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Kraton Kraton™MD SEBS MD4224 KU

    • Product Name: Kraton Kraton™MD SEBS MD4224 KU
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 587164
    Productname Kraton Kraton™MD SEBS MD4224 KU
    Polymertype Hydrogenated styrene-butadiene-styrene block copolymer (SEBS)
    Styrenecontent 42 wt% (typical)
    Physicalform Powder
    Specificgravity 0.91
    Bulkdensity 0.45 g/cm³
    Diblockcontent <1 wt%
    Shoreahardness 85 (typical)
    Tensilestrength 30 MPa (typical)
    Elongationatbreak 500% (typical)
    Meltflowrate 24 g/10 min (230°C/2.16 kg, typical)
    Volatilematter <0.5 wt%
    Ashcontent <0.1 wt%
    Particlesize ≤2 mm
    Color White to off-white

    As an accredited Kraton Kraton™MD SEBS MD4224 KU factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Kraton MD4224 KU SEBS is supplied in 25 kg moisture-resistant bags, palletized for industrial handling and storage.
    Container Loading (20′ FCL) Kraton™ MD SEBS MD4224 KU is palletized, shrink-wrapped, and securely loaded in a 20′ FCL container for ocean freight.
    Shipping Kraton™ MD SEBS MD4224 KU is not regulated as dangerous goods for transport. Ship in original sealed packaging, protected from moisture, heat, and sunlight. Keep cool, dry, and uncontaminated. No special UN number, hazard class, or packing group applies under standard transport regulations.
    Storage Store Kraton™ MD SEBS MD4224 KU in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizing agents. Keep containers tightly closed when not in use to prevent moisture ingress and contamination. Avoid dust generation and accumulation; use appropriate grounding if handling powders. Maintain good housekeeping and follow the supplier’s SDS and local regulations.
    Shelf Life Shelf life is typically 24 months from date of manufacture when stored in original, unopened packaging under cool, dry conditions.
    Application of Kraton Kraton™MD SEBS MD4224 KU
    In suction-truck discharge lines feeding a co-rotating intermeshing twin-screw extruder with shaft diameter 40 mm and L/D 40:1, pre-dried polyamide 6 pellets with moisture below 0.08 wt% are weight-loss dosed at 100 kg/h. Kraton MD4224 KU is metered into the main feed throat at 10–18 wt% of total polymer mass. The melt passes through a 10-zone barrel profile starting at 230 °C and peaking at 255 °C in the segmented kneading-block zones, with vacuum venting at -0.08 MPa downstream of the reaction zone. The maleic anhydride functionality on the saturated ethylene-butylene midblock opens and reacts with terminal primary amine groups at the polyamide interface within a residence time of 45–90 s. The resulting graft copolymer concentrates at the phase boundary and stabilizes a dispersed rubber particle size between 0.3 μm and 1.5 μm in glass-filled door-check brackets and powertrain cable clips. Notched Izod values measured per ISO 180:2023 or ASTM D256-23e1 move from brittle failure in the unfilled control toward ductile tearing at 23 °C once the addition level exceeds 8 wt%. Screening work on PA66 compounds generally targets 12–18 kJ/m² at 23 °C; values below 8 kJ/m² suggest insufficient interfacial grafting or excessive moisture. The operational ceiling is 285 °C. Barrel temperatures above this threshold promote anhydride elimination, succinimide decomposition, and polyamide thermo-oxidative reversion. The same feed throat should exclude amine-based heat stabilizers and multifunctional epoxy chain extenders because premature coupling can raise head pressure above 120 bar before the melt reaches the vacuum port.Polypropylene continuous-fiber glass sheet regrind and PA6 airbag chute regrind are co-fed at a 70:30 PP-to-PA6 mass ratio for garden power tool housings and wastewater pump covers. MD4224 KU is dry blended at 4–6 wt% and melt-mixed in a low-shear Buss kneader with shaft temperature 210 °C, screw speed 180–240 min⁻¹, and discharge head pressure below 80 bar. The maleated styrenic block copolymer accumulates at the PP-PA6 interface because the anhydride grafts react with PA6 terminal amines while the hydrogenated midblock remains miscible with the polypropylene matrix. This reduces interfacial tension, suppresses coalescence, and permits PA6 domain elongation into submicron lamellae rather than coarse spheres. Tensile properties are tested on ASTM D638-22 Type I specimens. The target is retention of at least 80% of the PP-rich matrix tensile strength and notched Izod improvement from 6 kJ/m² to 12 kJ/m² at 23 °C per ASTM D256-23e1. Melt temperatures below 220 °C fail to melt the PA6 regrind completely, while temperatures above 250 °C increase risk of maleic anhydride volatilization and PP oxidation. Because this feedstock is post-industrial, batch-to-batch moisture content varies and requires inline venting plus a dedicated hopper dryer set to 80 °C for nylon-rich fractions.

    What Limits the Two-Shot Bond Strength in Soft-Touch EV Charging Port Seals?

    The two-shot molding sequence uses a glass-filled PA66 first shot at melt temperature 270–290 °C and mold temperature 80–110 °C. The second shot contains 30–45 wt% MD4224 KU, 15–25 wt% polypropylene random copolymer, 30–45 wt% paraffinic process oil, 0.2–0.5 wt% hindered phenol antioxidant, and 0.3–0.7 wt% UV stabilizer. The compound is pelletized below 35 °C in a water bath to avoid oil exudation. Second-shot barrel temperatures are held at 190–220 °C, injection speed is 30–60 mm/s, holding pressure is 40–60 MPa, and mold temperature is 25–45 °C. Adhesion develops at the PA66-TPE interface through polar interaction between the maleated SEBS and the amide-rich substrate surface, but peel strength collapses if the PA66 surface cools below 120 °C before the second shot arrives. Lap shear values are measured per ISO 4587:2003. Target bond strength is above 4 MPa with cohesive failure in the TPE layer. Compression set is measured under ISO 815-1:2019 at 70 °C for 22 h; typical target is below 50%. The finished EV charging port gaskets and USB-C dust covers are assessed against RoHS 2011/65/EU, REACH SVHC obligations, and VDA 278 emission limits for automotive interior components.

    When Halogen-Free Sheath Compounds Approach 60 phr ATH but Retention Must Exceed 150%

    Halogen-free polyolefin sheath batches are mixed in a twin-screw extruder at 160–185 °C with aluminum trihydroxide filler fed in the mid-section at 50–65 phr. MD4224 KU is introduced as a coupling and impact-modifying component at 5–12 phr, together with 1–2 phr processing aid and 0.5 phr phenolic antioxidant. Melt temperature is kept below 190 °C because ATH begins endothermic dehydration in the 180–220 °C range. Screw speed is limited to 150–250 min⁻¹, and die pressure is held below 100 bar to reduce shear heating. Tensile strength and elongation at break are determined per IEC 60811-501:2012; the compound target is tensile strength above 10 MPa and elongation above 150%. Flame propagation is evaluated by IEC 60332-1-2:2015, smoke density by IEC 61034-2:2019, and acid gas generation by IEC 60754-1:2011. The maleated SEBS improves filler wetting and reduces surface defects on the cable jacket, which is critical for wind turbine tower harnesses and industrial 1 kV flexible cables. Zinc borate addition above 5 phr should be avoided in this system because it can accelerate anhydride ring-opening and shift the rheology into a high-torque regime before the filler is fully dispersed.
    Compounding zoneMelt temperature rangeMD4224 KU loadingCritical limiting variablePrimary test method
    PA6/PA66 reactive impact modification230–280 °C8–18 wt%Barrel above 285 °CISO 180:2023
    PP/PA6 regrind alloy230–245 °C3–8 wt%PA6 melt below 220 °CASTM D638-22
    TPE-S two-shot soft-touch190–220 °C30–45 wt%PA66 surface below 120 °CISO 4587:2003
    Halogen-free cable sheath160–185 °C5–12 phrMelt above 190 °CIEC 60811-501:2012
    Hot melt barrier lamination160–180 °C25–35 wt%Oxidative gel above 180 °CASTM D1876-08
    A slot-die coater applies a 20–30 μm adhesive layer of maleated SEBS to 12 μm polyester film at 165–175 °C for retortable pouch lamination. The adhesive formulation contains 25–35 wt% MD4224 KU, 35–45 wt% fully hydrogenated hydrocarbon tackifier, 15–25 wt% naphthenic oil, and 0.5–1.0 wt% hindered phenol antioxidant. Coat weight is controlled at 15–30 g/m², nip roll pressure is 3–5 N/mm, and line speed is 100–200 m/min. The maleated SEBS provides adhesion to aluminum foil, nylon film, and corona-treated polyester. Peel strength to aluminum foil is measured by ASTM D1876-08 and typically exceeds 6 N/15 mm after retort at 121 °C for 30 min. The adhesive falls within FDA 21 CFR 175.105 for food-contact adhesives. European use requires overall migration below 10 mg/dm² per EU 10/2011. Holding the adhesive at 190 °C for extended periods should be avoided because the saturated rubber midblock can form gel under oxidative conditions, increasing coat-weight variability. End products include retortable stand-up pouches for wet pet food and aseptic beverage spout laminates.

    PBT Connector Housings with Ductile Failure at -40°C

    Polybutylene terephthalate resin is pre-dried to below 0.02 wt% moisture and compounded with 8–15 wt% MD4224 KU at barrel temperatures between 240 °C and 260 °C. Injection molding uses melt temperature 245–265 °C, injection pressure 100–140 MPa, and mold temperature 70–90 °C. The maleic anhydride reacts with PBT terminal hydroxyl and carboxylic acid end groups, forming graft structures that stabilize the dispersed rubber phase. Notched Izod testing per ISO 180:2023 at 23 °C and -40 °C is used to confirm ductile failure in the final connector housing. The unfilled PBT control often shows notched Izod below 5 kJ/m²; the modified compound is screened for a target above 8 kJ/m² at 23 °C and above 6 kJ/m² at -40 °C. Instrumented puncture testing is performed per ISO 6603-2:2023 to verify energy absorption before crack propagation. The styrenic hard blocks begin to soften above 100 °C, so continuous service above 150 °C is not advised for load-bearing engine-compartment connectors. The terminal components are non-flame-retarded ECU connector backshells and sensor housings where low-temperature impact resistance is the primary mechanical requirement.
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    Certification & Compliance
    More Introduction

    Kraton™ MD4224 KU is supplied as a linear styrene-ethylene/butylene-styrene (SEBS) triblock copolymer in dense pellet form. The product is an unfilled, unplasticized hydrogenated styrenic block copolymer with a saturated ethylene/butylene midblock. Differential scanning calorimetry on the neat polymer typically shows an ethylene/butylene-domain glass transition below -40°C and a styrenic endblock glass transition in the region of 95°C. The morphology depends on phase separation of polystyrene endblock domains that act as thermally reversible crosslinks. This thermoplastic character permits processing on conventional extrusion and injection-moulding equipment without a vulcanization step and without a crosslinking agent.

    The grade is differentiated from general-purpose SEBS by its packaging for medical-device use, its narrower lot-to-lot rheological profile, and its low gel specification. Lot-to-lot variance in melt flow rate observed on production compounding lines is reduced relative to standard SEBS grades, which permits tighter control of tubing wall thickness when using a single-screw extruder with a barrier screw and a melt pump. In practice, polypropylene-based compounds with 20 wt% to 30 wt% MD4224 KU generate stable melt pressure at the die when barrel zones are held between 190°C and 220°C.

    Melt Filtration and Rheological Boundaries Across Extrusion and Injection Moulding

    A production-scale twin-screw compounding line with an L/D ratio of 30:1 to 40:1 is suitable for dispersing this material into isotactic polypropylene. The extruder should be equipped with melt filtering at 100 mesh to 250 mesh depending on gel sensitivity. Processing temperatures below 180°C produce incomplete melting of the styrenic endblock phase, and melt temperatures above 260°C can promote endblock relaxation and gel formation. At a melt temperature of 230°C, the viscosity profile is shear-thinning; injection-moulding conditions with a screw speed of 80 rpm to 150 rpm and back pressures of 5 bar to 10 bar are commonly used for small medical components. Published data for the exact capillary rheometry constants at very high shear rates associated with thin-wall injection moulding is limited, but the melt flow rate provides a comparative end-use control point.

    Pre-drying is not required for the neat pellets when stored in sealed packaging at ambient conditions. At a relative humidity above 60%, surface moisture on pellets can introduce measurable splay in translucent moulded parts and is controlled by drying at 60°C to 70°C for 2 h to 4 h in a desiccant dryer. Incompatibility with amine-based antistatic additives has been observed because residual amines can disrupt the styrenic cleavage and lead to yellowing above 200°C.

    In the unfilled state, the material exhibits a Shore A hardness of approximately 68 when measured after 30 s according to ASTM D2240. Tensile specimens die-cut from compression-moulded plaques produce tensile strength values near 27.5 MPa, a 100% secant modulus of 2.8 MPa, and an elongation at break of 650% when tested according to ASTM D412. These properties reflect the high restoring force of the polystyrene endblock network. In comparison with Kraton™ G series SEBS polymers, MD4224 KU maintains a lower diblock content and a lower solvent extractables profile, which is relevant for final-device biological evaluation under ISO 10993.

    Published typical physical properties of Kraton™ MD4224 KU
    Property Test Method Typical Value Unit
    Specific gravity ASTM D792 0.91 g/cm³
    Bound styrene ASTM D5775 31 wt%
    Hardness, 30 s ASTM D2240 68 Shore A
    Tensile strength at break ASTM D412 27.5 MPa
    Elongation at break ASTM D412 650 %
    100% modulus ASTM D412 2.8 MPa
    Melt flow rate 230°C/5 kg ASTM D1238 4.5 g/10 min

    These values are typical for neat, unfilled material and are not batch-release specifications; the certificate of analysis for each lot may include narrower acceptance criteria. The specific gravity of 0.91 g/cm³ is measured by ASTM D792. Bound styrene content, measured by ASTM D5775, is typically 31 wt%.

    What Distinguishes MD4224 KU from Standard Non-Medical SEBS Grades?

    Three molecular and physical characteristics separate MD4224 KU from general-purpose SEBS grades. First, the diblock content is controlled at a lower level, which raises tensile strength and reduces the viscous-flow fraction that contributes to creep in load-bearing parts. Second, the stabilizer package is selected for thermal processing without the use of alkylphenol ethoxylate or phthalate plasticizers, removing a significant source of extractables that must be quantified under ISO 10993-12. Third, the material is produced and packaged under conditions that reduce foreign-particle contamination for medical-device applications.

    In contrast to oil-extended SEBS compounds, MD4224 KU is supplied neat, so it does not introduce mineral-oil migration into medical surfaces. Compounds formulated with medical-white mineral oil show opacity and hardness reductions that scale with oil addition; at 20 phr oil, the Shore A hardness typically declines to approximately 50, while the flexibility of the saturated midblock improves. The absence of an oil carrier is an advantage in applications where extraction by lipid-containing fluids is a concern.

    When the Device Requires Repeated Steam Sterilization Rather than Gamma Irradiation

    Steam-sterilization exposure at 121°C for 30 min or 134°C for 5 min produces little irreversible property change in soft components formulated from MD4224 KU, provided the residual stress from injection moulding is minimized by gas counter-pressure or by post-mould annealing at 80°C for 2 h. Gamma irradiation at doses up to 50 kGy is reported to cause measurable reductions in elongation and slight yellowing; the magnitude is dependent on the presence of antioxidants and on the coexistence of polypropylene in the final compound. Electron-beam sterilization at similar doses produces faster oxidation of the polypropylene phase; published data for this specific neat resin under electron-beam at 70 kGy is limited and must be confirmed on the finished device.

    Applications reported for this grade include extruded medical tubing, overwrap film, respiratory circuit components, syringe seals, blood-contact valve components, and moulded ergonomic soft-touch features on hand-held diagnostic devices. In tubing applications, the material is commonly used in blends with polypropylene at loadings of 30 wt% to 50 wt% and with a medical-white oil addition up to 20 phr. The blend is then extruded into single-lumen or multi-lumen tubing with an outer diameter of 3 mm to 8 mm and a wall thickness of 0.5 mm to 1.5 mm.

    The Regulatory Limits are Met Only After Extractables Subtraction

    Conformity statements from the producer for the unfilled product typically reference 21 CFR 177.1810, 21 CFR 170.199, USP Class VI, ISO 10993-5, ISO 10993-10, ISO 10993-11, EU Regulation 10/2011, and REACH. The finished-device manufacturer is responsible for extractables testing because processing temperatures, coextruded layers, colorants, and sterilization can shift the extraction profile. Published data for extractables from a neat resin plaque is not a substitute for exhaustive migration testing on the finished device under the contact conditions specified in ISO 10993-18 and ISO 10993-12.

    Regulatory and biological evaluation status reported for unfilled MD4224 KU
    Standard or Requirement End Point Status
    USP Class VI Extraction, implantation, systemic injection Meets
    ISO 10993-5 Cytotoxicity Non-cytotoxic
    ISO 10993-10 Sensitization No sensitization
    ISO 10993-11 Acute systemic toxicity No adverse response
    21 CFR 177.1810 Styrene block copolymers in food contact Conforms
    EU Regulation 10/2011 Plastic materials in food contact Conforms
    REACH Registration and authorization Compliant
    RoHS Restricted substances Compliant

    Chemical resistance of the saturated midblock to polar solvents is superior to unsaturated styrenic block copolymers. The material is attacked by aromatic hydrocarbons and chlorinated solvents; ketone and ester extractants can swell the styrenic domains. For this reason, the material should not be used in contact with liquid formulations containing high concentrations of benzene, toluene, or methyl ethyl ketone. Alcohol-water mixtures such as 70% isopropanol produce negligible property loss in short-term exposures, but long-term recovery of the polymer network should be verified on the finished device.

    Naphthenic or paraffinic medical-white mineral oils are preferred for viscosity control; aromatic oils are not compatible with the saturated midblock and will produce exudation. Oil absorption is slower than in unsaturated SBS copolymers because the saturated midblock has no double bonds to solvate. A two-stage screw configuration with a distributive mixing section and oil injection downstream of the melting zone is used to avoid torque spikes when compounding oil into the polymer. In such coextruded structures, the melt-temperature split between the outer polypropylene layer and the inner MD4224 KU—typically 10°C to 20°C—should be validated by pyrometer measurements across the die.

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