| HS Code | 516201 |
| Polymer Type | SEBS (styrene-ethylene/butylene-styrene) block copolymer |
| Polymer Architecture | Linear triblock copolymer |
| Styrene Content | ~33 wt% |
| Specific Gravity | ~0.91 |
| Density | ~0.91 g/cm³ |
| Melt Flow Rate | ~11 g/10 min at 230°C/2.16 kg |
| Shore A Hardness | ~65 |
| Tensile Strength | ~20 MPa |
| Elongation At Break | ~600% |
| 300 Modulus | ~4.0 MPa |
| Tear Strength | ~30 kN/m |
| Volatile Matter | <0.5 wt% |
| Color | White |
| Form | Powder |
As an accredited Kraton Kraton™A SEBS RP6936 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kraton™ A SEBS RP6936 is supplied in 25 kg moisture-resistant multiwall bags, palletized for safe storage and handling. |
| Container Loading (20′ FCL) | Kraton™ A SEBS RP6936 loaded in a 20′ FCL container: palletized, dry, secure stowage, with compliant labeling and transport documentation. |
| Shipping | Kraton™ A SEBS RP6936 is shipped as solid polymer pellets in sealed bags or boxes. It is not classified as dangerous goods for transport. Store and transport in a dry, cool area away from direct sunlight and ignition sources, keeping containers closed to prevent moisture and contamination. |
| Storage | Store Kraton™A SEBS RP6936 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed in original packaging when not in use; protect from moisture, dust, and contamination. Avoid prolonged exposure to elevated temperatures and incompatible chemicals. Use secondary containment, follow local regulations, and label containers clearly. |
| Shelf Life | Kraton™A SEBS RP6936 typically has a 36-month shelf life when kept sealed in original packaging under dry, moderate conditions. |
Kraton™ A SEBS RP6936 is a saturated styrene-ethylene/butylene-styrene triblock copolymer used in thermoplastic elastomer compounding where saturated midblock stability, additive acceptance, and controlled oil extension are specified. The downstream scenarios below are restricted to industrial routes with documented SEBS conversion: automotive interior soft-feel parts, medical device elastomer components, consumer overmolding, polypropylene impact modification, hygiene elastic films, and halogen-free wire jacketing. Sulfur vulcanization packages and amine-based crosslinking additives should not be combined with this saturated block copolymer in the absence of published compatibility data; such systems can produce surface deposit defects and unstable melt viscosity. In all scenarios, addition ratios are given as weight percent of the total formulation unless otherwise indicated.
When RP6936 is selected for PP-based interior skins, the primary processing constraint is not tensile strength but the control of oil migration, fogging, and surface gloss stability. In a soft-feel trim compound, RP6936 is added at 20–35 wt%, polypropylene random copolymer at 30–50 wt%, paraffinic white oil at 30–45 wt%, a phenolic/phosphite antioxidant package at 0.2–0.5 wt%, and a silicone-based slip/anti-scratch additive at 0.5–1.5 wt%. The oil-to-SEBS weight ratio is held between 1.0:1 and 1.6:1; above 2.0:1, oil exudation to the part surface raises fogging values under VDA 278 and creates tack-related field complaints. Compliance for the finished interior part includes VDA 278 for VOC and FOG, ISO 12219-3 for cabin-air VOC, FMVSS 302 for burning rate, and the applicable OEM emission and odor specification from the vehicle platform. Compounding is performed on a co-rotating twin-screw extruder with L/D 40:1 to 48:1 and a side feeder located at barrel zone 6 of 12. The melt temperature profile is 180–220 °C; oil is injected after the polymer melt reaches 180 °C, because earlier addition can cause screw slippage in the feed zone, while later injection at melt temperatures above 220 °C can generate volatile oil haze at the die plate. Injection molding uses barrel settings of 190–230 °C, mold surface temperature 30–50 °C, and an edge-gate injection velocity tuned to avoid jetting. Mold temperatures above 50 °C increase cycle time and can create local gloss imbalance; below 30 °C, surface dullness and visible flow lines may appear. Finished part types for this formulation route include instrument panel soft-touch toppers, door panel armrest inserts, center console side panels, HVAC control knobs, and interior trim clip covers.
Medical device elastomer compounding with RP6936 follows a qualification path based on USP and ISO biological reactivity rather than mechanical property tabulation alone. In a medical TPE formulation, RP6936 is incorporated at 30–48 wt%, a medical-grade polyolefin elastomer at 10–18 wt%, USP white mineral oil at 30–40 wt%, a phenolic antioxidant at 0.1–0.3 wt%, and optional barium sulfate radiopacifier at 5–15 wt% when fluoroscopic visibility is required for the device. Final-component compliance is established under USP <88> Class VI, ISO 10993-5 for cytotoxicity, ISO 10993-10 for irritation and skin sensitization, ISO 10993-11 for systemic toxicity, and USP <381> for elastomeric closure extractables. Where the compound is intended for food-contact duty, migration testing under FDA 21 CFR 177.1810 and EU 10/2011 is applied to the finished article. Processing begins with drying at 70 °C for 2–4 h when inlet RH exceeds 60%; surface moisture otherwise creates bubbles in thin-wall tubing. Tubing is extruded on a single-screw extruder with L/D 30:1 and a screen pack at the breaker plate; die melt temperature is held within 190–205 °C to avoid sharkskin and die-lip deposit formation. Injection-molded closures and gaskets are produced in an ISO 14644-1 Class 8 cleanroom. Gamma sterilization at 25–50 kGy is tolerated when the antioxidant package is adjusted for radiolytic discoloration. Finished products include IV tubing, peristaltic pump tubing, syringe gaskets and plunger tips, vial stoppers, and infusion bag access ports.
On two-shot overmolding cells, RP6936-based TPE-S bonds to polypropylene substrates but does not develop reliable adhesion to PC/ABS or PA66 without an interfacial primer, polar tie layer, or maleic anhydride-modified compatibilizer; specifying an unmodified grade on these polar substrates is a known field failure mode. For consumer grip compounds, RP6936 is added at 25–40 wt%, polypropylene homopolymer or random copolymer at 20–30 wt%, white mineral oil at 25–35 wt%, a silicone-based slip package at 0.5–2 wt%, and color masterbatch at 2–4 wt%; the resulting hardness range is frequently Shore A 50–75 depending on oil ratio and PP melt flow. Compliance for consumer articles is based on REACH Annex XVII, RoHS Directive 2011/65/EU, and EN 71-3 migration limits where toy-contact is specified; California Proposition 65 screening is typically conducted on the compounded pellet. The production process is a two-shot injection cycle: the PP substrate is first molded and cooled to 60–80 °C before the second shot; RP6936 melt temperature is 190–220 °C; holding pressure and cooling time are set to prevent interfacial delamination and sink marks. Drying at 70 °C for 2 h is required when package RH exceeds 60%. Finished product types include power-tool soft-grip overlays, toothbrush handles, kitchen utensil grips, personal care razor grips, and beverage bottle cap covers.
The following compliance matrix consolidates the standard designations referenced in the application scenarios; it does not replace final-article certification.
| Application segment | Standard designation | Test focus |
|---|---|---|
| Automotive interior soft-feel | VDA 278; ISO 12219-3; FMVSS 302 | VOC/FOG; cabin air VOC; burn rate |
| Medical device elastomer | USP <88> Class VI; ISO 10993-5; ISO 10993-10; ISO 10993-11; USP <381>; FDA 21 CFR 177.1810; EU 10/2011 | Biological reactivity; cytotoxicity; irritation; systemic toxicity; extractables; food-contact migration |
| Consumer overmolding | REACH Annex XVII; RoHS Directive 2011/65/EU; EN 71-3 | Restricted substances; heavy-metal migration |
| PP impact modification | ASTM D256; ISO 180; ASTM D638; ISO 178 | Notched Izod; Charpy impact; tensile; flexural |
| Hygiene films | REACH Annex XVII; OEKO-TEX Standard 100; ISO 10993-5 where medical | Restricted substances; skin-contact safety; cytotoxicity |
| Halogen-free cable | IEC 60332-1; ISO 6722; SAE J1128; UL 1581 | Flame propagation; automotive cable performance; jacket physicals |
Impact modification of polypropylene with RP6936 is not a bulk dilution exercise; the modifier must form discrete elastomer domains of 0.5–2 µm in the PP matrix to shift the ductile-brittle transition downward. Addition of RP6936 at 5–15 wt% to PP homopolymer, with PP at 70–85 wt% and a processing aid at 0.05–0.15 wt%, is used for cold-temperature impact resistance. Mechanical testing follows ASTM D256 notched Izod, ISO 180 Charpy impact, ASTM D638 tensile, and ISO 178 flexural properties. Published comparative data for SEBS-modified PP indicate a shift of the ductile-brittle transition by 10–20 K at 10–15 wt% modifier loading; published data for this specific grade configuration is limited and must be verified per production lot. Compounding is performed on a twin-screw extruder with L/D 36:1–44:1 and a melt temperature of 220–250 °C; melt temperatures below 210 °C can preserve coarse SEBS domains and reduce low-temperature impact. Screw configuration emphasizes distributive mixing rather than high-intensity dispersive kneading, because excessive shear can reduce domain size below 0.5 µm and promote co-continuous morphology. Compliance for appliances and automotive components includes REACH, RoHS Directive 2011/65/EU, and applicable food-contact or UL requirements only where final-part specifications require them. Finished product types include appliance housings, luggage shells, automotive battery cases, and furniture structural panels.
In cast hygiene film extrusion, RP6936 is used where low coefficient of friction and controlled elastic recovery are required. The film formulation contains RP6936 at 15–30 wt%, polyolefin plastomer at 50–65 wt%, white mineral oil at 10–20 wt%, and slip/antiblock masterbatch at 0.5–1.5 wt%; cast film thickness is ordinarily 40–80 µm. Compliance for skin-contact non-medical laminates is based on REACH Annex XVII and OEKO-TEX Standard 100; if the laminate is intended for short-term dermal contact in a medical device, converters add ISO 10993-5 and ISO 10993-10 testing to the final construction. Processing uses a cast film extruder with a barrier screw L/D 30:1, melt temperature 200–230 °C, and chill roll temperature 15–25 °C; after casting, the film is directed through intermeshing grooved rollers for cross-direction stretching and activation, which sets the elastic recovery profile. Pre-drying at 70 °C for 2 h is required when inlet RH exceeds 60%. Finished product types include diaper ear films, waistband elastic laminates, adult incontinence side panels, and medical bandage laminates.
Halogen-free jacketing compounds use RP6936 as the elastomer phase that contributes flexibility and char integrity when combined with metal hydrate fillers. A typical formulation contains RP6936 at 15–25 wt%, ethylene-vinyl acetate or polyethylene matrix resin at 20–30 wt%, magnesium hydroxide or aluminum trihydroxide at 50–65 wt%, zinc borate synergist at 3–6 wt%, and processing lubricant at 1–3 wt%. The metal hydrate loading requires a compounding melt temperature not exceeding 190–210 °C because premature water release from aluminum trihydroxide begins at approximately 180–220 °C depending on grade; localized hot spots in the screw generate porosity and surface pinholes in the jacket. Compounding is performed on a high-torque co-rotating twin-screw extruder with L/D 40:1–48:1 and low-shear forwarding elements after the filler side feeder; the extruder vent is kept under reduced pressure to remove moisture. Jacketing is applied through a single-screw extruder with L/D 30:1 and a crosshead die. Compliance testing for finished cables includes IEC 60332-1 for vertical flame propagation, ISO 6722 for automotive low-voltage cables, SAE J1128 for automotive primary wire, and UL 1581 or UL 62 where applicable; RoHS Directive 2011/65/EU applies to the final jacket. Finished product types include EV charger cable jackets, sensor cable sheathing, appliance internal wiring jackets, and low-voltage automotive primary wire insulation.
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Kraton Kraton™ A SEBS RP6936 is a linear triblock copolymer in which polystyrene end-blocks are separated by a hydrogenated ethylene–butylene midblock. The saturated midblock removes allylic hydrogen positions that otherwise participate in rapid free-radical oxidation in butadiene-containing SBS. As a thermoplastic elastomer, the product relies on microphase-separated polystyrene domains for physical crosslinking; these domains soften above the styrenic glass transition, permitting melt processing, and re-form on cooling to restore rubbery properties. Published supplier documentation for this controlled-flow SEBS grade generally provides lot-level certificates of analysis rather than a single fixed property sheet. Plant specifications should therefore reference exact test methods and acceptance windows rather than generic datasheet values.
The grade is supplied as low-dust pellets. In bulk pneumatic conveying, pellet fracture at directional elbows can generate fines that segregate in the feed throat and produce injection moulding shot-weight drift. Hopper exit temperature should remain below 40 °C to avoid blocking. If the material is stored in a hot warehouse above 30 °C, pallet stacking should be limited to reduce pellet deformation. Incoming-quality specifications should include melt-mass flow rate, tensile properties, Shore A hardness, specific gravity, residual volatiles, and visual pellet uniformity.
Melt-mass flow rate is measured at 230 °C under a 2.16 kg piston load per ASTM D1238-20 or ISO 1133-1:2022. In this SEBS class, a controlled-flow designation implies a melt-viscosity profile adjusted for high-shear injection moulding without reducing molecular weight to the point where strand integrity and blow-moulding melt strength are lost. Capillary rheometry over apparent shear rates of 10¹ to 10⁴ s⁻¹ reveals pronounced shear thinning; melt viscosity at 10³ s⁻¹ is typically one to two orders of magnitude lower than zero-shear viscosity. Because the hydrogenated midblock has no carbon–carbon double bonds, the material tolerates melt temperatures up to 230 °C for short residence times without the catastrophic chain scission observed in unstabilized SBS at 190 °C.
Tensile properties are determined on compression-moulded plaques conditioned at 23 ± 2 °C and 50 ± 5 % RH per ASTM D638-14 or ISO 527-2. Shore A hardness is measured after a 3 s indentation per ASTM D2240-15. For SEBS grades in this family, tensile strength commonly falls between 15 MPa and 35 MPa, and elongation at break is typically above 400 %. These ranges are not RP6936-specific and must be verified against the supplier certificate of analysis for each lot. The styrenic end-block glass transition in SEBS typically appears between 95 °C and 105 °C when measured by differential scanning calorimetry at 10 °C/min heating rate per ASTM D3418-21.
On a corotating twin-screw extruder with an L/D ratio of 32:1 to 44:1, barrel set-points of 190 °C to 220 °C are typical for SEBS compounds. The polymer is fed at the main throat; paraffinic or naphthenic oil is side-injected after melting to prevent screw slip. A screw profile using broad distributive mixing elements rather than narrow intensive kneading blocks reduces local viscous heating. On production lines, die-hole freeze-off occurs when the die plate drops below 175 °C; maintaining die-plate temperature above 180 °C and reducing water-bath temperature differential stabilize strand diameter. A sudden drop in melt pressure at constant screw speed after an oil injection port indicates localized slip in the feed zone, not viscosity reduction. The corrective action is to move the oil injection point downstream rather than increasing barrel temperature.
The safe operating window for a saturated SEBS compound is bounded by two failure modes. At barrel temperatures below 180 °C, melt viscosity increases sharply and drive motor amperage rises beyond extruder capacity. At temperatures above 230 °C, thermal degradation of the polystyrene end-blocks can generate yellowing and gel formation. Operators on a 40 mm twin-screw extruder should monitor melt pressure upstream of the screen changer; excursions beyond ±0.5 MPa from baseline often indicate filler agglomeration or incipient die-hole freeze-off. Pre-drying at 70 °C for 2 h in a desiccant hopper dryer is recommended when the material has been exposed to relative humidity above 60 % RH. Although saturated SEBS absorbs less than 0.2 % moisture at 23 °C and 50 % RH, surface water can produce porosity in cast film and lower weld-line strength in injection-moulded parts.
RP6936 is a non-functionalized SEBS; it does not carry reactive maleic anhydride groups. Adhesion to polyamide, polyester, or aluminium is therefore limited to mechanical interlocking and interdiffusion rather than covalent bond formation. When a peel test per ASTM D903-20 on a flexible substrate requires a customer-specified minimum force, the compound should be reformulated with a maleated SEBS or a separate tie layer. Conversely, the non-functionalized surface reduces unwanted interaction with amine-terminated additives during compounding. The controlled-flow design of RP6936 fills an intermediate position between a high-viscosity SEBS and a high-flow SEBS: it provides better thin-wall mould filling than a high-viscosity grade, while retaining more melt strength than a low-viscosity grade.
| Factor | RP6936 controlled-flow SEBS | High-flow SEBS | Maleated SEBS | Butadiene-containing SBS |
|---|---|---|---|---|
| Midblock saturation | Hydrogenated | Hydrogenated | Hydrogenated | Unsaturated |
| Melt strength | Intermediate | Lower | Intermediate to high | Lower at elevated temperature |
| Adhesion to polar substrate | Mechanical/interdiffusional | Mechanical/interdiffusional | Covalent via anhydride | Mechanical/interdiffusional |
| Ozone resistance | High | High | High | Low without antiozonant |
| Typical processing temperature ceiling | Up to 230 °C | Up to 230 °C | Up to 230 °C with residence-time control | 190–200 °C |
Selection of RP6936 over a high-flow SEBS should therefore be based on a measured spiral-flow moulding trial using a 2 mm depth spiral cavity, not on melt-flow rate alone. The same trial reveals whether the higher injection pressure required by RP6936 in thin-wall sections is acceptable for the available clamp force and runner balance. When the part wall thickness is below 1.0 mm, a lower-viscosity SEBS may be necessary regardless of desired tear resistance.
Accelerated weathering under ASTM G154 Cycle 1 or ISO 4892-2 is used to rank SEBS and SBS compounds. Because the hydrogenated ethylene–butylene midblock lacks allylic hydrogen, SEBS compounds typically retain a higher percentage of original elongation after 500 h exposure than SBS of equivalent styrene content. However, SEBS is not inherently UV-stable; unpigmented outdoor parts require UV absorbers and hindered amine light stabilizers to avoid surface crazing and gloss loss. The saturated midblock also reduces the need for antiozonant additives that are normally required in butadiene-containing SBS compounds.
Compression set at 70 °C for 22 h per ASTM D395-18 is higher for SEBS than for crosslinked rubber; the polystyrene domains soften near their glass transition. RP6936 should not replace thermoset rubber in continuous service above 70 °C unless the part is designed with low strain and periodic recovery. In polyolefin impact modification, low-temperature impact strength is evaluated by notched Izod per ASTM D256-10 or ISO 180:2023. Published data for RP6936 in this specific configuration is limited, so a design-specific impact study is required before replacing a qualified impact modifier.
Regulatory status is governed by material identity and end-use. Styrene block copolymers may be considered under FDA 21 CFR 177.1810 for food-contact articles, provided end-use extraction testing satisfies the migration limits referenced in 21 CFR 176.170. European food-contact compliance is assessed under EU 10/2011/EC with an overall migration limit of 10 mg/dm² for general food contact unless a substance-specific migration limit applies. RoHS Directive 2011/65/EU Annex II restrictions apply at the homogeneous-material level.
| Regulation / standard | Relevant scope or test | Threshold or limit |
|---|---|---|
| FDA 21 CFR 177.1810 | Styrene block copolymers in food-contact articles | End-use extraction limits referenced in 21 CFR 176.170 |
| EU 10/2011/EC | Overall migration from plastic materials | 10 mg/dm² for general food contact |
| RoHS 2011/65/EU Annex II | Homogeneous material restrictions for electrical and electronic equipment | Pb 0.1 wt%; Cd 0.01 wt%; Hg 0.1 wt%; Cr(VI) 0.1 wt%; PBB/PBDE 0.1 wt% |
| REACH EC 1907/2006 | SVHC communication and authorization | Supplier declaration per Article 33 |
RP6936 should not be melt-blended with amine-containing additives at elevated temperatures because amine-induced degradation may discolour the melt. Halogenated flame retardants can generate acidic by-products at processing temperatures; an acid scavenger is required if such formulations are unavoidable. Storage beyond 24 months in unopened original packaging is not recommended without re-qualification, and bags should be kept below 40 °C to minimize blocking.
Soft-touch overmoulding on polypropylene uses RP6936 as the elastomer layer in a two-component injection moulding cell with a 100 t clamp force and a rotating platen or core-back tool. The nozzle melt temperature is maintained at 200 °C to 220 °C; mould surface temperature is controlled at 20 °C to 40 °C to ensure rapid solidification while allowing interfacial diffusion with the substrate. Bond strength is evaluated by peel testing per ASTM D903-20 or ISO 8510-2:2011 with 25 mm wide strips. Published peel data for RP6936 overmould bonded to polypropylene is limited; production validation should include peel panels moulded at the upper and lower processing limits, and weld-line tensile specimens per ISO 527-2 should be cut from parts with 0.8 mm and 1.5 mm wall thickness to establish a process capability run.