| HS Code | 771730 |
| Material Type | SEBS-based thermoplastic elastomer (TPE-S) |
| Density G Cm3 | approx. 1.10 |
| Tensile Strength Mpa | approx. 7 |
| Elongation At Break Percent | approx. 500 |
| Tear Strength Kn M | approx. 25 |
| Compression Set 23c 72h Percent | approx. 25 |
| Rebound Resilience Percent | approx. 45 |
| Abrasion Resistance Mm3 | approx. 200 |
| Electrical Grade | EL / electrically conductive |
| Volume Resistivity Ohm Cm | <= 1E4 |
| Surface Resistivity Ohm | <= 1E6 |
| Processing Methods | injection molding; extrusion |
| Recommended Melt Temperature C | 180-220 |
| Color | black |
As an accredited Bada AG BADAFLEX® SEBS-Comp. TPE-S 80A 5015 EL factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Bada AG BADAFLEX® SEBS-Comp. TPE-S 80A 5015 EL is packed in 25 kg polyethylene bags, 40 bags per pallet. |
| Container Loading (20′ FCL) | BADAFLEX® SEBS-Comp. TPE-S 80A 5015 EL is loaded in 20′ FCL containers, palletized, evenly distributed, and secured for safe transport. |
| Shipping | BADAFLEX® SEBS-Comp. TPE-S 80A 5015 EL is typically shipped as dry thermoplastic elastomer pellets in sealed moisture-barrier bags or octabins. It is normally non-hazardous for transport and should be kept at ambient temperature, protected from moisture, heat, and UV during standard road, sea, or air freight. |
| Storage | Store Bada AG BADAFLEX® SEBS-Comp. TPE-S 80A 5015 EL in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and moisture. Keep in original sealed packaging on clean pallets; avoid dust, oils, and contamination. Protect from UV and mechanical damage. Do not stack excessively to prevent deformation. Use first-in-first-out and observe manufacturer’s shelf-life and temperature guidance. |
| Shelf Life | Typical shelf life is 24 months in original unopened packaging, stored dry at room temperature away from direct sunlight. |
Power tool impact guards and hand-grip inserts are produced in two-shot injection moulds where the first shot is PP-GF30 and the second shot is this TPE-S. The compound flows at lower melt viscosity than glass-filled polypropylene; barrel profiles therefore place the PP screw between 230 °C and 250 °C while the TPE-S barrel is set from 180 °C at the feed throat to 210 °C at the nozzle. Interfacial adhesion is not an automatic property; it depends on diffusion of the EB midblock segments into the softened polypropylene skin. When pre-moulded PP inserts cool below 90–110 °C before the SEBS shot enters, peel strength on the finished part can fall to levels that allow separation at the grip edge. Moulders maintain the moving half at 40–60 °C and keep transfer time below 5 s when using insert loading. A recurring field failure in insert moulding is steam blistering at the bond line when PP plaques are stored in uncontrolled humidity; both the substrate and the TPE-S must be pre-dried before processing. Mould shrinkage differentials control part flatness: unreinforced SEBS compounds of this hardness typically show linear mould shrink in the range 1.5–2.5 % according to ISO 2577, while PP-GF30 shrinks below 0.5 %. Long flat grips therefore require symmetric gate placement, balanced flow channels, and delayed ejection until the part surface falls below 50 °C. Peel resistance is evaluated by DIN 53531 at a 90° peel angle, and the failure mode should be recorded as adhesive at the interface or cohesive within the TPE; cohesive rupture demonstrates that the bond line is not the limiting zone. Published independent peel values for this exact 5015 EL grade are limited, so converters should generate substrate-specific data on their own tool geometry before fixing cycle time estimates. If the overmoulded article carries a conductive or flame-retardant claim, the final assembly must be tested separately because the raw SEBS compound alone does not transfer a UL 94 classification or RTI.
Detergent dispenser sleeves, drain bellows, and curved flexible connectors in vertical-axis washing machines are extruded from the compound as thin-wall convoluted profiles that must accept repeated flex cycles at 0.1–0.3 Hz during normal operation. The extrusion line uses a single-screw machine with L/D 24–30, a screw compression ratio of 2.5:1, and a barrier zone that limits melt temperature variation caused by high plasticizer content. Barrel temperatures are set from 160 °C at the feed section to 190 °C at the die head; above 200 °C, the melt tends to smoke and the profile surface becomes tacky. Vacuum calibration with water at 15–25 °C is used to fix thin-wall geometry, but rapid quenching can induce surface micro-cracks at the convolution roots when wall thickness drops below 0.8 mm. A draw-down ratio below 1.2:1 is maintained between die gap and calibration to reduce frozen-in stress. Under detergent exposure, the EB midblock provides resistance to alkaline water and soap solutions, but contact with chlorinated disinfectants should be limited because chlorinated species accelerate embrittlement of the styrenic phase. Rejection conditions on production lines commonly include radial thinning at the bellows root, pinholes caused by insufficient melt homogenization, and tacky surfaces from oil migration after long storage. Surface tack can be reduced by storing the compound below 25 °C and avoiding direct UV exposure. Hardness retention after 500 detergent cycles in consumer appliance validation is often checked by ISO 868 on the final profile; a shift upward of 5–8 Shore A may be acceptable if the sealing lip still recovers. Published data for this particular 5015 EL formulation in long-term hot detergent aging is limited, so appliance manufacturers should qualify the compound on their exact profile and wash program.
Water-conditioning units, aquarium circulation assemblies, and floor-cleaning machines use this 80 Shore A compound in flexible tubing connectors that are pushed over barbed fittings and retained without additional clamps below internal pressure of 0.3 MPa. The conversion route is profile extrusion through a straight die with an air mandrel; because the material has high melt strength, sagging is controlled by keeping the die temperature at 180–200 °C and the cooling bath air gap below 30 mm. A common failure on start-up is lumen collapse when the puller speed is too high relative to the cooling capacity; processors therefore hold the ratio of puller speed to extruder output such that the tube outer diameter falls within ±0.15 mm immediately after cooling. For water-contact service, the converter must independently verify migration and sensory properties according to Regulation (EU) 10/2011 Annex II and, where applicable, FDA 21 CFR 177.1810; the raw compound certificate does not transfer food-contact or drinking-water approval to the finished tubing. So-called boiling-water disinfection cycles above 80 °C will soften the part and may cause plasticizer extraction; SEBS-based TPE-S is therefore not recommended for hot-water pressure lines. Swelling in non-polar liquids also limits use to aqueous media; contact with aromatic hydrocarbon-based cleaning solvents leads to volume increase and loss of interference fit. If peristaltic pump elements are considered, the fatigue limit should be evaluated on the finished tube under the actual roller geometry because pinching produces localized heat and can raise the inner surface temperature above the ambient liquid temperature. Hardness before and after immersion in water at 60 °C for 7 days can be measured by ISO 868; migration of low-molecular-weight oil fractions produces surface tack and a small upward hardness drift, which may be acceptable only if fitting retention force remains above the assembly specification.
Public transit window surrounds and interior glazing beads are candidates for the co-extrusion of a rigid polypropylene core and an outer sealing lip made from the 80 Shore A SEBS compound. The interest in replacement arises from the recyclability of the olefinic system, as well as lower compound density than vulcanized EPDM. Co-extrusion requires separate melt pumps and a feedblock die; the PP core is processed at 190–220 °C, while the TPE-S skin is maintained at 170–200 °C to limit degradation at the interface. Die swell of the SEBS component is greater than that of the rigid PP, so land length for the soft lip must be extended and the lip gap balanced by iterative trials. Downstream calibration uses low-friction vacuum blocks with water below 20 °C; rapid cooling increases lip stress but stabilizes profile geometry. For transit applications, the final profile assembly—not the raw TPE-S—must satisfy fire safety requirements such as EN 45545-2 R22 and R23; the plain SEBS compound cannot be assumed to meet higher hazard levels without flame-retardant testing. Ultraviolet stability is improved by the saturated EB midblock, but pigment and stabilizer loadings must still be qualified on the profile surface by accelerated weathering to ISO 4892-2. The material should not be used in areas continuously exposed to mineral oils, and it may become tacky if surface temperatures exceed 70 °C in direct sun. Manufacturers replacing EPDM should compare compression set after 70 h at 70 °C per ISO 815-1:2019, because SEBS compounds of this hardness typically have higher set than crosslinked EPDM but recover sufficiently for glazing bead retention in dry applications.
| Application boundary | Standard or directive | Test parameter | Application-specific acceptance condition |
|---|---|---|---|
| Automotive firewall grommet | ISO 815-1:2019 | Compression set, 22 h, 70 °C, 25 % deflection | Not exceeding 60 % for dry harness sealing; final article specification may be stricter |
| Overmoulded PP hand grip | DIN 53531 | 90° peel resistance after two-shot bonding | Record N/mm and failure mode; cohesive TPE failure required for bond-line approval |
| Washing machine bellows | ISO 868 | Hardness shift after detergent exposure | Upward shift of 5–8 Shore A may be allowed if sealing recovery is retained |
| Water-contact tubing | Regulation (EU) 10/2011 | Overall migration and sensory evaluation | Verified by converter for finished article; raw compound certificate does not transfer approval |
| Transit window profile | EN 45545-2 | R22 and R23 fire spread and smoke | Final assembly classification required; material alone has no blanket rating |
| Furniture impact edge | REACH Regulation (EC) No 1907/2006 | SVHC documentation | Batch-specific declaration required for institutional tenders |
Contract furniture impact edges in educational and institutional environments are injection moulded as impact-absorbing feet, bumper strips, and cable exit caps that are press-fitted over powder-coated steel tube. The 80 Shore A hardness provides a soft interference fit on dry powder-coated steel, and the static coefficient of friction should be measured by ASTM D1894 because antiskid performance is influenced by surface texture, dust, and skin sebum. Pre-drying is required only if storage RH has exceeded 60 %; 2 h at 70 °C in a desiccant dryer removes surface condensate. The tooling must account for weld lines at the cable exit openings; because the SEBS melt solidifies rapidly, the mould should use hot-runner valve gates or widen the gap at the weld line to prevent stress cracking. Melt temperature at the nozzle is 190–220 °C, injection pressure is 40–70 MPa, and the tool surface is held at 30–50 °C. Demoulding is facilitated by a textured surface in the cavity rather than by external release agents, which can cause long-term adhesion loss when painted steel is contacted. For indoor furniture, volatile organic compound emissions may be governed by regional schemes, and batch-specific SVHC documentation is expected under REACH Regulation (EC) No 1907/2006; electrical components integrated into the furniture are also within the scope of Directive 2011/65/EU (RoHS). The part should be tested for wear resistance under dry conditions using ISO 4649, but because SEBS is a relatively soft material, high abrasive floor contact will produce visible loss; floor-contact feet should therefore be designed with a replaceable geometry. Published abrasion loss data for this precise 5015 EL grade is limited, so institutional buyers should require material-specific test plaques rather than relying on generic SEBS literature.
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Introduced as a styrenic block copolymer compound, Bada AG BADAFLEX® SEBS-Comp. TPE-S 80A 5015 EL is classified as a thermoplastic elastomer based on a saturated ethylene-butylene midblock and polystyrene end blocks. The designation identifies a TPE-S family material with nominal Shore A hardness of 80, measured according to ISO 868 from a compression-moulded or injection-moulded test plaque. The SEBS backbone differentiates the material from unsaturated SBS grades because the absence of midblock double bonds limits oxidative chain scission under ultraviolet exposure and ozone attack. Published product-specific datasheets for this grade are not publicly available in full; where comparable SEBS TPE-S materials are referenced, the values below represent typical ranges for 80 Shore A SEBS compounds and should be verified against Bada AG release documentation. The suffix 5015 EL may indicate an electrical or electronic application designation within the BADAFLEX portfolio, but suffix decoding requires confirmation from the manufacturer.
At the molecular level, the polystyrene domains assemble into glassy physical crosslinks that soften above 90–95 °C, while the ethylene-butylene midblock retains elastomeric mobility to approximately -55 °C. This phase-separated morphology supports repeated deformation without chemical vulcanisation, giving melt reprocessability that thermoset rubbers do not exhibit. Hardness variation across the TPE-S series is primarily controlled by styrene content and oil loading; the 80 Shore A class balances stiffness and compliance for gripping surfaces, sealing lips, damping pads, and cable-related strain relief.
The processing window is defined at the lower bound by melt viscosity and at the upper bound by thermal degradation of the styrenic segments. SEBS compounds of this hardness typically exhibit a melt flow rate of 5–30 g/10 min when measured at 230 °C under 5 kg load according to ISO 1133-1:2022. Injection moulding barrel set points between 180 °C and 220 °C are usually required; melt temperatures above 260 °C can initiate yellowing and viscosity reduction from chain scission. Tool temperatures of 25–50 °C produce acceptable surface finish and reduce cycle-time increase. Pre-drying at 60–80 °C for 2–4 hours in a desiccant dryer is recommended when pellet surface condensation exceeds 0.10% moisture by mass, particularly after storage at relative humidity above 60%. Extrusion-grade conversion on single-screw machines with L/D ratios of 24:1–30:1 requires a compression or barrier screw and screen packs of 40–100 mesh, maintaining melt temperature below 230 °C to prevent formation of gel particles from degraded styrene domains.
Because the compound is shear thinning, fill times for thin-walled geometries are improved by raising injection speed rather than melt temperature. High-shear dispersion during compounding is achieved on co-rotating twin-screw extruders with L/D ratios of 36:1–48:1; oil absorption into the SEBS matrix controls the final Shore A value. When adding colour concentrates or processing aids, masterbatches based on SEBS or EVA are preferable to polyethylene-only carriers to preserve phase compatibility. Published data for this specific 5015 EL configuration is limited for additive interactions; preliminary compounding trials should include thermal gravimetric analysis at 10 K/min under nitrogen to identify mass-loss onset before production.
Adhesion between the SEBS compound and a polypropylene substrate is generated by interfacial interdiffusion of the olefinic midblock and the PP surface, not by covalent bonding. Substrate pre-warming to 50–80 °C and injection of the TPE-S melt at 190–220 °C promote melt-film interaction. If the PP substrate has a melt flow index below 15 g/10 min at 230 °C/2.16 kg, the surface may remain too crystalline for reliable adhesion; higher-flow PP copolymers reduce delamination failures. Injection pressures of 40–80 MPa and holding pressures of 20–40 MPa are typical for overmoulding cavity geometries of 1–3 mm elastomer thickness. Gate placement at the thickest section and venting of 0.02–0.04 mm at the parting line prevent gas entrapment and flow marks. Chill marks and jetting arise when melt-front velocity is too low or gate size is below 1 mm for a 2 mm wall. Mould release can be supported by a draft angle of 1°–3° and by avoiding undercuts that exceed the elastic recovery of the compound.
When benchmarked against other TPE chemistries, the 80 Shore A SEBS compound occupies a distinct position in density, moisture uptake, and solvent resistance. The following representative ranges are drawn from public material datasheets for comparable grades and are not product-specific release values.
| Property | Test method | SEBS TPE-S 80A | TPV 80A | TPU 80A |
|---|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.89–0.95 g/cm³ | 0.90–0.98 g/cm³ | 1.15–1.25 g/cm³ |
| Tensile strength | ISO 37:2017 | 6–15 MPa | 5–10 MPa | 30–50 MPa |
| Elongation at break | ISO 37:2017 | 400–800% | 300–600% | 400–600% |
| Compression set 23 °C/22 h | ISO 815-1:2020 | 20–35% | 15–30% | 25–45% |
Differences in processing also follow from molecular architecture. SEBS TPE-S materials do not require moisture-sensitive drying to the same extent as TPU, although surface condensation must be removed. TPV grades require the additional step of dynamic vulcanisation in the compounded pellet and generally demand higher melt temperatures; TPU requires desiccant drying below 0.02% moisture and has a narrower processing window because of hydrolysis above 190 °C in some polyester grades. SEBS compounds show lower density than TPU and better hot-water resistance than SBS; however, their oil resistance is below that of polar TPU and nitrile-containing TPVs.
Selection of BADAFLEX® SEBS-Comp. TPE-S 80A 5015 EL for electrical or electronic enclosures requires verification of substance restrictions and end-use compliance. The following references are commonly applied to SEBS compounds; they do not constitute a declaration of compliance for the specific grade.
| Domain | Reference / method | Rationale |
|---|---|---|
| RoHS restricted substances | Directive 2011/65/EU Annex II | Cadmium, lead, mercury, hexavalent chromium, PBB, PBDE |
| REACH SVHC screening | Regulation (EC) No 1907/2006 | Candidate list evaluation |
| Food-contact styrenic block copolymers | FDA 21 CFR 177.1810 | Conditions of use B through H may apply |
| Density | ISO 1183-1:2019 | Buoyancy or gas pycnometer method |
| Hardness | ISO 868:2003 | Shore A, 15 s at 23 °C |
| Tensile and elongation | ISO 37:2017 | Type 2 dumbbell, 500 mm/min |
| Surface resistivity | IEC 62631-3-1:2023 | Electrical/electronic grade screening |
For electrical enclosure applications where surface resistivity is a factor, SEBS compounds are inherently insulating; antistatic or dissipative variants require conductive fillers that are not indicated in the base designation. Published data for this specific configuration is limited, so volume resistivity should be measured according to IEC 62631-3-1:2023 on conditioned plaques at 23 °C and 50% relative humidity before qualifying the grade for live electronics. The material should not be exposed to aromatic solvents, ketones, or strong oxidising acids that swell the styrene domains or extract processing oils. Contact with low-molecular-weight polyolefin oils may cause plasticiser migration over time and shifts in Shore A hardness.
In injection moulding trials on hydraulic machines with clamp forces between 500 kN and 1500 kN, cavity pressure sensors record peak pressures of 30–60 MPa for parts with nominal wall thickness of 1.5–3.0 mm. The compound exhibits lower viscosity than comparable TPVs at high shear, allowing shorter fill times but requiring a controlled cushion of 3–6 mm. If the cushion is depleted below 2 mm, shot-to-shot variance in packing pressure produces sink marks and inconsistent adhesion in overmoulded parts. Screw recovery speed should be adjusted to avoid excessive shear heating; screw speeds above 100 rpm on 25 mm reciprocating screws may generate melt-temperature overshoot.
Part design for 80 Shore A SEBS TPE-S should account for viscoelastic recovery. Snap-fit features with undercuts greater than 0.5 mm may not return to shape after repeated insertion if local strain exceeds 100%. Living hinges are not recommended because the material lacks the crystalline fatigue resistance of polypropylene and may tear after repeated flexing. Sealing lips should have a compression ratio of 15–25% for adequate closure without excessive set; when using ISO 815-1:2020 data, laboratory compression set at 70 °C/22 h is a more reliable predictor than room-temperature values.