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LG Chem SBS LG-512

    • Product Name: LG Chem SBS LG-512
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 716983
    Manufacturer LG Chem
    Grade LG-512
    Product Family SBS
    Polymer Type styrene-butadiene-styrene block copolymer
    Block Structure linear triblock
    Melt Flow Rate Condition 200°C/5 kg

    As an accredited LG Chem SBS LG-512 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LG Chem SBS LG-512 is supplied in 25 kg moisture-resistant bags, palletized and shrink-wrapped for safe storage and transport.
    Container Loading (20′ FCL) LG Chem SBS LG-512 loaded in a 20′ FCL, palletized bags secured with straps and moisture protection for safe ocean transport.
    Shipping LG Chem SBS LG-512 is typically shipped as a non-hazardous thermoplastic elastomer in sealed bags or FIBCs. Use clean, dry, covered containers; protect from moisture, heat, direct sunlight, and contamination. No UN number or dangerous-goods class normally applies; follow SDS and local transport regulations.
    Storage Store LG Chem SBS LG-512 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and oxidizing materials. Keep containers or bags tightly closed to prevent moisture and contamination. Avoid prolonged high-temperature and UV exposure. Protect packaging from damage, maintain clean handling conditions, use first-in, first-out rotation, and do not store near food or feed.
    Shelf Life LG Chem SBS LG-512 typically has a 24-month shelf life when stored cool, dry, and away from direct sunlight.
    Application of LG Chem SBS LG-512

    LG Chem SBS LG-512 is a linear styrene-butadiene-styrene block copolymer whose polystyrene end-blocks form physically cross-linked domains in the melt and solid state, while the polybutadiene mid-block imparts extensibility and low-temperature flexibility. The linear architecture produces lower zero-shear viscosity and a different shear-thinning response compared with radial SBS grades of similar styrene mass fraction, which affects rotor-stator dispersion, injection pressure, and solvent dissolution. Downstream use is concentrated in six documented commercial routes: bitumen modification, torch-on waterproofing membranes, footwear TPE compounding, hot-melt pressure-sensitive adhesives, polypropylene impact modification, and soft-touch injection molded goods. All formulation percentages below are stated as mass percentages unless indicated as phr; the certificate of analysis for the supplied lot should be used to confirm melt-flow rate and styrene mass fraction before scale-up.

    Bitumen Modification and Storage Stability Limits

    Polymer-modified bitumen for dense-graded highway wearing courses, stone mastic asphalt, and airport pavements uses LG-512 at 3.5–5.5 wt% of the total binder when the base bitumen penetration is 60/70 or 80/100 measured under ASTM D5-06. The dosage is set at the lower end for high-temperature storage stability and at the upper end when the project requires a ring-and-ball softening point above 60°C under ASTM D36-95. Industry compliance for the finished PMB follows EN 14023:2010 for European supply and ASTM D5976-00 or AASHTO M 320-17 for North American specifications; the latter evaluates performance grade after rolling thin-film oven aging and pressure aging vessel conditioning. The production process passes base bitumen through a high-shear rotor-stator mixer, typically a Siefer Trigonal or Silverson unit with tip speed 20–30 m/s and rotor gap 0.3–0.6 mm, at 175–185°C for 30–60 min. After the polymer particle size drops below 10 μm and the torque curve stabilizes, the batch is transferred to a low-shear maturation tank at 160–170°C. If a storage-stable PMB is required, elemental sulfur or a sulfur-donor package is metered at 0.05–0.15 wt% of the binder to induce partial cross-linking of the polybutadiene phase; the mixer must not be re-engaged at high shear after sulfur addition because gel particles above 1 mm can appear. The operational boundary is 200°C; below that limit oxidative chain scission is manageable with the bitumen's natural antioxidant fraction, above it the softening point reverts and viscosity at 135°C under ASTM D4402-19 falls below the target window of 1.5–4.0 Pa·s. Terminal finished products derived from LG-512 PMB include hot-mix asphalt for motorway wearing course, SMA binder course, airport apron pavement, bridge deck waterproofing tack coat, and high-temperature climate PG 70-22 binder.

    In elastomeric bitumen waterproofing membranes, LG-512 is incorporated into a compound of straight-run bitumen, mineral filler, and stabilizer before being coated onto a polyester or glass-fleece carrier. The SBS content of the membrane compound is held at 8–12 wt%; below 8 wt% the low-temperature flexibility and tensile elongation required by EN 13956:2012 and ASTM D5147-18 are not consistently achieved, while above 12 wt% the compound viscosity at 180°C interferes with calender penetration into the reinforcement. Production compliance for polymer-modified bituminous sheet products additionally references ASTM D6298-16 for sheet property consistency. The production sequence uses a vertical or horizontal high-shear mixer at 170–190°C for 45–90 min, after which the melt is pumped to a two-roll or three-roll calender and applied to the carrier at line speed 5–20 m/min. The finished sheet is cooled to 30–40°C before winding to prevent blocking. Terminal products include torch-on roofing membranes, self-adhesive cold-applied membranes, plaza deck waterproofing, and below-grade foundation waterproofing sheets.

    What Controls Oil Migration and Compression Set in Footwear Compounds?

    LG-512 functions as the primary elastomeric phase in oil-extended TPE compounds for injection-molded footwear components. The formulation addition ratio for LG-512 is 25–40 phr, with naphthenic process oil at 15–30 phr, crystal polystyrene at 5–15 phr, and calcium carbonate at 0–20 phr; a styrene-ethylene-butadiene-styrene compatibilizer may be added at 0–10 phr to raise melt compatibility. Regulatory compliance for EU footwear compounds includes REACH 1907/2006 Annex XVII restrictions on polycyclic aromatic hydrocarbons in extender oils. Batch compounding is performed in an intermeshing or tangential internal mixer, such as a Banbury type, with fill factor 0.75–0.85, ram pressure 0.4–0.6 MPa, and drop temperature 140–155°C. The dumped batch is sheeted on a two-roll mill at 130–140°C, then strip-fed to a strand pelletizer. Injection molding of unit soles and midsoles uses a reciprocating screw machine with clamp force of 3–5 kN/cm² of projected area, barrel temperatures 160–190°C, mold temperature 25–45°C, and injection speed 30–80 cm³/s. Finished-part testing references ASTM D412-16 for tensile strength and elongation, ASTM D2240-05 for Shore A hardness, ASTM D1630-16 and DIN 53516-2018 for abrasion loss, and ASTM D395-18 for compression set after 22 h at 23°C and 70°C. Terminal product types include unit soles, midsoles, wedge soles, sport shoe sidewalls, anti-slip bottom plates, and indoor safety footwear components.

    In pressure-sensitive adhesive hot-melt production, LG-512 is melt blended at 20–35 wt% with C5 or hydrogenated C9 tackifier resin at 40–60 wt%, naphthenic or paraffinic process oil at 10–25 wt%, and a hindered phenolic-phosphite antioxidant package at 0.5–1.0 wt%. The mixer is an anchor or sigma-blade vessel heated to 150–170°C under nitrogen blanket; residence time above 175°C is limited to 60 min to avoid polybutadiene oxidation and shear viscosity drift. The molten adhesive is delivered through a slot-die coater to release liner or directly to paper and film substrates at coating weights between 25 g/m² and 50 g/m². Performance testing follows ASTM D3652-16 for shear adhesion failure temperature, ASTM D3330/D3330M-18 for peel adhesion, and ASTM D1876-08 for T-peel strength. Terminal products include carton sealing tapes, label stocks, envelope adhesives, and assembly adhesives for non-structural automotive interior parts.

    When LG-512 Is Introduced into Polypropylene Impact Modification at High Screw Speeds

    LG-512 is incorporated into homo-polypropylene at 5–15 wt% as a non-peroxidic impact modifier when the finished part must retain ductile failure below 0°C. The matrix polypropylene typically has a melt-flow rate of 10–25 g/10 min under ISO 1133-1:2022; at 10 wt% LG-512 loading, notched Izod impact strength under ISO 180:2019 commonly moves from 3.0 kJ/m² for the neat resin to 8–15 kJ/m² at 23°C, though the exact property shift must be confirmed on the specific PP grade and twin-screw configuration. Compounding is performed on a co-rotating twin-screw extruder with L/D 40:1, barrel temperatures 180–210°C, screw speed 350–600 rpm, vacuum venting at -0.08 MPa, and strand die pressure 2–4 MPa. LG-512 is introduced through a downstream side feeder at 3–5 D from the main feed to avoid excessive residence time in the melting zone; process oil may be injected at 0.5–2 wt% to lower strand swelling. Terminal product types include interior automotive trims, appliance housings, luggage shells, and caps and closures requiring low-temperature drop impact resistance. Relevant compliance for automotive and electrical applications includes REACH 1907/2006, RoHS 2011/65/EU, and the OEM-specific VOC/SVOC test procedures for interior cabin materials.

    Soft-touch injection molded grips and consumer articles are produced from dry-blended LG-512 compounds that use 30–50 phr SBS, 20–35 phr white mineral oil, 5–15 phr general-purpose polystyrene, and 0.5–1 phr phenolic antioxidant. When ambient relative humidity exceeds 60%, the pellets are pre-dried at 60–70°C for 2 h to prevent surface splay; barrel melt temperature is capped at 200°C to avoid butadiene chain scission. Injection parameters for a two-cavity grip tool include clamp force above 4000 kN, injection pressure 60–90 MPa, holding pressure 40–60 MPa, and total cycle time of 25–40 s. The finished articles are tested for Shore A hardness according to ASTM D2240-05 or ISO 868:2003, heavy metal migration under EN 71-3:2019 for toy applications, and substance restrictions under REACH 1907/2006 and RoHS 2011/65/EU. Terminal products include toothbrush handles, power tool overmolds, computer mouse side pads, remote-control battery covers, and toy components. Food-contact use is not assigned unless the compound is evaluated under FDA 21 CFR §177.1810 and the finished article meets the total non-volatile extractive limits.

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    Certification & Compliance
    More Introduction

    LG Chem SBS LG-512 is a linear styrene-butadiene-styrene block copolymer supplied in porous pellet form. The molecule is produced by anionic solution polymerization and comprises polystyrene terminal blocks covalently bonded to a polybutadiene central block. In the solid state, the polystyrene end-blocks segregate into glassy domains with a thermal relaxation range typically observed between 80 °C and 95 °C by dynamic mechanical analysis under ISO 6721-1. These domains act as physical crosslinks; the polybutadiene continuous phase provides elastic recovery at service temperatures from approximately −70 °C to 70 °C. Bound styrene content is specified on commercial control documents as 31.0 wt% ± 1.5 wt%, with the balance as polybutadiene. Density is measured under ISO 1183-1:2019 and is typically reported in the 0.93–0.95 g/cm³ band for linear SBS of this composition. The product is differentiated from radial SBS grades by its linear topology: lower low-shear melt viscosity, lower die-entry elasticity, and wider processing latitude in melt-compounded formulations. Published data for this specific configuration is limited; all lot-critical values should be confirmed against the manufacturer release certificate rather than generic SBS class tables.

    What Limits Melt Stability During High-Shear Compounding?

    Melt stability is governed by polybutadiene midblock unsaturation. The processing window recommended for linear SBS in this styrene range is 150–190 °C for injection molding and 160–200 °C for continuous extrusion, with residence times kept below 5 min. Above 210 °C, oxidative chain scission and double-bond crosslinking compete, producing simultaneous viscosity loss and gel formation. In a co-rotating twin-screw extruder with L/D 40:1 and segmented mixing elements, local shear heating in kneading blocks can raise polymer temperature by 15–25 °C above barrel set point. Therefore, barrel profiles typically rise from 120 °C in the feed zone to 180 °C at the die, with screw speed 250–400 min⁻¹ and specific mechanical energy input 0.15–0.30 kWh/kg for filled compounds. If regrind levels exceed 25 wt%, melt-flow variation under ISO 1133-1:2022 at 190 °C/5.0 kg should be monitored lot by lot.

    LG-512 is incompatible with strong oxidizers, concentrated mineral acids, and excessive free-radical initiators that are not part of a deliberate grafting sequence. The polymer is not hygroscopic; however, condensation on cold pellets fed into a hot screw can cause feed instability. Pre-drying is not normally required unless pellets have surface moisture above 0.1 wt% or are stored below 10 °C in high-humidity environments.

    Solution adhesive manufacturing with LG-512 commonly uses toluene, cyclohexane, or blends of toluene with ethyl acetate and methyl ethyl ketone. Solids content is set between 20 wt% and 40 wt% depending on application viscosity; typical solution viscosity at 25 wt% in toluene is reported in the 200–900 mPa·s range under Brookfield rotation at 20 min⁻¹. The shear-thinning character of the linear SBS solution is less pronounced than for radial grades, which allows more uniform roll-coating but may reduce wet tack in pressure-sensitive formulations unless a compatible tackifier such as a C5 or hydrogenated rosin ester is added at 40–80 phr. Drying of adhesive films above 60 °C can accelerate solvent evaporation but also promotes skin formation; use of a drying tunnel with staged airflow at 50 °C, 70 °C, and 85 °C reduces blisters. Residual solvent limits are set by the relevant end-use regulation such as EU 10/2011 or 21 CFR 175.300 depending on food-contact status.

    When LG-512 Replaces Radial SBS in Bitumen Modification, Mixing Torque and Storage Stability Must Be Revalidated

    Bitumen modification is among the largest-volume applications for linear SBS. A typical starting dosage of LG-512 in paving-grade bitumen is 3–6 wt%, milled into binder preheated to 170–180 °C with a high-shear colloid mill operating at 3000–5000 min⁻¹. Compared with radial SBS of similar styrene content, linear LG-512 disperses with lower torque and shorter grind times, often reaching a continuous polymer network after 45–90 min. The resulting polymer-modified binder is evaluated for softening point with ASTM D36, penetration with ASTM D5, elastic recovery under EN 14023, and performance grade according to AASHTO M 332. Storage-stability testing by EN 13399 measures separation under static heat; linear SBS grades can show larger softening-point differences than crosslinked or radial grades if base bitumen aromaticity is insufficient to keep the polybutadiene phase swollen.

    Lot-to-lot solution-viscosity variance influences the storage-stability result and the softening-point gain at fixed dosage. Incoming inspection should therefore trend the 25 °C toluene solution viscosity and melt-flow data together; a shift of more than 10% from the site baseline typically requires rebalancing the aromatic oil or reactive polymer content of the finished binder. This is a production-scale control point rather than a specification failure.

    For roofing membranes and waterproofing coatings, LG-512 may be compounded with mineral filler, antioxidant, and processing oil to yield torch-applied sheet with static load resistance tested under EN 1110 and low-temperature flexibility per EN 1109. The addition of 1–3 phr of a phenolic or phosphite stabilizer is required to suppress oxidation during prolonged high-temperature mixing, but published data for this specific configuration is limited.

    Differentiation of LG-512 from adjacent elastomer classes
    Polymer systemNetwork typeMelt processingOxidation resistance under ISO 188Principal limitation
    Linear SBS LG-512physical, glassy PS domainsyes, 150–200 °Cmoderate; requires stabilizerunsaturation; not for aerobic hot-oil contact
    Radial SBSphysical, star-branched PS domainsyes, 150–210 °Cmoderate; requires stabilizerhigher melt viscosity and die swell
    SEBSphysical, hydrogenated PS domainsyes, 180–240 °Chigh; retained tensile strength after 168 h at 100 °Chigher cost; lower compatibility with unsaturated tackifiers
    Random SBRchemical, sulfur or peroxide vulcanizationno; cures irreversiblymoderate to high depending on cure systemno melt recyclability
    EPDMchemical, sulfur or peroxide vulcanizationno; cures irreversiblyhighhigher viscosity and longer cure cycles

    In footwear-unit applications, LG-512 is commonly blended with general-purpose polystyrene, paraffinic or naphthenic oil, and mineral filler. A typical outsole compound may contain 100 phr SBS, 30–60 phr oil, 20–40 phr PS, and 10–30 phr silica or calcium carbonate. Mixing is conducted in an internal mixer or twin-screw extruder with drop temperature below 190 °C. Hardness is adjusted over 40–80 Shore A under ISO 868 by varying oil and PS ratio. Tensile strength and elongation are measured by ISO 37; tear strength by ISO 34-1; abrasion by ISO 4649. The linear structure of LG-512 provides lower melt viscosity and better flow into deep tread molds than radial SBS but may exhibit lower tear strength and less resistance to delamination at identical hardness. Non-marking compounds require replacement of carbon black with silica, because the polybutadiene phase readily adsorbs carbon black and can scuff.

    Sole injection molding with LG-512-filled compounds typically uses screw plastication units with 18:1–22:1 L/D and clamp force based on projected area; multi-impression sole molds often operate at 150–250 t clamp force. Mold temperature is held at 20–40 °C to reduce cycle time, but this increases flow resistance. The combination of linear SBS and naphthenic oil lowers injection pressure by 10–20% relative to radial SBS at equal hardness. However, frost-free part ejection requires reducing oil exudation through stabilizer selection and not exceeding oil loadings above the compatibility limit of the styrenic phase. Batch-to-batch melt-flow variation greater than 0.5 g/10 min under ISO 1133-1:2022 can shift injection pressure by 5–10%, so incoming inspection should include melt-flow and ash testing.

    Plastics Modification and Co-Continuous Morphology Requirements

    In rigid polymer modification, LG-512 is used to increase impact resistance and reduce brittle failure in general-purpose polystyrene or to compatibilise semicrystalline polyolefins. When melt-blended with GPPS at 5–20 wt%, the polystyrene terminal blocks mix with the matrix, whereas the polybutadiene midblock forms dispersed elastomer domains with a diameter range of 0.1–2.0 μm. Impact strength under ISO 179-1 improves only when domain size and interparticle distance are controlled; extruder screw design and shear history are therefore more decisive than simple let-down ratio. Co-continuity is attainable at higher SBS loading, but the transition concentration depends on viscosity ratio, not only composition. If the matrix is a polypropylene with high melt-flow rate, the viscosity ratio must be adjusted with oil or a high-molecular-weight grade of SBS to prevent phase inversion at low SBS content.

    Regulatory Status and Application Boundaries

    LG-512 is supplied under standard petrochemical safety data sheets. It is not a food-contact material by itself; food-contact status depends on the finished compound and applicable national or regional regulation. For European Union applications, compliance is assessed under EU 10/2011; for repeated-use rubber articles in the United States, 21 CFR 177.2600 may apply. The product is not classified as hazardous for supply under CLP Regulation EC 1272/2008, but processing releases small amounts of volatile organic compounds and requires local exhaust ventilation. REACH registration under EC 1907/2006 is maintained by the manufacturer for the polymer raw material. RoHS compliance is evaluated under 2011/65/EU annex II; typical heavy-metal and brominated-flame-retardant concentrations are below maximum concentration values when supplied from virgin polymerization, but recyclate or compounded pigments can alter this result.

    Relevant compliance and test method designations
    Property or obligationStandard or regulationCondition or unit
    Melt mass-flow rateISO 1133-1:2022190 °C/5.0 kg
    DensityISO 1183-1:2019g/cm³
    Tensile propertiesISO 37MPa, %
    Tear strengthISO 34-1kN/m
    Abrasion resistanceISO 4649mm³
    HardnessISO 868Shore A
    Accelerated ageingISO 188100 °C/168 h
    Polymer-modified bitumenEN 14023, EN 13399softening point, storage stability
    Food-contact articlesEU 10/2011 or 21 CFR 177.2600finished article compliance required
    REACHEC 1907/2006SVHC 0.1 wt%

    For hot-melt adhesive and sealant systems, LG-512 is melt-blended at 140–180 °C with rosin ester or C5/C9 hydrocarbon resins, polyisobutylene or paraffin wax, and hindered phenolic antioxidant. Thermogravimetric analysis under nitrogen at 10 °C/min is used to confirm drying and decomposition boundaries; production equipment should not exceed 200 °C for extended runs. Applications requiring continuous service above 70 °C, contact with hot mineral oil, or repeated steam sterilization are better served by hydrogenated styrenic block copolymers because unsaturated polybutadiene segments undergo progressive hardening and loss of elongation under aerobic aging. Incoming inspection of LG-512 should measure melt-flow rate under ISO 1133-1:2022 at 190 °C/5.0 kg, ash under ISO 247, and bound styrene by Fourier-transform infrared spectroscopy calibrated against the manufacturer reference.

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