| HS Code | 999069 |
| Product Name | SINOPEC Baling SEBS YH-501T |
| Manufacturer | SINOPEC Baling Petrochemical |
| Polymer Type | Hydrogenated styrene-butadiene-styrene block copolymer (SEBS) |
| Structure | Linear |
| Appearance | White powder |
| Styrene Content | 30% (typical) |
| Density | 0.90 g/cm³ (typical) |
| Melt Flow Rate | 1.0 g/10 min (typical) |
| Shore A Hardness | 70 (typical) |
| Tensile Strength | ≥20 MPa |
| Elongation At Break | ≥500% |
| Volatile Matter | ≤1.0% |
| Ash Content | ≤0.2% |
| Moisture Content | ≤0.5% |
As an accredited SINOPEC Baling SEBS YH-501T factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SINOPEC Baling SEBS YH-501T comes in 25 kg PP woven bags, typically supplied in full pallet quantities. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with SINOPEC Baling SEBS YH-501T in sealed bags, palletized, shrink-wrapped, and secured for ocean shipment. |
| Shipping | SINOPEC Baling SEBS YH-501T is shipped as a non-hazardous thermoplastic elastomer, typically in 25 kg woven bags or jumbo bags, palletized and stretch-wrapped. Store in a dry, ventilated area away from moisture, direct sunlight, and heat. No UN number or dangerous goods classification applies; standard freight handling is required. |
| Storage | Store SINOPEC Baling SEBS YH-501T in a cool, dry, well-ventilated warehouse, ideally below 40°C, away from direct sunlight, heat, flames, and moisture. Keep original packaging tightly sealed and pallets off the floor to prevent contamination and water absorption. Avoid dust, oil, and UV exposure; use clean handling equipment and follow first-in, first-out stock rotation. |
| Shelf Life | Shelf life is typically 24 months when stored in a cool, dry, well-ventilated place, away from direct sunlight and moisture. |
Competitive SINOPEC Baling SEBS YH-501T prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
SINOPEC Baling SEBS YH-501T is a linear styrene-ethylene-butylene-styrene block copolymer produced by selective hydrogenation of the midblock of a styrene-butadiene-styrene precursor. The saturated ethylene-butylene segment removes the olefinic unsaturation characteristic of SBS grades and shifts the thermal, UV, and ozone resistance profile into the range required for long-life outdoor and high-temperature applications. In YH-501T, the polystyrene end-block mass fraction is approximately 30 wt%, placing the grade in the mid-styrene region of the Baling SEBS product ladder. The product is supplied as a white porous pellet or powder, depending on packaging configuration, and is formulated without intentionally added processing oil. Typical applications include polymer modification, bitumen modification, oil-extended adhesives and sealants, and flexible compounded materials requiring stable elastic recovery after repeated thermal cycling. The manufacturer’s published datasheet for YH-501T reports typical values within the ranges listed in Table 1; lot-specific certificates of analysis should be consulted for exact current limits.
| Property | Typical datasheet value | Test method |
|---|---|---|
| Styrene mass fraction | 30 ± 2 wt% | Internal H-NMR method |
| Density | 0.91 g/cm³ | ISO 1183-1 |
| Hardness, Shore A, 15 s | 72–78 | ISO 868 |
| Tensile strength at break | ≥ 20.0 MPa | ISO 37 |
| Elongation at break | ≥ 500 % | ISO 37 |
| Melt flow rate, 230 °C, 5 kg | 1.0–5.0 g/10 min | ISO 1133-1:2022 |
| Volatile matter | ≤ 0.70 mass% | ISO 248-2 |
| Ash | ≤ 0.50 mass% | ISO 3451-4 |
Processors compounding YH-501T on production-scale co-rotating twin-screw extruders should treat the upper melt-temperature boundary as the primary processing constraint. Because the hydrogenated midblock is fully saturated but not crosslinked, melt viscosity is governed by chain entanglement density and styrenic domain dissociation rather than by unsaturation-driven vulcanization. On a 40 L/D co-rotating twin-screw extruder with segmented kneading blocks, barrel set points of 170–210 °C are typical. Screw speeds above 350 rpm can raise melt temperature above 230 °C, at which point localized chain scission begins to reduce solution viscosity and tensile strength. Capillary rheometry should be performed at 230 °C over shear rates of 100–1,000 s⁻¹ in accordance with ASTM D3835-16 to establish the actual shear-thinning exponent. Pre-drying at 80 °C for 2–4 h is recommended when ambient relative humidity exceeds 60 %, not because the neat polymer is strongly hygroscopic, but because surface moisture on cold pellets can produce voiding and surface splay during injection molding. The neat grade has a narrow processing window: melt temperature lower than 170 °C yields high melt elasticity and die swell, while temperature above 230 °C initiates degradation. For injection molding, mold temperatures should be held at 20–40 °C to allow rapid re-formation of styrenic glassy domains.
Because YH-501T is a non-functionalized saturated triblock, sulfur- and peroxide-based vulcanization systems intended for unsaturated SBS or EPDM do not produce a stable network density in this material. Formulations requiring covalent crosslinking should use a maleic anhydride-grafted SEBS or a separate reactive compatibilizer. The material is incompatible with strong oxidizing acids, and long-term immersion in aromatic hydrocarbon solvents can plasticize the polystyrene domains, leading to loss of cohesive strength. During extrusion, a downstream oil-injection port should be used for oil-extended compounds; oil added in the feed zone can reduce particle friction and cause barrel slippage, feed instability, and lower dispersive mixing efficiency. Vacuum devolatilization at -0.08 MPa to -0.09 MPa is standard for removing low-volatility oil fractions and preventing porosity in the strand pellet.
In hot-melt pressure-sensitive adhesive compounding, YH-501T is typically extended with hydrogenated paraffinic or naphthenic oils to reduce melt viscosity and shift the loss tangent toward pressure-sensitive response. The choice of tackifier is constrained by the hydrogenated midblock: hydrogenated C5/C9 hydrocarbon resins and stabilized rosin esters are preferred over aromatic or highly polar resins. A representative starting point is 100 parts YH-501T, 50–100 parts naphthenic oil, 80–120 parts hydrogenated tackifier, and 1–3 parts hindered phenolic antioxidant. Melt blending is carried out in a sigma-blade mixer at 160–180 °C or in a continuous extruder with liquid oil injection after the first kneading zone. Adhesive performance is evaluated by loop tack per ASTM D6195-20, 180° peel adhesion per ASTM D3330/D3330M-20, and shear adhesion failure temperature per ASTM D4498-07. Cohesive failure at elevated temperature is a more direct indicator of styrenic domain network retention than room-temperature tack. YH-501T’s 30 wt% styrene content gives a higher shear adhesion failure temperature than grades with styrene content near 20 wt%, while retaining adequate wet-out compared with grades above 40 wt% styrene. The EB midblock glass transition near -50 °C provides low-temperature tack and peel, while the polystyrene domains with a glass transition near 95 °C provide high-temperature shear resistance. Published peel and tack values for this specific YH-501T formulation are limited, so compound validation under the intended application temperature range is required.
Addition of YH-501T to paving-grade bitumen targets simultaneous improvement of rutting resistance at high pavement temperature and crack resistance at sub-zero temperature. The hydrogenated EB midblock provides oxidative and UV ageing stability that is not available from SBS-modified binders, because unsaturated polybutadiene segments in SBS are vulnerable to chain scission during hot mix asphalt production and long-term atmospheric exposure. High-shear rotor-stator mixing at 180–190 °C and 4,000–6,000 rpm is commonly necessary because the solubility of SEBS in bitumen is lower than that of SBS. Without sufficient shear, the polymer phase remains as dispersed particles rather than forming a continuous network. Dosage levels are typically in the range of 3–6 wt% on binder mass, but published data for this specific configuration is limited, and optimal dosage depends on binder source and asphaltene content. Performance is assessed by softening point per ASTM D36/D36M-14, penetration per ASTM D5-20, low-temperature ductility per ASTM D113-17, dynamic shear rheometer per AASHTO T315 or ASTM D7175-15, and bending beam rheometer per AASHTO T313 or ASTM D6648-16.
Compared to SBS-modified binders, SEBS-modified binders exhibit inferior high-temperature storage stability in many bitumen sources because of the absence of residual vinyl unsaturation for sulfur stabilization. The addition of sulfur-based crosslinking agents is less effective for YH-501T and can produce brittle binder morphologies. The density difference between the saturated EB midblock and bitumen can also accelerate phase separation during static storage; rotating-cork storage stability tests at 163 °C for 48 h per ASTM D7173-20 may show larger softening-point differences between top and bottom layers than SBS formulations. This is a known operational boundary rather than a defect of the polymer itself. In applications where storage stability is critical, formulation adjustments are required, such as the use of compatibilizing resins, mineral stabilizers, or substitution of a portion of the bitumen with aromatic-rich flux oil.
YH-501T can be dry-blended with polypropylene or low-density polyethylene for injection-molded and extruded flexible goods. In such blends, the SEBS phase contributes impact resistance and permanently elastic behavior, while the polyolefin phase reduces surface tack and improves chemical resistance. For flame-retardant wire and cable jacketing, the saturated midblock allows high loadings of intumescent or mineral fillers, but tensile retention must be verified after twin-screw compounding because filler dispersion quality is sensitive to the melt viscosity of the SEBS phase. Formulations with polyethylene or polypropylene carriers are typically processed between 180 °C and 220 °C; the SEBS phase should be added to the melt after the polyolefin phase to avoid excessive melt residence time. Electrical insulation and jacketing compounds are evaluated by tensile strength and elongation after ageing per ISO 37 and ISO 188, hot-set testing per IEC 60811-507, and low-temperature bending per IEC 60811-504; these are not intrinsic properties of YH-501T alone but reflect compound design. Regulatory documentation should be verified by lot: RoHS 2011/65/EU Annex II heavy metal limits, REACH Regulation EC No 1907/2006 SVHC declarations, and ISO 10993-5 cytotoxicity data if the compounded article is intended for medical device use. The neat resin is not a medical-grade material unless explicit regulatory approval is stated by the manufacturer for the specific product configuration.
In comparative compounding studies, YH-501T displays lower melt viscosity at 230 °C than high-styrene linear SEBS grades with styrene mass fractions of 40–45 wt%, because the lower polystyrene block length reduces the order-disorder transition temperature and the plateau modulus. This lower processing temperature allows YH-501T to be used in oil-extended systems where high-styrene grades would require excessive heating and risk degradation. Relative to unsaturated SBS, YH-501T shows lower initial melt elastic response and lower adhesion to polar substrates, but it withstands continuous service temperature near 120 °C for short-term exposure and exhibits better ozone resistance under ASTM D1149-18. The absence of maleic anhydride functionality means that YH-501T does not improve notched Izod impact strength in glass-fiber-reinforced polyamide blends unless a separate compatibilizer is used; impact-modified polyamide compounds are typically formulated with maleated SEBS rather than non-functional grades.
| Property or behavior | YH-501T, linear SEBS, 30 wt% styrene | Unsaturated SBS, linear or radial, 30 wt% styrene | High-styrene linear SEBS, 40–45 wt% styrene | Maleic anhydride-grafted SEBS |
|---|---|---|---|---|
| Midblock saturation | Fully hydrogenated | Unsaturated | Fully hydrogenated | Fully hydrogenated with grafted maleic anhydride |
| Thermo-oxidative ageing resistance | Higher than SBS | Lower; requires stabilizers | Higher than SBS | Higher than SBS |
| Hardness and tensile modulus | Moderate | Moderate | Higher | Slightly higher due to polarity |
| Oil extension tolerance | High | Moderate–high | Moderate | Moderate |
| Adhesion to polar substrates | Low–moderate | Low–moderate | Low–moderate | Higher |
| Use in reactive extrusion | Not reactive | Limited by unsaturation | Not reactive | Reactive with polyamides, polyesters, polycarbonates |
The linear architecture of YH-501T produces a lower viscosity at equivalent molecular weight than radial or star-branched SEBS grades, which can be advantageous in low-pressure injection molding and high-speed extrusion but reduces melt strength in blow molding and thick-wall extrusion. The saturated EB midblock does not undergo the shear-induced crystallization observed in some ethylene-containing polyolefins, and therefore YH-501T compounds retain elastic recovery after repeated strain. However, the lack of crystallinity also reduces solvent resistance compared with partially crystalline polyolefin elastomers. These boundaries define the material’s appropriate use: YH-501T is selected when high oil extension, thermal ageing resistance, and low-temperature elasticity outweigh the need for polar adhesion or solvent resistance.