| HS Code | 465130 |
| Productname | LCY Chemical Globalprene SEBS 7550U |
| Manufacturer | LCY Chemical |
| Polymertype | SEBS |
| Appearance | White powder |
As an accredited LCY Chemical Globalprene® SEBS 7550U factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LCY Chemical Globalprene® SEBS 7550U is typically supplied in 25 kg net multilayer paper bags with PE liners, palletized. |
| Container Loading (20′ FCL) | 20′ FCL loading of LCY Chemical Globalprene® SEBS 7550U in 25 kg bags, palletized and secured for ocean shipment. |
| Shipping | LCY Chemical Globalprene® SEBS 7550U is shipped as non-hazardous, solid thermoplastic elastomer pellets in sealed moisture-barrier bags or 25 kg sacks/big bags on pallets. Transport under dry ambient conditions, protecting from moisture, heat, sunlight, and contamination; no UN hazard class applies. |
| Storage | Store LCY Chemical Globalprene® SEBS 7550U in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and moisture. Keep material in its original, tightly sealed packaging to prevent contamination and degradation. Avoid prolonged exposure to UV light, ozone, and strong oxidizing agents. Maintain good housekeeping and follow local regulations and supplier safety data sheet recommendations. |
| Shelf Life | Typical shelf life is 24 months under dry, cool, well-ventilated storage, protected from direct sunlight and moisture. |
Competitive LCY Chemical Globalprene® SEBS 7550U prices that fit your budget—flexible terms and customized quotes for every order.
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LCY Chemical Globalprene® SEBS 7550U is supplied as a pelletized hydrogenated styrene-ethylene/butylene-styrene block copolymer intended for compounding into thermoplastic elastomer formulations. The grade is not oil-extended, and the saturated midblock eliminates main-chain unsaturation, which changes thermo-oxidative and ozone-resistance behavior relative to unsaturated styrene-butadiene-styrene copolymers. In the supplier’s published technical data, the styrene content is nominally 30 wt%; the melt flow index is reported as 5 g/10 min when measured at 230 °C under a 2.16 kg load according to ISO 1133-1:2022. Typical mechanical properties are obtained on compression-molded specimens and include a Shore A hardness of 68 per ISO 7619-1:2019, a tensile strength of 27.5 MPa per ISO 37:2017, an elongation at break of 550% per ISO 37:2017, and a 300% modulus of 3.2 MPa per ISO 37:2017. The 7550U designation denotes a built-in ultraviolet stabilization package, but the grade still requires formulation-level light stabilizers when exposed to prolonged UV irradiation in thin pigmented sections.
Unsaturated SBS grades contain olefinic double bonds in the polybutadiene midblock. When tested according to ISO 1431-1:2019 under static ozone exposure, those double bonds undergo electrophilic addition with ozone, followed by chain scission and surface cracking unless antiozonant additives are present. In 7550U, hydrogenation converts the midblock to an ethylene/butylene saturated sequence. The saturation removes the primary reaction site for ozone attack, but the terminal polystyrene domains still exhibit a glass transition near 95 °C, which limits dimensional stability under load above that range. Heat aging in forced-air ovens per ISO 188:2019 generally shows higher elongation retention for SEBS than for SBS, though the exact numerical retention depends on the stabilizer package and specimen thickness. Published data for 7550U under ISO 188:2019 at 100 °C and 168 h is limited in the public product literature. The practical consequence is that 7550U compounds are selected over SBS when exterior exposure, hot-air aging, or intermittent contact with body oils and perspiration is expected, while unsaturated SBS may remain serviceable only in indoor or cost-driven applications where antiozonant bloom is acceptable.
The following values are reproduced as typical data from the manufacturer’s published product information. They are not to be construed as specification limits, and lot-to-lot variation should be controlled against agreed internal quality plans.
| Property | Test designation | Typical value | Unit |
|---|---|---|---|
| Melt flow index | ISO 1133-1:2022 | 5 | g/10 min at 230 °C/2.16 kg |
| Hardness | ISO 7619-1:2019 | 68 | Shore A |
| Tensile strength | ISO 37:2017 | 27.5 | MPa |
| Elongation at break | ISO 37:2017 | 550 | % |
| 300% modulus | ISO 37:2017 | 3.2 | MPa |
| Specific gravity | ISO 1183-1:2019 | 0.91 | g/cm³ |
| Styrene content | Internal LCY method | 30 | wt% |
On a 40:1 L/D co-rotating twin-screw extruder with 12 temperature-controlled barrel zones, the feed throat is kept below 50 °C and zone 1 is set at 150–170 °C to prevent pellet agglomeration at the screw inlet. Subsequent barrel zones are operated at 180–210 °C, and the die is maintained at 190–210 °C. If the melt temperature exceeds 260 °C, styrene endblocks undergo thermo-oxidative chain scission; the visible indicators are yellowing, deposit formation on the die lips, and a measurable loss of tensile strength on molded plaques. Vacuum devolatilization is applied at -0.06 MPa gauge or lower to remove moisture and volatile degradation products. For compounds exposed to moisture before processing, pre-drying in a desiccant dryer at 80 °C for 2–4 h is required to reduce residual water to below 0.03%. Failure to meet that moisture limit produces surface splay and internal bubbles in extruded profiles and injection-molded parts. On an injection molding line, barrel temperatures between 180 °C and 220 °C and mold temperatures between 20 °C and 50 °C are typical for moderate-viscosity compounds made from 7550U. The observed processing defect of screw slip is more common with high oil loadings than with neat 7550U, and it is addressed by barrel temperature profile adjustment rather than by increasing screw speed alone.
Because 7550U is supplied undiluted, the compounder retains direct control over plasticizer content. Paraffinic oil is the standard extending fluid for the saturated midblock. In a co-rotating twin-screw extruder, oil added before the polymer has transitioned to a rubbery melt forms a lubricant film on the screw elements, reduces the specific energy input needed for melting, and may interrupt solids conveying. On a 40:1 L/D machine with 12 barrels, side-stuffing of oil is normally placed at barrel 6 or later when the oil content exceeds 20 phr. Early addition at barrel 3 is associated with melt-pressure oscillation at the die and throughput surging rather than steady shredding of the pellet bed. Oils with kinematic viscosity between 40 cSt and 100 cSt at 40 °C are typically compatible; aromatic or naphthenic oils are avoided because plasticization of the styrenic endblocks lowers tensile strength and raises the risk of surface exudation. Polypropylene addition at 5–15 wt% is used to increase hardness and increase thermal resistance, but polypropylene loadings above 30 wt% increase modulus at the expense of elongation and produce a brittle cold-temperature response. Dry blending of 7550U pellets, polypropylene, and stabilizers in a low-shear ribbon blender for 10 min is sufficient for pre-distribution before melt compounding.
In automotive interior skin foils, 7550U is typically formulated with polypropylene, a paraffinic oil, and a mineral filler to produce a low-gloss, cohesive thermoplastic olefin-like surface. The saturated midblock provides resistance to accelerated heat aging in interior cabins, while the styrenic endblocks provide mechanical integrity at ambient temperature. For exterior profiles and weatherstrip applications, compounded 7550U is tested under xenon-arc exposure to ISO 4892-2:2013 or SAE J2527 depending on the end market. The built-in UV stabilization package contributes to retention of surface appearance, but pigmented compounds still require supplementary hindered amine light stabilizers and UV absorbers when prolonged outdoor exposure is specified. In soft-touch overmolding onto polypropylene substrates, adhesion is generated primarily by melt interdiffusion into an olefinic substrate; the failure mode is assessed by a 180° peel fixture on a universal tensile machine according to the final part specification. Published data for these specific configurations is limited, so compound validation is required for each substrate grade and mold texture. In polymer modification, 7550U is added at 5–20 wt% to polypropylene or polyolefin blends to improve impact retention at sub-zero temperatures. In adhesive and sealant formulations, the grade serves as a high-styrene, non-oil-extended base for cohesive strength development; tackifier resins are added separately to control tack and open time. For cable jacketing and wire coating compounds, the saturated midblock allows exposure to moisture and ozone without the cracking typical of unsaturated SBS, but final compounds must be tested for volume resistivity and hot-set elongation under the applicable harmonized cable standards.
Supplier documentation for 7550U includes statements relevant to European Union REACH Regulation EC 1907/2006 and the EU RoHS Directive 2011/65/EU as amended. The base styrene block copolymer may be reviewed against FDA 21 CFR 177.1810 for styrene block copolymers intended for use in contact with food, but the UV-stabilized 7550U grade requires end-use additive compliance review before any food-contact claim is made. Medical-grade or pharmaceutical-grade status is not automatically conferred by the polymer backbone; any claim for skin contact under ISO 10993-5:2023 cytocompatibility or ISO 10993-10:2021 irritation requires testing on the fully formulated compound. Operational boundaries include the avoidance of strong polar solvents, ketones, and esters at elevated temperature, which can extract process oils and additives from the compound. Aliphatic hydrocarbon solvents cause reversible swelling of the midblock and may reduce tensile strength until the solvent evaporates. Oxidizing acids and chlorinated solvents should be avoided in service because they attack the stabilizer package and may accelerate surface degradation. The material is not suitable for continuous exposure above its polystyrene endblock softening range without structural support, and thin sections exposed to combined heat, ozone, and UV should be validated under the specific service conditions rather than extrapolated from generic SEBS field experience.