| HS Code | 623092 |
| Productname | SINOPEC Baling Hunan SBS YH-791E |
| Manufacturer | Sinopec Baling Petrochemical |
| Grade | YH-791E |
| Polymertype | Styrene-butadiene-styrene block copolymer (SBS) |
| Structure | Linear |
| Styrenecontent | 30% (typical) |
| Oilcontent | Oil-extended grade |
| Appearance | White to light-yellow pellets |
| Volatilematter | ≤0.70% |
| Ashcontent | ≤0.20% |
| Hardnessshorea | 65–75 (typical) |
| Tensilestrength | ≥15 MPa |
| Elongationatbreak | ≥700% |
| Meltflowrate | 1.0–5.0 g/10 min |
| Density | 0.94–0.96 g/cm3 |
As an accredited SINOPEC Baling Hunan SBS YH-791E factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SINOPEC Baling Hunan SBS YH-791E is supplied in 25 kg woven bags with PE liners, 40 bags per pallet (1,000 kg net). |
| Container Loading (20′ FCL) | 20′ FCL loaded with SINOPEC Baling Hunan SBS YH-791E in 25 kg bags, palletized, wrapped, and secured for ocean shipment. |
| Shipping | SINOPEC Baling Hunan SBS YH-791E is a non-hazardous styrene-butadiene-styrene block copolymer shipped as palletized bags in dry, ventilated containers. Keep packaging intact and protect from moisture, heat, and direct sunlight. Store in a cool, well-ventilated area away from ignition sources. Not regulated for transport under DOT, IMDG, IATA, or ADR. |
| Storage | Store SINOPEC Baling Hunan SBS YH-791E in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and open flames. Keep in tightly sealed original packaging to prevent moisture and contamination. Avoid prolonged UV/high-temperature exposure and excessive stacking. Use good housekeeping and spill control; protect from oils, chemicals, and incompatible materials. |
| Shelf Life | The shelf life of SINOPEC Baling Hunan SBS YH-791E is about 24 months under dry, cool, unopened storage conditions. |
YH-791E is a linear styrene-butadiene-styrene triblock with a nominal styrene mass fraction of 30 wt%. In paving-grade bitumen, the high-temperature grade shift obtainable with YH-791E depends principally on the formation of a continuous polymer-rich network across the bitumen phase. The addition level is set by the base binder penetration grade and the required climatic envelope. For a 70/100 penetration bitumen, YH-791E is milled into the hot binder at 3.0–5.0 wt% of the total binder mass. A rotor-stator homogenizer with a tip speed of 15–25 m/s operates at 175–190 °C for 30–60 min. The polymer-rich phase forms only after the SBS pellets swell, fragment, and disperse. Below 170 °C, residual gel particles remain and separation occurs under static storage. Above 200 °C, thermo-oxidative chain scission reduces the elastic network; apparent viscosity drops, and rutting resistance cannot be recovered by extended digestion.
The low-temperature flexibility limit is not governed by polybutadiene glass transition alone but by the continuity of the swollen SBS phase. When YH-791E is dosed below approximately 3.0 wt%, the blend remains a bitumen-continuous dispersion with limited elastomeric recovery. At 5.0–6.0 wt%, the phase inversion threshold is approached and the softening point rises sharply. Storage stability is checked under EN 13399, with a top-bottom softening point difference not exceeding 5 °C. The Fraass breaking point is measured by EN 12593. Rutting resistance is evaluated by wheel tracking under EN 12697-22. For European paving applications, the polymer-modified bitumen grade must satisfy EN 14023. For the US market, classification follows AASHTO M320, but published data for this specific YH-791E configuration under AASHTO M320 is limited.
Self-adhered SBS-modified bitumen membranes require a manufacturing viscosity window that allows knife-over-roll coating at line speed without compromising the elastomeric network developed during cooling. YH-791E is compounded with oxidized or paving-grade bitumen at 8–12 wt% of the membrane compound. A separate blend incorporates limestone filler at 25–35 wt%, C5 hydrocarbon tackifier at 2–6 wt%, and naphthenic oil at 5–10 wt%. The mixer is a low-shear planetary unit operating at 150–170 °C, and mixing continues until the compound shows a smooth, glossy drawdown with no visible polymer particles. The hot compound is coated onto polyester mat or glass fleece at 0.8–2.0 mm thickness. Release liner is applied in-line before the membrane enters a water-cooled drum. Peel adhesion to concrete is evaluated after 24 h conditioning at 23 °C using ASTM D903. Cold flexibility is screened by EN 1109. Factory production control is governed by EN 13969. Terminal products include torch-free foundation waterproofing membranes, tunnel lining membranes, and below-grade tanking systems. A process constraint arises from the interaction of filler and tackifier: an excess of C5 resin above 6 wt% lowers the cold flex temperature but reduces the softening point below the requirement for vertical surface support in hot service.
| Standard | Test / control purpose |
|---|---|
| EN 13969 | Factory production control for bitumen damp-proofing membranes |
| EN 1109 | Cold flexibility of bitumen sheets |
| ASTM D903 | Peel adhesion of self-adhered membrane to prepared substrate |
For YH-791E-based hot-melt pressure-sensitive adhesives, the dynamic mechanical behaviour between room temperature and shear-induced flow conditions determines coating behaviour. The elastomer is charged at 100 parts by mass. C5 aliphatic tackifier is added at 80–120 parts, naphthenic oil at 40–80 parts, and hindered phenolic antioxidant at 1.0–2.0 parts. The melt is processed in a vertical conical mixer under nitrogen at 160–180 °C. Viscosity is measured at 180 °C by ASTM D3236. The formulation must remain pumpable for slot-die coating on release liner at 20–30 g/m². The coated film is transfer-laminated to BOPP or PET facestock. Tack is measured by PSTC-16, peel by ASTM D3654, and shear adhesion by PSTC-107. Aromatic oil is not used above 20 parts because it plasticizes the polystyrene endblock domains, leading to a loss of shear holding power. Terminal products include label stock, tape, and protective films. For indirect food contact applications, the adhesive must comply with FDA 21 CFR 175.105; within the EU, food-contact status is addressed through Regulation (EC) No 1935/2004 and migration testing. The raw polymer alone does not confer food-contact clearance.
| Component | Function | Parts per hundred rubber |
|---|---|---|
| YH-791E | Styrenic block network | 100.0 |
| C5 aliphatic tackifier | Surface wetting and tack | 80.0–120.0 |
| Naphthenic oil | Viscosity reduction | 40.0–80.0 |
| Hindered phenolic antioxidant | Thermal stabilization | 1.0–2.0 |
Viscosity hysteresis between heating and cooling cycles is an important control parameter. If the measured viscosity at 160 °C on cooling deviates by more than 10% from the heating value, the formulation has undergone progressive block structure breakdown or oil exudation; the batch is rejected for slot-die coating.
When injection-molded unit soles are formulated with YH-791E as the base thermoplastic elastomer, the dominant processing constraint is not melt temperature but the oil distribution between polybutadiene midblock and polystyrene endblocks. The oil-extension step determines compound hardness, abrasion resistance, and flow length in multi-cavity molds. YH-791E pellets are tumble-blended with white oil at 30–50 parts per hundred rubber, styrenic resin at 10–20 phr, calcium carbonate at 5–10 phr, and antioxidant at 0.5–1.0 phr. The cold blend is matured for 8–12 h so the oil migrates into the rubber phase before extrusion compounding. A co-rotating twin-screw extruder with an L/D 48 configuration is operated at 150–180 °C barrel temperature, 170 °C die temperature, and 300 rpm screw speed. The pelletized compound is injection-molded with a clamp force of 80–120 t and a mold temperature of 30–50 °C. Hardness is set to 55–65 Shore A. Tensile strength is tested by ISO 37, tear strength by ISO 34-1, and abrasion resistance by ISO 4649. Terminal products are injection-molded unit soles, sandal soles, and inner sock components. In high-humidity plants above 60% RH, pellet surface condensation can produce gas traps and delamination in thick sections; pre-drying is therefore applied at 60 °C for 2 h when relative humidity exceeds 60%.
Blends of YH-791E with polypropylene develop co-continuous morphologies only after the rubber phase reaches a critical volume fraction; below this fraction the system behaves as a brittle impact-modified thermoplastic rather than a flexible elastomer. The transition is influenced by the viscosity ratio between the SBS and the PP melt, extruder residence time, and dispersed phase breakup under elongational flow. A typical impact-modification range is 5–15 wt% YH-791E in isotactic polypropylene. The blend is processed in a co-rotating twin-screw extruder at 180–220 °C with a screw speed of 250–350 rpm. Injection-molded specimens are subjected to notched Izod impact testing per ISO 180/1A at 23 °C and -20 °C. Tensile yield stress is measured per ISO 527-2. Terminal products include automotive interior trims, appliance housings, and power-tool casings. The limitation is low-temperature ductility: because the polybutadiene midblock has a glass transition near -90 °C, the blend retains flexibility at low temperatures only if the SBS phase maintains sufficient interparticle distance. Electrical/electronic applications require RoHS recast 2011/65/EU and REACH SVHC screening. Published data for the specific YH-791E/PP morphology are limited, so the compounder must perform a design-of-experiments screen across screw configurations and PP melt flow indices before setting a production recipe.
In solvent-borne cold-applied roofing adhesives and mastics, YH-791E is dissolved into aliphatic or aromatic hydrocarbon solvent at 10–15 wt% solids before addition of limestone filler and short glass fiber. The resulting mastic is trowel-applied or cartridge-dispensed for roofing repair and concrete joint sealing. Solvent recovery and VOC regulations under EU Directive 2004/42/CE impose a maximum volatile organic compound content that determines the solvent choice. Published data for this specific YH-791E configuration is limited.
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SINOPEC Baling Hunan SBS YH-791E is a linear styrene-butadiene-styrene thermoplastic elastomer produced by sequential anionic polymerization. The product is supplied as non-oil-extended porous pellets and is used in polymer-modified bitumen, hot-melt pressure-sensitive adhesives, footwear compounds, and impact modification of polyolefins. The grade is identified by a nominal bound styrene content of 30 wt% and a polybutadiene continuous phase; the block structure forms physical crosslinks through polystyrene domains while retaining melt processability. Unlike random styrene-butadiene copolymers, YH-791E exhibits a distinct rubbery plateau between the polybutadiene glass transition and the polystyrene domain softening temperature. The CAS registry number is 9003-55-8, and the material is not oil-extended, allowing the formulator to control plasticizer type and level independently.
Published specification limits for YH-791E include a volatile matter requirement of 0.70% maximum according to ASTM D5668 and an ash content limit of 0.20% maximum under ISO 247-1. Tensile strength is controlled at 18 MPa minimum with elongation at break at 700% minimum when measured on compression-molded sheets according to ISO 37:2017. Hardness is specified at 70 Shore A with a permissible spread of ±5 units under ASTM D2240. Melt mass-flow rate is typically reported in the range of 0.1–1.0 g/10 min at 200°C and 5 kg load using ISO 1133-1:2022. Density is approximately 0.94 g/cm³ when determined according to ISO 1183-1:2019. The producer controls bound styrene at 30 wt% by spectrometric or refractometric methods. Solution viscosity data for this specific grade in toluene is limited; the linear architecture produces lower solution viscosity than star-branched SBS of identical styrene content.
| Property | Test method | Unit | Published requirement |
|---|---|---|---|
| Bound styrene content | ISO 21561 | wt% | 30 |
| Volatile matter | ASTM D5668 | % | ≤0.7 |
| Ash content | ISO 247-1 | % | ≤0.2 |
| Tensile strength | ISO 37:2017 | MPa | ≥18 |
| Elongation at break | ISO 37:2017 | % | ≥700 |
| Hardness | ASTM D2240 | Shore A | 65–75 |
| Melt flow rate | ISO 1133-1:2022 | g/10 min | 0.1–1.0 |
| Density | ISO 1183-1:2019 | g/cm³ | 0.94 |
Thermal processing limits are governed by the polybutadiene midblock rather than by styrene domain degradation. In twin-screw extruders with L/D ratios of 32:1 to 48:1, barrel profiles are typically set from 150°C in the feed zone to 180°C at the die, with melt-temperature alarms at 210°C. Residence time above 200°C should not exceed 20 min; oxidative gel formation begins as a gradual viscosity increase and then produces visible specks in extrudate. Capillary rheometry at 180°C shows shear-thinning behavior; apparent viscosity decreases by approximately 50–60% when apparent shear rate increases from 100 s⁻¹ to 1000 s⁻¹ under ISO 11443. Pre-drying at 60–70°C for 1–2 h in a dehumidified-air hopper dryer is required when pellets have been stored open at relative humidity above 60%. For hot-melt adhesives, mixing at 160–180°C under nitrogen blanket is typical; overheating beyond 190°C accelerates tackifier reaction and color shift. The product should not be processed with strong oxidizing acids or high concentrations of chlorinated solvents. Incompatible additives include certain amine-based curing agents that can react with residual double bonds and produce premature crosslinking.
The polystyrene domains exhibit a glass-transition temperature near 95°C, while the polybutadiene domains show a glass-transition temperature near −80°C when measured by dynamic mechanical analysis at 1 Hz. This architecture provides rubbery response between these transitions. The unsaturated butadiene midblock is sensitive to oxidative attack; the producer incorporates a hindered phenolic antioxidant and a secondary phosphite stabilizer. YH-791E is insoluble in water and polar solvents such as methanol and acetone, but dissolves readily in toluene, cyclohexane, and methyl ethyl ketone at concentrations up to 25 wt% under ambient conditions. Incoming quality-control laboratories typically monitor a 25 wt% solution in toluene at 25°C to detect molecular-weight drift; published data for this specific grade is limited, but linear SBS of this styrene content generally falls within 4,000–8,000 mPa·s under Brookfield viscometry.
Quality assurance on YH-791E uses in-process control of bound styrene, Mooney viscosity, and solution viscosity. Batch-release certificates report tensile strength, elongation, hardness, melt flow rate, volatile matter, and ash. Each lot is pressed into test sheets at 160°C for 10 min before tensile testing. Downstream incoming quality control often includes a 25 wt% toluene solution viscosity measurement to detect molecular-weight drift. Batches with solution viscosity below the lower control limit produce lower tensile strength and lower melt viscosity; batches above the upper control limit can create incomplete dispersion in bitumen and higher extruder torque. In hot-melt adhesive lines, excessively fragmented pellets can cause feed-throat bridging in gravimetric feeders; pellet integrity is therefore controlled by the producer. Moisture content above 0.1% in incoming pellets is a rejection criterion in processes with residence times above 5 min at 180°C, as degradation can occur.
In paving-grade bitumen modification, YH-791E is typically added at 4–6 wt% based on bitumen mass. The mixing sequence uses a high-shear rotor-stator mill at 180–190°C for 60–120 min, followed by low-shear agitation to allow polystyrene domain formation. The resulting polymer network increases the softening point and elastic recovery of the binder. Storage stability is tested according to ASTM D7173 or EN 13399; separation temperature differences below 2.5°C between top and bottom samples are generally acceptable for many paving specifications. The linear structure of YH-791E usually requires less shearing energy than star-branched grades because of lower molecular weight. Field experience on production-scale asphalt blending units shows that inhomogeneous feeding of porous pellets into hot bitumen can create gel particles if local concentration exceeds 10 wt% before shear is applied. Therefore, pellets are added gradually under high shear, and stagnant zones in the tank are avoided. Elastic recovery measured at 25°C under ASTM D6084 typically shows values above 70% for well-digested binders at 5 wt% loading. At 5 wt% loading in a nominal 70/100 penetration-grade bitumen, rotational viscosity at 135°C by ASTM D4402 commonly reaches 1.5–3.0 Pa·s after complete digestion. Rutting factor G*/sin δ at 64°C may increase above 1.0 kPa after modification, measured by ASTM D7175; the failure temperature is often raised by 10–20°C relative to neat bitumen depending on base bitumen source. At polymer contents above 6 wt%, gelation can occur at 160°C, particularly with high-asphaltene bitumens, producing an elastic paste that cannot be pumped easily.
In waterproofing membranes and bitumen sheets, YH-791E is used at 8–12 wt% in combination with fillers and flame-retardant additives. The grade provides low-temperature flexibility measured by cold flexibility tests according to EN 1109; compounds typically achieve a cold bending temperature of −20°C or lower depending on formulation. At these loadings, melt viscosity is influenced strongly by filler surface area; shear mixing under vacuum is required to remove entrapped air. Because the butadiene segmer is unsaturated, heat-aged sheets must be protected with antioxidants. Accelerated aging per ASTM D5721 should show less than 10% change in ring-and-ball softening point for a properly stabilized formulation.
Hot-melt pressure-sensitive adhesive compounds based on YH-791E use tackifier resins, typically C5 aliphatic or hydrogenated rosin ester, and plasticizing oil, typically naphthenic or paraffinic. A starting formulation may contain 100 phr YH-791E, 120 phr tackifier, and 50 phr oil, with 1.0 phr antioxidant. The blend is mixed at 170–180°C until homogeneous; viscosity measured by ASTM D3236 at 180°C after 4 h thermal aging should not increase by more than 20% to ensure pot stability. Because YH-791E is not oil-extended, the formulator controls oil type and content independently; this differs from oil-extended SBS grades where the fixed oil level limits formulation flexibility. Melt viscosity at 180°C is lower than radial SBS types, which permits slot-die coating on standard hot-melt lines without gear-pump pressures above 80 bar. Slot-die lines may operate at 20–100 m/min; coat weights of 18–25 g/m² are common for label stocks. However, the lower molecular weight also reduces high-temperature cohesive strength; creep resistance at 60°C may be lower than star-branched SBS unless the formulation is reinforced with end-block reinforcing resin. Shear adhesion failure temperature measured by ASTM D4498 may range from 55°C to 70°C depending on tackifier softening point and oil level. Loop tack depends on coating weight and substrate; validation is performed according to ASTM D6195 on polyester film. For food-contact adhesive applications, the final adhesive formulation must be evaluated under 21 CFR 175.105 or applicable regional regulations; the raw YH-791E polymer does not carry independent food-contact clearance.
In direct comparison with SINOPEC Baling YH-792, a linear SBS with a nominal bound styrene content of 40 wt%, YH-791E has lower hardness, lower tensile strength, and higher elongation. The higher butadiene content of YH-791E provides greater low-temperature flexibility in modified asphalt and lower modulus in adhesive films. YH-792 is preferred where higher tensile strength and higher service temperature are needed, such as rigid polymer modification and certain footwear sole compounds. Compared with star-branched SBS grades, YH-791E has a narrower molecular-weight distribution and lower melt viscosity; this translates to lower compounding torque on twin-screw extruders and easier mixing into bitumen. On production-scale bitumen units with rotor-stator mixers below 50 kW, YH-791E is often fully dispersed in 60 min, whereas radial grades may require 120 min or more, depending on bitumen source and tip speed. However, star-branched grades generally show higher tensile strength, better elastic recovery at elevated temperature, and greater resistance to permanent set. In adhesive applications requiring low creep at 70°C, YH-791E may require a higher polystyrene end-block resin level; a star-branched grade may meet the same creep specification without modification. Published data for direct comparative creep testing of YH-791E against star grades in identical adhesive formulations is limited; selection should be confirmed on production-scale coating equipment with the intended tackifier package.
Compounding of YH-791E into footwear microcellular sole formulations is carried out in internal mixers or twin-screw lines with EVA or polypropylene. Typical addition levels range from 10–30 phr in compounds where the SBS contributes impact modification and soft-touch properties. In polypropylene impact modification at 5–20 wt%, the notched Izod impact at −30°C is improved relative to unmodified material; testing is conducted according to ISO 180/A on specimens conditioned for 24 h. Melt mixing is performed in twin-screw extruders at 190–220°C with distributive mixing elements to avoid phase coalescence. Compression set of YH-791E compounds measured per ISO 815-1 at 70°C for 24 h is typically below 40% for high-styrene-end-block formulations, but compound-specific validation is required. Published data for the specific YH-791E grade in polypropylene is limited, but the response follows linear SBS impact-modifier behavior. Because the butadiene segment is unsaturated, outdoor exposure requires antioxidants, antiozonants, or carbon black loading above 2 phr.
YH-791E is packaged in 25 kg polyethylene bags, which should be stacked no more than 5 layers to prevent agglomeration. Storage below 40°C and away from direct sunlight is required. Under these conditions, a shelf life of 24 months from date of manufacture is stated by the producer. Opened bags should be reclosed and consumed within 30 days if ambient relative humidity exceeds 70%.