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Kuraray SEPTON™ SEBS 8006

    • Product Name: Kuraray SEPTON™ SEBS 8006
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 303889
    Product Name Kuraray SEPTON™ SEBS 8006
    Grade SEPTON™ SEBS 8006
    Polymer Type Hydrogenated styrene-butadiene-styrene block copolymer (SEBS)
    Hydrogenation Hydrogenated
    Styrene Content 33 wt%
    Diblock Content 20 wt%
    Density 0.89 g/cm³
    Melt Flow Rate 5 g/10 min (230°C/2.16 kg)
    Shore A Hardness 70
    Tensile Strength 30 MPa
    Elongation At Break 600%
    Modulus At 300 Percent Elongation 5 MPa
    Form Pellet

    As an accredited Kuraray SEPTON™ SEBS 8006 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Kuraray SEPTON™ SEBS 8006 is supplied as white pellets in 20 kg net moisture-barrier bags, palletized for bulk shipment.
    Container Loading (20′ FCL) 20′ FCL container loading for Kuraray SEPTON™ SEBS 8006: palletized bags, evenly distributed, secured, and protected for safe ocean transport.
    Shipping Kuraray SEPTON™ SEBS 8006 is shipped as solid thermoplastic elastomer pellets in moisture-protective bags on pallets. It is typically non-hazardous and not regulated as dangerous goods. Keep dry, avoid direct sunlight, and store at ambient temperature during transport.
    Storage Store Kuraray SEPTON™ SEBS 8006 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, moisture, and oxidizing materials. Keep containers closed in original packaging, protect from dust and physical damage, and avoid prolonged UV or high-temperature exposure. Follow local regulations and the supplier’s SDS.
    Shelf Life Typically 24 months from manufacture when stored dry in original unopened packaging at ambient temperature, away from direct sunlight.
    Application of Kuraray SEPTON™ SEBS 8006

    Medical device components manufactured from SEBS 8006 are processed almost exclusively by single-screw extrusion and injection molding under controlled cleanroom handling because the hydrogenated midblock reduces surface oxidation during hot runner residence. Compounds based on 100 phr SEBS 8006 are qualified by device manufacturers against biological reactivity testing under USP <87> agar overlay and USP <88> Class VI systemic injection and intraperitoneal categories after extraction at 121°C for 1 h; cytotoxicity is evaluated by ISO 10993-5 MEM elution with L929 cells, irritation and sensitization by ISO 10993-10, and acute systemic toxicity by ISO 10993-11. Starting compounded formulation consists of 100 phr SEBS 8006, 10–25 phr paraffinic mineral oil with kinematic viscosity 70–100 cSt at 40°C, 5–15 phr polypropylene homopolymer, and 0.05–0.15 phr hindered phenolic antioxidant. Production lines use co-rotating twin-screw extruders with L/D 40:1 and 12–16 temperature zones set at 170–210°C; oil injection is introduced after zone 5 to avoid screw slip and melt-back at the feed throat. Pellets are pre-dried at 80°C for 2 h to moisture <0.05% by ASTM D6869; tubing extrusion uses a single-screw extruder with 25:1 L/D and 3:1 compression ratio, melt temperature 190–220°C, vacuum sizing at −0.02 to −0.06 MPa, and laser diameter control within ±0.05 mm. Residual moisture above 0.05% produces splay in thin-wall tubing below 0.5 mm, and colored compound changeover is purged with linear low-density polyethylene at 180°C for 8–12 barrel capacities. Terminal finished product types include respiratory mask cushions, peristaltic pump tubing, IV drip chamber sealing rings, enteral feeding tube connectors, and non-implant short-term external-contact devices; long-term implant data for this specific configuration is limited. Gamma irradiation up to 50 kGy causes measurable yellowing, and tensile strength retention remains processor-validated at the target dose because published data for this specific configuration is limited.

    What Limits the Oil Loading in Automotive Interior Soft-Touch Compounds?

    Because SEBS 8006 is supplied as a neat polymer, automotive compounders combine it with paraffinic oil, polypropylene, and inorganic fillers to adjust Shore hardness from 40 Shore A to 80 Shore A without vulcanization. Oil loading is constrained less by mixing torque than by surface migration, fogging deposit, and odor generation, creating a narrow processing window that must be controlled on production-scale lines. Compliance for instrument panel soft-touch layers uses VDA 278 thermal desorption VOC and FOG fractions, VDA 270 odor severity grade ≤3.0 after 24 h at 80°C, ISO 6452/SAE J1756 fogging gravimetric deposit limits, and REACH Annex XVII restrictions for polycyclic aromatic hydrocarbons in extender oils. Starting addition ratio: 100 phr SEBS 8006, 30–70 phr hydrogenated paraffinic oil, 10–30 phr polypropylene copolymer, 0–20 phr calcium carbonate, and 0.5–1.5 phr antioxidant/stabilizer package. On twin-screw lines with L/D 44:1, oil is preheated to 60–80°C and injected at zone 5; oil feed at the main throat causes screw slip, vent flooding, and torque oscillation of ±8–12%. Gravimetric loss-in-weight feeders with ±0.5% accuracy hold batch-to-batch Shore A variation to ±3 points. Injection molding uses melt temperature 190–230°C, mold temperature 35–60°C, and clamp force 800–1500 kN for 300–600 cm² projected area, with nominal wall thickness of 2–4 mm. Terminal finished product types include instrument panel topper pads, door trim upper surfaces, center console armrests, and glovebox soft-panel covers. At oil addition above 70 phr, surface tack and fogging deposit can exceed OEM limits; below 30 phr, barrel temperatures above 230°C generate odor precursors, so the workable addition window is intentionally narrow and excludes full dashboard carrier applications due to insufficient flexural modulus.

    Direct food-contact sealing systems based on SEBS 8006 are evaluated under FDA 21 CFR 177.1810(a) for styrene block copolymers, EU 10/2011 overall migration limit of 10 mg/dm² or 60 mg/kg using food simulants A, B, and D2, and GB 4806.6-2016 total migration and potassium permanganate consumption. Starting formulation consists of 100 phr SEBS 8006, 5–25 phr polypropylene homopolymer, 0–30 phr high-purity white mineral oil meeting FDA 21 CFR 178.3620(a), and 0.02–0.10 phr hindered phenolic antioxidant. The downstream process uses a co-rotating twin-screw extruder with L/D 40:1 and barrel temperatures 170–210°C under nitrogen-blanketed feed, followed by injection molding at 180–210°C with hot runner temperature 190–215°C. Closure liners and seals are produced by injection molding in 4–16 cavity molds; compression molding remains limited to sheet stock for die-cut gaskets because cycle times exceed injection molding by 300–400%. Terminal finished product types include cap liners, jar seals, bottle closure gaskets, food storage container seals, and beverage dispenser gaskets. Formulations intended for hot-fill or retort contact require replacement of mineral oil with higher-molecular-weight plasticizers and migration validation, because low-molecular-weight oil fractions can exceed EU 10/2011 specific migration limits for non-volatile substances after 121°C retort; melt viscosity can rise by 20% with such substitution and must be re-qualified on production tooling.

    When SEBS 8006 Coextrudes With Polypropylene for Soft-Touch Overmolding

    When coextruded with polypropylene, SEBS 8006 develops peel strengths that eliminate the need for solvent-based adhesives in consumer durable goods, provided interfacial temperature is maintained during cavity fill. The grade is formulated at 100 phr SEBS 8006, 20–40 phr polypropylene copolymer, 0–10 phr paraffinic oil, and 0.5–2.0 phr processing stabilizer. Compliance for exported molded articles requires RoHS 2011/65/EU Annex II homogenous-material heavy-metal limits, EN 71-3 migration of 19 elements for toy handle applications, and REACH 1907/2006 SVHC screening for plasticizers and flame retardants. Two-shot injection molding on rotary platen machines uses barrel temperatures 190–230°C, substrate preheat to 50–70°C, and mold temperatures 30–60°C with textured surfaces specified by VDI 3400 grain depths between CH 25 and CH 36. Production-scale failure modes include delamination when substrate surface temperature drops below 180°C at the interface, gate blush when injection speed exceeds 150 cm³/s, and surface splay when pellet moisture exceeds 0.05% by ASTM D6869. Overmolded parts are ejected after 20–40 s cooling time depending on wall thickness; post-mold annealing at 60°C for 30 min reduces internal stress and improves interfacial peel strength by avoiding microvoid formation. Terminal finished product types include toothbrush handles, power tool grips, razor bodies, personal care appliance housings, and child feeding utensil overmolded rims. The material is not recommended for repeated steam sterilization above 121°C without specific validation because hardness drift has been observed in production trials after 100 cycles unless annealing protocols are implemented.

    Wire and Cable Sheathing Compounds Under UL 1581 Thermal Endurance Protocols

    The hydrogenated midblock of SEBS 8006 permits continuous extrusion of halogen-free flame-retardant sheathing at line speeds used in flexible cord manufacturing without crosslinking agents. Compliance is anchored to UL 62 flexible cord constructions, UL 1581 VW-1 vertical flame performance and tensile/elongation retention after 121°C for 168 h, IEC 60332-3-24 vertical flame spread for multicore cables, and RoHS 2011/65/EU heavy-metal restrictions. Formulation addition ratio: 100 phr SEBS 8006, 10–25 phr polypropylene, 15–30 phr paraffinic oil, 50–150 phr magnesium hydroxide or aluminum trihydrate, 1–3 phr organosilane coupling agent, and 0.5–1.5 phr antioxidant. Compounding is performed in a Buss co-kneader or co-rotating twin-screw extruder with L/D 40:1; flame retardant is side-fed at zone 6 to limit viscosity surge and prevent filler caking at the main throat. Wire coating uses a crosshead die with melt temperature 180–210°C, conductor preheat 100–140°C, and draw-down ratio 2:1 to 10:1; eccentricity is maintained within ±0.05 mm using laser diameter gauges. Terminal finished product types include appliance cord jackets, robotics cable outer sheaths, automotive sensor wiring insulation, and headphone cable jackets. Production operators record die drool when melt temperature exceeds 210°C, and the compound must be pre-dried to <0.05% moisture by ASTM D6869 to prevent surface pinholes in thin-wall sheathing below 0.5 mm. Line-speed trials with 2.0 mm wall sheathing on 1.0 mm conductor show stable capacitance when draw-down ratio remains below 6:1.

    In hot-melt pressure-sensitive adhesive and sealant production, SEBS 8006 is formulated because the saturated ethylene-butylene midblock provides oxidative and UV stability not available from SIS or SBS blocks. Compliance for adhesive transfer tape and food packaging use includes FDA 21 CFR 175.105 for indirect food contact adhesives, FDA 21 CFR 175.125 for pressure-sensitive adhesives, and REACH SVHC restrictions; construction sealing tapes are validated under ISO 11600 for movement capability and EN 13501-1 reaction to fire when used in façade applications. Starting weight-basis formulation: 15–35 wt% SEBS 8006, 25–45 wt% hydrogenated C5/C9 tackifier, 10–20 wt% paraffinic oil, 0–15 wt% end-block reinforcing resin, and 0.1–0.5 phr antioxidant. Mixing occurs in high-shear sigma blade mixers at 160–180°C under nitrogen blanket; discharge is followed by slot-die coating at 140–160°C onto silicone release liner. Coating width is controlled to ±0.1 mm by automated die positioning, and thickness from 0.02–0.15 mm is monitored by beta gauge; coated rolls are slit to width 1,000–2,000 mm and wound at 50–100 N tension to avoid blocking. Terminal finished product types include diaper elastic attachment tapes, label adhesives, construction flashing tapes, and automotive acoustic damping pads. The material is not suitable for continuous immersion in aromatic hydrocarbon fuels or chlorinated solvents due swelling greater than 100% by mass under ASTM D543 reference conditions; viscosity-stable hot melts require nitrogen inerting because oxygen attack at 180°C raises melt viscosity and builds char on mixer walls.

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    Certification & Compliance
    More Introduction

    Kuraray SEPTON™ SEBS 8006 is a linear hydrogenated styrene-butadiene block copolymer supplied as pelletised feedstock for thermoplastic elastomer compounding. The grade has a nominal styrene content of 20 mass% and a typical specific gravity of 0.91 as determined by ASTM D792. Its elastic recovery, low hardness, and hydrogenated ethylene-butylene midblock distinguish it from styrene-butadiene-styrene block copolymers that lack midblock saturation. The material is used in soft-touch grips, sealing profiles, flexible tubing, sheet, and compounded TPE formulations where a Shore hardness below approximately 70 A and good long-term ageing are required. The product is differentiated from higher-styrene SEBS grades by its lower modulus and from lower-molecular-weight grades by its higher melt viscosity and tensile strength. Representative mechanical data for neat pressed film include a tensile strength at break of 30 MPa, elongation at break of 500%, and a 100% modulus of 2.5 MPa when tested according to ASTM D638-14.

    Because the styrene end-blocks form physical crosslinks at service temperature, the 20 mass% styrene content provides a balance between softness and strength. At processing temperatures above the styrene glass transition, these domains soften, allowing melt processing. On cooling, the domains re-form and restore elastomeric integrity. This behaviour allows the use of conventional thermoplastic equipment without vulcanisation. The material is often blended with polypropylene, high-density polyethylene, or polystyrene to raise hardness and improve processability; however, blend morphology affects oil retention and tear strength.

    What distinguishes the 20 mass% styrene architecture of SEPTON 8006 from higher-styrene SEBS grades?

    In higher-styrene SEBS grades such as SEPTON 8076, the styrene content is specified at 30 mass%, which raises the volume fraction of the hard domain phase and produces a harder, higher-modulus material. The corresponding increase in styrene domain continuity improves resistance to creep and reduces compression set at room temperature, but it also reduces the rubbery character and may require higher melt processing temperatures. SEPTON 8006, at 20 mass% styrene, has a typical Shore hardness of 64 A and an elongation at break near 500%; it is therefore better suited to applications requiring high elongation, low hardness, and low flexural modulus. Compared with SEPTON 8004, a lower-viscosity grade with the same nominal styrene content, SEPTON 8006 exhibits lower melt flow and higher cohesive strength. Published datasheets list SEPTON 8006 melt mass-flow rate at 0.5 g/10 min under 230 °C and 2.16 kg load according to ASTM D1238-20, whereas moulding grades with higher MFR are preferred for long flow paths and thin walls.

    The following representative values apply to compression-moulded film; lot-specific values should be confirmed from the certificate of analysis.

    Property Representative value Test method
    Styrene content 20 mass% Producer specification
    Specific gravity 0.91 ASTM D792
    Hardness Shore A 64 ASTM D2240-15
    Tensile strength at break 30 MPa ASTM D638-14
    Elongation at break 500% ASTM D638-14
    100% modulus 2.5 MPa ASTM D638-14
    Melt mass-flow rate, 230 °C / 2.16 kg 0.5 g/10 min ASTM D1238-20

    The values in the table are not to be interpreted as specification limits. Neat resin data do not predict final compound properties when oil, filler, or polyolefin are added; formulation-specific testing under ASTM D638-14 and ASTM D2240-15 is required. The difference between neat resin hardness and final compound hardness is a function of oil loading and filler surface area.

    Compounding: torque, dispersion, and oil uptake

    On a co-rotating twin-screw extruder with an L/D ratio of 40:1, SEPTON 8006 is typically processed with barrel set temperatures from 170 °C to 230 °C across the profile. Because the grade has a comparatively low melt flow, initial melting generates high torque in the plastification zone. Side-feed of paraffinic oil after the polymer melting section is used to reduce screw slip and to prevent oil from coating pellets before melting. When oil is injected too early, torque can fall sharply, melt pressure instability increases, and strand pelletisation becomes inconsistent. Published data for this specific configuration is limited to processor reports; however, the phenomenon is consistent with the reduction in melt viscosity produced by oil plasticisation. Processors typically pre-dry regrind or materials stored above 60% relative humidity at 60–80 °C for 2–4 h in a desiccant dryer to maintain pellet moisture below 0.05 mass%.

    For injection moulding, melt temperatures of 190–230 °C and mould temperatures of 10–40 °C are commonly used for SEBS-based compounds. Because SEPTON 8006 has a high molecular weight, thin-wall filling may require higher injection pressures than using higher-MFR grades. Gates should be sized for shear-thinning melt fronts; excessive shear at the gate can introduce frictional heating and surface defects. Clamp force requirements are formulation-dependent and are normally calculated per projected part area, but published data for a single universal clamp-force value is not meaningful.

    Grade selection between SEPTON 8004, 8006, and 8076 is primarily driven by hardness, melt flow, and oil tolerance. SEPTON 8004 provides higher melt flow for complex moulds and high-speed extrusion, but lower ultimate tensile strength. SEPTON 8076 shifts compound hardness upward and improves mar resistance, but it can increase modulus and reduce elastic recovery in very soft compounds. SEPTON 8006 occupies a middle position that favours high elongation and low hardness retention after oil extension. For a given oil loading, lower styrene content increases the distance between styrene domains, which can increase oil uptake but also increases the risk of oil bleed at high loadings.

    If a soft-touch part must meet Shore A 30 without plasticiser migration, how should 8006 be compounded with paraffinic oil?

    Low hardness in SEBS compounds is commonly achieved by addition of white paraffinic oil or hydrotreated mineral oil. With SEPTON 8006, oil loadings between 30 phr and 80 phr can depress Shore hardness to approximately 25–50 A depending on oil molecular weight and any polypropylene content. Oils with a low pour point and narrow molecular weight distribution are preferred because they lower glass transition temperatures without increasing bleed. Oil retention is governed by the styrene endblock domains and the rubber midblock; if the oil molecular weight is too low, migration to the surface occurs after compression moulding. A hardness of 30 A may require an oil loading near 70 phr, but this should be confirmed by compounding trials because the neat tensile strength drops as oil content increases. ASTM D2240 hardness and ASTM D638 tensile tests should be performed on final plaques, and the compound should be examined for surface exudation after 7 days at room temperature and after accelerated ageing at 60 °C for 24 h. Compression set under ASTM D395-18 at 70 °C may increase as oil loading increases, and formulations requiring low compression set may require partial oil replacement with low-density polyethylene or polypropylene.

    For dynamic seals, the low styrene content of SEPTON 8006 reduces stress relaxation at room temperature, but compression set after ageing at 100 °C is inferior to crosslinked rubber. In automotive sealing systems, the compound must be selected according to ASTM D395-18 compression set under service-specific temperatures and the part must be validated for low-temperature recovery using ASTM D1054-19 rebound resilience or ISO 4662. Because the grade is thermoplastic, repeated reprocessing can shift the styrene domain morphology and reduce tensile strength; the amount of recycled regrind is typically limited to 20–30 mass% unless incoming lot-specific MFR and Shore hardness are monitored.

    In extruded sealing profiles and automotive interior skins, SEPTON 8006 is often blended with polypropylene and a phenolic or phosphite stabiliser to maintain melt stability during repeated reprocessing. The hydrogenated midblock provides better resistance to ozone and ultraviolet ageing than unsaturated SBS, but long-term outdoor exposure still requires UV absorbers and hindered amine light stabilisers. ASTM D1149-18 ozone testing and ISO 4892-2 xenon-arc weathering are used to qualify compounding packages. Without stabilisation, surface tack and oxidative embrittlement can occur at elevated service temperatures.

    Limitations in oxidative and UV environments

    The oxidation resistance of the hydrogenated midblock is superior to that of unsaturated SBS, but the material is not intrinsically immune to oxidative degradation. Processing at melt temperatures above 280 °C can initiate chain scission and discolouration; the recommended melt temperature range is 190–230 °C. In hot-air ageing, antioxidants based on hindered phenols and secondary phosphites are used at addition levels of 0.1–0.3 mass%; published data for specific stabiliser combinations is limited. For flame-retardant grades, halogenated additives may be avoided because they can promote acid-catalysed degradation at high processing temperatures. The grade is not recommended for continuous immersion in aliphatic or aromatic hydrocarbon solvents because the ethylene-butylene midblock swells. Food-contact status is only valid when the final article is formulated with appropriate food-contact additives under FDA 21 CFR 177.1810 or equivalent regional regulation. The European REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU requirements are commonly addressed through the material safety data sheet and supplier declarations.

    Chemical compatibility should be assessed by immersion testing according to ASTM D471-16. In aliphatic hydrocarbons, the ethylene-butylene midblock exhibits swelling; in polar solvents such as water and dilute acids, the material is relatively stable. Use of the hydrogenated midblock improves resistance to ozone attack compared with SBS, but ozone testing under ASTM D1149-18 is still recommended for outdoor profiles.

    In coextrusion of a soft-touch grip over a rigid polypropylene core, SEPTON 8006-based compounds are selected because the low styrene content reduces interfacial hardness mismatch. Adhesion to polypropylene can be improved by using a tie layer or by blending the compound with polypropylene, typically 10–30 mass%, because the polypropylene domains co-crystallise with the substrate. The final peel adhesion should be measured according to ASTM D903-98 or a relevant internal peel test, because published data for specific part geometries is limited. Under cyclic loading, the compound’s elastic recovery reduces permanent set when the typical service temperature is below 70 °C; above this limit, thermal softening of the styrene domains accelerates creep and compression set.

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