Products

SINOPEC Baling SEPS YH-4052

    • Product Name: SINOPEC Baling SEPS YH-4052
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 512258
    Product Name SINOPEC Baling SEPS YH-4052
    Chemical Type Styrene-ethylene-propylene-styrene block copolymer (SEPS)
    Hydrogenation Hydrogenated
    Appearance White powder
    Styrene Content 30%
    Density 0.90 g/cm3
    Melt Flow Rate 5.0 g/10 min
    Shore A Hardness 60
    Tensile Strength ≥18 MPa
    Elongation At Break ≥600%
    Volatile Matter ≤0.5%
    Ash Content ≤0.1%
    Solubility Soluble in toluene and cyclohexane

    As an accredited SINOPEC Baling SEPS YH-4052 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SINOPEC Baling SEPS YH-4052 is supplied in 25 kg bags, typically packed as 1,000 kg per pallet.
    Container Loading (20′ FCL) SINOPEC Baling SEPS YH-4052 loaded in a 20′ FCL container, palletized in sealed bags, dry and ventilated, away from heat and moisture.
    Shipping SINOPEC Baling SEPS YH-4052 is a non-hazardous thermoplastic elastomer supplied in 25 kg bags, palletized and shrink-wrapped. Transport as general cargo in a dry, ventilated container; protect from moisture, heat and direct sunlight. No UN/class required.
    Storage Store SINOPEC Baling SEPS YH-4052 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat sources, and moisture. Keep original packaging sealed and palletized off the floor to prevent contamination and water absorption. Avoid contact with strong oxidizers and keep away from open flames. Maintain stable temperature; use stock rotation and observe supplier shelf-life recommendations.
    Shelf Life Typically 24 months in original unopened packaging, stored cool, dry, ventilated, away from sunlight and moisture.
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    Certification & Compliance
    More Introduction

    Designated as a linear hydrogenated styrenic block copolymer, SINOPEC Baling SEPS YH-4052 is produced by anionic polymerization of styrene and a diene midblock followed by selective hydrogenation to form a saturated ethylene/propylene rubber segment. The molecular architecture consists of polystyrene end-blocks and a saturated ethylene/propylene midblock; at service temperature the polystyrene domains act as physical cross-links, while the midblock provides elastic recovery, low-temperature flexibility, and resistance to oxidative chain scission. The grade is supplied as dense pellets for thermoplastic melt processing and does not require sulfur or peroxide vulcanization. Typical downstream uses include adhesive and sealant bases, overmolding compounds for polypropylene, clear consumer articles, impact modification of polyolefins, and wire-and-cable jackets where retention of color and mechanical properties after thermal aging is specified. In comparison with unhydrogenated styrenic block copolymers, the saturated midblock narrows the range of analytical methods needed to detect residual diene unsaturation.

    What Distinguishes YH-4052 from Unhydrogenated SIS and from SEBS in Thermoplastic Elastomer Compounds?

    Compared with unhydrogenated styrene-isoprene-styrene copolymers, YH-4052 eliminates most midblock double bonds through selective hydrogenation. This raises the onset of oxidative degradation and reduces yellowing under ultraviolet and thermal exposure; retention of tensile properties is commonly evaluated by ASTM D638 after hot-air aging at 70 °C, and surface color change is measured on compression-molded plaques. Compared with styrene-ethylene/butylene-styrene grades of similar bound styrene content, the ethylene/propylene midblock of YH-4052 exhibits lower crystallinity and higher chain mobility, yielding softer compounds and better low-temperature recovery at equivalent oil loadings. The reduced midblock crystallinity also lowers melt-energy input during compounding with polypropylene. When compared with EPDM, YH-4052 requires no vulcanization, permits regrind reuse, and can be processed on standard thermoplastic equipment; however, crosslinked EPDM may retain superior resistance to certain hot polar fluids and sustained compression set after long-term stress relaxation.

    Table 1. Qualitative comparison of YH-4052 SEPS with conventional elastomer classes.
    CharacteristicYH-4052 SEPSSISSEBSEPDM
    Midblock saturationSaturatedUnsaturatedSaturatedSaturated backbone
    Thermoplastic processabilityYesYesYesNo
    UV/oxidative resistanceHighLowHighHigh
    Low-temperature flexibilityHighHighModerate to highHigh
    Vulcanization requiredNoNoNoYes
    Soft-touch overmolding on PPYesLimited by color stabilityYesRequires adhesive

    For incoming inspection and formulation development, YH-4052 is characterized by bound styrene content, melt mass-flow rate, Shore A hardness, tensile strength at break, elongation at break, specific gravity, volatile matter, and ash. Because Baling Petrochemical may report properties under different national or internal methods, direct substitution into a production formula should be based on a current certificate of analysis rather than on a single published figure. The values in Table 2 consolidate representative published data for the SEPS product family and are not intended as independent lot acceptance limits.

    Table 2. Published representative values for SINOPEC Baling SEPS YH-4052; current lot data from certificate of analysis takes precedence.
    PropertyTest methodRepresentative value
    Bound styrene contentSupplier internal method28–33 wt%
    HardnessASTM D2240 / ISO 7619-160–70 Shore A
    Tensile strength at breakASTM D638 / ISO 3716–22 MPa
    Elongation at breakASTM D638 / ISO 37400–600%
    Melt mass-flow rateISO 1133-1:2022, 230 °C/2.16 kg2–6 g/10 min
    Specific gravityISO 1183-10.90–0.93
    Volatile matterSupplier method≤0.5 wt%
    AshSupplier method≤0.1 wt%

    Property response to plasticizer loading in YH-4052 compounds is nonlinear and must be mapped before mass production. At oil loadings below 30 phr, tensile strength decreases gradually while elongation increases; above 70 phr, oil exudation and loss of tensile recovery become measurable unless a high-molecular-weight SEPS grade or a polypropylene modifier is present. Hardness can be adjusted from approximately 30 Shore A to 65 Shore A by varying paraffinic oil and polypropylene content. The transition from a tacky sealant to a dry-feel overmolding compound occurs near 50 phr paraffinic oil and is best defined by torque rheometry on the production mixer. Published data for this specific formulation gradient using YH-4052 is limited; pilot runs are required to fix the oil type, tackifier softening point, and screw speed.

    Compounding of YH-4052 on an intermeshing co-rotating twin-screw extruder with an L/D ratio of 32:1 to 48:1 is carried out at melt temperatures of 170 °C to 210 °C. The styrenic end-blocks soften sufficiently in this range to allow dispersion of paraffinic extender oil and hydrocarbon tackifier; oil addition above 20 phr is typically split between barrel side ports to prevent screw slip and phase inversion. At barrel temperatures above 230 °C, polystyrene domain reformation becomes slower and the risk of midblock oxidative degradation increases, particularly at residence times beyond 5 min. Pre-drying at 60 °C to 80 °C for 2 h is applied when storage relative humidity exceeds 60%, because surface moisture can create surface defects and reduce molecular-weight retention in hot-melt mixing. Batch-to-batch variation in melt mass-flow rate should be monitored by ISO 1133-1:2022 to adjust oil loading and torque limits.

    Rheological Boundaries for Injection Molding and Extrusion Without Crosslinking Agents

    Injection molding of YH-4052-based compounds uses barrel profiles between 160 °C and 200 °C, with mold temperatures of 20 °C to 40 °C to freeze polystyrene domain morphology and permit demolding of soft-touch surfaces. Holding pressure and injection speed are set to avoid high shear heating at gates smaller than 1 mm; shear rates above 104 s−1 are not recommended for unfilled formulations because adiabatic temperature rise can approach 20 °C to 30 °C and alter viscosity. Extrusion compounds containing YH-4052 can be processed on single-screw extruders with a compression ratio of 2.5:1 to 3.5:1; a breaker plate and screen pack with 60 mesh is used to remove agglomerated additive particles. Because the material is thermoplastic, reprocessed scrap can be blended at up to 30 wt% in noncritical applications, provided that the scrap is dry and free of PVC or acetal contamination. Mold shrinkage is generally lower than that of highly plasticized PVC and is measured by ISO 294-4 on test plaques.

    In hot-melt adhesive and sealant compounding, YH-4052 is combined with fully hydrogenated hydrocarbon tackifiers and paraffinic or naphthenic process oils in heated sigma-blade mixers at 170 °C to 190 °C. Rosin ester tackifiers may be used only after pilot testing because partial incompatibility can raise room-temperature peel adhesion but reduce elevated-temperature shear resistance; ASTM D3654 shear adhesion failure temperature and ASTM D4498 heat-fail temperature are used to compare formulations. Softening point of the final adhesive is controlled primarily by tackifier level, while viscosity is adjusted with oil. Because the saturated midblock resists oxidative color shift, the grade is used in high-clarity pressure-sensitive adhesives and low-odor sealants. Peel adhesion is compared by ASTM D3330, loop tack by ASTM D6195, and melt viscosity by rotational rheometry at 180 °C; published data for specific open-time ranges for YH-4052 are limited and should be generated on the target coating line.

    Medical and consumer overmolding compounds based on YH-4052 are processed onto polypropylene substrates with mold temperatures of 25 °C to 35 °C to promote melt bonding without substrate distortion. Adhesion to polypropylene is influenced by interdiffusion of the ethylene/propylene midblock and the substrate, and by cooling rate at the interface. Peel strength is commonly tested by ASTM D6862 for T-peel or ASTM D903 for adhesive strength; the method is selected according to part geometry. Articles requiring sterilization by ethylene oxide or gamma irradiation may shift hardness and color; validation must include post-sterilization tensile and color measurement to define allowable dose ranges. Regulatory conformity statements for medical use must be obtained from Baling and from the compounder, because the raw pellet grade does not independently carry a universal medical certificate. In food-contact applications, FDA 21 CFR 177.1810 or 177.2600 may apply to finished articles, but section applicability is product-specific and requires migration testing under the intended conditions of use.

    When YH-4052 Is Used as a Polyolefin Modifier in High-Clarity Blends

    Addition of 5 wt% to 20 wt% YH-4052 to polypropylene random copolymer reduces low-temperature brittleness and improves impact strength while retaining clarity because the saturated midblock does not introduce large dark particles. Optical property development depends on the refractive index difference between the SEPS domains and the polypropylene continuous phase; haze is measured by ASTM D1003, and notched impact strength by ASTM D256 or ISO 179-1. At loadings above 25 wt%, tensile modulus declines and the continuous phase may become co-continuous, leading to a transition from impact modification to thermoplastic elastomer behavior. Processing is performed on the same twin-screw equipment used for polypropylene, with temperature profiles adjusted to 190 °C to 210 °C and screw speeds selected to deliver specific energy input of 0.15 kWh/kg to 0.30 kWh/kg. Published data for this specific configuration is limited, so pilot-scale compounding is necessary before commercial specification.

    Wire-and-cable jackets based on YH-4052 require addition of flame-retardant systems such as magnesium hydroxide or aluminum trihydrate; these fillers reduce tensile strength and require silane coupling agents to maintain elongation above 300%. Volume resistivity is measured by ASTM D257, and insulation integrity after thermal aging is assessed by IEC 60811 procedures. The saturated midblock improves heat-shock resistance compared with SBS, but highly filled compounds may require a co-additive such as low-density polyethylene to maintain surface finish at line speeds above 100 m/min. Smoke density and acid-gas generation are application-specific and must be tested on the finished jacket rather than on the neat SEPS pellet.

    Molecular-weight characterization of YH-4052 is performed by gel permeation chromatography using tetrahydrofuran or trichlorobenzene as solvent; the saturated midblock requires solvent selection that dissolves both styrenic and rubber phases. Differential scanning calorimetry by ASTM D3418 is used to verify the rubber-phase glass transition; the styrenic end-block transition is less pronounced but may be detected at approximately 80 °C to 100 °C. The narrow molecular-weight distribution contributes to consistent melt flow, low die swell in profile extrusion, and stable viscosity during hot-melt aging. Neat YH-4052 pellets contain a storage antioxidant package that is not a substitute for compounded stabilizers in finished articles.

    The operating envelope of YH-4052 tightens when parts are exposed to aromatic solvents, chlorinated hydrocarbons, low-molecular-weight ketones, or strong oxidizing acids, because these agents swell or solvate the styrenic domains and reduce tensile strength. Continuous outdoor use without UV stabilizer is not recommended despite the saturated midblock; surface discoloration and microcracking of styrenic domains may still occur, so formulations should include a hindered phenolic antioxidant and a phosphite processing stabilizer. Avoid melt blending with polyvinyl chloride or polyacetal; degradation by-products from these polymers can attack the hydrogenated midblock and cause odor. Avoid coformulation with strong pro-oxidant metal ions such as copper or iron, which accelerate thermo-oxidative degradation. Storage should be in sealed containers below 40 °C and away from direct sunlight, with inventory rotation by production date because long-term storage may compact pellets and increase surface oxidation.

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