| HS Code | 248474 |
| Product Name | SINOPEC Baling Hunan SBS YH-1401 |
| Manufacturer | SINOPEC Baling Petrochemical |
| Grade | YH-1401 |
| Material Type | Styrene-butadiene-styrene block copolymer (SBS) |
| Structure | Linear |
| Form | Pellets |
| Appearance | White/off-white porous pellets |
| Styrene Content | 30% |
| Butadiene Content | 70% |
| Volatile Matter | ≤0.7% |
| Ash Content | ≤0.2% |
| Tensile Strength | ≥15 MPa |
| Elongation At Break | ≥700% |
| Shore A Hardness | 70-80 |
| Density | 0.94 g/cm3 |
As an accredited SINOPEC Baling Hunan SBS YH-1401 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SINOPEC Baling Hunan SBS YH-1401 is packaged in 25 kg moisture-proof woven bags with inner liners, supplied on standard export pallets. |
| Container Loading (20′ FCL) | SINOPEC Baling Hunan SBS YH-1401 is bagged, palletized, and loaded into a 20-foot FCL container for ocean shipment. |
| Shipping | SINOPEC Baling Hunan SBS YH-1401 is a non-hazardous styrene-butadiene-styrene block copolymer for industrial use, normally shipped in 25 kg bags or jumbo bags, palletized, shrink-wrapped and labeled. No special UN hazard class is assigned. Store dry, ventilated, away from heat and direct sunlight; standard freight transport applies. |
| Storage | Store in a cool, dry, well-ventilated warehouse below 40°C, away from direct sunlight, rain, moisture, and heat sources. Keep in original sealed packaging and avoid contamination by oils, acids, alkalis, or oxidizers. Prevent open flames or sparks. Do not stack excessively high to avoid deformation. Maintain stable conditions and observe shelf-life. |
| Shelf Life | Typically 24 months in unopened original packaging, stored dry, cool, well-ventilated, and away from direct sunlight. |
SINOPEC Baling Hunan SBS YH-1401 enters paving-grade bitumen modification as a linear styrene-butadiene-styrene block copolymer with a nominal styrene content of 40 wt%; in compression-molded sheets, tensile strength values above 18 MPa and elongation at break above 700% are reported on the product datasheet, giving the polymer sufficient cohesive strength to reinforce bitumen without embrittling the matrix. At a polymer addition of 4.5–6.0 wt% based on neat bitumen mass, the polymer-rich phase becomes continuous when dispersed through a rotor-stator high-shear mill in a batch or continuous PMB plant. The bitumen is heated to 175–185 °C, and the polymer is dosed into a tank fitted with an external high-shear mixer operating at 4,000–5,000 rpm and a recirculation loop; mill residence time is held between 45 min and 60 min, after which low-shear agitation at 150–160 °C preserves morphology during storage. Batch-to-batch variance in base bitumen aromatic content alters the time to phase inversion: a shift from 18% to 22% aromatic fraction can reduce the required milling time by approximately 10 min, while high-asphaltene feeds may require a 10–15% increase in polymer loading to reach the same storage stability.
Compliance for this downstream segment is assessed under EN 14023:2010 framework specifications for polymer-modified bitumen, with storage stability measured by EN 13399:2018 separation difference in softening point below 5 °C, and with performance grading under AASHTO M 320-23 targeting PG 76-22 or PG 82-22 depending on the base bitumen and climate. Terminal final products include heavy-duty porous asphalt binder, SMA mixtures, and bridge-deck waterproofing mastics. Operation above 195 °C accelerates thermo-oxidative scission of the butadiene midblock, raises the carbonyl index, and reduces elastic recovery; in-line viscosity spikes above 3,500 mPa·s at 135 °C hot-storage conditions may cause metering pump cavitation, so storage tanks are maintained below 160 °C and under low-shear agitation. Published data for this specific configuration in crosslinked PMB storage beyond 72 h is limited.
The compliance frameworks applied to the downstream routes are compiled in the matrix below.
| Downstream scenario | Mandatory framework / directive | Test or performance standard | Typical acceptance threshold |
|---|---|---|---|
| Paving-grade PMB | EN 14023:2010, AASHTO M 320-23 | EN 13399:2018, EN 1427, AASHTO T 313 | separation difference ≤5 °C |
| Bituminous waterproofing membrane | EN 13707:2013, ASTM D6222/D6222M-16 | DIN EN 1109, DIN EN 1110 | class-dependent cold bending temperature |
| Footwear outsoles | REACH Annex XVII entries 50–52, EN ISO 20344:2021 | ISO 20871:2018, ISO 17707:2005 | per harmonized standard class |
| Solvent-based contact cements | 2010/75/EU Solvent Emissions Directive | ASTM D903-98(2017), ISO 4587:2003 | per end-use bond strength specification |
| PP impact modification | RoHS recast 2011/65/EU, REACH | ASTM D256-23, ISO 180:2023, ISO 1133-1:2022 | per polymer grade datasheet |
| Hot-melt pressure-sensitive adhesives | FDA 21 CFR 175.105, 21 CFR 175.125 | ASTM D3330/D3330M-24, ISO 11339:2022 | per product class |
During membrane production, the polymer is added at 8–12 wt% based on the bitumen fraction before filler introduction. A two-stage mixing system—high-shear dispersion at 170–185 °C followed by low-speed paddle agitation with 25–35 wt% slate or calcium carbonate filler—produces the compound mass for polyester carrier impregnation. The melt is transferred to a continuous calendering line, where tension-controlled polyester mat is passed through a dip tank held at 175–180 °C and then through calendering rolls to set thickness from 3 mm to 5 mm; sand, slate chips, or polyolefin film are applied inline. Foam formation in the dip tank from filler moisture above 0.2 wt% creates pinholes that reduce watertightness in finished membranes.
Membrane products are tested under EN 13707:2013 for reinforced bitumen sheets for roof waterproofing, with cold bending measured by DIN EN 1109 and flow resistance determined by DIN EN 1110; ASTM D6222/D6222M-16 covers SBS-modified bituminous sheet materials in North America. Terminal finished goods are torch-applied and self-adhesive roofing membranes and underlayment for balconies, concrete decks, and low-slope roofs. Filler addition before complete polymer dispersion produces gel specks and poor low-temperature flexibility. Batches held beyond 8 h at 170 °C without nitrogen blanketing show viscosity drift from oxidation, and process temperatures above 190 °C may initiate chain scission that lowers elongation at break of the finished membrane.
The practical processing envelope is defined by the melt viscosity of the compounded TPR. In formulations where YH-1401 is the primary styrenic elastomer at 50–65 phr, a melt blend with general-purpose polystyrene at 20–30 phr, naphthenic oil at 15–25 phr, and calcium carbonate or precipitated silica at 10–20 phr yields a Shore A hardness between 55 and 75, depending on oil loading. Compounding on a co-rotating twin-screw extruder with L/D 32:1 to 44:1 and downstream pelletizing uses a barrel profile of 150–180 °C. Injection molding is performed with melt temperature 165–185 °C, mold surface temperature 20–40 °C, and clamping force in the range 120–180 t for multicavity soles. Mould fill analysis indicates spiral flow length decreases when melt temperature falls below 165 °C, producing weld lines at the midsole junction.
Finished outsole compliance for personal protective equipment follows EN ISO 20344:2021, with abrasion resistance measured under ISO 20871:2018 and flex-crack resistance under ISO 17707:2005. REACH Annex XVII entries 50, 51, and 52 restrict PAHs and phthalates in articles placed on the market. Terminal finished types include safety footwear outsoles, slip-resistant work boots, and casual dual-density sole units. Avoid pre-drying compounded pellets at temperatures above 60 °C for more than 4 h when hygroscopic fillers are present; retained moisture above 0.15 wt% causes surface porosity and reduces adhesion to polyurethane midsole foam. Published data for microcellular foaming of YH-1401-specific TPR is limited, so closed-loop gas-counterpressure tooling evaluations are required before specifying foam sole products.
Reformulation from an oil-extended SBS with lower styrene content to YH-1401 changes the shear-thinning profile of the adhesive and raises the high-shear viscosity at application solids. A formulation with 12–18 wt% YH-1401 on total wet formulation, 25–35 wt% solids, and a C5/C9 hydrogenated or rosin ester tackifier in toluene/ethyl acetate/hexane blends is prepared in a closed dissolver at 35–45 °C for 90–120 min. Coating on doctor-blade or comma-roll lines at 15–25 m/min with 60–80 g/m² dry coat weight, followed by forced-air drying at 50–60 °C, yields open times between 10 min and 25 min before bonding.
Adhesive bond strength is evaluated by ASTM D903-98(2017) peel testing and ISO 4587:2003 lap-shear testing; EU Solvent Emissions Directive 2010/75/EU Annex VII sets emission limits for coating operations. Terminal finished goods include footwear assembly adhesives, automotive trim lamination, and construction contact cements for decorative laminates. Solvent blends containing more than 20% methyl ethyl ketone or heavy aromatic naphtha can promote micelle formation and phase separation during dilution. Addition of low-molecular-weight rosin ester above 40 wt% of tackifier solids may reduce final peel strength and accelerate oxidative embrittlement during long-term ageing.
In polypropylene compounds produced on twin-screw extruders with L/D 40 and side-feed ports for talc or glass fiber, YH-1401 is added at 5–15 wt% based on the total compound to improve notched impact behavior without eliminating the stiffness contribution of the polypropylene matrix. The butadiene-rich midblock absorbs impact energy through cavitation and shear yielding in the PP matrix, but the styrene end-blocks require melt temperatures above 190 °C to remain discrete and prevent co-continuous morphology that would reduce tensile yield stress. Compounding uses a temperature profile from 190 °C at the feed throat to 220 °C at the die, screw speed 300–500 rpm, and specific mechanical energy input between 0.18 kWh/kg and 0.25 kWh/kg; strand pelletizing or underwater pelletizing yields pellets of 3–5 mm. Pelletized YH-1401 with bulk density in the range 0.35–0.45 g/cm³ can cause feed throat bridging in loss-in-weight feeders if not conditioned upstream.
Notched Izod impact is evaluated according to ASTM D256-23 or ISO 180:2023, and melt flow characteristics are controlled under ISO 1133-1:2022. REACH and RoHS recast 2011/65/EU apply to finished E&E, automotive, and appliance components. Terminal finished types include automotive interior trims, appliance housings, and battery-tool casings. Active peroxide masterbatches used for polypropylene visbreaking must be added downstream only after YH-1401 dispersion is complete; simultaneous addition of peroxide and SBS may initiate free-radical attack at the butadiene double bond and reduce impact performance. Barrel temperatures above 230 °C induce butadiene double-bond degradation and generate gel particles in the melt stream.
Batch preparation in jacketed sigma-blade mixers under nitrogen uses YH-1401 at 15–25 wt% of total formulation, with an aromatic-free naphthenic or white oil at 10–20 wt%, and a hydrogenated hydrocarbon tackifier at 45–60 wt%. The mixer is operated at 150–170 °C for 60–90 min until the melt becomes optically clear; temperature above 180 °C triggers viscosity drift and darkening. Coating through slot-die systems at 160–175 °C onto release liner or facestock, followed by silicone liner lamination at 10–50 m/min, produces coated films with coat weights from 18 g/m² to 30 g/m².
For indirect food-contact label and tape applications, formulations are assessed under FDA 21 CFR 175.105 and 21 CFR 175.125. Tape performance is measured by ASTM D3330/D3330M-24 loop tack and peel testing, and ISO 11339:2022 provides flexible-to-flexible peel comparisons. Terminal finished forms include removable labels, industrial tapes, and floor-marking films. Prolonged residence time beyond 120 min at 170 °C without nitrogen blanketing raises carbonyl species and reduces tack. Combination with amine-based stabilizers is avoided because amine groups can interact with ester tackifiers and promote color body formation. Published data for YH-1401 in radiation-cured HMPSA configurations is limited.
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Sinopec Baling Hunan SBS YH-1401 is a linear styrene-butadiene-styrene thermoplastic elastomer manufactured by the Sinopec Baling Petrochemical subsidiary in Hunan, China. The grade is supplied as a white porous pellet or granular solid with a nominal styrene/butadiene mass ratio of 40/60 and a non-oil-extended formulation. It is positioned in the Baling SBS portfolio for bituminous waterproofing, polymer-modified asphalt, high-strength thermoplastic compounds, and solvent-borne adhesives. The property values in this document are representative supplier technical literature data, not a batch release certificate; contract specifications may set narrower release limits.
| Property | Typical value or range | Test method |
|---|---|---|
| Styrene/butadiene mass ratio | 40/60 | Supplier internal method |
| Diblock content | ≤1 wt% | Supplier GPC method |
| Volatile matter | ≤1.0 wt% | ASTM D5668 |
| Ash | ≤0.2 wt% | ISO 247-1 |
| Melt flow rate | 0.3–2.0 g/10 min at 200 °C/5 kg | ISO 1133-1:2022 |
| Tensile strength | ≥24 MPa | ISO 37:2017 |
| Elongation at break | ≥600% | ISO 37:2017 |
| Hardness | 85–90 Shore A | ISO 48-4:2018 / ASTM D2240 |
| Density | 0.93–0.95 g/cm³ | ISO 2781:2018 |
Lot-to-lot variation in the SBS polymerization can shift the diblock content from 0.5 wt% to 1.0 wt%. In asphalt modification, diblock content above 1.0 wt% may reduce elastic recovery because non-coupled butadiene chains do not participate in the styrene-crosslinked network. Production-scale users therefore monitor the grade by gel permeation chromatography and Fourier-transform infrared spectroscopy after incoming receipt.
The 40/60 styrene/butadiene mass ratio produces a two-phase morphology in which the polybutadiene midblock forms a continuous rubber phase and the polystyrene end-blocks segregate into glassy domains. These domains act as physical crosslinks below the polystyrene glass transition near 95 °C; above that threshold the domains soften, allowing thermoplastic flow. The polybutadiene phase contributes low-temperature flexibility with a glass transition near -85 °C, although the unsaturated midblock remains susceptible to oxidation and UV degradation unless stabilised.
The linear architecture and high molecular weight of YH-1401 result in a melt flow rate in the range of 0.3–2.0 g/10 min under 200 °C/5 kg load according to ISO 1133-1:2022. This is lower than standard adhesive-grade SBS materials such as YH-792, which typically shows higher melt flow. In compounding, the material is usually processed on corotating twin-screw extruders with L/D 48 or greater, using a barrel profile from 140 °C in the feed zone to 190 °C at the die. Screw speeds of 250–400 min⁻¹ provide sufficient shear for dispersion; melt temperatures above 200 °C are not recommended because the butadiene block can undergo thermal degradation and gel formation.
The grade has a tensile strength not less than 24 MPa and elongation at break not less than 600% when tested on compression-molded sheets according to ISO 37:2017. Hardness is typically 85–90 Shore A under ISO 48-4:2018 or ASTM D2240. Density at 23 °C is approximately 0.94 g/cm³ under ISO 2781:2018. The low diblock content, usually ≤1 wt%, is significant because higher diblock fractions lower tensile strength and increase cold flow in adhesive and asphalt applications.
Because the material is non-oil-extended, it is shipped as high-hardness crumb or pellets. Cold flow during ambient storage can occur in warehouses above 30 °C; pallet stacking above two high may cause blocking. SBS pellets should be stored below 40 °C and protected from UV exposure. Surface oxidation, visible as yellowing, does not necessarily alter bulk melt viscosity but can affect clarity in light-colored compounds.
At 4–6 wt% addition to paving-grade bitumen, YH-1401 is typically dispersed in a high-shear mixer at 170–180 °C for 40–60 min. Rotor-stator clearances below 0.5 mm are used on production-scale polymer-modified bitumen plants to break the SBS pellets into a fine continuous network. The resulting polymer-modified bitumen is evaluated according to EN 14023:2010, ASTM D36 for softening point, ASTM D6084 for elastic recovery, and ASTM D4402 for Brookfield viscosity at 135 °C. On production-scale PMB units, batch-to-batch variation in SBS pellet size can influence wetting and dispersion rate. Preheating the bitumen to 160 °C before SBS addition and maintaining high-shear recirculation prevents undispersed gel particles that would otherwise appear in fluorescence microscopy as swollen SBS domains larger than 10 µm.
In mill-scale and plant-scale trials, the practical upper dosing limit is normally governed by viscosity increase rather than solubility. At 6 wt% SBS, Brookfield viscosity at 135 °C may exceed 3 Pa·s, requiring heated transfer lines and positive-displacement pumps; at 4 wt% the viscosity remains lower and is more compatible with conventional road paving equipment. Published data for this specific grade in all regional bitumen sources is limited, so the exact viscosity plateau must be confirmed against the project bitumen’s saturate, aromatic, resin, and asphaltene fractions.
The type of bitumen has a large effect on phase stability. In paraffinic or high-wax bitumen, storage stability can be lower because the SBS phase separates during static storage. The tube test under EN 13399 can quantify top-bottom softening point difference. For such systems, the SBS dosage may be reduced to 2–4 wt% and a reactive compatibility agent is added. In naphthenic aromatic bitumen, YH-1401 typically disperses without compatibility agents because the aromatic fraction swells the polystyrene domains and improves network formation.
The high styrene content of 40 wt% contributes to high-temperature softening point and elastic recovery but raises low-temperature flexibility limits compared with 30/70 SBS grades. In cold-climate modified asphalt, formulators may blend YH-1401 with lower-styrene grades or process oils to balance high-temperature rutting resistance with low-temperature cracking resistance under EN 12591 or ASTM D6373 conditions.
When YH-1401 is compounded into solvent-borne contact adhesives and sealants, the high molecular weight produces high solution viscosity at moderate solids. For a 20 wt% solids solution in toluene, Brookfield viscosity can reach several Pa·s, which restricts spray application and favours brush or roller coating. Reducing solids to 15 wt% or blending with YH-792 is common when lower-viscosity spray systems are required.
For solvent-based adhesives, the polymer is allowed to dissolve under low-shear agitation at 20–25 °C for 4–8 h to avoid excessive chain breakdown. High-speed dispersers can generate enough heat to raise solution temperature above 40 °C, which accelerates oxidation; nitrogen blanketing or antioxidant addition is used in large tanks.
Compatible tackifier systems include C5 aliphatic resins, C9 aromatic resins, and rosin esters. Aromatic process oils above 30 phr should be avoided because they preferentially swell the polystyrene domains and reduce cohesive strength. Naphthenic or paraffinic oils at 5–20 phr are used for viscosity adjustment with less loss of tensile properties. Reference adhesion values are tested according to ASTM D903 or ISO 4587 on bonded substrates; peel strength depends on substrate surface energy, coat weight, and open time.
Pre-drying of pellets at 60–80 °C for 1–2 h with desiccant-dried air is recommended when storage relative humidity exceeds 60%. The grade is hydrophobic, but surface moisture can create steam bubbles during melt compounding. Avoid melt temperatures above 200 °C and avoid strong oxidizing agents; the unsaturated polybutadiene block can degrade by chain scission and crosslinking under prolonged high-shear and high-temperature conditions.
In polypropylene and polystyrene compounds, YH-1401 is incorporated at 10–30 wt% to improve impact toughness and reduce brittle failure. The trade-off is a reduction in flexural modulus and heat deflection temperature. On a corotating twin-screw extruder, the material is typically fed in the main throat with the polyolefin, while oil or lubricants are injected downstream. Impact results are evaluated under ISO 180 or ASTM D256; flexural modulus under ISO 178 or ASTM D790.
In impact modification, the SBS rubber particle size and distribution depend on screw configuration. A kneading block section with 30–45° forward angles is used to disperse the SBS into a continuous polypropylene matrix. Too high specific mechanical energy input above 0.25 kWh/kg can degrade the polybutadiene block and reduce Charpy notch impact strength. Processors usually calibrate screw speed and throughput to maintain melt temperature below 190 °C at the die plate.
In footwear compounds, YH-1401 acts as a high-strength modifier for rubber-resin blends. It is blended with polystyrene, hydrocarbon resin, and oil at 140–170 °C in internal mixers or extruders. The non-oil-extended nature of YH-1401 requires the formulator to control oil level separately; oil uptake is lower than oil-extended grades, so the final hardness can be adjusted over a wider range. Slip resistance and abrasion are measured according to ASTM D5963 or ISO 4649.
The grade is produced under an ISO 9001 quality system. For final articles intended for food-contact use, converters must verify that the specific compound meets FDA 21 CFR 177.1810, which covers styrene block polymers used in repeated-use rubber articles. REACH and RoHS compliance statements are typically provided by the supplier on a per-shipment basis. EN 71-3 migration of certain elements applies only to finished toy formulations, not to the neat SBS granulate.
The primary distinction between YH-1401 and lower-styrene linear grades such as YH-791 is the styrene/butadiene mass ratio. YH-791 is typically supplied at 30/70 and has lower tensile strength and Shore hardness, which makes it softer and more rubbery but less resistant to high-temperature deformation. YH-1401, at 40/60, exhibits higher tensile strength, higher modulus, and higher hardness, although it sacrifices some low-temperature elasticity. Both are linear, but YH-1401 is positioned for applications requiring higher mechanical integrity.
Compared with YH-792, which also has a 40/60 styrene/butadiene ratio but a lower molecular weight, YH-1401 has lower melt flow and higher solution viscosity. In adhesive and footwear applications where fast wetting and low melt viscosity are required, YH-792 is often preferred. In bituminous systems where high molecular weight improves high-temperature elastic recovery and storage stability, YH-1401 is selected. The exact molecular weight cut is not disclosed on the public datasheet, but the melt flow difference is measurable under ISO 1133-1:2022.
Against star-branched SBS grades such as YH-802, the linear YH-1401 generally shows lower melt elasticity and lower coupling efficiency but more predictable thermoplastic flow. Star-branched structures can provide higher tensile strength at equal molecular weight, though they may require higher processing temperatures. The choice between YH-1401 and a star-branched grade depends on whether the downstream process is elongation-dominated or shear-dominated; in extrusion and bitumen dispersion, the linear grade is often easier to handle at moderate shear, while star grades may be chosen for high melt strength and improved cohesive strength.