phr and mould temperature falls below 30°C. Terminal parts include instrument panel lower skins, door trim inserts, centre console mats, and soft-touch airbag cover areas where low surface tack and reduced gloss are specified. Process controls must avoid melt residence above 240°C for more than 5 min because the hydrogenated midblock undergoes oxidative chain scission, detected as a loss in tensile elongation under ISO 37:2017.

    Hot-melt sealant formulations intended for household appliance assembly use S.O.E.™ SEBS S1613 as the midblock elastomer at 12–28 wt%, blended with hydrogenated hydrocarbon tackifier at 40–60 wt%, naphthenic/paraffinic processing oil at 10–22 wt%, and stabilizer at 0.5–1.2 wt%. Compliance for food-contact edge applications refers to FDA 21 CFR §175.105 without direct food contact, with REACH 1907/2006 and RoHS 2011/65/EU declarations required for appliance export. Production uses a sigma-blade or helical ribbon mixer at 165–190°C under nitrogen blanketing, followed by gear pump transfer to a slot-die coater or multi-bead extrusion head depositing 0.5–1.5 mm sealant beads onto metal or polyolefin substrates. Finished products include appliance assembly tapes, HVAC duct gaskets, hygiene elastic attachment adhesives, and automotive interior film lamination adhesives. Published data for this specific S1613 adhesive configuration is limited for exact shear adhesion failure temperature; converters validate hot shear resistance by ASTM D4498-07 and peel adhesion by ASTM D903-98, while limiting melt temperature to 190°C to avoid tackifier degradation and viscosity drift exceeding ±15% from initial melt viscosity measured by ISO 1133-1:2022.

    What Changes When Flexible PVC Is Replaced in Non-DEHP Medical Tubing?

    Replacement of flexible PVC in non-DEHP medical tubing shifts the formulation window toward a compound containing S.O.E.™ SEBS S1613 at 30–70 wt%, medical white oil at 10–40 phr, and polypropylene at 10–30 phr; radiopaque grades add barium sulfate at 5–15 wt% when fluoroscopic visibility is specified. The compliance screening for this segment includes cytotoxicity under ISO 10993-5:2009, irritation and sensitization under ISO 10993-10:2010, biological reactivity in vitro under USP <87>, and in vivo biological reactivity under USP <88> Class VI; drug packaging interfaces additionally require physicochemical testing per USP <661.1>. Tubing is produced on a single-screw extruder with L/D 25:1, compression ratio 3:1, barrel profile 175–215°C, vacuum sizing to an outer diameter tolerance of ±0.05 mm, and downstream silicone coating for lubricity. Vacuum calibration water temperature is held below 15°C to prevent dimension drift on multi-lumen lines. Terminal products include non-DEHP extension sets, enteral feeding tubes, respiratory circuit tubing, and pharmaceutical transfer lines. Gamma sterilization at 25–40 kGy is used; exposure above 40 kGy may produce measurable yellowing and a 5–15% shift in tensile strength under ISO 37:2017, requiring design validation for the finished device rather than raw-material certification alone.

    Compliance testing matrix for S1613 medical compound candidates
    StandardTest focusCondition/limit
    ISO 10993-5:2009In vitro cytotoxicityMEM extract, viability ≥ 70%
    ISO 10993-10:2010Irritation and sensitizationSingle-dose patch, 24–72 h
    USP <87>Biological reactivity in vitroAgar overlay and MEM elution
    USP <88> Class VIIn vivo biological reactivity145°C saline and cottonseed oil extracts
    USP <661.1>Plastic packaging physicochemicalBuffer capacity, non-volatile residue

    When a low-density ethylene-octene midsole foam fails compression set at 50% deflection under ISO 815-1:2014 after 72 h at 23°C, S.O.E.™ SEBS S1613 is introduced into the expandable compound at 40–70 phr together with ethylene-octene at 20–40 phr, general-purpose polystyrene at 5–15 phr, and chemical blowing agent masterbatch at 1.0–3.0 wt%. The compound is extruded on a co-rotating twin-screw unit with L/D 36:1–44:1 at 150–190°C, pelletized, and then injection moulded with a shut-off nozzle and mould temperatures of 40–60°C to activate the blowing agent while keeping the skin layer below the blowing agent decomposition onset. Finished product types include running-shoe midsoles, insoles, and shock pads; compression set is specified under ISO 815-1:2014, tear strength under ISO 34-1:2015, and hardness under ISO 868:2003. REACH Annex XVII polycyclic aromatic hydrocarbon restrictions apply to the consumer article, and the expansion ratio is typically controlled between 1.2 and 1.8 because higher expansion reduces tear strength and increases batch-to-batch density variation beyond ±0.03 g/cm³. Published data for this specific S1613 foam configuration is limited for fatigue durability; converters validate dynamic compression under ASTM F1976-20 or cobblestone flexing protocols before serial production.

    Halogen-Free Cable Jacketing Where Abrasion Resistance Dictates Formulation

    Halogen-free cable jacket formulations add S.O.E.™ SEBS S1613 at 20–35 wt% to an ethylene-vinyl acetate and linear low-density polyethylene matrix at 20–30 wt% and 15–25 wt%, with magnesium dihydroxide at 45–60 phr, maleated polyolefin coupling agent at 0.5–1.5 phr, and antioxidant at 0.3–0.8 phr. The compound requires compliance with IEC 60754-1:2011 for halogen acid gas, IEC 60754-2:2011 for acidity, IEC 61034-2:2005 for smoke density, and RoHS 2011/65/EU for restricted substances; cable OEMs also apply EN 50620 for e-mobility charging cables where relevant. Compounding is run on a twin-screw kneader at L/D 32:1–44:1 with barrel temperatures held at 160–200°C to prevent magnesium dihydroxide decomposition above 220°C, followed by crosshead cable extrusion with a wall thickness of 2.0–3.5 mm and melt pressure 120–180 bar. Terminal products include flexible appliance cords, industrial control cable sheathing, and electric vehicle charging cable jackets where abrasion loss is measured by ISO 4649:2017. Zinc stearate above 0.5 phr is avoided because volume resistivity may fall below 10^12 Ω·cm when measured by IEC 60093, and any batch exceeding 250 mm³ abrasion loss is rejected by cable specification limits. Die build-up at the crosshead becomes evident after 6–8 h when the coupling agent is overdosed, producing surface roughness that increases jacket friction under ASTM D1894-14.

    Halogen-free cable jacketing compliance matrix for S1613 compounds
    StandardParameterTypical requirement
    IEC 60754-1:2011Halogen acid gas determinationpH ≥ 4.3; conductivity ≤ 10 µS/mm
    IEC 60754-2:2011Acidity of combustion gases≤ 5 mg/g
    IEC 61034-2:2005Smoke densityMinimum light transmittance ≥ 60%
    ISO 4649:2017Abrasion loss≤ 250 mm³
    IEC 60093Volume resistivity≥ 10^12 Ω·cm

    Overmoulding of polypropylene manual tool bodies and kitchen utensils with a soft-touch S.O.E.™ SEBS S1613 compound at 15–35 wt% requires pre-drying at 70°C for 2 h when ambient relative humidity exceeds 60%; the two-shot injection moulding process maintains S1613 compound barrel temperatures of 200–230°C and mould temperatures of 30–50°C. Compliance for food-contact applications is evaluated under FDA 21 CFR §177.1810 for styrene block polymers and EU Regulation 10/2011/EU with an overall migration limit of 10 mg/dm² for food contact. Terminal product types include toothbrush soft-touch grips, cutlery handles, storage container seals, and power tool overmoulds. Published data for this specific configuration is limited for repeated-use food-contact extraction behaviour; converters must validate final part migration under EN 1186-1:2002 and not assume raw-material compliance transfers automatically to the finished article.

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    Certification & Compliance
    More Introduction

    Asahi Kasei S.O.E.™ SEBS S1613 is a hydrogenated styrene–ethylene/butylene–styrene block copolymer classified under ISO 18064:2022 as TPE-S. The saturated midblock removes olefinic unsaturation from the butadiene precursor, which reduces ozone-induced chain scission and ultraviolet embrittlement while retaining thermoplastic processability. S1613 is supplied as pellets and is typically used in compounded form rather than as a neat polymer; polyolefin modification, soft-touch overmoulding, profiles, grips, and gaskets are common application fields. The grade is positioned in the higher-hardness segment of the S.O.E. series because its styrene content is approximately 30 wt%, yielding Shore A hardness values in the 60–68 range and a melt flow rate near 3.5 g/10 min under ASTM D1238-23 at 230 °C/2.16 kg. Unlike unsaturated styrene-butadiene-styrene, S1613 does not require vulcanization, and scrap can be reground into thermoplastic recycle streams within the limits described below.

    Typical Property Envelope and Test Standards

    PropertyTest methodRepresentative valueUnit
    Specific gravityASTM D792-200.91—
    Melt flow rateASTM D1238-23, 230 °C/2.16 kg3.5g/10 min
    HardnessASTM D2240-15/ISO 868:2003, 15 s65Shore A
    Tensile strengthASTM D638-22, Type IV, 500 mm/min27MPa
    Ultimate elongationASTM D638-22, Type IV650%
    Compression setASTM D395-18 Method B, 70 °C/22 h42%
    Tear strengthASTM D624-20, Die C45kN/m

    The values above are representative compact-moulded values determined after 24 h conditioning at 23 °C and 50 % RH; they are not release limits. Melt flow and tensile properties shift with oil extension, polyolefin addition, and moulding conditions. Because S1613 is often compounded with paraffinic oil at 50–120 phr, mechanical properties in final articles may be lower than neat-polymer values. Published data for oil-extended S1613 in specific overmoulding applications is limited; full qualification on production tooling is required.

    Why Is S1613 Positioned as a Higher-Hardness S.O.E. Grade?

    The 30 wt% polystyrene end-block fraction controls the thermal and mechanical response of S1613. Under ASTM D638-22, tensile modulus and yield behaviour are rate-dependent: deformation above 50 mm/min promotes shear yielding of the polystyrene domains, while slow deformation below 5 mm/min allows greater viscous flow and higher elongation. The saturated poly(ethylene/butylene) midblock provides a sub-ambient glass transition, typically near −50 °C, which retains flexibility in low-temperature impact-modification applications. In polypropylene blends, addition of 10–30 wt% S1613 can improve impact resistance, but the exact low-temperature impact improvement must be verified by ASTM D3763-18 or ISO 6603-2:2000 on injection-moulded plaques because particle size and domain dispersion depend on screw design. Tensile set under ASTM D412-16 is higher than vulcanised rubber, which is a limitation in long-term cyclic loading.

    Within the Asahi Kasei S.O.E. SEBS line, S1613 is differentiated from lower-styrene grades by its higher polystyrene end-block content, which raises hardness, tensile strength, and compression resistance. The harder grades in the S1600 series show less room-temperature creep than low-hardness gel grades, but they require higher melt temperatures and more shear to achieve uniform dispersion in polyolefin matrices. Compared with unsaturated SBS, S1613 retains its midblock oxidative stability because the ethylene/butylene segment has no allylic hydrogen; this allows outdoor weathering performance to be evaluated by ASTM D1149-18 ozone testing or ISO 1431-1:2022 accelerated ozone exposure. The trade-off is that the fully saturated midblock is less polar than nitrile or urethane elastomers, so solvent resistance remains limited to nonpolar and mildly polar environments.

    InputS1605S1611S1613
    Styrene content20 wt%30 wt%30 wt%
    Melt flow rate at 230 °C/2.16 kg8.0 g/10 min1.0 g/10 min3.5 g/10 min
    Hardness38 Shore A62 Shore A65 Shore A
    Primary differentiationLow-hardness gel and sealant flowHigh melt strength extrusionBalanced flow and hardness for injection moulding

    The comparison above is based on typical S.O.E. series data for unfilled, non-oil-extended grades; compounded formulations can shift these relative positions. S1613 is therefore not a direct drop-in for S1605 in soft gel applications unless hardness and oil acceptance are rebalanced. No single grade substitution should be made without re-measuring tensile set under ASTM D412-16 and compression set under ASTM D395-18, because molecular weight and domain spacing produce lot- and grade-dependent recovery kinetics. S1613 differs from Asahi Kasei SEPS grades because the ethylene/butylene midblock has a longer run length between chain folds than hydrogenated isoprene; this affects low-temperature flexibility and compression set. Published data for direct property comparison between S1613 and SEPS in the same hardness range is limited, so selection should be based on prototype testing under ASTM D395-18 and ASTM D624-20.

    Melt rheology of S1613 follows a shear-thinning pseudo-plastic response typical of styrenic block copolymers. At 200 °C, apparent viscosity under low shear can exceed 1,000 Pa·s, but at injection-moulding shear rates of 10,000–50,000 s⁻¹, viscosity falls sufficiently to fill thin sections. The pressure-temperature window is less severe than for reactive TPVs; no ±5 °C cliff-edge exists. However, oil phase compatibility and PS domain stability impose a practical melt-temperature upper limit of 250 °C. Residence times above 10 min at melt temperatures above 230 °C can produce gel particles and an increase in yellowness index. Use of nitrogen purge and low-shear screw elements is recommended for optical-critical parts. Capillary rheometry per ISO 11443:2021 should be used to generate viscosity curves for mould-filling simulation; single-point melt flow rate is inadequate for thin-wall tool design.

    Compounding of S1613 on a corotating twin-screw extruder with an L/D ratio of 32:1 to 44:1 typically uses zone setpoints of 160–210 °C and a die temperature of 200–230 °C. Paraffinic white oil with kinematic viscosity between 40 mm²/s and 100 mm²/s at 40 °C is added downstream of the melt seal to control phase inversion and avoid excessive shear heating. Screw speeds of 250–350 rpm are common for 25 mm laboratory lines; production-scale 50–75 mm machines require lower rotational speeds and specific energy monitoring because viscous dissipation can exceed 0.25 kWh/kg and produce local melt temperatures above 240 °C. At melt temperatures above 250 °C, the polystyrene end blocks begin to degrade by chain scission; the saturated midblock is more thermally stable, but gel particles and viscosity drift can occur. S1613 should be pre-dried if surface moisture exceeds 0.05 wt%, typically at 80 °C for 2 h in a desiccant dryer. In injection moulding, melt temperatures of 190–230 °C and mould temperatures of 20–50 °C are used; clamp force requirements follow standard polyolefin calculations of approximately 3–5 tonnes per square inch of projected area, but thin-wall parts with flow-length-to-thickness ratios above 150:1 require independent pressure-drop simulation. Published data for S1613 on specific production-scale extruder configurations is limited, so start-up should include a melt-temperature survey and residence-time distribution measurement.

    For a typical 50 Shore A compound, S1613 is often blended with a polypropylene homopolymer and paraffinic oil. The oil-to-SEBS ratio controls hardness and migration. If the oil loading exceeds the absorption capacity of the saturated midblock, bleed-out occurs within weeks at ambient temperature; this failure mode is observed on production lines as surface tack and dust pickup. Gravimetric aging at 70 °C for 168 h followed by visual inspection and mass loss measurement is used to screen formulations, but no single ASTM method captures all migration modes. Polyolefin addition above 30 wt% can reduce compression set but increases tension set and surface hardness. The final formulation should be stabilised with an antioxidant package suitable for food or medical use if those markets are intended.

    When Chlorinated Solvents, Aromatic Oils, or Strong Oxidizers Contact S1613

    S1613 is not a solvent-resistant elastomer. The polystyrene end blocks are swollen or dissolved by aromatic hydrocarbons, chlorinated solvents, ketones, and esters; contact with these fluids causes hardness loss, dimensional change, and extractables migration. Paraffinic and naphthenic oils are commonly used as extenders, but the aromatic fraction in the plasticiser should be kept below approximately 5 wt% of the oil because aromatic components partition into the polystyrene domains and reduce service temperature. Strong oxidizers, including concentrated hydrogen peroxide and hypochlorite solutions, attack the saturated midblock at elevated temperature; long-term immersion above 50 °C is not recommended without aging trials. The polymer withstands water, dilute acids, and dilute bases at room temperature, but continuous hot water above 80 °C can reduce physical crosslink integrity rather than cause hydrolysis. In overmoulding onto polypropylene or copolyester substrates, premature delamination can occur if substrate surface temperature falls below the PS block softening range. On production lines, substrate preheating to 60–80 °C and use of a texture depth above 15 µm improve mechanical interlock. Published data for this specific S1613 configuration is limited; destructive peel testing per ASTM D6862-11 is necessary to establish bond strength.

    In wire and cable jacketing, S1613 can be used in blends with polypropylene or low-density polyethylene to achieve flexibility and heat resistance. The saturated midblock provides good electrical resistivity; volume resistivity may fall in the 10¹⁴–10¹⁶ Ω·cm range for unfilled compounds, but final values depend on carbon black or flame-retardant additives. Combustion performance must be formulated with halogen-free flame retardants such as magnesium hydroxide or aluminium trihydrate; these fillers reduce tensile strength and require coupling-agent optimization. A limiting factor in cable applications is the high loading of flame retardant needed to pass vertical flame tests, which can reduce extrudability and increase melt pressure. Production-scale single-screw extruders with 24:1 to 30:1 L/D and low-compression screws are used, but published data for S1613 in this specific configuration is limited.

    For medical tubing or stopper applications, the chosen compound must be formulated without extractable processing oils above migration limits. Neat S1613 has lower extractables than oil-extended compounds, but the moulder should verify cytotoxicity and hemolysis under ISO 10993-5:2009 and ISO 10993-4:2017 on the final device. Sterilisation by gamma irradiation at 25 kGy or ethylene oxide can alter tensile strength and colour; dose mapping and post-sterilisation compression set testing are required. Published data for S1613 in radiation-sterilised medical devices is limited; users should request supplier ageing studies rather than assume stability.

    Field failures with SEBS overmoulded parts often involve gloss change, tackiness, or loss of adhesion after cleaning agents. These are not inherent to S1613 alone but to the compound. For cleaning-agent resistance, the finished assembly should be exposed to the actual solvent blend for 72 h at 40 °C under ISO 2812-1:2017 and then tested for hardness retention and visual change. Chlorinated and aromatic cleaning solvents are particularly aggressive; alcohol-based cleaners are typically less damaging but can extract low-molecular-weight stabilisers.

    Regulatory and food-contact status for S1613 must be established on the finished article, not assumed from the neat grade. The supplier certificate should be reviewed for compliance with REACH Article 33 obligations, RoHS 2011/65/EU Annex II thresholds for cadmium, lead, mercury, hexavalent chromium, PBB, and PBDE, and any applicable FDA 21 CFR sections such as 177.1810 or 177.2600 if repeated food-contact conditions are claimed. The neat polymer is not biodegradable and should not be incinerated in uncontrolled facilities; emissions during thermal decomposition include carbon monoxide and low-molecular-weight hydrocarbons. S1613 has a shelf life typically limited to 24 months when stored below 30 °C and away from direct ultraviolet exposure; long-term storage above 40 °C may cause pellet blocking and antioxidant depletion. For medical device applications, ISO 10993-1:2018 biocompatibility assessment is required on the sterilised finished device, and ethylene oxide or gamma irradiation must be validated for physical property retention. If the compound contains oil or polyolefin modifiers, the regulatory status of the final blend can differ from the neat S1613 grade.

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