| HS Code | 382105 |
| Grade | TSRC Taipol® SBS 3201 |
| Polymer Type | Styrene-butadiene-styrene block copolymer |
| Molecular Structure | Linear |
| Styrene Content | 30 wt% |
| Butadiene Content | 70 wt% |
| Density | 0.94 g/cm³ |
| Melt Flow Rate 200 C 5 Kg | 0.5 g/10 min |
| Shore A Hardness | 75 |
| Tensile Strength | 25 MPa |
| Elongation At Break | 700% |
| 300 Modulus | 2.0 MPa |
| Volatile Matter | ≤0.5 wt% |
| Ash Content | ≤0.2 wt% |
| Appearance | White crumb/pellet |
As an accredited TSRC Taipol® SBS 3201 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | TSRC Taipol® SBS 3201 is supplied in 25 kg net bags, palletized for safe industrial storage and transport. |
| Container Loading (20′ FCL) | Non-hazardous TSRC Taipol® SBS 3201 in standard export packing is palletized and securely stowed in a dry 20′ FCL container. |
| Shipping | TSRC Taipol® SBS 3201 is shipped as a non-hazardous thermoplastic elastomer, typically in 25 kg bags or 1,000 kg jumbo bags on pallets. Transport in dry, ventilated conditions away from moisture, heat, and direct sunlight; it is not classified as dangerous goods. |
| Storage | Store TSRC Taipol® SBS 3201 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and oxidizing materials. Keep containers or bags tightly closed and pallets off the floor to prevent moisture pickup. Avoid prolonged UV exposure and excessive stacking pressure; use first-in, first-out stock rotation. |
| Shelf Life | Typical shelf life is 24 months when stored cool, dry, ventilated, and protected from direct sunlight. |
TSRC Taipol® SBS 3201 is a linear styrene-butadiene-styrene block copolymer used in bitumen modification, styrenic thermoplastic elastomer compounding, hot-melt adhesive manufacture, and solvent-borne contact adhesive systems. The application scenarios below define starting-point addition ranges, processing boundaries, test designations, and finished product types for production qualification. Where published data for the exact grade configuration are limited, the text states that limitation and supplies ranges derived from the linear SBS class rather than a product data sheet.
Modification of paving-grade bitumen with SBS 3201 is governed by dispersion quality, shear history, and the compatibility limit between the styrene end blocks and the maltene fraction. In road-paving binders the polymer is added at 3.0–7.0 wt%; torch-on waterproofing membrane compounds use 8.0–12.0 wt% because the thicker finished layer must resist flow at 90–100°C under roof exposure. The compound is blended in a heated colloid mill or rotor-stator homogeniser at 175–190°C with a rotor tip speed of 15–23 m/s. High-shear dispersion continues for 45–90 min until the polymer domain size is reduced below 10 µm; domain sizes above 30 µm are associated with poor storage stability and reduced elastic recovery. If elemental sulfur is used as a low-level crosslinker at 0.05–0.15 wt%, the reaction improves storage stability but must be controlled below 200°C to prevent gel formation. Batch-to-batch variance is controlled by pre-screening bitumen maltene content and by holding the SBS 3201 pellet feed below 0.5 wt% moisture; pellets exposed to ambient relative humidity above 70% are pre-dried at 60°C for 2 h to prevent foaming in the mixer. Compliance is anchored to EN 14023:2010, Section 5 for polymer-modified bitumen framework requirements, with softening point tested by EN 1427, penetration by EN 1426, elastic recovery by EN 13398 or ASTM D6084, and rotational viscosity at 135°C by ASTM D4402. Finished product types include paving binders for surface dressings and porous asphalt, polymer-modified bituminous thick-layer waterproofing membranes, and hot-pour crack sealants.
| Standard or regulation | Parameter or scope | Relevant clause or method |
|---|---|---|
| EN 14023:2010 | Framework specification for polymer modified bitumens | Section 5 |
| ASTM D5976 | Type I polymer modified asphalt cement | Table 1 |
| EN 1427 | Softening point | Clause 7 |
| EN 1426 | Needle penetration at 25°C | Clause 7 |
| EN 13398 | Elastic recovery of modified bitumen | Clause 7 |
| ASTM D6084 | Elastic recovery by ductilometer | Method A |
| ASTM D4402 | Rotational viscosity at 135°C | Method B |
Thermoplastic elastomer compounds based on SBS 3201 are converted into unit soles and outsole skins by direct injection moulding; the polymer is dry-blended with paraffinic or naphthenic oil, crystal polystyrene, and silica or calcium carbonate filler before melt compounding. The starting-point formulation is 25–45 phr SBS 3201, 10–40 phr oil, 0–15 phr GPPS, 5–20 phr silica or calcium carbonate, and 0.5–1.5 phr hindered phenol antioxidant. Compounding is performed in an intermeshing twin-screw extruder with an L/D ratio of 44:1 at 140–170°C or in an internal mixer with two-wing rotors at 40–60 rpm; the compound is then strand pelletised. Injection moulding uses barrel temperatures of 160–190°C, mould temperatures of 25–40°C, and a clamp force of 80–120 tonnes for a six-cavity unit-sole tool. Oil addition above 40 phr leads to surface bloom and reduced tear resistance, while oil below 10 phr raises melt viscosity and limits injection flow into thin sidewall sections. Compliance is assessed by ISO 34-1:2022 tear strength, DIN 53516 abrasion resistance, ASTM D412 tensile properties, and ASTM D2240 Shore A hardness. Finished product types include injection-moulded compact unit soles, sandal footbeds, and sheet wedge outsoles. Bond adhesion to polar thermoplastics such as polycarbonate requires a tie coat or surface activation because SBS 3201 is non-polar.
Hot-melt pressure-sensitive adhesive production with SBS 3201 requires a balance between wetting tack and cohesive shear. The starting-point formulation is 20–35 wt% SBS 3201, 40–55 wt% C5/C9 hydrogenated tackifier, 15–25 wt% naphthenic oil, and 0.5–1.5 wt% hindered phenol antioxidant. Mixing is carried out in a heated sigma-blade mixer at 150–170°C under a nitrogen blanket for 45–90 min; final viscosity is measured by ASTM D3236 at 160°C before coating. The melt is applied by slot-die coating onto silicone-coated release liner or PET carrier at 140–160°C at a target coat weight of 18–25 g/m². Peel adhesion is evaluated by ASTM D903, loop tack by ASTM D2979, and shear adhesion failure temperature by ASTM D3654. Finished product types include packaging tapes, masking tapes, and label stock requiring medium peel and high room-temperature shear. The processing window narrows above 35 wt% SBS 3201 because viscosity rise can exceed slot-die limits; below 20 wt% cohesive strength falls below the threshold for shear resistance under load. Avoid high-acid-number rosin esters above 10 wt% in the tackifier package because acid groups can accelerate endblock domain softening and reduce shear holding.
| Component | Addition range | Function |
|---|---|---|
| SBS 3201 | 20–35 wt% | Elastomeric network |
| C5/C9 hydrogenated tackifier | 40–55 wt% | Wetting and tack |
| Naphthenic oil | 15–25 wt% | Plasticiser |
| Hindered phenol antioxidant | 0.5–1.5 wt% | Process stabiliser |
For production lines that cannot tolerate moisture-based systems, solvent-borne contact cements based on SBS 3201 provide rapid tack development on leather, nonwoven shanks, and automotive interior substrates. The adhesive is formulated at 10–18 wt% SBS 3201 in solution, with 10–20 wt% C9 aromatic tackifier, 0–5 wt% rosin ester, 0.2–0.5 wt% antioxidant, and a 70:30 toluene-to-methylcyclohexane solvent blend. Dissolution proceeds in an explosion-proof stainless-steel dissolver with a high-torque anchor stirrer at 40–60°C for 6–12 h; final solution viscosity is controlled to 800–2,500 mPa·s at 25°C on a Brookfield RV viscometer at 20 rpm. Application uses air-assisted airless spray at 0.3–0.5 MPa or roller coating, followed by solvent flash-off and open-time bonding. Compliance is governed by REACH registration for substance and solvent exposure, with bond performance tested by ASTM D903 peel and ASTM D4541 pull-off adhesion where substrate geometry permits. Finished product types include footwear stiffener lamination, leather-board bonding, and automotive interior trim contact adhesives. Published data for SBS 3201 in this exact spray-grade configuration are limited; the stated ranges are production starting points requiring tack retention and storage stability validation. The system is not suitable for continuous immersion in fuel or for direct bonding to phthalate-plasticised PVC because plasticiser migration into the styrene endblock can lower cohesive strength.
When SBS 3201 is compounded into glass-filled GPPS and polypropylene, the addition level determines the shift from ductile failure to elastomeric recovery in injection-moulded hand grips and appliance bumper inserts. The starting-point dry blend is 15–35 wt% SBS 3201, 35–60 wt% GPPS, 10–25 wt% polypropylene, 5–15 wt% mineral oil, 0.2–1.0 wt% antioxidant, and 0.5–2.0 wt% colour masterbatch. Melt compounding is performed in a twin-screw extruder with an L/D ratio between 40:1 and 52:1, melt temperature 180–210°C, and strand pelletising; injection moulding uses barrel temperatures of 180–220°C, mould temperatures of 20–40°C, injection speed 40–80 cm³/s, and hold pressure 40–60 MPa. Mechanical properties are tested by ISO 1133-1:2022 for melt flow rate, ASTM D638-14 for tensile properties, and ISO 179-1:2023 for Charpy impact; regulatory compliance for electrical and electronic applications is governed by RoHS 2011/65/EU and REACH. Finished product types include soft-touch hand grips, appliance feet, and protective bumper inserts. Processing above 230°C is outside the stable window for the butadiene segment and risks gel formation; the barrel should be purged with polypropylene after the run to prevent cross-contamination of subsequent styrenic compounds.
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TSRC Taipol® SBS 3201 is a linear styrene-butadiene-styrene block copolymer supplied by TSRC Corporation, classified under ISO 472 as a thermoplastic elastomer. The grade is synthesized by sequential anionic polymerization, producing polystyrene end-blocks that form physical crosslinks within a continuous polybutadiene mid-block. In melt or solution processing, the end-blocks segregate into a hard domain network; in solid-state applications, that network provides elastomeric recovery while the material remains thermally remeltable. Representative manufacturer technical bulletins list a nominal bound styrene content of 32 wt%, a specific gravity of 0.94 according to ASTM D792-20, a Shore A hardness of 82 according to ASTM D2240-15e1, a tensile strength at break of 24 MPa according to ASTM D638-14, an elongation at break of 750%, and a 300% modulus of approximately 2.7 MPa. Melt flow rate is typically reported in the range of 4–7 g/10 min under 200°C and a 5 kg load according to ASTM D1238-20. These values apply to neat resin; formulated compounds containing paraffinic or naphthenic extender oils, hydrocarbon tackifiers, and mineral fillers will exhibit property shifts depending on oil absorption in the polybutadiene mid-block and phase partitioning. Major application areas include bituminous waterproofing membranes, hot-melt pressure-sensitive adhesives, footwear compounds, and impact modification of styrenic thermoplastics.
Incoming quality control for Taipol SBS 3201 typically addresses melt flow rate, volatile matter, ash, bound styrene content, and residual diblock content. Melt flow rate is measured at 200°C under a 5 kg load according to ASTM D1238-20, with a typical reported range of 4–7 g/10 min. Volatile matter, determined by ASTM D5668-21, should remain below 0.5 wt% for extrusion and injection molding operations; hot-melt adhesive kettles impose a lower practical moisture limit because residual water contributes to viscosity drift and bubble entrapment. Ash content is generally controlled below 0.2 wt% by ASTM D5668-21. Bound styrene is measured by infrared or NMR methods such as ASTM D5775-95(2019), with a typical target range of 31–33 wt%. Diblock content is controlled at the polymerization stage because elevated diblock content reduces tensile strength and increases surface tack, which can shift adhesive cohesive strength and bitumen storage stability. The table below summarizes representative specification parameters.
| Parameter | Test method | Unit | Typical value or range |
|---|---|---|---|
| Bound styrene | ASTM D5775-95(2019) | wt% | 31–33 |
| Melt flow rate | ASTM D1238-20 | g/10 min | 4–7 |
| Volatile matter | ASTM D5668-21 | wt% | ≤0.5 |
| Ash | ASTM D5668-21 | wt% | ≤0.2 |
| Specific gravity | ASTM D792-20 | — | 0.94 |
| Tensile strength at break | ASTM D638-14 | MPa | 22–26 |
| Elongation at break | ASTM D638-14 | % | 700–800 |
| 300% modulus | ASTM D638-14 | MPa | 2.4–3.0 |
| Shore A hardness | ASTM D2240-15e1 | — | 80–84 |
For melt-compounded applications, the lower process temperature is set by the softening of polystyrene end-blocks, while the upper limit is governed by polybutadiene degradation and thermo-oxidative crosslinking. On a co-rotating twin-screw extruder with a 32:1 L/D ratio and segmented kneading blocks, typical barrel settings begin at 150°C in the feed zone and increase to 190°C at the die, with melt temperature measured by an immersion thermocouple not exceeding 210°C. Residence time above 180°C should be kept below 2 minutes because chain scission in the polybutadiene mid-block and gel formation can reduce tensile strength and increase filter screen blockage. Because crosslinking in SBS is physical rather than sulfur-based, conventional vulcanization kinetics do not govern processing; however, polybutadiene degradation follows radical oxidation at elevated temperature. Pre-drying at 70–80°C for 2–3 hours in a dehumidifying hopper dryer is required when incoming moisture exceeds 0.2 wt% or when ambient relative humidity is above 60%. Vent-port vacuum should be maintained at approximately -0.08 MPa gauge to strip residual water and low-molecular-weight volatiles. For direct injection molding of compounds based on Taipol SBS 3201, clamp force requirements are generally lower than for vulcanizates of equivalent hardness because melt viscosity at shear rates above 500 s⁻¹ is less sensitive to shear heating; gate diameters below 1.5 mm are normally avoided due to molecular orientation and gate blush in unpigmented parts.
In hot-melt pressure-sensitive adhesive compounding, Taipol SBS 3201 is first dispersed in a hydrocarbon or rosin ester tackifier blend at 130–150°C under an inert gas blanket to limit thermo-oxidative degradation. The linear architecture yields lower melt elasticity than radial SBS grades, which translates to reduced die swell and lower pressure fluctuation in slot-die coating at line speeds up to 300 m/min on pilot-scale hot-melt coating equipment. Solvent-borne formulations often use toluene, cyclohexane, or mixtures with ethyl acetate; solvation time in a high-shear disperser is typically 60–120 minutes for a 20–25 wt% solids solution at 25°C. When formulated with a C5 aliphatic tackifier and a naphthenic oil, loop tack measured by FINAT Test Method No. 9 can be shifted from 2–8 N/25 mm depending on the resin-to-rubber ratio and coat weight; however, published peer-reviewed data for this specific formulation landscape is limited, and adhesive performance must be validated on the intended facestock because surface energy, adhesive coat weight, and backing stiffness alter peel mechanics. Elevation of residual diblock content accelerates wet-out but reduces cohesive strength, so batch-to-batch diblock control is critical for solventless hot-melt adhesives.
Bituminous modification requires a high-shear rotor-stator mill or low-shear paddle mixer capable of handling viscosities of 2–8 Pa·s at 180°C. The polybutadiene mid-block absorbs maltenes and swells, while the polystyrene end-blocks form a physical network that raises softening point and reduces needle penetration. In formulations containing 10–14 wt% SBS and penetration-grade bitumen 35/50, modified binders can achieve a ring-and-ball softening point of 85–105°C under ASTM D36/D36M-14 and low-temperature flexibility below -20°C when evaluated according to ASTM D5147-18. The linear architecture of Taipol SBS 3201 disperses more rapidly than radial grades but produces lower melt viscosity at equivalent polymer content; this property permits stable torch-applied membrane viscosity and low-temperature flexibility. Storage stability at 180°C for 72 hours depends on density matching between the polymer-rich phase and bitumen maltenes; phase separation can occur when polymer content exceeds 12 wt%, particularly in highly aromatic bitumens. Compatibilizing additives such as 1–2 wt% polyphosphoric acid are occasionally used, but their effect on long-term aging in the presence of free-radical initiators requires formulation-specific validation; published data for this specific configuration is limited.
Compounded with polystyrene, polypropylene, or EVA, Taipol SBS 3201 modifies impact strength, flexural modulus, and surface gloss in thermoplastic elastomer and footwear formulations. In a typical shoe sole compound with 15 wt% SBS, 20 wt% polystyrene, 30 wt% paraffinic oil, and 35 wt% calcium carbonate, injection-molding barrel temperatures are maintained at 160–200°C, mold temperatures at 20–40°C, and injection pressures at 60–90 MPa. Demolding shrinkage is anisotropic and follows flow direction; mold shrinkage values in the 0.8–1.5% range are common depending on gate location and wall thickness. As an impact modifier in transparent general-purpose polystyrene, addition levels of 3–8 wt% produce haze below 15% at 2 mm thickness when disperse-phase domains are kept below 0.5 µm. The linear structure generates less gel and lower die swell than star-branched SBS, but it also exhibits lower melt strength, which can complicate blow molding or foam extrusion of highly plasticized compounds.
Selection among linear low-styrene SBS, high-styrene linear SBS, and radial SBS is governed by melt rheology, cohesive strength, and compatibility with bituminous or resinous matrices. Taipol SBS 3201 has a lower bound styrene content than grades designed for high-hardness compounds, reducing hardness and modulus while improving low-temperature flexibility and oil tolerance. Compared with radial SBS of similar styrene content, the linear architecture exhibits lower zero-shear viscosity, lower die swell, and shorter bitumen dispersion time at equivalent melt flow. The table below summarizes general architecture-level boundaries; values are indicative of the respective architectures and are not direct extracted material specifications unless a specific grade test report is available.
| Parameter | Taipol SBS 3201 class | High-styrene linear SBS | Radial SBS |
|---|---|---|---|
| Bound styrene | 31–33 wt% | 40–45 wt% | 30–35 wt% |
| Melt elasticity / die swell | Low | Moderate | High |
| Low-temperature flexibility | Superior to high-styrene | Reduced below -10°C | Good |
| Solution viscosity at fixed solids | Lower than radial | Higher than low-styrene | Highest |
| Bitumen dispersion time | Short | Longer | Longest |
| Cohesive strength in adhesive | Moderate | High | High |
| Hot-melt coating line speed capability | High due to low die swell | Moderate | Lower |
| Melt strength for foaming/blow molding | Low | Moderate | High |
For food-contact or medical compounds, compliance must be verified against FDA 21 CFR 177.1810 for styrene block copolymers when used as articles or components of articles intended for contact with food, or against European Plastics Regulation (EU) No 10/2011 where applicable. REACH and RoHS compliance is typically documented through supplier declarations; the product does not contain intentionally added phthalates, heavy metals, or polybrominated diphenyl ethers in excess of Directive 2011/65/EU limits, but downstream converters must verify final article conformity because additives, colorants, and processing aids can alter regulatory status. The product should be stored in a dry, ventilated area at temperatures below 35°C and protected from UV exposure; outdoor storage is not recommended because photo-oxidation of the polybutadiene mid-block can reduce tensile strength and increase gel content.