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LCY Chemical Globalprene® SBS 3710

    • Product Name: LCY Chemical Globalprene® SBS 3710
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 493989
    Polymer Type Styrene-butadiene-styrene (SBS) block copolymer
    Block Structure Linear triblock
    Styrene Content 30%
    Butadiene Content 70%
    Density 0.94 g/cm3
    Melt Flow Index 4 g/10 min (200°C/5 kg)
    Hardness 70 Shore A
    Tensile Strength 25 MPa
    Elongation At Break 700%
    300 Percent Modulus 2.5 MPa
    Solution Viscosity 1,200 mPa·s (25% in toluene)
    Volatile Matter ≤0.5%
    Ash Content ≤0.2%
    Appearance White crumb

    As an accredited LCY Chemical Globalprene® SBS 3710 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg moisture-resistant woven bags, palletized and lot-labeled for safe industrial storage and transport.
    Container Loading (20′ FCL) 20′ FCL container loading: LCY Globalprene® SBS 3710 in 25 kg bags, palletized and securely stowed for export.
    Shipping Non-hazardous thermoplastic elastomer pellets; not classified as dangerous goods for transport. Supplied in 25 kg bags or jumbo bags on pallets. Keep dry, cool, and away from direct sunlight, heat, moisture, and contamination during storage and handling.
    Storage Store LCY Chemical Globalprene® SBS 3710 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, ignition sources, and moisture. Keep original packaging sealed and off the floor; avoid UV exposure and contamination. Use first-in, first-out stock rotation, and inspect containers regularly. Avoid prolonged high temperatures and ozone exposure. Maintain good ventilation and prevent water ingress.
    Shelf Life LCY Chemical Globalprene® SBS 3710 has a typical shelf life of 24 months when stored dry in original packaging.
    Application of LCY Chemical Globalprene® SBS 3710

    In polymer-modified bitumen (PMB) for high-stress asphalt pavements, bridge deck waterproofing, and airport taxiway overlays, Globalprene® SBS 3710 is introduced at 4.0–6.5 wt% of total bitumen mass in a vertical stainless steel tank equipped with a rotor-stator high-shear mixer. The base bitumen is preheated to 170–185°C before SBS addition; after polymer feed, shear is maintained at 2,500–4,000 rpm for 45–90 min until the system transitions from a discontinuous SBS particle dispersion to a continuous interpenetrating polymer network. During this phase inversion, maltene fractions migrate into the polybutadiene midblock, swelling the elastomer phase and leaving a styrene-rich network that resists permanent deformation under heavy braking and high summer pavement temperatures. Dispersion quality is monitored by fluorescence microscopy on a compressed 5 μm film and by storage-stability testing under EN 13399:2010, where a softening point difference greater than 3.0°C between top and bottom portions indicates inadequate compatibility. Road binder compliance follows EN 14023:2010 in the EU and ASTM D6373-21 performance grading in North America. Representative laboratory ranges for a 60/70 penetration-grade base bitumen modified with 4.5–6.0 wt% SBS 3710 are given in the table below. End products include porous asphalt mixes subjected to high shear stress at intersections, high-temperature taxiway surfaces, and bridge deck membranes requiring cold bending at -10°C. The critical processing window is 185–195°C; sustained temperatures above 200°C accelerate polybutadiene thermo-oxidative chain scission, causing rapid loss of elastic recovery and an increase in low-temperature stiffness. Nitrogen blanketing or 0.1–0.3 wt% hindered phenolic antioxidant is advised when the binder is held at temperature for more than 6 h.

    Test parameter and methodBase 60/70 bitumen4.5 wt% SBS 37106.0 wt% SBS 3710
    Softening point, ASTM D3648–52°C68–75°C82–90°C
    Penetration at 25°C, ASTM D560–70 dmm45–55 dmm38–46 dmm
    Elastic recovery at 25°C, ASTM D6084<5%55–65%70–80%
    Storage stability, EN 13399N/A2.0–4.0°C4.0–6.0°C

    When SBS 3710 is compounded into hot-melt pressure-sensitive adhesives, tackifier selection governs the balance between loop tack and cohesive shear

    Formulations for paper-label and carton-sealing hot-melt pressure-sensitive adhesives typically combine 20–35 wt% SBS 3710, 40–55 wt% hydrogenated rosin ester or C5/C9 aliphatic-aromatic tackifier, 15–25 wt% naphthenic process oil, and 0.5–1.5 wt% hindered phenolic antioxidant. Melt blending is carried out in a jacketed sigma-blade mixer or a co-rotating twin-screw extruder with an L/D ratio of 40:1 and screw temperature profile from 120°C at feed to 160°C at the die. A slot-die coater applies the melt at 140–160°C to release liner or face stock at line speeds of 50–150 m/min. The polybutadiene midblock is readily dissolved by high-aromatic tackifiers, reducing cohesive holding power, whereas high-softening-point hydrogenated rosin esters preserve styrene domains and increase shear adhesion failure temperature. Adhesive performance is measured by ASTM D6195 loop tack, ASTM D3330/D3330M-04 180° peel adhesion, ASTM D3654/D3654M-06 static shear at 1.0 kg and 70°C, and ASTM D4498 shear adhesion failure temperature. Food-contact label adhesives must comply with FDA 21 CFR 175.105 and EU 10/2011 where migration testing is required. End products include permanent paper labels, carton side-seam adhesives, and low-temperature freezer tape laminates. A defined processing boundary exists: aromatic tackifier levels above 50 wt% of total formulation may reduce shear adhesion failure temperature below 60°C, while oil levels above 25 wt% reduce peel on recycled corrugated board due to excessive plasticizer migration into the substrate.

    In injection-molded footwear unit soles, Globalprene® SBS 3710 is dry-blended with general-purpose polystyrene, naphthenic oil, and precipitated silica before being fed to a shoe sole injection molding machine with a three-stage screw and a clamp force between 100 and 150 tonnes. A typical compound uses 100 phr SBS 3710, 20–40 phr GPPS, 20–50 phr naphthenic oil, 20–40 phr precipitated silica, 1.0–2.0 phr antioxidant, and 0.5–1.0 phr wax. Barrel temperatures are profiled from 150°C at the feed throat to 185°C at the nozzle; mold temperature is held at 25–50°C to freeze the styrene domains rapidly and reduce cycle time. The GPPS phase raises hardness and abrasion resistance, while the oil selectively plasticizes the polybutadiene midblock, lowering compound viscosity and improving flow into thin midsoles and sole edge details. Physical property requirements for athletic and casual footwear are checked with ASTM D412 tensile strength, ASTM D624 trouser tear, ASTM D2240 Shore A hardness, and DIN 53516 abrasion loss. A Shore A hardness of 55–70 is typical for midsole formulations, while outsole compounds are adjusted to 60–75 Shore A. Compliance with REACH Annex XVII requires that none of the eight restricted polycyclic aromatic hydrocarbons exceed 1 mg/kg in rubber parts intended for prolonged skin contact. The main processing limitation is scorch in compounding: if the mixture is held above 190°C for more than 8 min in an internal mixer, diblock chains begin coupling and the melt viscosity rises, producing surface defects on thick sole sections. End products are injection-molded unit soles, sport sandal straps, and direct-injection safety shoe overlays.

    How does SBS 3710 alter the notched impact response of recycled polypropylene at sub-zero temperatures?

    When compounded into recycled injection-grade polypropylene, SBS 3710 is metered at 5–15 wt% into a co-rotating twin-screw extruder with 36–44 L/D and vacuum devolatilization. The PP feed zone is set to 180°C, the mixing zones to 190–210°C, and the die to 190–200°C; sustained temperatures above 220°C are avoided because the polybutadiene segments undergo allylic hydrogen abstraction and chain scission, releasing volatile aldehydes and reducing impact modification efficiency. The elastomer phase must be dispersed as domains below 2 μm in the PP matrix; this is achieved by feeding SBS 3710 downstream after PP melting or by using a side-feeder at 40–60% of barrel length. Notched impact is measured according to ISO 180/A at 23°C and -20°C; flexural modulus is measured by ISO 178, and tensile yield stress by ISO 527-2. In recycled PP homopolymer with an initial notched impact of 2.5–3.0 kJ/m², addition of 10 wt% SBS 3710 can raise sub-zero impact by 40–100% depending on nucleating agents, molecular weight, and residual polymer degradation. Reported improvements vary; published data for this specific recycled PP configuration is limited. End products include automotive wheel arch liners, reusable logistics crates, and appliance connector housings. Compliance is typically governed by RoHS 2011/65/EU for lead, cadmium, mercury, chromium VI, PBB and PBDE content when the article falls under electrical and electronic equipment scope, and by REACH candidate list restrictions when recycled feedstock originates from post-consumer sources. A key operational boundary is batch-to-batch variance in recycled PP: the same SBS 3710 addition may yield a notched impact increase of only 10–20% in streams containing high levels of calcium carbonate filler or polyethylene contamination above 8 wt%.

    Low-temperature flex resistance and filler dispersion in SBS-modified torch-applied roofing membranes

    In reinforced roofing membranes, Globalprene® SBS 3710 is compounded into oxidised or vacuum-distilled flux bitumen at 10–15 wt%, with mineral filler additions of 20–30 wt% and a polyester or glass-fibre reinforcement embedded between two layers of compound. Mixing is performed in a horizontal ploughshare mixer or high-shear inline blender at 170–190°C until the SBS network is fully swollen and filler agglomerates are dispersed below 40 μm. The finished compound is calendered onto the reinforcement at 150–170°C, then cooled on a water-cooled belt so the styrene domains vitrify and lock in dimensional stability. Low-temperature flexibility is assessed by EN 1109 cold bending on a mandrel of specified diameter, with typical requirements between -10°C and -25°C depending on climatic zone. Mechanical properties are checked by EN 12311-1 tensile strength and elongation, and dimensional stability by EN 1107-1. Product standards include EN 13707:2004+A2:2009 for reinforced bitumen sheets for roof waterproofing and ASTM D5147/D5147M-18 for sampling and testing of modified bituminous sheet material in North America. The end products are torch-applied or self-adhered roofing membranes, bridge deck underlays, and foundation tanking sheets. A practical failure mode observed on production lines is edge tearing at the polyester reinforcement interface when SBS 3710 dispersion is incomplete; this is traced to reduced mixing time below 60 min or bitumen temperature below 165°C, which leaves unswollen SBS particles that act as stress concentrators.

    Solvent evaporation gradients control open time in sprayed contact adhesives

    For solvent-borne contact adhesives used in furniture assembly and footwear upper bonding, SBS 3710 is dissolved in toluene, cyclohexane, methyl ethyl ketone, or acetone/toluene blends at 15–25 wt% solids. The solution viscosity is controlled between 2,000 and 8,000 mPa·s at 25°C by adjusting the ketone fraction; MEK content above 20 wt% of the solvent system lowers viscosity sharply but shortens wet layover time, creating dry edge failures on large-area laminates. Tackifying resin levels of 5–10 wt% on total solids are used to extend open time and improve bond formation to PU foams and PVC coated fabrics. The adhesive is applied by compression roller or spray gun at 80–150 g/m² wet film weight, force-dried at 50–60°C for 2–5 min, then mated under 0.3–0.6 MPa nip pressure. Peel strength is evaluated by ASTM D903 or ISO 11339 T-peel at 23°C. Compliance for industrial solvent emissions follows EU Directive 2010/75/EU and applicable local VOC limits; the adhesive itself, when formulated for indirect food-contact packaging, must comply with FDA 21 CFR 175.105. The main limitation is the low thermal resistance of the bond line: because SBS 3710 contains unsaturated polybutadiene, sustained service above 70°C in contact with high-sulfur substrates may lead to hardening and loss of peel. End products include foam-bonded shoe uppers, headliner laminates, and edge-banding contact adhesives. Published data for this specific solution formulation with SBS 3710 is limited; formulation adjustments must be validated on production-scale spray lines.

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    Certification & Compliance
    More Introduction

    Globalprene® SBS 3710, manufactured by LCY Chemical Corporation, is a linear styrene-butadiene-styrene block copolymer supplied as a neat thermoplastic elastomer. The material is positioned for bitumen modification, impact modification of styrenic and olefinic matrices, and solvent-borne adhesive systems. The polybutadiene midblock is unsaturated, so oxidative stabilization and end-use temperature limits must be evaluated under ISO 188 and ASTM D2000 service-class criteria before substitution into high-temperature or outdoor applications. Unlike hydrogenated styrenic block copolymers, 3710 offers lower melt viscosity and faster solution dissolution but requires antioxidant packages and controlled melt residence time. The product is characterized through ASTM D638 or ISO 527-2 for tensile properties, ASTM D2240 for Shore A hardness, ASTM D1238 or ISO 1133-1:2022 for melt mass-flow rate, and ISO 2453 for bound styrene content. Vendor-issued certificates of analysis control lot-specific values.

    Architecturally, the grade belongs to the low-styrene linear SBS segment, typically containing terminal polystyrene blocks in the range of 30–32 wt% and a mixed cis-1,4, trans-1,4, and 1,2-vinyl polybutadiene midblock. This composition yields lower Shore A hardness and lower tensile modulus than high-styrene SBS grades while increasing elongation at break and low-temperature flexibility. Compared with radial SBS grades, linear architecture reduces die swell in profile extrusion and lowers solution viscosity at equivalent solids content, but may reduce melt strength and creep resistance at elevated temperature. Because vinyl content and block molecular weight are production-lot variables, the polymer–solvent interaction parameter and order–disorder transition temperature in solution formulations should be re-established when changing supplier lots or production lines.

    What standard test matrix governs lot acceptance for Globalprene SBS 3710?

    Property classPreferred standard methodApplication relevance
    Melt mass-flow rateASTM D1238, ISO 1133-1:2022Lot-to-lot control in thermoplastic compounding
    Tensile stress at breakASTM D638, ISO 527-2Finished-compound mechanical acceptance
    HardnessASTM D2240, ISO 7619-1Elastomer phase stiffness and tactile specification
    Bound styrene contentISO 2453Architecture verification and compatibility
    Softening pointASTM D36High-temperature consistency in bitumen
    Storage stabilityASTM D5973Phase separation of polymer-modified asphalt
    Rotational viscosityASTM D4402Asphalt pumping and handling at 135 °C
    Notched Izod impact strengthASTM D256Toughening efficiency in plastics modification

    Pre-drying of the pellet or crumb is required when the material has been stored at relative humidity above 60%. Surface moisture can generate voids and reduce throughput in a co-rotating twin-screw extruder with L/D 40:1. A circulated-air hopper set at 60–70 °C for 2–4 h is commonly applied; SBS is less hygroscopic than polyamide or thermoplastic polyurethane, so dew-point control is usually less critical than uniform heat exposure. Barrel temperature profiles are ordinarily set between 160 °C and 190 °C, with die-head temperature controlled at 190–200 °C. Continuous operation above 210 °C accelerates oxidation of the unsaturated diene phase and gel formation, particularly when residence time exceeds 90 s. For production-scale compounding, a co-rotating twin-screw extruder with L/D 32:1 to 44:1 and atmospheric or vacuum devolatilization is specified to remove residual process oils and low-molecular-weight oligomers. Screw configurations should place kneading blocks after the primary feeding zone to limit shear heating; melt temperature at the die plate should be logged against screw speed and specific mechanical energy input. Injection molding of compounds containing 3710 generally uses melt temperatures of 180–200 °C and mold temperatures of 20–40 °C. Apparent viscosity at gate shear rates above 1,000 s⁻¹ can be measured by capillary rheometry according to ASTM D3835. Maximum recommended melt hold-up time in the barrel is 5 min at melt temperature above 190 °C to limit gel formation and yellowing.

    Raw-material storage should be maintained below 40 °C in a dry, ventilated area. Direct sunlight and ozone exposure should be avoided because the unsaturated midblock undergoes surface oxidation and may form a crosslinked skin on pellets or crumb. In thermoplastic compounds, 0.1–0.5 phr of a hindered phenolic antioxidant and 0.1–0.3 phr of a phosphite co-stabilizer are typically added during compounding to preserve melt stability and retention of color. Amine-based additives are not preferred with SBS in sulfur-curing systems because they can interfere with vulcanization kinetics and promote premature crosslinking during high-shear mixing.

    In solvent-borne adhesive compounding, Globalprene 3710 is dissolved in aliphatic, cycloaliphatic, or aromatic hydrocarbon solvents at solids contents of 20–40 wt%. The linear architecture supports lower Brookfield viscosity at 25 °C than radial SBS grades, which can reduce solvent demand in spray-applied contact adhesives. Tackifier addition with C5 hydrocarbon resins at 80–120 phr shifts the glass transition temperature of the polybutadiene phase and alters peel adhesion measured by ASTM D6862 or ISO 8510-2. Because the diene midblock is unsaturated, adhesive solutions require antioxidant packages at 0.5–1.5 phr and nitrogen blanketing during storage above 40 °C to suppress viscosity drift. Solvent selection is governed by Hansen solubility parameters; aromatic content below 10% may be used for low-odor formulations, but dilution can cause micelle formation and viscosity anomalies if the aliphatic concentration is raised without phase-diagram verification.

    Chemical resistance of Globalprene SBS 3710 follows the solubility behavior of polystyrene and polybutadiene blocks. Aromatic hydrocarbons, chlorinated solvents, and ketones attack the polystyrene domains, causing softening or dissolution; aliphatic hydrocarbons swell the polybutadiene phase. The material is not recommended for continuous contact with strong oxidizing acids, mineral acids above 10% concentration, or ester-based hydraulic fluids at elevated temperature. For compounded articles, resistance is validated by immersion testing under ISO 1817 or ASTM D471 using the actual service fluid and temperature.

    Bitumen modification windows and storage-stability testing

    Modification of paving-grade bitumen with 3–7 wt% Globalprene 3710 is performed in a high-shear rotor-stator mill at 170–190 °C. The polymer is dry-blended with bitumen preheated to 165–175 °C and dispersed until fluorescence microscopy no longer shows visible polymer agglomerates above 10 µm. Dispersion time is typically 45–180 min depending on bitumen aromaticity, disperser tip speed, and batch size. Storage stability is evaluated by ASTM D5973; after 48 h at 163 °C, the softening point difference between the top and bottom sections should not exceed 2.5 °C for stable hot storage. Softening point is measured by ASTM D36, penetration by ASTM D5, and rotational viscosity by ASTM D4402 at 135 °C and 165 °C using a Brookfield Thermosel. Higher-styrene SBS grades produce greater high-temperature stiffness, whereas 3710 provides lower mixing viscosity and improved low-temperature flexibility. Formulations that require both rutting resistance and storage stability may incorporate sulfur at 0.1–0.2 wt% or reactive crosslinkers to build network strength; this practice increases viscosity and shortens workable storage life.

    The sulfur-crosslinked network formed during hot storage can be monitored by measuring elastic recovery according to ASTM D6084 and by observing the disappearance of the polymer-rich phase under fluorescence microscopy. Elastic recovery for SBS-modified bitumen at 25 °C commonly exceeds 70% when the polymer network is fully developed, but this value depends strongly on bitumen source and polymer content. Crosslinking with elemental sulfur at 0.1–0.2 wt% produces sulfide bridges in the polybutadiene phase and increases the softening point; excessive sulfur or temperatures above 190 °C can induce gelation and uncontrollable viscosity increase in the storage tank.

    Relative to ethylene-vinyl acetate-based bitumen modifiers, SBS 3710 imparts higher elastic recovery and lower temperature susceptibility, but requires high-shear mixing and is more prone to oxidative degradation during extended hot storage. Compared with hydrogenated SEBS, the unsaturated polybutadiene midblock of 3710 enables faster sulfur crosslinking but lowers the continuous use temperature ceiling. In polymer-modified asphalt, long-term aging is assessed by ASTM D2872 rolling thin-film oven exposure followed by ASTM D4402 viscosity and ASTM D5 penetration retention. Published data for 3710 in some geographic binder grades and aggregate compatibility tests is limited; plant trials on the specific bitumen source are required to establish compatibility and storage hysteresis.

    Rheologically, the linear architecture of 3710 produces a terminal Newtonian plateau in small-amplitude oscillatory shear testing at 180 °C. The zero-shear viscosity is a strong function of total molecular weight; a shift of 10–15% in molecular weight can alter zero-shear viscosity by a factor of 2–3 due to the power-law dependence of linear polymer diffusion. This sensitivity requires melt-flow monitoring at receiving and during compounding. In contrast, radial SBS grades exhibit broader molecular weight distribution and higher storage modulus at low frequency, which can provide better dimensional stability in extruded profiles but increases torque in high-shear asphalt mixing.

    Impact modification of polystyrene and high-impact polystyrene feedstock with Globalprene 3710 is conducted at addition levels of 5–15 wt%. Compounding is performed in a co-rotating twin-screw extruder with L/D 32:1 to 44:1 and vacuum devolatilization. The dispersed SBS phase is sensitive to over-shear; screw-speed ramps and melt-temperature logs are used to preserve elastomer domain size above the critical threshold for craze stabilization. Notched Izod impact strength is measured under ASTM D256 at 23 °C and -30 °C, while tensile properties are determined per ISO 527-2. For polypropylene impact modification, the incompatibility of terminal polystyrene blocks with the polyolefin matrix may require a compatibilizer or controlled vis-breaking; peroxide addition must be kept below 0.05 wt% to prevent crosslinking of the diene block during compounding. Capillary rheometry at 230 °C under ASTM D3835 is used to monitor blend viscosity and detect lot-to-lot shifts in SBS melt flow. Published data for this specific configuration is limited in engineering thermoplastics; design-of-experiment validation on production equipment is required to establish the processing window for each finished compound.

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