| HS Code | 749883 |
| Polymer Type | SEBS linear triblock copolymer |
| Styrene Content | 20 wt% |
| Density | 0.90 g/cm³ |
| Melt Flow Rate | 5 g/10 min at 230 °C/5 kg |
| Hardness | Shore A 65 |
| Tensile Strength | 25 MPa |
| Elongation At Break | 500% |
| 300 Modulus | 4 MPa |
| Bulk Density | 0.40 g/cm³ |
| Physical Form | Powder |
As an accredited Kraton Kraton™G SEBS G1646 V factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kraton™G SEBS G1646 V is supplied in 25 kg moisture-resistant bags, packed on standard shipping pallets. |
| Container Loading (20′ FCL) | Twenty-foot FCL container loading for Kraton™G SEBS G1646 V: securely packed chemical for safe, efficient ocean transport and handling. |
| Shipping | Kraton™ G SEBS G1646 V is supplied as solid thermoplastic elastomer pellets in moisture-barrier bags, multilayer sacks, or bulk containers. It is not regulated as dangerous goods for transport. Store and ship in a dry, moderate-temperature area, away from direct sunlight, moisture, and contamination. |
| Storage | Store Kraton™ G SEBS G1646 V in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep containers closed and labels intact; protect pellets from moisture, dust, and contamination. Use good housekeeping to prevent dust accumulation. Follow the manufacturer’s SDS and local regulations for safe storage and handling. |
| Shelf Life | Kraton G1646 V has a shelf life of 2 years from manufacture when stored in original packaging under cool, dry, recommended conditions. |
Kraton™ G SEBS G1646 V functions as the primary styrenic block copolymer in oil-extended thermoplastic elastomer compounds for soft-touch overmolding and medical device enclosures. The polymer is a linear S-E/B-S triblock with a nominal bound styrene content of 18 wt%; in a compounded melt, the polystyrene end-blocks form a physical network that is plasticized by paraffinic or naphthenic process oils, while the ethylene/butylene midblock retains elastic recovery after injection molding. In continuous twin-screw compounding, a representative formulation places 25–45 wt% G1646 V with 15–25 wt% polypropylene homopolymer, 30–50 wt% white mineral oil, and 0.2–0.5 wt% hindered phenolic antioxidant. The dry blend is metered into a co-rotating twin-screw extruder with L/D 40:1 and segmented screws; barrel temperatures are set from 170°C at zone 1 to 220°C at the die plate, and the oil is split-fed into zone 4 or zone 5 after the SEBS/PP melt seal has formed. If oil is injected before the melt seal, production lines commonly exhibit phase inversion, vent flooding, and screw surging, because the low-viscosity oil displaces the polymer melt and destabilizes the partially filled conveying zones. Pelletizing is performed by underwater die-face cutting with water temperature held below 30°C to prevent pellet agglomeration and tailing. The finished compound is injection molded at barrel temperatures of 190–230°C, mold temperature 25–50°C, and clamp force between 800 kN and 1,500 kN; at the upper melt-temperature boundary, residence time should remain below 5 min above 230°C to avoid chain scission in the ethylene/butylene midblock. Compliance for food-contact and medical-housing grades rests on 21 CFR 177.1810 for styrene block polymers, EU 10/2011 overall migration testing by EN 1186-1, and ISO 10993-5 cytotoxicity when the device-level biocompatibility file requires it. Mechanical verification follows ISO 37 for tensile strength and elongation, ISO 815-1 for compression set at 70°C, and ISO 48-4 for hardness. Finished components produced from this class of compound include overmolded hand grips on dental instruments, diagnostic monitor enclosures, infant care components, toothbrush handles, and power tool soft-grip overmolds, with Shore A hardness typically in the 25–75 range and compression set values below 35% at 70°C for oil-extended formulations.
Hot-melt pressure-sensitive adhesive formulations based on Kraton™ G SEBS G1646 V are constructed with 15–30 wt% SEBS, 40–60 wt% hydrogenated tackifying resin, 5–20 wt% plasticizing oil, and 0.5–1.0 wt% antioxidant. Hydrogenated C5 or C9 resins with softening points between 95°C and 110°C are selected because they associate with the ethylene/butylene midblock and lower plateau modulus without fully dissolving the polystyrene end-block network. Mixing is carried out in a jacketed sigma-blade mixer or a twin-screw hot-melt extruder at 150–180°C under nitrogen blanketing, with total hold time maintained below 45 min; production lots held above 180°C for longer than 60 min show viscosity drift and darkening due to oxidative chain scission, even with antioxidant protection. The adhesive is applied by slot-die coating or spiral-spray systems at coating weights of 10–50 g/m² onto nonwoven, polyethylene film, or medical tape substrates. When coating temperature exceeds 170°C, interfacial failure at the substrate interface becomes more frequent than cohesive failure within the adhesive layer, because the tackifier-oil phase loses viscosity and the SEBS network cannot maintain sufficient plateau modulus at low shear rates to retain peel force on low-energy surfaces. Compliance for indirect food-contact adhesive applications is evaluated under FDA 21 CFR 175.105, while EU 10/2011 is applied for plastic layers and FINAT FTM 1 or PSTC 101 are used for peel and loop tack verification. Terminal product types include disposable diaper elastic attachment adhesives, feminine hygiene positioning strips, medical dressing transfer films, and automotive interior trim assembly adhesives subject to VDA 278 VOC and FOG limits.
Kraton™ G SEBS G1646 V is added to polypropylene homopolymer and impact copolymer melt streams to produce impact-modified injection molding grades and soft-feel automotive interior TPO compounds. The addition ratio is normally 5–15 wt% SEBS, with 0.1–0.3 wt% antioxidant and optional 5–10 wt% talc or calcium carbonate when dimensional stability is required. Compounding is performed on a co-rotating twin-screw extruder with L/D 36:1–44:1, with melt temperature controlled between 200°C and 230°C; the SEBS is often side-fed after the primary melting zone to avoid excessive viscous heating and to keep the elastomer domain size uniform. Injection molding of the compound at melt temperatures above 230°C can reduce melt elasticity and cause gloss variation on ribs and bosses; at SEBS contents above 15 wt%, screw recovery time increases noticeably because the compound shifts toward shear-thinning elastic flow, and thin-wall filling may require higher holding pressure. Verification of mechanical properties follows ISO 179-1 or ISO 180 for notched impact, ISO 178 for flexural modulus, and ISO 1133-1 for melt flow rate at 230°C/2.16 kg. Automotive interior compliance is checked through ISO 3795 horizontal burning, VDA 278 VOC and FOG, and REACH Annex XVII restrictions; food-contact PP-based compounds require EU 10/2011 and FDA 21 CFR 177.1520 evaluation. Finished product types include door panel soft-feel inserts, center console side cushions, appliance vibration dampers, and refrigerator door gaskets where the compound provides low-temperature impact retention.
| Downstream application | Regulation or specification | Verification method | Boundary condition |
|---|---|---|---|
| Soft-touch TPE medical/consumer compound | 21 CFR 177.1810, EU 10/2011 | EN 1186-1, ISO 10993-5 | Non-implant housing; no amine-based additives in autoclavable grades |
| Hot-melt pressure-sensitive adhesive | FDA 21 CFR 175.105 | FINAT FTM 1, PSTC 101 | Hold time below 45 min at 150–180°C |
| PP impact/TPO modification | ISO 3795, VDA 278 | ISO 179-1, ISO 1133-1 | SEBS addition ≤15 wt% to avoid screw recovery loss |
| Wire and cable jacketing | IEC 60332-1-2, UL 1581 VW-1 | IEC 60754-1, IEC 61034 | Flame-retardant filler loading ≤60 phr for stable die-head pressure |
| Footwear foam | REACH Annex XVII | ISO 17707, ISO 20871 | Premature peroxide decomposition below 130°C during compounding |
| Bituminous waterproofing | EN 13707, EN 13969 | ASTM D36, ASTM D5 | Mastic viscosity ≤4,000 mPa·s at 180°C |
Flexible low-voltage insulation and jacketing compounds based on Kraton™ G SEBS G1646 V are formulated with 15–30 wt% SEBS, 20–40 wt% ethylene-vinyl acetate copolymer containing 18–28 wt% vinyl acetate, 20–40 wt% linear low-density polyethylene, 30–60 phr magnesium dihydroxide or ammonium polyphosphate flame retardant, 5–10 wt% process oil, and 0.3–0.5 wt% antioxidant. The formulation is mixed in a co-rotating twin-screw extruder with L/D 40:1 at 180–210°C; the flame-retardant filler is introduced through a side-feed port after the polymers are melted to avoid abrasive wear in the primary feed zone and to maintain filler dispersion. After underwater pelletizing, the compound is extruded through a single-screw extruder with L/D 24:1–30:1 and a crosshead die at melt temperatures of 175–205°C; the tubular jacket is drawn through a water trough and spark-tested before rewinding. A production bottleneck observed at side-feed filler loadings above 60 phr is the sharp rise in melt viscosity at shear rates below 10 s⁻¹, producing die-head pressure instability, surface sharkskin, and inconsistent concentricity. Compliance verification for low-voltage flexible cords includes IEC 60332-1-2 or IEC 60332-3-24 for flame spread, IEC 60754-1 for halogen acid gas content, IEC 61034 for smoke density, UL 1581 VW-1 for vertical flame performance, UL 62 for flexible cord jacket physical properties, and RoHS 2011/65/EU for restricted substances. Finished product types include flexible cords for household appliances, medical power supply cables, industrial robot drag chain cables, and outdoor electric vehicle charger cable jackets where low-temperature flexibility remains a specified requirement.
Kraton™ G SEBS G1646 V modifies EVA-based injection midsoles when the compound requires both low density and improved low-temperature flex crack resistance. A typical addition is 10–20 phr SEBS in a system containing EVA with 18–28 wt% vinyl acetate, 5–10 phr polyolefin elastomer, 0.5–1.0 phr dicumyl peroxide, 2–4 phr azodicarbonamide blowing agent, and 0.1–0.3 phr antioxidant. Compounding is performed in a twin-screw extruder with barrel temperature held below 130°C to prevent premature peroxide decomposition; the pelletized compound is then injection molded or compression molded at 170–185°C to initiate simultaneous crosslinking and foaming. Compliance for footwear components is assessed through REACH Annex XVII restrictions, ISO 17707 flex resistance, and ISO 20871 abrasion resistance. Terminal product types include casual footwear midsoles, orthotic inserts, and low-density sandals with typical foam density of 0.35–0.55 g/cm³.
Polymer-modified bitumen for self-adhered roofing, bridge deck waterproofing, and below-grade damp proofing incorporates Kraton™ G SEBS G1646 V at 5–12 wt% of the total compound, with 55–75 wt% penetration-grade bitumen, 15–30 wt% limestone filler, and 0.1–0.3 wt% antioxidant. The SEBS is added slowly to a heated high-shear rotor-stator mixer or modified asphalt plant at 180–200°C, after the bitumen has reached 180°C, to prevent agglomeration at the mixer wall. Viscosity is monitored at 180°C using a rotational viscometer; when mastic viscosity exceeds 4,000 mPa·s at 10 rpm, the compound becomes difficult to pump through the coating head and membrane thickness variation increases on the carrier line. The mixed compound is calendered or cast onto polyester or glass-fiber carrier and cooled at a controlled rate below 5°C/min to maintain the elastomeric network structure instead of allowing continuous bitumen phase separation. Compliance for waterproofing sheets is verified under EN 13707, EN 13969, ASTM D36 for softening point, and ASTM D5 for penetration. Terminal product types include self-adhered torch-free roofing membranes, bridge deck waterproofing sheets, pipe coating tapes, and below-grade damp proof courses. Published industrial data for G1646 V in this specific bitumen configuration is limited compared with SEBS grades marketed for bitumen modification, so pilot-scale phase inversion and low-temperature flexibility trials are necessary before production commitments.
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Kraton™ G1646 V is a linear styrene-ethylene/butylene-styrene block copolymer supplied in dense pellet form. The polymer is based on a styrene hard block and a hydrogenated ethylene/butylene soft block; supplier literature commonly reports a styrene mass fraction near 19 %, a specific gravity of 0.90 g/cm³ when measured by ASTM D792, and a Shore A hardness of 42 after 10 s per ASTM D2240. The grade is differentiated within the Kraton G series by its relatively high molecular weight, low hardness without oil extension, and high elongation at break, typically reported in the range 700–800 % under ASTM D638-14. The product is intended for compounding, polymer modification, adhesive and sealant formulations, and soft-touch thermoplastic elastomer systems.
The following typical values are compiled from publicly available supplier technical data and should not be interpreted as batch-release specification limits. Injection-molded or compression-molded specimen geometry, conditioning time, and test speed can shift the reported values, particularly for tensile and elongation measurements.
| Property | Typical value | Test method |
|---|---|---|
| Styrene content | 19 % | Supplier-reported mass-balance method |
| Specific gravity | 0.90 g/cm³ | ASTM D792 |
| Hardness | 42 Shore A | ASTM D2240 |
| Tensile strength at break | 22 MPa | ASTM D638-14 |
| Elongation at break | 730 % | ASTM D638-14 |
| Melt flow rate | 3 g/10 min at 230 °C/5 kg | ISO 1133-1:2022 |
| Modulus at 300 % elongation | 3.0 MPa | ASTM D638-14 |
Compounding operations typically expose G1646 V to co-rotating twin-screw extrusion with segmented screw elements at length-to-diameter ratios of 40:1 or greater. At barrel setpoints between 180 °C and 220 °C, the polymer is melted in the first kneading zones before paraffinic oil is injected downstream through a gear pump or positive-displacement metering system. Injection of oil before complete melting produces torque instability and can reduce dispersion of the polystyrene end-blocks; the resulting morphology shows hardness variation across the extrudate. On start-up, operators frequently observe torque excursions if the feed throat temperature falls below 170 °C because the high-molecular-weight SEBS does not develop sufficient shear thinning at low melt temperature. For this reason, screw designs with aggressive kneading blocks are generally favored over all-conveying screw profiles. Published data for specific extruder diameter and screw speed combinations is limited; therefore, process settings should be developed on a pilot line with identical L/D and screw configuration.
The higher mixing energy of G1646 V relative to oil-extended SEBS compounds follows from the absence of a pre-added plasticizer phase in the pellet. Oil-extended grades carry a paraffinic or naphthenic oil that lowers the bulk viscosity and permits lower extrusion torque at standard screw speeds. In neat G1646 V, the ethylene/butylene midblock remains entangled and requires greater specific energy input to achieve melt homogeneity; compounding lines therefore record higher specific energy per kilogram when the same throughput is maintained. Addition of 50–100 phr of paraffinic oil restores processability, but the oil should be introduced incrementally across two or three downstream ports to avoid phase inversion and oil exudation. The melt flow rate, measured at 230 °C/5 kg under ISO 1133-1:2022, is typically reported near 3 g/10 min; this value places G1646 V in the low-flow category of the Kraton G series and explains why injection molding requires higher melt temperatures and larger gates than SBS or lower-viscosity SEBS grades.
In thermoplastic elastomer compounds, G1646 V is dry-blended with polypropylene homopolymer, paraffinic white oil, and a phenolic or phosphite antioxidant package before twin-screw compounding. The hydrocarbon resin and filler loadings are adjusted to meet Shore A hardness targets between 40 and 70; the tensile and tear properties are measured under ASTM D412 or ASTM D638-14 depending on the compound hardness. Compounders targeting soft-touch grips often combine G1646 V with 0.5–1.0 wt% of a polypropylene homopolymer to increase upper service temperature without sacrificing surface matteness. The compound should be pre-dried at 70 °C for 2–4 h when pellet surface moisture is present, particularly at relative humidity above 60%, to prevent splay and inconsistent surface finish. Published data for this specific configuration is limited for highly filled compounds, so the maximum filler loading should be determined through response-surface trials rather than linear extrapolation.
In hot-melt and solvent-borne adhesive formulations, G1646 V is dissolved or plasticized with hydrogenated tackifying resins and low-aromatic paraffinic oil. Hydrogenated tackifier compatibility is assessed by dynamic mechanical analysis of the adhesive film; phase separation appears as a secondary tan-delta peak and should be avoided by using hydrogenated C5/C9 resins rather than high-aromatic rosin esters. Adhesive formulations prepared at 20–40 % solids in toluene or methylcyclohexane require high-shear mixers with jacketed heating to maintain solution viscosity below 10,000 mPa·s for web coating. The stock solution stability depends on moisture exclusion and antioxidant addition, typically 0.1–0.3 % of a hindered phenolic antioxidant by total polymer mass. Because G1646 V is not pre-plasticized, the formulator has more freedom to choose the oil and tackifier system than with oil-extended SEBS, but the final adhesive properties should be measured under ASTM D1876 for peel strength and ASTM D3654 for shear adhesion failure temperature.
Outdoor profiles, window seals, and soft-touch surfaces expose the polymer to ultraviolet radiation, ozone, and thermal oxidation. Under ASTM G154 UVA-340 cyclic weathering, saturated midblock SEBS grades such as G1646 V generally exhibit less surface cracking and lower delta-yellowness index than unsaturated SBS formulations at equal Shore A hardness. This difference becomes visible after 500–1000 h accelerated weathering, although the exact threshold depends on the co-stabilizer package and pigment loading. Replacement of SBS with G1646 V in such profiles requires an increase in processing temperature from the 150–180 °C range typical of SBS to the 180–220 °C range required for SEBS; screw speed and back pressure should be reduced to avoid excessive shear heating. The improved weatherability is accompanied by higher compound cost and lower flow, so the substitution is usually justified only where service life exceeds five years or where ozone resistance is specified by DIN 53509 or equivalent test methods.
The product occupies a low-styrene, high-elongation position within the Kraton SEBS portfolio. Higher-styrene grades such as those with styrene contents near 30 % provide greater tensile strength, higher hardness, and better upper service temperature, but they require more oil to soften and exhibit higher set. G1646 V at 19 % styrene yields a softer, more elastic base polymer with less rigid polystyrene domain continuity, which lowers hardness but also reduces tensile strength relative to high-styrene grades. Compared with SBS, the hydrogenated midblock of G1646 V removes main-chain unsaturation, improving resistance to oxidative and ozone attack; however, the hydrogenation also raises the glass transition of the rubber phase and increases melt viscosity at equivalent molecular weight. Against oil-extended SEBS grades, G1646 V offers greater flexibility in compound formulation because the compounder controls the paraffinic oil level rather than starting with a pre-oiled pellet. The trade-off is higher mixing energy and lower melt flow, requiring intensive twin-screw compounding rather than simple low-shear blending.
End-use compliance is not conferred by the polymer alone; additives, pigments, fillers, and final processing conditions determine the regulatory status of the finished article. The following checklist identifies the principal standards that may apply when G1646 V is used in consumer, industrial, or medical products.
| Standard or regulation | Scope | Verification requirement |
|---|---|---|
| FDA 21 CFR 177.1810 | Styrene block copolymer food-contact uses | Confirm grade-specific suitability with supplier; extraction testing may be required for end-use conditions |
| REACH (EC) No 1907/2006 | EU chemical registration and downstream user obligations | Substance registration must be validated by the EU importer or legal entity placing the compound on the market |
| RoHS 2011/65/EU | Restricted heavy metals in electrical and electronic articles | Neat polymer typically contains no intentionally added restricted metals; compound additives require screening |
| ISO 10993-1:2018 | Biological evaluation of medical devices | Not an intrinsic resin approval; finished-device testing depends on patient contact duration and route |
| USP Class VI | Plastics for pharmaceutical contact | Must be demonstrated on the final article after sterilization and post-processing |
Storage of G1646 V under high-humidity conditions does not typically lead to bulk hydrolysis, but surface moisture can be absorbed on pellet surfaces. Strongly aromatic process oils, chlorinated paraffins, and certain amine-based antioxidants should be avoided or evaluated individually because they can alter oxidative stability, cause discoloration, or reduce upper service temperature. The product should be kept away from open flame and high-temperature sources exceeding 260 °C for extended periods because SEBS degradation can generate volatile decomposition products. Published data for the specific combination of G1646 V with halogenated flame retardants or peroxides is limited; such formulations require laboratory-scale torque and thermal stability screening before production trials.