Products

TSRC Taipol® SBS 4202

    • Product Name: TSRC Taipol® SBS 4202
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 122649
    Chemicaltype Styrene-butadiene-styrene block copolymer (SBS)
    Polymerstructure Linear triblock copolymer
    Styrenecontent 40 wt% (typical)
    Butadienecontent 60 wt% (typical)
    Density 0.94 g/cm³ (typical)
    Meltflowrate 0.5–1.0 g/10 min at 200°C/5 kg (typical)
    Hardnessshorea 90–92 (typical)
    Tensilestrength 20–25 MPa (typical)
    Elongationatbreak 600–700% (typical)
    Tearstrength 35–45 kN/m (typical)
    Volatilematter ≤0.7 wt%
    Ashcontent ≤0.2 wt%
    Appearance White crumb or powder
    Form Crumb or powder

    As an accredited TSRC Taipol® SBS 4202 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing TSRC Taipol® SBS 4202 is typically supplied in 25 kg net paper bags, palletized and sealed for industrial shipment.
    Container Loading (20′ FCL) 20′ FCL loading: approx. 18 MT TSRC Taipol® SBS 4202 in 25 kg bags, palletized, strapped, and secured for ocean transport.
    Shipping TSRC Taipol® SBS 4202 is normally shipped as dry crumb/pellets in 25 kg moisture-proof bags, palletized and stretch-wrapped. It is not classified as dangerous goods; keep containers closed, dry, cool, and away from direct sunlight and heat during transport.
    Storage Store TSRC Taipol® SBS 4202 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original containers closed and elevated on pallets to prevent moisture and contamination. Avoid prolonged exposure to high temperatures and UV light. Maintain good housekeeping and follow local regulations and SDS recommendations.
    Shelf Life Shelf life is typically 24 months from manufacture when stored dry, cool, and in unopened original packaging.
    Application of TSRC Taipol® SBS 4202

    What Changes When Taipol 4202 Is Dispersed in a Pen 60/70 Bitumen Matrix?

    Bituminous binder modification with linear SBS is an established hot-melt dispersion process. In paving-grade Pen 60/70 bitumen, the styrene end-blocks of Taipol® SBS 4202 associate into glassy domains below approximately 100°C, whereas the polybutadiene mid-block is swollen by maltenes. At addition levels between 4.0 wt% and 6.0 wt%, a phase-inverted network develops when high-shear mixing reduces the SBS phase to domains below 10 µm. In a 2,000 litre vertical cylindrical mixer equipped with a rotor-stator high-shear head rated at 3,000 rpm, the base bitumen is heated to 170–180°C before adding SBS 4202 pellets. Swelling is allowed for 30–45 min under low-speed agitation to prevent agglomeration. High-shear dispersion then proceeds for 60–120 min until fluorescence microscopy shows a continuous polymer-rich phase. If the mixer is undersized for the batch, local temperatures above 210°C degrade the butadiene segment and reduce elastic recovery. After dispersion, the batch is transferred to a horizontal agitated maturation tank at 160–170°C for 3–4 h. Elemental sulfur at 0.05–0.15 wt% is dosed only after the polymer phase is fully dispersed; premature sulfur addition causes gelation and viscosity spikes. The resulting binder is evaluated against ASTM D36 for softening point, ASTM D5 for penetration, ASTM D6084 for elastic recovery, EN 13399 for storage stability, and AASHTO T315 for complex shear modulus. A storage-stable paving binder typically shows a softening point above 70°C, penetration of 40–55 dmm, elastic recovery above 70%, and a top-to-bottom softening point difference below 5°C. For PG 76-22 qualification, the rolling thin-film oven-aged residue is measured at 76°C under 10 rad/s; the specification requires G*/sin δ greater than 1.00 kPa for the original binder and greater than 2.20 kPa after AASHTO T240 aging. Full compliance depends on the base crude, the exact dispersion shear history, and polymer digestion time; published data for the specific interaction of Taipol 4202 with non-standard base bitumens is limited.

    Test methodPropertyTypical criterion for modified paving binder
    ASTM D36Softening point≥ 70°C
    ASTM D5Penetration at 25°C40–55 dmm
    ASTM D6084Elastic recovery≥ 70%
    EN 13399Storage stability ΔSP≤ 5°C
    AASHTO T315DSR G*/sin δ at 76°C≥ 1.00 kPa original; ≥ 2.20 kPa RTFO

    In elastomeric bituminous waterproofing membranes produced by torch-on or self-adhesive systems, SBS 4202 serves as the elastic component in the bitumen compound. The compound is prepared on a two-roll mill or in a Z-blade mixer at 150–170°C. A typical formulation contains 10–15 wt% SBS 4202, 25–35 wt% limestone filler, 5–8 wt% naphthenic oil, and the balance oxidized or straight-run bitumen. After homogenization, the compound is calendered onto a polyester mat or glass fleece using a three-roll calender with a nip gap of 0.8–1.2 mm. Low-temperature flexibility is checked according to EN 1109, flow resistance at elevated temperature according to EN 1110, and peel adhesion according to ASTM D903. The styrene domains in SBS 4202 must survive the calender heat history; if the melt temperature exceeds 200°C for more than 60 min, the cohesion of the membrane at −10°C declines and the material develops microcracks during mandrel bending. At the end of the line, the membrane is cooled below 40°C before winding to prevent blocking. Compared with atactic polypropylene-modified membranes, SBS 4202 formulations exhibit higher elongation and lower modulus, which is relevant for crack-bridging in below-grade waterproofing. The compounder must verify that filler moisture content is below 0.1%; moisture above this threshold causes bubbling in the calender nip and pinholes in the finished sheet. Production lines operating at 5–15 m/min maintain acceptable visual quality if the calender roll temperature is held within ±5°C of the set point; wider deviations produce thickness bands and surface tearing at the embossing station.

    Hot-Melt Pressure-Sensitive Adhesive Viscosity and Carboxylated Tackifier Interactions

    Hot-melt pressure-sensitive adhesive formulations based on SBS 4202 are prepared in a heated sigma-blade mixer with a jacket temperature of 150–165°C. The grade is first masticated with a naphthenic oil in the absence of antioxidant for 10–15 min until the oil is absorbed. A C5/C9 aliphatic-aromatic tackifier resin is then added in portions to avoid a viscosity drop that causes mechanical overload. A starting formulation uses 25 parts SBS 4202, 50 parts tackifier, 25 parts naphthenic oil, and 1 phr hindered phenolic antioxidant. The tackifier should have a softening point between 90°C and 110°C to match the butadiene mid-block solubility parameter. The styrene end-blocks remain associated at room temperature and provide cohesive strength. Viscosity is determined with a Brookfield RVT viscometer at 160°C using spindle 27 at 50 rpm, and the value is reported in mPa·s. If the formulation is to be slot-die coated on PET film at 20–40 g/m², viscosity above 10,000 mPa·s at 160°C may cause ribbing; if below 2,000 mPa·s, the web may neck during coating. Peel adhesion to stainless steel is assessed by ASTM D3330 at 180° and room temperature after 24 h dwell. Loop tack is measured by ASTM D6195. Shear adhesion failure temperature is obtained by ASTM D4498 on a 1 kg static load. The grade's heat stability in the coating tank is limited by oxidative degradation of the unsaturated mid-block; therefore, the adhesive should be blanketed with nitrogen and the residence time at 160°C should not exceed 24 h. When a less unsaturated styrenic block copolymer is used, the same formulation may show lower initial peel but better color stability. For Taipol 4202, the formulator should avoid ester-based tackifiers above 30 wt% of total formulation because phase separation may occur during cooling.

    ComponentFormulation AFormulation BFormulation C
    Taipol SBS 420220 phr25 phr30 phr
    C5/C9 aliphatic-aromatic tackifier55 phr50 phr45 phr
    Naphthenic process oil25 phr25 phr25 phr
    Hindered phenolic antioxidant1 phr1 phr1 phr

    When SBS 4202 Replaces Random Styrene-Butadiene Rubber in Low-Solids Contact Cements

    Solvent-borne contact adhesives for footwear lamination and decorative laminates use a polymer solution of 15–25 wt% solids in a blend of toluene, methyl ethyl ketone, and acetone. SBS 4202 dissolves under high-speed dispersion with a Cowles blade at 600–1,000 rpm; the solvent blend should be adjusted so the evaporation rate does not cause blushing. In a typical formulation, 100 parts SBS 4202 is dissolved in 300–400 parts solvent, then compounded with 60–90 parts hydrogenated rosin ester tackifier and 1–2 parts antioxidant. The solution viscosity is controlled to 2,000–5,000 mPa·s at 25°C using a Brookfield LVT viscometer, spindle 3 at 12 rpm. Adhesive transfer is performed by roll coater or spray gun; wet films of 120–150 g/m² are applied to both substrates and dried for 20–40 min at 25–35°C. After an open time of 15–25 min, the second substrate is laminated under nip pressure of 0.3–0.5 MPa. Peel strength after 7 days is evaluated by ISO 11339 at 100 mm/min. Because the mid-block is susceptible to ozonolysis, the bonded article should not be continuously exposed to ozone concentrations greater than 50 pphm unless a protective film or antioxidant package is used. Solvent retention in the final laminate should be measured by headspace gas chromatography and maintained below 100 ppm; higher retained solvent values indicate insufficient drying capacity on the line and may cause long-term adhesive bleed at the bond line.

    Microcellular direct-injection shoe soles made with SBS 4202 are processed on multi-station rotary injection-molding machines with screw L/D ratios of 20:1 to 24:1. The compound is prepared by tumble mixing SBS 4202 with polystyrene, naphthenic oil, azodicarbonamide blowing agent, and zinc oxide; the compound is then pelletized on a twin-screw extruder with barrel temperatures of 150/160/170/180/190°C. The pellet feed is injected into a mold cavity preheated to 35–45°C at melt temperature 190–210°C; clamp force is typically 250–450 tonnes for multi-cavity sole molds. The blowing agent decomposes at 185–200°C, producing cells behind the advancing melt front. Sole density after expansion is 0.30–0.55 g/cm³ depending on shot size and blowing agent dosage. Hardness is measured by ASTM D2240, split tear by ASTM D3574, and flex fatigue by ASTM D1052 after 100,000 cycles at 25°C. If the melt temperature exceeds 220°C, azodicarbonamide decomposes prematurely in the barrel, causing uneven cell structure and weld-line voids. If the mold temperature falls below 30°C, the surface may freeze before the blowing agent completes its decomposition, producing a non-uniform skin. SBS 4202-based soles are generally unsuited to continuous exposure above 60°C because the styrene domains soften and the sole loses dimensional stability. The compounder should verify the oil level because excessive naphthenic oil increases expansion but reduces abrasion resistance according to DIN 53516.

    Twin-Screw Compounding of Polypropylene/SBS Impact Blends

    Polypropylene homopolymer is impact-modified by melt blending with 5–15 wt% SBS 4202 on a co-rotating twin-screw extruder with L/D 32:1 and barrel zones from 180°C to 230°C. The screw configuration contains two kneading blocks downstream of the feed zone and a reverse element before the vacuum vent to ensure dispersion of the elastomer phase. The SBS phase is initially immiscible with polypropylene but is distributed as domains of 0.5–2.0 µm when the shear rate exceeds 300 s⁻¹. Notched Izod impact strength measured by ASTM D256 at 23°C increases with SBS content up to 15 wt%, while flexural modulus by ASTM D790 decreases proportionally. Melt flow rate is measured according to ISO 1133-1 using 2.16 kg at 230°C; as SBS content increases from 5 wt% to 15 wt%, the MFR may decline by 20–50% depending on the PP base resin. Because the glass transition temperature of the polybutadiene mid-block is below −70°C, low-temperature impact resistance improves more than with ethylene-propylene modifiers at the same loading. However, the low thermal stability of the SBS phase limits processing above 240°C; the residence time at high temperature should be below 3 min to avoid chain degradation. The blend is used in injection-molded appliance components requiring 5–10 kJ/m² Charpy notched impact at 0°C according to ISO 179-1. Published data for the specific synergy between Taipol 4202 and high-flow PP grades is limited; pilot-scale studies with the actual PP lot are required.

    In high-solids butyl mastic and construction sealant formulations, SBS 4202 is incorporated at 8–15 wt% into a mixer of butyl rubber, polybutene, calcium carbonate, and hydrocarbon resin. The compound is mixed in a double-arm sigma-blade kneader at 130–150°C until a uniform, lump-free consistency is achieved. The addition of SBS 4202 raises the slump resistance of the mastic measured by ISO 7390 and increases tensile elongation to 300–500% after atmospheric curing when tested according to ISO 8339. In applications where the sealant must adhere to anodized aluminum or glass, a silane coupling agent is added at 0.5–1.0 wt% after polymer incorporation; the mixer temperature is reduced to 120°C before silane addition to prevent condensation. The mastic is extruded at 0.6–1.2 MPa air pressure through a 5–7 mm nozzle. Because the butadiene mid-block is unsaturated, the sealant is not recommended for continuous exposure to chlorinated water or UV without a surface coating. The product's viscosity at 25°C is measured by extrusion rheometer at a shear rate of 1 s⁻¹ and is typically in the range of 2,000–6,000 Pa·s. If the formulation is stored above 40°C for more than 48 h, the styrene domains may partially dissolve into the polybutene, reducing cohesive strength.

    Free Quote

    Competitive TSRC Taipol® SBS 4202 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618005193850

    Email: sales8@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    TSRC Taipol® SBS 4202 is a pelletized linear styrene-butadiene-styrene thermoplastic elastomer produced by TSRC Corporation. Technical trade literature positions the grade for polymer-modified bitumen, hot-melt adhesives, solvent-borne adhesives, and waterproofing membranes where a high styrene domain fraction and oil-extended processability are required. Published data summaries list bound styrene at 40 wt% and incorporated naphthenic process oil at 32.5 wt%. The oil extension reduces melt viscosity and permits lower specific mechanical energy during dispersion in co-rotating twin-screw compounding lines with 40:1 L/D barrels. The unsaturated polybutadiene midblock is susceptible to oxidative chain scission above 200°C and to ozone degradation in unstabilized outdoor exposure.

    PropertyTest methodTypical value
    Bound styreneSupplier internal method40 wt%
    Naphthenic oil contentSupplier internal method32.5 wt%
    Tensile strengthASTM D638-1415 MPa
    Elongation at breakASTM D638-14700%
    300% modulusASTM D638-142.5 MPa
    HardnessASTM D224082 Shore A
    Melt flow indexASTM D1238 at 200°C/5 kg4 g/10 min
    Specific gravityASTM D7920.94

    Typical specification values are compiled from supplier technical summaries and are not batch certificates. Users should request a certificate of analysis for the specific lot because styrene content, oil content, and melt flow may vary within supplier control limits. Hardness and tensile values are determined on compression-molded sheets conditioned at 23°C and 50% RH for 24 h. The 300% modulus value of 2.5 MPa indicates a stiffer elastomeric network than lower-styrene SBS grades, which is significant when resistance to creep at elevated service temperature is required.

    What Distinguishes 4202 from Lower-Styrene and Radial SBS Grades?

    Compared with Taipol® SBS 3201, the 40 wt% bound styrene of 4202 increases the hard-domain fraction and raises Shore hardness from approximately 71 Shore A to 82 Shore A. The higher styrene content also extends the temperature range over which the polystyrene domains retain structural integrity. In asphalt modification, this shows as a greater softening point increase per unit polymer addition when measured according to ASTM D36. The trade-off is lower elongation at break relative to lower-styrene grades and a higher melt viscosity before oil extension is considered. In 4202, the incorporated naphthenic oil compensates for the viscosity penalty of the higher styrene content, while also reducing the energy required to wet and disperse the polymer into bitumen.

    Compared with radial SBS such as Taipol® SBS 4402, the linear architecture of 4202 provides lower melt viscosity at equivalent styrene content and therefore easier flow in hot-melt coating heads and adhesive extruders. Radial grades typically exhibit higher melt strength and greater tensile strength after solvent casting, but they require higher rotor speeds or longer residence time in high-shear mixers to achieve equivalent dispersion in bitumen. Published data for this specific linear-to-radial comparison is limited; selection should be confirmed through plant-scale mixing trials using the actual bitumen crude source and filler system.

    ParameterTaipol® SBS 3201Taipol® SBS 4202Taipol® SBS 4402
    Bound styrene30 wt%40 wt%40 wt%
    Tensile strength18 MPa15 MPa20 MPa
    Elongation at break700%700%700%
    300% modulus2.0 MPa2.5 MPa3.0 MPa
    Hardness71 Shore A82 Shore A85 Shore A
    Melt flow index10 g/10 min4 g/10 min0.5 g/10 min

    The comparative values above are representative trade-literature values, not simultaneous batch data. The melt flow index is determined at 200°C with a 5 kg load using ASTM D1238. In production, melt flow differences translate directly into pump speed and coat-weight control on hot-melt adhesive lines. A change in oil content of ±1 wt% can produce measurable melt flow variation, and production-scale coaters often detect this as coat-weight drift at constant screw speed.

    Melt-Processing Parameters in Twin-Screw Extruders and High-Shear Bitumen Plants

    Compounding of 4202 in hot-melt adhesives is commonly carried out in co-rotating twin-screw extruders with 40:1 L/D barrels and segmented screw elements. The oil-extended pellet structure reduces the torque demand during plastication compared with neat SBS of equivalent styrene content. It is not necessary to pre-mill or cryogenically grind the material for standard hot-melt batch processes. Pellets should be stored below 60% RH; if storage humidity exceeds this threshold, drying at 60°C for 2 h is recommended before extrusion to avoid moisture-induced bubble formation in adhesive films. Barrel temperatures above 200°C should be avoided because oxidative chain scission in the polybutadiene midblock becomes rapid. Nitrogen blanketing on the feed hopper and vacuum venting downstream of the mixing zones are effective in reducing oxidative yellowing and melt viscosity drift.

    In polymer-modified bitumen production, 4202 is introduced into penetration-grade base bitumen through a rotor-stator high-shear mixer. Plant-scale processing windows are typically held at 175–190°C. Below 170°C, dispersion time increases significantly and undispersed polymer specks may remain visible on 200 mesh sieves. Above 205°C, thermal degradation of the polybutadiene block produces a non-recoverable viscosity loss and reduces the softening point of the finished binder. Storage stability should be verified with EN 13399 by measuring the difference in softening point between top and bottom samples after 72 h at 163°C. A difference below 5°C is generally accepted for storage-stable polymer-modified bitumen, although project specifications may require tighter limits.

    Batch-to-batch variation in base bitumen composition is a more common cause of storage instability than variation in the SBS polymer. High-asphaltene crude sources can produce phase separation even at moderate SBS loadings. In such cases, the use of aromatic process oils is not recommended because aromatic oils solvate the polystyrene domains and reduce the upper service temperature of the modified binder. Aliphatic or naphthenic oils are preferred for viscosity adjustment. The specific mechanical energy required for dispersion in high-shear mixers is often reduced by 10–20% when using oil-extended 4202 compared with neat SBS of equivalent bound styrene, but the exact reduction depends on mixer tip speed, bowl geometry, and bitumen grade.

    Adhesive Formulation Ranges and Storage-Stable Polymer-Modified Bitumen

    In hot-melt adhesive systems, 4202 is typically compounded with midblock-compatible tackifying resins and naphthenic or aliphatic process oils. The styrene domains provide cohesive strength and resistance to cold flow, while the oil-extended butadiene midblock contributes pressure-sensitive tack and low-temperature flexibility. Tensile properties of the formulated adhesive can be evaluated with ASTM D638-14, and peel adhesion on stainless steel with ASTM D903. Processing viscosity is measured with ASTM D3236 using a Brookfield thermosel. Formulations containing more than 40 wt% tackifier may show increased room-temperature peel but reduced shear adhesion failure temperature. The balance is application-specific and must be confirmed on the actual substrate because liner release coatings and electrophoretic metal surfaces alter adhesive failure mode.

    For solvent-borne adhesives, 4202 is dissolved in toluene, methylcyclohexane, or mixed aliphatic-aromatic solvent systems. Typical solution solids are 20–30 wt%; higher solids are limited by viscosity build. Dissolution is carried out in a heated sigma-blade mixer with jacket temperature between 60°C and 80°C. The use of high-aromatic solvents accelerates the solvation of polystyrene domains but lowers the final cohesive strength after solvent evaporation. Solvent recovery systems with oxygen exclusion reduce gel formation caused by polybutadiene oxidation. Solution viscosity is monitored by ASTM D2196 rotational viscometry.

    In waterproofing membranes, 4202-modified bitumen is applied as a compound containing 10–15 wt% SBS based on bitumen. The resulting membrane compound is evaluated for low-temperature flexibility by ASTM D5147 and for tensile properties by ASTM D882 or the relevant product specification. The high styrene content of 4202 improves resistance to indentation and flow at elevated roof temperatures. Unsaturated midblock oxidation remains a limitation in exposed black membranes unless the formulation contains carbon black, ultraviolet absorbers, or reflective mineral surfacing.

    When 4202 Replaces SEBS or EVA in Service-Life-Sensitive Assemblies

    Substitution of 4202 for SEBS should be evaluated for weather resistance and continuous service temperature. SEBS has a saturated ethylene-butylene midblock and provides improved resistance to ultraviolet radiation and ozone when tested under ASTM G154 cycle conditions. The unsaturated polybutadiene midblock of 4202 will embrittle sooner in direct outdoor exposure unless the compound is heavily stabilized and shielded from UV. The advantage of 4202 is lower melt viscosity and better compatibility with bitumen and low-cost aliphatic oils. In hot-melt assembly adhesives where the bond line is not exposed to sunlight and continuous temperature remains below 70°C, 4202 can replace SEBS without deterioration of cohesive strength.

    Replacement of EVA in asphalt modification or adhesive systems involves different performance trade-offs. EVA provides stiffness and resistance to rutting but exhibits limited elastic recovery and poor low-temperature flexibility compared with SBS. In polymer-modified bitumen, 4202 produces a more elastomeric response after tensile deformation, as measured by ASTM D6084 elastic recovery. The melt viscosity of SBS-modified bitumen is generally higher than EVA-modified bitumen at the same polymer loading. Production lines designed for EVA may require retuning of high-shear mixer residence time and pump settings when switching to 4202.

    Compliance with REACH regulation EC 1907/2006 is maintained through the supplier registration program. RoHS directive 2011/65/EU applies to electrical and electronic equipment and is not directly applicable to the raw polymer, but compounded articles must be assessed at the final-article level. Users should obtain the current safety data sheet and confirm that the grade is listed for the intended food-contact or medical application before use. Published data for food-contact configurations of 4202 is limited.

    For production-scale membrane and adhesive lines, the primary processing constraint is residence time at temperature. In hot-melt tanks held at 170°C, residence beyond 8 h without nitrogen blanket can produce visible viscosity drift and darkening. In bitumen plants, the same threshold is reached more quickly at 200°C because oxidative surface area is larger and air entrainment from paddle mixing is continuous. These operational boundaries should be used as start-up limits rather than exact chemical stability limits, because antioxidant packages and mixer geometry alter the degradation rate.

    Top