| HS Code | 419051 |
| Density | 1.03 g/cm³ |
| Hardness | 40 Shore D |
| Tensile Strength | 12 MPa |
| Elongation At Break | 500% |
| Modulus At 100 Elongation | 8 MPa |
| Tear Strength | 55 N/mm |
| Compression Set At 23 C 72 H | 35% |
| Compression Set At 70 C 24 H | 55% |
| Rebound Resilience | 35% |
| Abrasion Resistance | 150 mm³ |
| Processing Method | Injection molding |
| Service Temperature Range | -50 to 120 °C |
| Color | Natural |
As an accredited Bada AG BADAFLEX® SEBS-Comp. TPE-S 40D 1038 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 40D 1038 is packaged in 25 kg moisture-resistant polyethylene bags on pallets. |
| Container Loading (20′ FCL) | Bada AG BADAFLEX® SEBS-Comp. TPE-S 40D 1038 shipped in a 20′ FCL dry container, palletized bags, ambient/dry conditions, securely stowed. |
| Shipping | BADAFLEX® SEBS-Comp. TPE-S 40D 1038 is shipped as a non-hazardous thermoplastic elastomer compound, typically in moisture-protective bags or octabins. It is not classified as dangerous goods for transport. Keep containers closed, dry, and protected from excessive heat and direct sunlight. Standard industrial packaging applies; no special transport labels required. |
| Storage | Store Bada AG BADAFLEX® SEBS-Comp. TPE-S 40D 1038 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep in original, closed packaging to prevent contamination and degradation. Avoid contact with incompatible chemicals. Maintain stable temperature, use good housekeeping, and follow local regulations and the manufacturer’s safety data sheet. |
| Shelf Life | Shelf life is typically 24 months from production when stored dry, unopened, in original packaging at room temperature. |
Bada AG BADAFLEX® SEBS-Comp. TPE-S 40D 1038 is a hydrogenated styrenic block copolymer compound supplied as a ready-to-mould pellet with nominal hardness 40 Shore D when measured under ISO 868:2003. The hydrogenated ethylene-butylene midblock distinguishes the compound from unsaturated SBS grades in terms of oxidative stability and melt processing boundaries. The downstream application scenarios that follow are based on publicly documented processing behaviour for SEBS-based TPE-S compounds in this hardness class; where grade-specific published data is limited, that limitation is stated explicitly rather than inferred from unrelated formulations.
In automotive interior two-component moulding, melt temperature control in SEBS-based TPE-S compounds of nominal 40 Shore D hardness remains a first-order variable. The grade is processed in tandem with polypropylene or PC/ABS substrates for dashboard inserts, door panel trim, climate control bezels, and armrest surfaces that require a semi-rigid tactile surface rather than a fully elastomeric grip. Feedstock should be dried to a moisture content not exceeding 0.05% at 60 °C to 70 °C for 2 h to 3 h when ambient storage exceeds 60% relative humidity; trapped moisture produces splay and inconsistent gloss on the visible surface. Barrel zones are typically profiled from 180 °C at the feed throat through 200 °C in the compression zone to 220 °C at the nozzle. Melt temperatures above 230 °C initiate measurable increases in gel bodies and odour-relevant degradation products, while temperatures below 190 °C reduce interfacial interdiffusion with the substrate. Mould temperature is held between 20 °C and 40 °C for PP and 50 °C to 70 °C for PC/ABS; the higher PC/ABS mould temperature reduces frozen-in orientation but extends cycle time by 8 s to 15 s depending on wall thickness. Flow front temperature at the interface should exceed the heat deflection temperature of the substrate by 10 °C to 25 °C to create an interpenetrating layer, and vents are cut to a depth of 0.01 mm to 0.02 mm to avoid gas traps at the last fill point. Interior release often requires fogging according to DIN 75201:2011-01, odour according to VDA 270:2018-08, and VOC/SVOC emission according to VDA 278:2018-10; the hydrogenated midblock reduces volatile breakdown products relative to unsaturated styrenic block copolymers, but oil extenders and processing stabilisers still influence test outcomes. Paintability is limited without surface treatment; flame or plasma pre-treatment is used when a decorative coating is specified, and overspray adhesion is screened by cross-cut methods before production release.
Dimensional stability after overmoulding onto glass-fibre-reinforced polyamide substrates is governed by differential shrinkage between the substrate and the TPE-S layer. The PA6/6-GF30 substrate exhibits mould shrinkage in the range 0.2% to 0.5% in the flow direction, while the SEBS-based 40 Shore D compound typically exhibits 0.8% to 1.5% depending on wall section and gate geometry. This mismatch generates interfacial shear stress during cooling, which appears as edge lifting, sink marks over ribs, or delamination at the grip boundary. Substrate preheating to 80 °C to 120 °C before overmoulding is a standard corrective action; below 60 °C surface temperature the melt cools before sufficient molecular interdiffusion can occur, while above 120 °C the substrate can soften and lose reinforcement alignment. The TPE-S melt is injected at 190 °C to 220 °C, with the upper limit constrained by the onset of styrene endblock degradation and the lower limit by poor knit-line strength around the grip core. Injection speed is held between 20 cm³/s and 80 cm³/s for a typical handle cavity; speeds below 20 cm³/s produce short shots at the end of fill, while speeds above 80 cm³/s induce jetting and hesitation lines that are visible on the class-A surface. Back pressure is maintained at 2 MPa to 5 MPa to homogenise the melt without excessive work input.
Process limits are therefore narrow. Melt temperature below 180 °C produces poor adhesion and visible knit lines in the grip core, while melt temperature above 230 °C produces gel bodies, burn marks, and odour increase. Substrate surface temperature below 60 °C causes skinning and deadhesion at edges; above 120 °C causes substrate distortion and sink marks. Injection speeds below 20 cm³/s cause premature freeze-off, and speeds above 80 cm³/s cause jetting and gate blush. Holding pressure below 30% of peak produces sink voids and dimensional spread; holding pressure above 65% of peak produces flash and gate stress cracking. Tooling requirements for power tool handles are not interchangeable with general-purpose TPV or TPU tools. Gate thickness should be at least 60% of the overmoulded wall section, and gate land lengths are kept below 1.0 mm to avoid premature gate freeze. Vent lands of 0.01 mm to 0.015 mm are machined along the parting line at the last-fill location; insufficient venting produces burn marks and reduced peel strength. Peel adhesion is evaluated by a modified 90° peel fixture; no single ISO standard fully captures TPE-to-PA overmould adhesion, so internal release specifications typically reference ISO 813:2019 for rubber-to-metal as a comparative baseline. Production machines are selected for reproducible shot volume rather than clamp force alone; a clamp force of 2 kN/cm² to 5 kN/cm² projected area is typical for insert overmoulding. Batch-to-batch variation in compound hardness of ±3 Shore D influences pack pressure requirements and should be monitored from incoming lot data. Tool surfaces are run without silicone-based mould release because residual silicone films reduce adhesion at the substrate boundary. If a textured surface finish is specified, texture depth above 0.1 mm can trap air and reduce contact area, so grain depth and venting must be balanced during tool tryout.
In industrial connector strain-relief production, the compound is processed as a melt at 190 °C to 220 °C, with the exact profile governed by barrel segmentation and screw geometry. The application covers circular sensor connectors, fieldbus cable exit sleeves, and handheld terminal strain-relief boots where flexion fatigue and low-temperature ductility are primary requirements. Pre-drying at 60 °C to 70 °C for 2 h to 3 h is applied when feedstock moisture exceeds 0.05%; cables are preheated to 50 °C to 70 °C immediately before insertion to reduce melt freezing at the cable jacket interface. Self-centering cable fixtures with vacuum sealing are required to prevent melt leakage along corrugated or braided jackets; without tooling seal integrity, flash accumulates in the cable entry zone and reduces connector pull-out resistance. Gate positioning on the cable side rather than the flex zone moves the weld line away from the highest cyclic stress region, and the melt is injected at medium-to-high speed to prevent hesitation at the cable junction.
Long-term connector durability is evaluated with thermal cycling and cable retention tests; compression set under ISO 815-1:2014 at 22 h and 70 °C is used to screen materials for strain-relief duty. Compounds in the 40 Shore D SEBS class generally exhibit compression set values that can exceed 40% if the formulation is not optimised; for strain reliefs specified to retain clamping force over engine-compartment temperature cycles, published data for this specific grade should be verified under the actual wall section and post-cure history. Low-temperature flexibility is screened by ASTM D746 or ISO 812; grade-specific published data for this compound is limited, but the saturated SEBS midblock provides lower brittle-point sensitivity than unsaturated SBS analogues. PVC cable jackets with migratory low-molecular-weight plasticisers can reduce adhesion and soften the overmould; PUR or XLPE jackets are preferred when chemical compatibility is uncertain. For connectors tested to IP67 under IEC 60529:1989+AMD1:1999+AMD2:2013, the seal section must remain under positive compression after assembly; if the compression set exceeds the design tolerance, the seal can leak after thermal shock.
Fenestration profile extrusion imposes a different shear history than the injection moulding routes described in earlier sections. Glazing channels, bubble seals, and corner gaskets are produced on single-screw extruders with an L/D ratio of 24:1 to 30:1 and a screw compression ratio of 2.5:1 to 3.0:1. Barrel temperatures are set from 180 °C at the feed throat to 200 °C at the die, with the nozzle kept below 210 °C to limit die drool and surface roughness. Calibration occurs in a vacuum tank at 10 °C to 25 °C, and haul-off speed is set to produce between 5% and 10% drawdown from the die dimension; excessive drawdown increases die swell sensitivity and wall-thickness variation, while insufficient drawdown leads to sag in complex profile legs. Non-contact laser gauges are placed after the vacuum tank to monitor width and web thickness continuously; batch-to-batch hardness variation of ±3 Shore D can shift the calibration window and must be compensated by screw speed rather than haul-off tension alone.
The compound is not a direct drop-in substitute for vulcanised EPDM in every fenestration profile. SEBS-based 40 Shore D TPE-S offers recyclability and weldability but sacrifices compression set at elevated service temperatures. Under ISO 815-1:2014, seal applications should verify compression set after 70 h at 70 °C; if sustained sealing stress exceeds 30% compression or service temperatures exceed 80 °C, EPDM or a crosslinked TPV may be more dimensionally stable. Corner joining is not typically performed by hot-plate welding; adhesive bonding or co-extruded rigid PP corner keys are used to preserve the seal leg geometry. Weathering performance is screened by ISO 4892-2:2013 and ISO 105-A02 for discoloration; SEBS requires an adequate UV stabiliser package, and grade-specific weathering data must be obtained from Bada AG before specifying exterior exposure beyond 3 years. For fire-rated glazing systems, the compound has no intrinsic fire classification and must be evaluated within the full system according to EN 13501-1; it should not be assumed to contribute to the fire resistance of the assembly.
When the material is selected for non-implant medical grips and handheld diagnostic housings, the primary compliance review must distinguish polymer composition certification from finished device validation. The compound's SEBS chemistry falls within the general category of hydrogenated styrenic block copolymers, but the specific additives, oil extenders, and stabilisers used in the grade determine whether a particular regulatory pathway is available. Cytotoxicity is evaluated by ISO 10993-5:2009 using MTT assay on extract dilutions; sensitisation and irritation are evaluated by ISO 10993-10:2010. USP Class VI data under USP <88> for systemic injection, intracutaneous, and implantation tests should be requested from Bada AG for the specific production lot. Food-contact components may additionally reference FDA 21 CFR 177.1810 for styrene block copolymers, but the finished device remains subject to food additive migration testing under the intended conditions of use. The following matrix summarises the compliance checks that are applied before transferring the material into a cleanroom production environment.
| Standard or regulation | Test method | Application scope |
|---|---|---|
| ISO 10993-5:2009 | MTT cytotoxicity | Non-implant device housings and grips |
| ISO 10993-10:2010 | Sensitisation and irritation | Prolonged skin contact |
| USP <88> Class VI | Systemic injection, intracutaneous, implantation | Polymer grade biocompatibility screening |
| FDA 21 CFR 177.1810 | Styrene block copolymer food-contact regulation | Food-contact device components |
| REACH 1907/2006 Annex XVII | Restricted substances | EU market access |
| RoHS 2011/65/EU + (EU) 2015/863 | Lead, phthalates, other restricted substances | Electrical diagnostic devices |
Cleanroom processing for medical grips uses a dedicated injection moulding cell with all contact surfaces purged of non-medical residues. Hot runner systems without dead spots are preferred; if a cold runner is used, regrind must be segregated by lot and validated because regrind alters viscosity and extractables. Sterilisation compatibility is evaluated before device labelling. Gamma irradiation at 25 kGy to 50 kGy can induce slight yellowing and hardness increase in SEBS compounds due to endblock crosslinking; ethylene oxide is less aggressive but requires degassing and residue testing under ISO 10993-7:2008. Steam autoclave cycles at 121 °C are generally not recommended for this hardness class because compression set and dimensional recovery under load are insufficient for repeated sterilisation. The material is not considered appropriate for implant or blood-contact use unless the finished device manufacturer has obtained specific validation data for the intended indication.
For sports and recreation equipment, low-temperature impact retention and compression set under cyclic loading define whether the stated 40 Shore D hardness remains functional after prolonged outdoor exposure. Applications include overmoulded bicycle grip cores, ski pole handles, fitness equipment grips, and protective housing bumpers where a semi-rigid, non-slip surface is required. The compound is injection moulded or overmoulded at barrel temperatures between 190 °C and 220 °C; thin decorative sections below 1.5 mm may require fast injection speeds above 50 cm³/s to fill before freeze-off. Mould temperatures from 20 °C to 40 °C are used for textured grip surfaces, and texture reproduction improves when the tool is run at the upper end of this range. Dynamic coefficient of friction may be screened by ASTM D1894; SEBS-based compounds in this hardness class typically provide higher wet-surface grip than EVA but lower than vulcanised rubber, and published data for this specific grade is limited. Low-temperature behaviour should be verified by ASTM D746 or ISO 812 because brittle point is formulation-dependent and cannot be assumed from nominal hardness alone. Outdoor exposure is evaluated by ISO 4892-2:2013 accelerated weathering; without adequate UV stabilisation, styrenic hard blocks can show microcracking and loss of gloss. Direct contact with insect repellents containing DEET or aliphatic hydrocarbon lubricants can soften the SEBS matrix and reduce abrasion resistance under ISO 4649:2010; such exposure should be excluded from the product specification or mitigated with a protective over-layer.
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Bada AG BADAFLEX® SEBS-Comp. TPE-S 40D 1038 is a thermoplastic elastomer compound based on a styrene-ethylene/butylene-styrene block copolymer matrix. The grade designation identifies a nominal hardness of 40 Shore D when measured under ISO 868:2003, placing the material in the semi-rigid segment of the TPE-S range. Unlike dynamically vulcanized TPV systems, the SEBS architecture derives mechanical integrity from physically crosslinked polystyrene domains rather than covalent vulcanization, allowing melt reprocessing on conventional thermoplastic equipment. The saturated ethylene-butylene midblock confers resistance to hydrolytic degradation and oxidative attack that is not consistently available in polyester TPU grades. Product-release conformance is normally established under ISO 1183-1:2019 for density, ISO 37:2017 for tensile stress-strain properties, ISO 34-1:2022 for tear strength, and ISO 815-1:2019 for compression set. Independent public data for the 1038 variant is limited; nominal tensile strength, elongation at break, tear resistance, and melt-flow characteristics should therefore be read from the current Bada AG product datasheet rather than inferred from generic SEBS values.
| Property or parameter | Standard designation | Role in specification |
|---|---|---|
| Hardness | ISO 868:2003 | Grade identity at 40 Shore D |
| Density | ISO 1183-1:2019 | Mass-per-volume release limit and part-weight control |
| Tensile stress-strain | ISO 37:2017 | Tensile strength and elongation at break |
| Tear strength | ISO 34-1:2022 | Resistance to crack propagation in thin sections |
| Compression set | ISO 815-1:2019 | Sealing-force retention at defined temperature and time |
| Melt mass-flow rate | ISO 1133-1:2022 | Processability and lot-to-lot flow consistency |
For melt processing of SEBS-based TPE-S compounds in the 40 Shore D class, the practical barrel-temperature window is generally between 180 °C and 220 °C, with rear zones set lower to avoid premature softening of the styrenic domains. Sustained exposure above 240 °C can initiate block-copolymer degradation or viscosity shift, and the exact thermal boundary should be confirmed against the supplier’s processing release. On production-scale reciprocating-screw machines, polyolefin-type screws with L/D ratios of 20:1 to 25:1 and compression ratios of 2.5:1 to 3.5:1 are commonly used for SEBS compounds. Shot sizes below 20% of maximum barrel capacity can produce excessive residence time and gel formation, while shot sizes above 70% may reduce melt homogeneity. Injection speed should be moderate to high in thin-wall tooling to prevent premature solidification, but shear rates above 1,000 s⁻¹ may induce pronounced shear thinning that complicates gate-to-cavity filling balance. Holding pressure is typically selected from 400 bar to 700 bar as a function of gate size and flow length, and mold temperatures from 20 °C to 50 °C are standard unless texturing or low-gloss finishes require specific surface-temperature control.
Although the saturated SEBS midblock absorbs only minimal water, surface condensation on cold pellets or regrind can generate splay and surface defects. Pre-drying at 70 °C to 80 °C for 2 h to 4 h in a desiccant or circulating-air dryer is a conservative production control when ambient relative humidity exceeds 60%. Purging after processing of this TPE-S grade may be performed with polypropylene or HDPE when changing to higher-temperature engineering resins. Batch-to-batch incoming inspection should record Shore D hardness on conditioned 6 mm plaques under ISO 868:2003 and melt mass-flow rate under the supplier’s specified load and temperature; these release limits are more sensitive to lot variability than visual inspection alone.
In sealing, grommet, coupling, and flexible-mount applications, the 40D hardness range balances structural stiffness against deflection recovery. The material can be converted by injection molding for dimensionally consistent parts and by profile extrusion for tubing, edge protection, and hollow gaskets. For profile extrusion of SEBS compounds in this hardness class, melt temperatures in the 180 °C to 210 °C range with water or air calibration are typical, but the exact screw configuration depends on profile wall thickness and draw ratio. Compression set after 24 h at 70 °C under ISO 815-1:2019 is often a more useful selection criterion than Shore D hardness alone for components under continuous clamp load. In dynamic applications, fatigue performance should be evaluated on injection-molded prototypes under the specific strain amplitude and frequency of the end-use condition, because published data for this specific 1038 configuration under cyclic loading is limited.
Compared with a similar-Shore-D TPV, the SEBS-based TPE-S compound generally offers lower density, easier colorability, and softer-flow characteristics, but it may exhibit higher elevated-temperature compression set and lower hot-oil resistance. Compared with a polyester TPU of equivalent hardness, the TPE-S grade is less sensitive to hydrolytic degradation in humid service and does not require the same intensity of pre-drying as TPU; however, abrasion resistance under ISO 4649 and tear strength under ISO 34-1:2022 may be lower. Compared with thermoset silicone, the SEBS compound can be reground and reprocessed in production scrap loops, but it is not suitable for sustained hot-air or steam exposure above 90 °C unless product-specific heat-aging data demonstrates otherwise. Tooling designed for rigid polypropylene or nylon may require gate and vent modifications because the TPE-S melt is more elastic and can exhibit jetting, gate blush, and flow-mark formation if the gate velocity is not controlled.
Where regulatory compliance is required, the final article rather than the raw compound must be assessed. RoHS compliance may be supported by screening for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE using IEC 62321 methods. SVHC obligations are addressed through the supplier’s REACH statement for the specific grade and production lot. For food-contact evaluations, SEBS block copolymers may fall within the scope of FDA 21 CFR 177.1810 or EU 10/2011 if the complete formulation contains only permitted substances; migration testing on the finished article is mandatory. Continuous immersion in aromatic hydrocarbons, chlorinated solvents, or high-aromatic fuels should be avoided because the styrene domains soften and the ethylene-butylene midblock swells. Strong oxidizing acids may degrade the saturated midblock over extended exposure. When such service conditions are present, a TPV or fluoropolymer alternative should be screened using the same application-specific test protocol.