| HS Code | 502432 |
| Polymer Type | Styrene-butadiene-styrene block copolymer (SBS) |
| Molecular Structure | Linear triblock |
| Bound Styrene Content | 30 wt% |
| Butadiene Content | 70 wt% |
| Density | 0.94 g/cm³ |
| Melt Flow Rate | 3.5 g/10 min (190 °C/2.16 kg) |
| Volatile Matter | ≤0.5 wt% |
| Ash Content | ≤0.2 wt% |
| Shore A Hardness | 75 |
| Tensile Strength | ≥25 MPa |
| Elongation At Break | ≥700% |
| Modulus At 300 Percent Elongation | ≥2.0 MPa |
| Solution Viscosity | 1200 mPa·s (25 wt% in toluene, 25 °C) |
As an accredited LCY Chemical Huizhou Globalprene® SBS 3411 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LCY Globalprene® SBS 3411 is typically supplied in 25 kg paper bags, 40 bags per pallet, totaling 1,000 kg net. |
| Container Loading (20′ FCL) | 20′ FCL loading of LCY Chemical Huizhou Globalprene® SBS 3411: bagged thermoplastic elastomer, palletized and securely stowed for ocean shipment. |
| Shipping | LCY Chemical Huizhou Globalprene® SBS 3411 is typically shipped as non-hazardous styrene-butadiene-styrene block copolymer crumb/pellets in 25 kg bags or jumbo bags, palletized in dry containers. Protect from moisture, heat, direct sunlight, and ignition sources during storage and transport. |
| Storage | Store LCY Chemical Huizhou Globalprene® SBS 3411 in a cool, dry, well-ventilated warehouse. Keep bags/containers closed, off the floor, and protect from moisture, direct sunlight, heat, sparks, and open flames. Avoid prolonged high temperatures and UV exposure. Keep away from oxidizers and incompatible chemicals. Use first-in/first-out rotation; avoid excessive stacking or packaging damage. Follow local regulations and the SDS. |
| Shelf Life | Typically 24 months when stored dry, cool, ventilated, away from direct sunlight and heat in original packaging. |
Injection-grade styrenic TPR compounds for fashion footwear outsoles and midsoles are frequently based on LCY Chemical Huizhou Globalprene® SBS 3411 as the elastomeric block. The polymer is pre-blended in a high-speed mixer at 500–800 rpm for 2–4 min with general-purpose polystyrene, naphthenic or paraffinic processing oil, calcium carbonate, and a phenolic antioxidant before melt compounding. SBS 3411 addition levels in injection-molded sole compounds normally occupy 25–45 phr, while polystyrene is held at 10–20 phr to increase modulus and melt flow, processing oil at 20–40 phr is selected by aniline point to avoid excessive polystyrene-domain softening, and calcium carbonate at 5–15 phr provides dimensional stability. Compounding is performed on co-rotating twin-screw extruders with L/D 40:1–48:1, segmented conveying and dispersive mixing elements, oil injection downstream at barrel 6 of 10, and strand or underwater pelletizing. Melt temperature at the die is kept at 150–170°C; residence above 190°C for more than 3–5 min produces gel specks and reduces trouser tear strength measured by ASTM D624. Production-scale experience indicates that early oil injection into the feed throat causes screw slippage and batch-to-batch Shore A variation of ±3 points, while calcium carbonate above 15 phr raises DIN 53516 abrasion loss above 250 mm³. Finished outsoles and midsoles are injection-molded at barrel set points of 150–180°C, mold temperature of 25–40°C, and clamping force from 150–250 t depending on cavity count; gate freeze is completed before cavity pressure drops below 10 MPa. Finished compound Shore A values typically range from 55–75 depending on oil and polystyrene ratio, with tensile strength of 5–12 MPa and elongation at break of 500–800% under ASTM D412-16. The terminal product types are fashion outsole units, unit soles, and midsoles for casual and children’s footwear. Compliance assessments for these components reference ASTM D412-16 for tensile properties, ASTM D2240-15e1 for hardness, ISO 4649 and DIN 53516 for abrasion, ASTM D624 for tear, REACH Regulation (EC) No 1907/2006 Annex XVII entry 50 for PAH restrictions, and RoHS 2011/65/EU where electrical or electronic accessories are involved.
In polymer-modified bitumen production for road paving, LCY Chemical Huizhou Globalprene® SBS 3411 is metered into hot asphalt at 3.0–7.0 wt% of binder weight, with sulfur or sulfur-donor crosslinking agents at 0.05–0.15 wt% to develop a storage-stable elastomeric network. The production line comprises a hot bitumen feed tank, a rotor-stator high-shear mill of 50–75 hp for 10–15 t batches, and agitated maturation tanks. Milling is conducted at 170–190°C for 30–60 min, followed by maturation at 150–170°C under low-shear agitation for 2–4 h. High-shear mill rotor tip speed is maintained above 20 m/s to achieve phase inversion; below this threshold the SBS phase remains dispersed and elastic recovery stays below 65%. If sulfur dose exceeds 0.15 wt%, the binder can gel and become unsuitable for spraying and pumping. The critical field failure mode is high-temperature storage separation in vertical tanks, detected by a ΔR&B value greater than 2.5°C after 72 h at 160°C. This condition usually points to incompatible maltene fractions, insufficient milling time, or poor crosslinker distribution. The finished PMB binder is tested under EN 14023:2010, ASTM D5976, EN 1426 for penetration, EN 1427 for softening point, and EN 13398 for elastic recovery. Terminal products include PMB binders for dense-graded asphalt concrete, stone mastic asphalt, and porous friction course mixtures.
Representative production trends for SBS 3411 in a 160/220 penetration-grade base bitumen are summarized below. These values are recorded ranges from PMB plant trials and are not supplier batch specifications.
| SBS 3411 addition (wt%) | Softening point via EN 1427 (°C) | Penetration at 25°C via EN 1426 (dmm) | Elastic recovery at 25°C via EN 13398 (%) | Storage stability ΔR&B after 72 h (°C) |
|---|---|---|---|---|
| 3.0–4.5 | 52–68 | 45–65 | 65–80 | ≤2.5 |
| 4.5–6.0 | 68–82 | 35–50 | 80–90 | 2.0–3.5 |
| 6.0–7.5 | 82–96 | 25–40 | 88–95 | 3.0–5.0 |
Pressure-sensitive hot-melt adhesive formulations for polypropylene carton sealing tapes and high-speed label applications often use LCY Chemical Huizhou Globalprene® SBS 3411 at 12–25 wt% as the styrenic block copolymer backbone, combined with C5 or partially hydrogenated C9 tackifier resins at 40–55 wt%, naphthenic or paraffinic white oil at 20–35 wt%, and an antioxidant/stabilizer package at 0.3–1.0 wt%. High-viscosity mixing is conducted in heated sigma-blade kneaders or continuous twin-screw compounders at 150–170°C under nitrogen blanketing, followed by melt filtration and slot-die coating. On 1.2 m-wide coating lines, viscosity drift greater than ±15% over an 8-hour shift typically indicates midblock oxidation, with gel particles accumulating at the die lip. Operating above 175°C with high free-oil content shortens pot life and reduces peel adhesion on corrugated board; coating weight for carton sealing tapes is usually 18–25 g/m². The downstream terminal products are carton sealing tapes, label stock, disposable hygiene assembly adhesives, and window profile masking tapes. Compliance for finished adhesives includes FDA 21 CFR 175.105 for indirect food contact, REACH Regulation (EC) No 1907/2006, and performance testing under PSTC-6 for peel adhesion, PSTC-7 for shear adhesion failure temperature, and ASTM D4498 for hot shear flow.
For torch-applied SBS-modified bituminous membranes, LCY Chemical Huizhou Globalprene® SBS 3411 is incorporated at 10–16 wt% of the coating compound, with mineral filler at 25–35 wt% and the balance comprising oxidized bitumen or bitumen fluxant. Production uses high-shear mixers at 180–200°C until the SBS network swells into a continuous elastic phase; the compound is then calendered onto polyester or glass-fleece carriers at 120–160 m/min depending on coating weight. Critical operational boundaries include viscosity rise from midblock swelling and filler networking; when coating weight exceeds 5 kg/m², calender line speed is reduced to prevent transverse thickness variation. Recirculated compound held at 200°C for more than 6 h without inert gas blanketing develops gel from oxidative coupling, which appears as surface pinholes in the finished membrane. The terminal products are torch-applied roofing membranes for low-slope roofs, foundation waterproofing sheets, and underlayment membranes for mechanically fastened roof systems. Compliance testing is referenced to EN 13707 and EN 13969 for reinforced bitumen sheets, ASTM D6164 or ASTM D6163 depending on carrier type, and EN 13501-5 for fire classification of exposed roofing assemblies.
General-purpose polystyrene compounds for extruded packaging sheet and injection-molded cosmetic cases are modified with LCY Chemical Huizhou Globalprene® SBS 3411 at 5–20 wt% to increase impact strength and reduce melt fracture during deep-draw thermoforming. Compounding blends SBS 3411 with polystyrene in a co-rotating twin-screw extruder with L/D 36:1–44:1, barrel profile 170–200°C, and vacuum devolatilization at -0.08 MPa to remove residual moisture and low-molecular-weight volatiles. At addition levels above 20 wt%, the compound’s Vicat softening temperature measured by ISO 306 can fall below the threshold required for hot-fill or high-service-temperature applications; below 5 wt%, impact modification is generally insufficient for thin-wall snap-fit closures. Production-scale data indicate that screw speeds above 450 rpm raise melt temperature by 8–15°C and may produce gel specks in transparent grades. Published data for this specific configuration is limited, so plant-scale design-of-experiments on the actual screw profile is recommended before specifying a fixed formulation. Terminal products include extruded packaging sheet, disposable cutlery, and cosmetic component housings. Compliance testing is governed by ISO 1133-1:2022 for melt flow rate, ASTM D638-14 for tensile properties, ISO 180 for notched Izod impact, and REACH Regulation (EC) No 1907/2006.
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LCY Chemical Huizhou Globalprene® SBS 3411 is a linear styrene-butadiene-styrene triblock copolymer supplied as a porous pellet. In this architecture, polystyrene end-blocks associate into glassy physical crosslink domains at service temperature, while the unsaturated polybutadiene midblock provides elastic recovery and low-temperature flexibility. The grade is produced by anionic solution polymerization and is positioned in the non-oil-extended segment of the LCY Globalprene SBS portfolio. A styrene content in the 31 wt% class yields a balance between cohesive strength and cold-flow resistance for adhesives, bitumen modification, footwear compounding, and impact-modification workflows. Because the midblock retains carbon-carbon unsaturation, the polymer participates in oxidative and free-radical reactions more readily than hydrogenated SEBS grades; antioxidant and process stabilizer selection therefore forms part of every downstream formulation.
Lot-release documentation for linear SBS grades is generally organized around bound styrene content, rheology, mechanical properties of a standard laboratory sheet, and volatiles. Supplier certificates of analysis for 3411 list values obtained under specified sample preparation. The following property envelope is representative of a 31 wt% styrene linear SBS and should not be read as a guaranteed specification unless codified in a supply contract.
| Property | Test method | Typical range or value |
|---|---|---|
| Bound styrene content | ISO 21561 or equivalent FTIR | 30–32 wt% |
| Specific gravity | ISO 1183-1 / ASTM D792 | 0.94 g/cm³ |
| Tensile strength at break | ASTM D412 Die C, 500 mm/min | ≥18.0 MPa |
| Elongation at break | ASTM D412 | ≥700% |
| 300% modulus | ASTM D412 | 2.0–2.5 MPa |
| Hardness | ASTM D2240, 15 s delay | 78–82 Shore A |
| Melt flow rate | ISO 1133-1, 190°C/5.0 kg | 1.0–3.0 g/10 min |
| Solution viscosity | Rotational viscometer, 25 wt% in toluene, 25°C | 2,000–4,000 mPa·s |
| Ash content | ISO 247 | ≤0.5 wt% |
| Volatile matter | ASTM D5663 | ≤0.5 wt% |
The tensile and hardness values are obtained on compression-molded sheets prepared at 150–160°C to remove thermal history. Melt flow rate is not an intrinsic viscosity; it is a single shear-stress extrusion value and does not provide full shear-thinning behavior. Formulators requiring process-relevant viscosity should measure capillary rheometry from 100 s⁻¹ to 10,000 s⁻¹ at 180–200°C in a twin-bore rheometer instead of relying on melt flow rate alone.
Bitumen modification with 3411 is conducted by dispersing 2–6 wt% polymer into a heated bitumen phase at 170–185°C under a rotor-stator mixer, for example a Silverson LSM or equivalent, operating at 3,000–5,000 rpm for 30–60 min. The polybutadiene midblock swells in maltenes while the polystyrene end-blocks remain associated, producing a continuous polymer-rich network when concentration crosses the percolation threshold. Blends are commonly evaluated by ASTM D36 softening point, ASTM D5 penetration, ASTM D4402 dynamic viscosity at 135°C, and ASTM D6084 elastic recovery. Storage stability is assessed by cigar-tube sampling after 48 h at 163°C; phase separation can occur if the aromatic content of the base bitumen is insufficient to solvate the polystyrene domains. Processing above 200°C or with prolonged air injection accelerates oxidative degradation of the unsaturated midblock. Published data for this specific configuration is limited for polymer-modified asphalt formulations containing high reclaimed asphalt pavement content.
Solution adhesives based on 3411 are prepared at 20–40 wt% solids in aromatic, aliphatic, or mixed hydrocarbon solvents; toluene, cyclohexane, and methyl ethyl ketone are common. Brookfield viscosity at 25°C is formulation-dependent but follows the polymer solution viscosity listed above. Tackifier resins such as C5/C9 hydrocarbon resins and rosin esters are added at 50–150 phr relative to polymer to shift glass transition and wetting behavior. The polymer contributes cohesive strength from its polystyrene network; peel and shear are evaluated by ASTM D6195 loop tack, ASTM D3330 180° peel, and ASTM D3654 static shear. Hot-melt formulations are processed in turbine mixers or twin-screw compounders at 160–180°C under nitrogen or in a vacuum vessel; residence times above 2 h at melt temperature are not recommended due to thermal-oxidative degradation and viscosity shift. If porous pellets have been stored at relative humidity above 60%, pre-drying at 60–65°C for 2–3 h in a desiccant dryer is required before melt processing to prevent bubble defects.
At addition levels of 5–20 wt% in general-purpose polystyrene, 3411 disperses as rubbery domains whose particle size depends on interfacial tension and shear history. Co-rotating twin-screw extruders with L/D 32–40 are typically used, with barrel temperatures from 150°C near the feed throat to 200°C at the die, screw speed 200–350 rpm, and melt temperature held below 210°C to limit degradation. The block copolymer structure reduces interfacial tension and prevents coalescence during processing. Impact performance is measured by notched Izod according to ASTM D256, tensile properties by ASTM D638, and processability by melt flow rate according to ISO 1133-1. In polypropylene and polyethylene, the unsaturated midblock is thermodynamically immiscible; mixing without compatibilizer tends to produce coarse morphologies and poor stress transfer. Low-density polyethylene blends may be used to improve cold-temperature impact, but published data for this specific configuration is limited when the polyolefin phase exceeds 70 wt%.
Footwear compounds containing 3411 are typically batch-mixed in an internal mixer at 120–150°C with polystyrene, process oil, fillers, and blowing agents, then discharged to a two-roll mill for sheeting. Injection molding of SBS-rich compounds is carried out on reciprocating-screw machines with barrel temperatures 160–190°C, injection pressures 60–100 MPa, and mold temperatures 30–60°C. Physical tests follow ASTM D2240 for hardness, ASTM D412 for tensile and elongation, ASTM D624 for tear, and DIN 53516 for abrasion. The unsaturated midblock limits continuous service temperature; soling compounds should be formulated with sufficient antioxidant if prolonged heat ageing at 70°C is specified, using ISO 188 or ASTM D573 as accelerated ageing references.
Selection between 3411, oil-extended SBS, and hydrogenated SEBS depends on the balance of cohesive strength, melt viscosity, and ageing resistance. Relative to oil-extended SBS grades, 3411 contains no extender oil; the bulk density is higher and the as-supplied polymer contributes a higher tensile strength and modulus before formulation. Oil-extended grades reduce compound cost and melt viscosity but dilute the polystyrene crosslink density; tensile strength by ASTM D412 is correspondingly lower, and oil migration can change bond peel after ageing. Compared with high-styrene SBS grades, the 31 wt% styrene content of 3411 yields a lower modulus and lower Shore A hardness, which is measured as a softer dry feel in adhesive films and bitumen compounds; grades with 40 wt% styrene or higher give higher hardness and modulus but generally lower low-temperature flexibility. Compared with hydrogenated SEBS, 3411 does not have a saturated polybutadiene midblock. This unsaturation gives broader compatibility with aromatic tackifiers and aromatic bitumen fractions but lower resistance to ultraviolet radiation, oxygen, and elevated-temperature ageing. Continuous service above 70–80°C in air is generally outside the design window for this unsaturated SBS grade; SEBS grades with the same styrene class are specified for higher-temperature or outdoor ageing applications. In processing, 3411 can be run in standard extruders and injection molders without predispersion of oil; however, the melt must not be held above 200°C under air for extended residence times.
| Feature | SBS 3411 | Oil-extended SBS | Hydrogenated SEBS |
|---|---|---|---|
| Midblock saturation | Unsaturated | Unsaturated | Saturated |
| Extender oil in as-supplied grade | None | 10–50 phr | None |
| Upper continuous service temperature in air | 70–80°C | 60–70°C | 100–120°C |
| Solubility in aliphatic solvent | Moderate | Higher due to oil | Moderate |
| Oxidative ageing resistance | Low-moderate | Low-moderate | High |
| Typical hardness range in unfilled compounds | 75–90 Shore A | 35–75 Shore A | 65–90 Shore A |
For regulatory dossiers, the grade is covered as a styrene-butadiene-styrene block copolymer under the EU REACH polymer exemption, but monomer and additive compliance require supplier confirmation. If the material is intended for food-contact articles, the finished compound must be evaluated under FDA 21 CFR 177.1810 or Regulation (EU) No 10/2011; migration testing must be carried out on the final article under OM2 or OM3 conditions as applicable. Halogenated flame retardants should not be assumed absent; request a material disclosure if IEC 61249-2-21 or RoHS compliance is required. The product is not a medical-grade material; no USP Class VI or ISO 10993 certification should be inferred from the absence of heavy metals on a certificate of analysis.