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Kraton Kraton™G SEBS G1633 ES

    • Product Name: Kraton Kraton™G SEBS G1633 ES
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 875627
    Product Name Kraton™ G SEBS G1633 ES
    Manufacturer Kraton Corporation
    Polymer Type SEBS (hydrogenated styrene-ethylene/butylene-styrene block copolymer)
    Molecular Structure linear triblock copolymer
    Styrene Content 30 wt% (typical)
    Physical Form powder
    Color white to off-white
    Density 0.91 g/cm3 (typical)
    Melt Flow Rate 5 g/10 min (typical, 230 °C/5 kg)
    Shore A Hardness 60 (typical)
    Tensile Strength 25 MPa (typical)
    Elongation At Break 600% (typical)
    Glass Transition Temperature styrene blocks about 100 °C; ethylene/butylene midblock about -55 °C (typical)
    Water Absorption low
    Hydrocarbon Resistance limited/poor
    Acid Base Resistance good
    Uv Oxidation Stability good due to hydrogenated midblock

    As an accredited Kraton Kraton™G SEBS G1633 ES factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Kraton™ G SEBS G1633 ES is packaged as pellets in 25 kg moisture-resistant bags, with 1,000 kg bulk bags available.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized 25 kg bags of Kraton G SEBS G1633 ES, shrink-wrapped and secured for ocean transport.
    Shipping Kraton™ G SEBS G1633 ES is typically shipped as non-hazardous polymer pellets in moisture-resistant bags, boxes, or bulk containers. Keep dry and away from direct sunlight, heat, and contamination. It is generally not classified as dangerous goods; follow local regulations and the SDS.
    Storage Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers tightly closed to prevent moisture, dust, and contamination. Avoid dust generation and accumulation; use grounding and bonding when handling bulk material. Maintain stable temperature, preferably below 50 °C, and store separately from incompatible materials. Follow local regulations and the safety data sheet.
    Shelf Life Shelf life is 24 months from manufacture when stored unopened in original packaging at temperatures below 30°C.
    Application of Kraton Kraton™G SEBS G1633 ES

    Compounding of Kraton™ G1633 ES into flexible medical tubing compounds is carried out on a co-rotating twin-screw extruder with 40:1 L/D ratio because the SEBS phase requires passing through one melting zone and two dispersive kneading blocks before polypropylene addition. A base formula uses 55 wt% G1633 ES, 42 wt% random copolymer polypropylene with melt flow rate 2.0 g/10 min at 230 °C/2.16 kg, and 3 wt% white mineral oil. The blend is pre-dried at 75 °C for 2 h when ambient relative humidity exceeds 60%. Single-screw extrusion into tubing on a 24:1 L/D extruder with a 2.5:1 compression ratio and a 60/80/100 mesh screen pack is operated with barrel zone set points of 160 °C, 185 °C, 205 °C, 210 °C, and die temperature 205 °C. The sizing vacuum is held at −0.25 bar, and the waterbath temperature is controlled at 20 °C. Annealing at 80 °C for 4 h after extrusion relaxes orientation stresses and reduces post-extrusion kink radius. If SEBS content falls below 45 wt%, peristaltic pump segments exhibit earlier flexural fatigue in the pinched zone, though published data for this specific formulation is limited. Cytotoxicity screening is conducted per ISO 10993-5:2009, and hemolysis is evaluated per ISO 10993-4:2017. The compound is not compatible with prolonged contact with aromatic hydrocarbons or with autoclave cycles exceeding 121 °C unless crosslinked or stabilised specifically for those conditions.

    What Limits Wall Thickness Stability in Coextruded Medical Film?

    When Kraton™ G1633 ES is used in the core layer of a three-layer blown film, the main constraint is not melt strength but die-lip deposit formation above 235 °C and the narrow solidification window of the SEBS phase. A 60 mm grooved-feed extruder runs the outer PP-random skins at 210 °C, while a 45 mm extruder delivers the core blend containing 25 wt% G1633 ES and 75 wt% PP random copolymer at 220 °C. The die gap is set to 1.0 mm, the blow-up ratio is 2.0:1, and the frost line is maintained at 200–300 mm above the die face. Melt pressure fluctuation at the die is held below ±1.5 MPa; excursions beyond this value on older barrel-temperature controllers produce visible gauge bands in the lay-flat film. Because SEBS is nonpolar, the finished film cannot be sealed by radio-frequency welding on standard PVC dielectric sealing machines. Instead, thermal impulse sealing is operated at 160–180 °C jaw temperature with 0.3–0.5 s dwell and 2.5 bar jaw pressure. Oxygen transmission is tested per ASTM F2622-21, and water vapour transmission per ASTM E96/E96M-24. Where oxygen ingress below 150 cm³/(m²·day) is required, the core must be supplemented with an EVOH barrier layer; Kraton™ G1633 ES contributes flexibility, clarity, and low extractables to the film, not primary barrier performance.

    Low-Haze Impact Modification of Clarified Random Copolymer Polypropylene

    Addition of Kraton™ G1633 ES to clarified random copolymer polypropylene is performed as a pellet blend at 10–20 wt% on a co-rotating twin-screw extruder with 36:1 L/D. The screw configuration can be limited to two kneading blocks downstream of the feed throat and one distributive mixer before the die to avoid excessive shear heating. Melt temperature is clamped at 215–225 °C; above 240 °C the styrenic endblock network loses structural integrity and haze control becomes inconsistent. For a 15 wt% SEBS loading, notched Izod impact strength measured per ISO 180:2023 at 23 °C on injection-moulded 2 mm specimens generally rises from 2.5–3.0 kJ/m² to 5.5–8.0 kJ/m² in comparable clear impact-modified PP systems, while haze per ASTM D1003-13 remains below 12% on the same plaque gauge. Tensile yield strength per ISO 527-2:2012 decreases, with a modulus drop of 15–25% relative to the unmodified PP. Food-contact suitability is not automatically granted by the resin supplier; migration testing under FDA 21 CFR 177.1810 and Commission Regulation (EU) No 10/2011 is required on the final article because additive packages and processing residues affect overall migration and specific migration limits.

    Hot-melt assembly adhesives based on Kraton™ G1633 ES are manufactured in a 50 L sigma-blade mixer because the high torque at 170–180 °C during initial tackifier incorporation requires a low-slip mixing bowl. The charge comprises 25 wt% G1633 ES, 55 wt% hydrogenated hydrocarbon tackifier, 18 wt% white mineral oil, and 0.5 wt% hindered phenolic antioxidant. The polymer is added last after the tackifier and oil reach 160 °C, preventing excessive thermal history on the SEBS endblock. Brookfield viscosity at 180 °C is controlled between 3,000 mPa·s and 6,000 mPa·s for slot-die coating onto polypropylene film. Tensile overlap shear per ASTM D1002-10 on PP-to-PET joints typically falls between 0.8 MPa and 1.5 MPa, with cohesive failure observed when the substrate surface energy exceeds 38 mN/m after corona treatment. Adhesion to untreated polyethylene remains weak; surface activation is required below 30 mN/m. The formulation is not suitable for fuel-contact adhesive lamination because aliphatic and aromatic hydrocarbons swell the SEBS midblock and cause bond softening within 24 h of immersion at 40 °C.

    When Two-Shot Moulding Requires Chemical Bonding to Engineering Thermoplastics

    Insert or two-shot moulding of Kraton™ G1633 ES onto polycarbonate/ABS substrates is processed with the SEBS barrel set at 190–220 °C and the substrate mould temperature maintained at 40–70 °C. Mechanical interlock alone is insufficient on smooth PC/ABS ribs; a tie layer of maleic anhydride-grafted polyolefin at 5–10 wt% in the SEBS compound improves adhesion by promoting polar interactions at the interface. Injection speed is set at 80–100 mm/s with a hold pressure of 600–800 bar; void formation in thick-section overmoulds is reduced by applying 2–3 s of gas counterpressure. Peel adhesion per ISO 11339:2022 on T-peel specimens with 25 mm bond width typically reaches 2–4 N/mm only after the tie layer is used; without it, adhesive failure occurs below 1 N/mm. Continuous service temperature is limited to 80 °C under load because compression set of the SEBS midblock per ASTM D395-18 method B rises above 30% after 22 h at 70 °C. The compound should not be used in direct contact with ketone-based cleaning agents or plasticised PVC gaskets without migration testing.

    Heat Seal Integrity in Cold-Formable Diagnostics Film Depends on Molecular Weight Distribution

    For thermoformed diagnostic lidding stock, 35 wt% Kraton™ G1633 ES in a cast film based on a metallocene-catalysed polyolefin is extruded on a 45 mm single-screw cast line with a 0.8 mm die gap and polished roll temperature set to 25 °C for low haze. The film is thermoformed at 100–120 °C into shallow trays and heat-sealed to PP microplates at 125–135 °C and 1.5 bar seal pressure for 1.0–1.5 s. Seal strength is measured per ASTM F88/F88M-21; peel force below 2.0 N/15 mm on uncoated PP after sealing indicates inadequate heat transfer through the SEBS-rich layer, which can be corrected by reducing film gauge from 250 μm to 180 μm or increasing the seal bar dwell by 0.3 s. Because G1633 ES has a low glass transition temperature, the film maintains flexibility at 4 °C, but the styrenic domains soften at autoclave temperatures. The film is not a primary moisture barrier; moisture vapour transmission per ASTM E96/E96M-24 on a 200 μm monolayer is above 5 g/(m²·day) at 38 °C and 90% RH, so silica gel or aluminium-foil lamination is required for moisture-sensitive reagents. Published data for this exact G1633 ES cast-film configuration is limited, and sealing equipment settings must be verified on the specific line because seal bar force distribution varies across microplate cavity densities.

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    Certification & Compliance
    More Introduction

    The product entry described here is Kraton Kraton™G SEBS G1633 ES, a linear triblock copolymer with polystyrene end-blocks and a saturated ethylene/butylene mid-block. The producer reports bound styrene at 30 mass%; this value is measured by a polymer-specific method and controls the room-temperature modulus and the onset of flow. Pellets are supplied with a specific gravity of 0.90–0.92 under ISO 2781. An unfilled compression-moulded plaque develops a hardness of 65–70 Shore A using ISO 48-4 with a 15 s dwell, while tensile strength at break is observed in the 28–32 MPa range and elongation at break in the 500–700% band under ISO 37. These values are a reference for a stabilizer-free moulded sheet, not a finished-compound specification, because cooling rate and specimen thickness influence the physical crosslink density of the styrene domains.

    Typical producer-reported properties of unfilled Kraton™ G SEBS G1633 ES
    PropertyTest methodTypical range
    Bound styrene contentProducer method30 mass%
    Specific gravityISO 27810.90–0.92
    HardnessISO 48-4 / ASTM D224065–70 Shore A
    Tensile strength at breakISO 3728–32 MPa
    Elongation at breakISO 37500–700%

    What Melt Processing Limits Apply on a Co-Rotating Twin-Screw Line?

    On an intermeshing co-rotating twin-screw extruder with a length-to-diameter ratio of 30:1 to 52:1, Kraton™ G SEBS G1633 ES is normally fed in the first barrel with polypropylene or another thermoplastic phase. Paraffinic oil is injected downstream of the first kneading block to prevent free oil in the feed throat and to avoid torque peaks associated with early plasticization. Because SEBS exhibits pronounced shear-thinning, barrel temperatures are maintained at 170–200 °C in the melting zone and 190–220 °C at the die. Melt temperatures above 240 °C should be limited to approximately 10 min residence time to reduce yellowing and gel formation. Reverse kneading elements are generally not required for this grade; when they are used for distributive mixing, screw speed is kept in the 200–300 min⁻¹ range. A documented production failure occurs when oil injection is positioned before the first melting peak. The resulting melt viscosity loss reduces the pumping efficiency of upstream screw elements and forces either a higher barrel temperature or a lower throughput. Moisture control is handled by pre-drying at 70 °C for 2 h in a desiccant dryer when ambient relative humidity exceeds 60%. Residual pellet moisture above 0.1 mass% can produce surface splay and microvoids in the extrudate; the saturated ethylene/butylene backbone is not hydrolytically degraded in the manner of polyester or polyamide.

    When Paraffinic Oil Loading Approaches 80 phr in Shore A Reduction

    In thermoplastic elastomer compounds where hardness is reduced by addition of a hydrogenated paraffinic or naphthenic process oil, the practical oil-absorption region is limited by the styrene domain network. Compounders report that at oil loadings above 80 phr, tensile strength falls below 5 MPa and compression set measured under ISO 815-1 at 70 °C climbs above 60%. These values indicate domain plasticization rather than a universal formulation ceiling. For a final hardness of 40–50 Shore A, typical formulations contain 50–70 phr of a hydrogenated paraffinic oil with a kinematic viscosity of 40–100 mm²/s at 40 °C under ISO 3104. Polypropylene is added at 20–30 wt% relative to the total polymer phase to restore upper service temperature and reduce surface tack. The oil is introduced through a single injection point after the first melting section; split injection across two ports is used above 60 phr to avoid free oil accumulation and screw slip.

    In polypropylene impact modification, the grade is used at 10–20 wt% relative to the total compound. The ethylene/butylene mid-block contributes energy absorption under ISO 180 notched Izod loading, while the saturated backbone limits melt-flow depression relative to high-molecular-weight SEBS grades. Published data for this specific grade in every polypropylene matrix is limited; compounders should not transfer an impact-modification ratio from one PP grade to another without a pilot trial. Injection-moulded parts are processed at a melt temperature of 190–220 °C, a mould temperature of 30–60 °C, and a clamping force sufficient to prevent flash at the selected wall thickness.

    Hot-melt sealant and adhesive mixtures based on Kraton™ G SEBS G1633 ES are compounded with hydrogenated hydrocarbon tackifiers having a ring-and-ball softening point of 85–105 °C under ASTM E28. The tackifier is added at 30–50 wt% of the total formulation to reduce the plateau modulus and produce pressure-sensitive tack. The saturated mid-block permits processing at 180–200 °C without the rapid odour generation observed with unsaturated SBS at the same temperature. Polar tackifiers such as rosin esters are kept below 10 wt% because the ethylene/butylene block is nonpolar; above that range, phase separation can produce haze and reduced shear strength. Batch mixing is performed in a planetary mixer or sigma-blade mixer at 160–190 °C with a thermal-oil jacket held at 180 °C. The most common production fault is cold-wall accumulation when polymer pellets are added too quickly to a partially filled mixer, creating ungelled particles in the final adhesive.

    The Saturation Difference Between SEBS and SBS in Outdoor Service

    The saturated mid-block is the main structural difference between Kraton™ G SEBS G1633 ES and styrene-butadiene-styrene block copolymers. SBS contains polybutadiene mid-block double bonds that can participate in thermal-oxidative crosslinking and chain scission; SEBS has no measurable olefinic unsaturation in the rubber block after selective hydrogenation. Under ISO 4892-2 xenon-arc weathering, SEBS compounds generally retain tensile elongation longer than equivalent-hardness SBS compounds, although exact retention times depend on UV stabilizer type and dosage. Published data for this specific grade at every irradiance level is limited. In comparison with higher-molecular-weight linear SEBS grades such as Kraton™ G1651 ES, Kraton™ G SEBS G1633 ES is selected where lower melt viscosity and faster dispersion in solvent-free hot-melt equipment are required. The concurrent limitation is lower high-temperature tensile strength and higher permanent set after extension. Lower-styrene SEBS grades may be softer but exhibit reduced upper service modulus and greater oil bleed at equivalent oil content; higher-styrene grades raise hardness but require more heat input during mixing.

    Regulatory assessments for Kraton™ G SEBS G1633 ES begin with the producer safety data sheet and the final article matrix. The raw polymer is not a finished food-contact article; end-use compliance depends on the formulated compound, processing history, migration testing, and any surface coatings applied after moulding. The table below lists the regulatory instruments most frequently checked when the grade is used in consumer goods, appliance seals, and packaging-adjacent elastomers.

    Typical compliance-check matrix for Kraton™ G SEBS G1633 ES as a raw polymer and in a final article
    Regulation or standardReference clause or methodAssessment basis
    EU REACHRegulation (EC) No 1907/2006, Title II registrationProducer SDS lists registration status; article obligations remain with the downstream user
    RoHS recastDirective 2011/65/EU, Annex IINo intentionally added Pb, Cd, Hg, Cr(VI), PBB, PBDE
    US food-contact21 CFR 177.1810Styrene block copolymers may be used subject to end-use and extractive limits; final article must be tested
    EU food-contact plasticsRegulation (EU) No 10/2011Overall migration tested on finished article under relevant OM conditions
    Heavy metalsIEC 62321 or EN 71-3Requires certificate of analysis from the compounder, not the raw polymer
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