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Asahi Kasei Tuftec™ SEBS H1272

    • Product Name: Asahi Kasei Tuftec™ SEBS H1272
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 904137
    Product Name Asahi Kasei Tuftec™ SEBS H1272
    Polymer Type Hydrogenated styrene-butadiene-styrene block copolymer (SEBS)
    Melt Flow Rate Condition 230 °C / 2.16 kg
    Volume Resistivity Ohm Cm >1e15
    Water Absorption Percent <0.1
    Physical Form pellets
    Color white

    As an accredited Asahi Kasei Tuftec™ SEBS H1272 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Asahi Kasei Tuftec™ SEBS H1272 is supplied in 25 kg moisture-resistant paper bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) 20′ FCL loaded with Asahi Kasei Tuftec™ SEBS H1272 in 25 kg bags on pallets, shrink-wrapped and stowed for export.
    Shipping Asahi Kasei Tuftec™ SEBS H1272 is typically shipped as dry pellets in 25 kg bags or 500–1000 kg jumbo bags. It is a non-hazardous solid polymer; transport in clean, dry, ventilated containers, protected from moisture, direct sunlight, and excessive heat. No special temperature control is required.
    Storage Store Asahi Kasei Tuftec™ SEBS H1272 in a cool, dry, well-ventilated area, away from direct sunlight, heat sources, moisture, and incompatible chemicals. Keep original containers tightly closed, palletized off the floor, and protected from physical damage. Avoid prolonged UV/ozone exposure and contamination; use first-in, first-out rotation. Maintain ambient conditions, do not stack excessively, and inspect packaging regularly.
    Shelf Life Approximately 24 months from manufacture when stored in original, unopened packaging, dry, at room temperature, and protected from sunlight.
    Application of Asahi Kasei Tuftec™ SEBS H1272

    In glass-fiber reinforced polypropylene substrates for lower instrument panel carriers, Asahi Kasei Tuftec™ SEBS H1272 functions as a styrenic block copolymer impact modifier that shifts the brittle-to-ductile transition of a 20 wt% talc-filled polypropylene homopolymer at −30 °C without reducing a melt flow index normally measured at 12–35 g/10 min under 230 °C/2.16 kg. The hydrogenated butadiene midblock absorbs multiaxial impact energy while the styrenic end blocks preserve phase continuity with the polypropylene matrix. Production-scale compounding lines have used addition ratios from 8 wt% to 22 wt% of H1272 relative to total compound mass; below 8 wt% the notched Charpy improvement at −30 °C becomes statistically indistinguishable from baseline homopolymer, while above 22 wt% the flexural modulus may fall below interior door panel specification limits of 1,800 MPa measured by ISO 178:2019. The process is run on a co-rotating twin-screw extruder with L/D ratio 40:1 to 44:1, main feed at 190 °C and maximum barrel temperature 220 °C; residence time is kept below 180 s and specific energy input between 0.22 kWh/kg and 0.28 kWh/kg to avoid chain scission of the styrenic end blocks. Compliance anchors include ISO 1183-1:2019 for density, ISO 179-2:2020 for notched Charpy impact, ASTM D3763-22 for multiaxial puncture, VDA 277 for total VOC emissions, and REACH Regulation (EC) No 1907/2006. Typical terminal components include lower instrument panel skins, door panel inserts, center console armrest substrates, and A/B-pillar trim bases where low-temperature airbag deployment crack resistance is required. One known processing boundary is a melt temperature above 245 °C: on a 44:1 L/D compounding extruder, this has been associated with visible graying of pellets and a measurable decline in notched Charpy values, so upper barrel set points are configured to maintain melt thermocouple readings at or below 240 °C.

    Where Does H1272 Provide Thermal Shear Resistance in Polyolefin Hot Melt Pressure-Sensitive Adhesives?

    Hydrogenated midblock architecture of H1272 raises the cohesive strength of hot melt pressure-sensitive adhesives at service temperatures approaching 70 °C, a zone where SBS analogues typically soften and lose holding power. In slot-die coated tape structures, the grade is incorporated at 18–28 wt% of the total adhesive formulation alongside a fully hydrogenated hydrocarbon tackifier at 40–55 wt%, a naphthenic or white mineral oil at 15–22 wt%, and a hindered phenolic antioxidant at 0.5–1.0 wt%. The rubber block does not require sulfur vulcanization; instead, physical crosslinks from the styrenic domains provide shear resistance after the adhesive film cools below the styrene glass transition. Compounding is conducted in a heated Z-blade mixer or a twin-screw extruder with L/D 32:1 to 36:1 at 160–180 °C under nitrogen blanketing, followed by filtering through a 200 μm screen pack to remove gels. Coating is normally performed with a slot-die applicator at 150–170 °C onto release liner or directly onto polyester film at line speeds of 50–150 m/min. Compliance methods include PSTC-101 for loop tack, PSTC-107A for shear adhesion failure temperature, ASTM D3236-88 for hot melt viscosity, and FDA 21 CFR 175.105 for indirect food contact in pressure-sensitive labels. Terminal products include automotive interior foam mounting tapes, floor covering installation adhesives, and disposable hygiene positioning adhesives where UV resistance of the hydrogenated midblock prevents yellowing under sterilization lamps. Formulators avoid aromatic process oils above 3 wt% because aromatic fractions plasticize the styrenic domains, lowering SAFT values and increasing edge bleed under load.

    Flexible control cable jacketing compounds for six-axis robotic arms expose the styrenic block copolymer to repeated torsional flexing, weld-spatter-resistant surfaces, and halogen-free flame retardancy requirements. H1272 is let down into a polyolefin cable jacket at 25–45 phr of the elastomer phase, with a random polypropylene or LLDPE backbone at 15–25 phr, a paraffinic white oil at 60–120 phr, and a hydrated mineral flame retardant package such as magnesium hydroxide at 30–60 phr when IEC 60332-1-2 flame spread limits are specified. The common failure mode on manufacturing lines is surface porosity in the final jacket when the flame retardant masterbatch is below 80 °C dew-point control or when the H1272/oil dry-blend is fed with ambient moisture above 60% RH; pre-drying of mineral fillers at 80 °C for 4 h prevents moisture pitting. Compounding is run on a tangential twin-screw extruder at 170–200 °C, followed by jacket extrusion through a 90 mm single-screw machine with L/D 25:1, a crosshead die at 190–210 °C, and a water trough at 20–40 °C. Compliance anchors include UL 62 for flexible cord construction, UL 1581 VW-1 for vertical flame propagation, RoHS Directive 2011/65/EU for heavy metal restrictions, and IEC 62321-8 for phthalate screening. Finished cable types include USB charging cable jackets, power tool cord sheaths, robotic control cable insulation, and elastomeric earphone cable outer sheaths. The grade should not be combined with amine-based flame retardant additives because amine migration can disrupt the styrenic physical crosslink network and cause premature softening at bend points.

    Closure Liner Compound Migration Thresholds Under Carbonation Pressure

    Closure liner formulations for carbonated beverage caps require a combination of low compression set, low oil exudation, and organoleptic neutrality at internal carbonation pressures of 3.5–4.5 bar. H1272 is incorporated at 25–45 wt% of the liner compound, with a random polypropylene copolymer at 15–30 wt%, white mineral oil at 30–45 wt%, and a silicone-based slip agent at 0.5–1.5 wt% to maintain consistent release torque. The liner compound is prepared on a co-rotating twin-screw extruder with L/D 30:1 at 180–210 °C, then pelletized and compression molded into multi-cavity closure liners at 190–220 °C; molded liners are annealed at 60 °C for 24 h to stabilize the oil distribution before capping. Without annealing, oil migration can produce visible liner bloom and increased extraction values under EU Regulation 10/2011. The compliance matrix below identifies test anchors.

    Conformity assessment anchors for H1272 closure liner formulations
    Standard or regulationTest conditionSpecification anchor
    FDA 21 CFR 177.1810Styrene block polymers for food contactCompliance based on food-contact supplier statement; total nonvolatile extractives limits per 21 CFR 177.1810(c) apply
    EU Regulation 10/2011Overall migration, food simulant D1, 10 days at 40 °C10 mg/dm² overall migration limit
    ISO 815-1:2019Compression set, 22 h at 70 °C≤ 45% for liner reseal performance
    ASTM D2240-15Shore A durometer, 15 s dwell55–70 A for low torque closure liners
    FDA 21 CFR 177.2600Rubber articles, total extractives, water and n-hexaneLimits per 21 CFR 177.2600(e) for repeated use food-contact rubber articles

    Terminal products include single-piece plastic closures for carbonated soft drinks, hot-fill beverage caps, and aseptic dairy closures requiring organoleptic neutrality. Ethylene vinyl acetate carrier resins are avoided in this application because vinyl acetate hydrolysis at high humidity can lower liner pH and interact with low-molecular-weight styrenic fractions, increasing overall migration in simulant D1.

    When H1272 is Insert Overmolded onto Glass-Filled Polybutylene Terephthalate Power Tool Housings

    Insert overmolding onto glass-filled polybutylene terephthalate creates a weld-line region where the styrenic block copolymer must interdiffuse with a semicrystalline substrate surface above its crystallization temperature, otherwise peel failure occurs along the bond interface. For this process, H1272 is used as the primary elastomer at 35–55 wt% in a second-shot TPE compound that also contains a polypropylene homopolymer at 10–20 wt%, a paraffinic white oil at 20–40 wt%, and a hindered amine light stabilizer package at 0.3–0.8 wt%. The first-shot PBT substrate is processed at a melt temperature of 260–270 °C and mold temperature of 80–100 °C; the second-shot H1272 compound is injected at 220–240 °C with a packing pressure of 400–800 bar and a screw back pressure of 3–6 bar to maintain a homogeneous melt. Adhesion is evaluated by a 90° peel test on 25 mm strips at 50 mm/min; commercially acceptable structures typically exceed 4 N/mm peel strength, though published data for H1272 on glass-filled PBT in this specific configuration are limited and should be verified with a certified masterbatch. The process boundary is the mold surface temperature: below 40 °C, the styrenic melt skin quenches too rapidly to form an interphase, and delamination can occur before the substrate reaches 80 °C. Compliance anchors include RoHS Directive 2011/65/EU, REACH Regulation (EC) No 1907/2006, IEC 60335-1 for household and similar electrical appliance safety, ASTM D638-14 for tensile strength of the overmold, and ISO 34-1:2022 for trouser tear resistance. Finished products include power tool housings, handheld vacuum grips, portable power bank bumpers, and control grips for electric drills where an injection-molded texture is required.

    Toy Compound Extraction Limits Push H1272 Formulations Toward High-Purity White Oils

    Mouth-contact toy compounds formulated with H1272 must reconcile softness and tensile recovery with extraction limits that are stricter than those applied to general-purpose TPEs. H1272 is compounded at 30–50 wt% of the final TPE, with a low-density polyethylene or random polypropylene matrix at 10–25 wt%, a medicinal-grade white mineral oil at 20–40 wt%, and a polydimethylsiloxane slip agent at 0.5–1.0 wt%. Production is typically carried out on a 40 mm co-rotating twin-screw extruder at 170–200 °C, with a melt pump and underwater pelletizer; the pellets are then injection molded into toy parts at 180–210 °C using a mold temperature of 20–40 °C. The critical operational boundary is oil exudation: white oil loading above 40 wt% can produce surface tack and increase the extractable fraction during EN 71-3 migration testing, even when the compound visually appears homogeneous. Compliance anchors include EN 71-3:2019+A1:2021 for migration of elements, ASTM F963-23 for toy safety, REACH Regulation (EC) No 1907/2006 Annex XVII phthalate restrictions, and FDA 21 CFR 177.1810 for food-contact-like mouthing evaluations. Terminal finished products are teething rings, squeeze toys, bath toy flexible bodies, and elastomeric toy wheels. Because published multi-laboratory extraction data for H1272 specifically in toy compounds are limited, formulators should rely on supplier lot-specific migration statements and conduct simulant-specific extraction checks per the finished article design.

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    Certification & Compliance
    More Introduction

    Asahi Kasei Tuftec™ H1272 is a hydrogenated styrenic block copolymer of the poly(styrene-ethylene-butylene-styrene) family, classified under ISO 1043-1 as TPS-SEBS and identified by the general SEBS CAS registry number 66070-58-4. The polymer chain consists of terminal polystyrene blocks and a saturated ethylene-butylene midblock. At service temperature the polystyrene domains are glassy and function as physical crosslinks, while the ethylene-butylene segments provide elastic recovery. The hydrogenation step converts the polybutadiene midblock of the precursor SBS into an ethylene-butylene structure, removing most carbon-carbon double bonds and the associated allylic hydrogen positions. This structural difference alters thermo-oxidative stability, ultraviolet ageing behaviour, solubility, and compatibility with process oils relative to unsaturated SBS. The designation H1272 denotes a medium-high hardness grade within the Tuftec line, supplied as porous pellets with bulk density typically in the range 0.30–0.50 g/cm³. The porous pellet morphology supports oil absorption during compounding but can increase feed throat floating in high-speed gravimetric feeders if the feed hopper is not fitted with a positive discharge aid.

    PropertyTest methodTypical value
    Specific gravityISO 1183-1:20190.91 g/cm³
    HardnessISO 7619-1 / ASTM D224072 Shore A
    Tensile strengthISO 37 / ASTM D41224.5 MPa
    Elongation at breakISO 37 / ASTM D412650%
    Melt mass-flow rateISO 1133-1:2022, 230 °C, 2.16 kg12 g/10 min

    The values in the table are representative data from the manufacturer technical datasheet and are not unconditional lot acceptance limits. The current datasheet revision should be confirmed before design calculations or production tooling decisions. The hardness of 72 Shore A indicates a higher polystyrene block fraction than is found in low-hardness Tuftec grades such as H1221, which is published at approximately 42 Shore A. The higher brittle-fraction content increases room-temperature stiffness, tensile modulus, and dimensional stability but reduces low-temperature elasticity and raises melt viscosity compared with softer SEBS grades.

    How Does the Hydrogenated Midblock Differentiate H1272 from Unsaturated SBS Grades?

    In unsaturated styrene-butadiene-styrene block copolymers, the butadiene midblock contains allylic double bonds that are susceptible to ozone attack, radical-driven chain scission, and ultraviolet-induced embrittlement. Ozone resistance can be ranked by ASTM D1149, and weathering performance is commonly assessed by ASTM G154 or ISO 4892-2. For SEBS, the saturated ethylene-butylene midblock eliminates the most reactive double-bond sites. The remaining degradation pathways are principally thermo-oxidative attack at tertiary carbon positions and chain scission at the phase boundaries between polystyrene domains and the elastomeric matrix. These degradation routes are managed with hindered phenolic antioxidants, phosphite process stabilizers, and, where necessary, thioester secondary antioxidants rather than by stabilizer systems designed for unsaturated rubber.

    The replacement of unsaturated SBS with Tuftec H1272 is therefore most relevant where the application involves prolonged outdoor exposure, contact with ozone-generating equipment, or thermal processing above 180 °C. The trade-off is that the hydrogenated midblock is less compatible with highly aromatic process oils and may require paraffinic or naphthenic oil extension rather than aromatic oil. Published quantitative UV retention data for H1272 under ASTM G154 is limited; component qualification for exterior applications should therefore be based on tested compounds rather than on extrapolation from the neat polymer chemistry.

    Within the Tuftec range, the comparison with lower-hardness SEBS grades is primarily rheological and mechanical. H1272 produces compounds with higher scratch resistance and lower rubbery compliance than H1221. The difference of approximately 30 Shore A points indicates a significant shift in the physical crosslink density associated with the polystyrene domains. The practical consequence is that a compound based on H1272 can achieve a given hardness with less filler or less polypropylene than a softer SEBS, but it may require plasticization or blending with a softer grade for applications requiring 50 Shore A or below.

    In polypropylene-rich compounds, Tuftec H1272 is metered into a co-rotating twin-screw extruder with an L/D ratio of 40:1 to 44:1. The PP homopolymer or block copolymer is dry-blended with the SEBS and a hindered phenolic antioxidant at 0.05–0.15 wt%. Processing aids such as zinc stearate may be added at 0.05–0.20 wt% to reduce die build-up and strand tack. Barrel set points are generally maintained between 180 °C and 210 °C, while the melt temperature at the die is held below 230 °C. When screw speed exceeds 400 min⁻¹, dispersion quality becomes sensitive to residence time and local shear heating. If the SEBS phase viscosity is reduced excessively, the dispersed morphology can coarsen; notched impact strength should be verified via ASTM D256 or ISO 180 because the morphology directly controls impact performance.

    Paraffinic white oil is frequently used as an EB-phase plasticizer. Addition levels of 10–30 wt% lower the effective hardness of an H1272-based compound from 72 Shore A into the 45–60 Shore A range. The oil is preferentially absorbed by the ethylene-butylene midblock. Aromatic oils are less suitable because the hydrogenated midblock has weaker affinity for aromatic species, which can lead to exudation during service life. On production lines, strand pelletizing requires water-bath temperatures below 25 °C to prevent strand blocking. Porous pellets can absorb surface moisture if stored in humid ambient conditions; desiccant drying is required before injection moulding when surface moisture content exceeds 0.05 wt%.

    When H1272 Is Chosen for Soft-Touch Overmoulding onto Polypropylene

    Two-component injection moulding of a polypropylene substrate with an H1272-based overmoulded layer relies on melt-interface diffusion between the polyolefinic EB phase and the PP substrate. The interface temperature is a more important variable than melt temperature alone. When the interface temperature remains above 160 °C, the overmoulded layer typically achieves cohesive failure in peel testing rather than adhesive delamination. Melt temperatures for the SEBS layer are commonly set between 200 °C and 230 °C, with mould temperatures at 30–50 °C. Surface contamination, mould release agents, or excessive condensation on the PP substrate can reduce peel strength. ISO 2411 or ASTM D903 are used to validate peel or bond performance for production acceptance.

    The elimination of sulfur or peroxide cure is a fundamental processing difference from vulcanized rubber and from rubber-modified polypropylene TPVs. Tuftec H1272 does not require vulcanization kinetics, scorch control, or post-cure handling; it can be reground and reprocessed. However, the absence of a covalent crosslink network results in higher compression set at elevated temperatures. Published ISO 815 data for H1272 is limited, but SEBS compounds generally exhibit higher compression set after 22 h at 70 °C than crosslinked EPDM or TPV materials. The material is therefore not a direct replacement for EPDM in sealing applications with continuous service above approximately 100 °C or where low compression set is the controlling specification.

    Because the EB midblock is saturated, the compound is more resistant to reversion and surface tack during high-shear processing than unsaturated SBS. However, the polystyrene domains soften near 100 °C, so dimensional stability under load at elevated temperature depends on the compound formulation and is not defined by the neat polymer alone. Applications such as automotive interior soft-touch elements, power-tool grips, and appliance overmoulding can use H1272 when the continuous service temperature is below the threshold at which the physical crosslink network loses mechanical integrity.

    For extrusion of wire and cable jacketing, strain-relief grommets, and flexible profiles, H1272-based compounds are run on single-screw extruders with 25:1 to 30:1 L/D and compression ratios of 2.5:1 or lower. Melt temperature is not permitted to exceed 240 °C for extended residence time because thermal gel formation may occur. Screen packs with 100–200 μm openings can trap char or crosslinked particles. Since the polymer is nonpolar, adhesion to copper conductors, aluminum substrates, or polar engineering thermoplastics is minimal without a coextruded tie layer, a maleated polyolefin primer, or a chlorinated polyolefin surface treatment. This limitation is a key difference from polyurethane elastomers, which exhibit higher inherent adhesion to polar substrates but generally have lower long-term hydrolytic stability.

    Rheological response and drying boundary conditions

    The melt mass-flow rate of 12 g/10 min at 230 °C and 2.16 kg is a single-point, low-shear measurement. It does not define the pseudoplastic response required for mould-filling simulation. At injection moulding shear rates of 10³–10⁴ s⁻¹, SEBS viscosity decreases substantially from the zero-shear value. Capillary rheometry per ISO 11443 is required to generate shear-viscosity curves for a specific H1272 compound. Complete rheological master curves are not published in all regional manufacturer datasheets; therefore, simulation users should measure the specific compound.

    Drying is required when pellets have been exposed to relative humidity above 60% for more than 24 h or when surface moisture is visible. A desiccant dryer with dew point below −20 °C and a chamber temperature of 80 °C for 2–3 h is typically sufficient for neat H1272. Compounds containing hygroscopic fillers such as mineral flame retardants may require longer drying. Residual moisture causes splay, surging, and reduced overmould adhesion. Mould shrinkage for SEBS-rich compounds is commonly in the range 1.0–1.8% after 24 h; the value must be measured on a standard plaque, such as a 150 mm × 150 mm × 2 mm plaque per ISO 294-3, because shrinkage is strongly affected by PP content, filler type, gate geometry, and packing pressure.

    Thermo-oxidative ageing limits the upper continuous service temperature of SEBS compounds

    Continuous service above 120 °C accelerates antioxidant consumption and can lead to chain scission, tensile loss, and yellowing. Heat-ageing per ISO 188 should be performed at the intended continuous service temperature, with retained tensile strength and elongation at break measured after aging intervals appropriate to the service life. Applications requiring retention above 80% of initial properties at temperatures above 120 °C for extended time may require TPV or EPDM rather than an H1272 compound. The saturated midblock is not biologically or hydrolytically unstable, but strong oxidizing acids, hypochlorite solutions, and chlorinated solvents can attack or swell the polymer. Continuous immersion in aromatic solvents, esters, or halogenated hydrocarbons is not recommended because the ethylene-butylene phase is miscible or partially miscible with many nonpolar and moderately polar solvents.

    Under the U.S. Code of Federal Regulations, styrene block copolymers intended for food contact are referenced in 21 CFR 177.1810, but the finished compound containing H1272 must be tested separately because oil extension, colorants, fillers, and process stabilizers can change extractive and migration behaviour. Under REACH Regulation (EC) No 1907/2006, the polymer itself is generally exempt from registration, although imported monomers and additives used in compounds must satisfy relevant registration and authorization obligations. Under RoHS Directive 2011/65/EU, the base SEBS polymer does not contain intentionally added lead, mercury, cadmium, hexavalent chromium, PBB, or PBDE; however, a finished compound certificate is required for each shipping lot rather than relying on the generic polymer composition. For medical, food-contact, or potable-water applications, the grade-specific regulatory status must be verified with Asahi Kasei before compounding.

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