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Kraton Kraton™MD SEBS MD6953 MU

    • Product Name: Kraton Kraton™MD SEBS MD6953 MU
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 200572
    Polymertype SEBS linear triblock copolymer
    Styrenecontent 31%
    Density 0.91 g/cm³
    Meltflowrate 11 g/10 min (230 °C/2.16 kg)
    Shoreahardness 65
    Tensilestrength 27 MPa
    Elongationatbreak 600%
    Flexuralmodulus 25 MPa
    Vicatsofteningtemperature 70 °C
    Bulkdensity 0.45 g/cm³
    Volatilematter <0.5%
    Ashcontent <0.1%
    Processingmethod Injection molding, extrusion
    Appearance Powder

    As an accredited Kraton Kraton™MD SEBS MD6953 MU factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Kraton™ MD SEBS MD6953 MU is packaged in 25 kg polyethylene-lined paper bags, palletized for industrial use.
    Container Loading (20′ FCL) 20′ FCL: palletized Kraton MD6953 MU SEBS in dry container; secure stowage, weight-limit compliance, MSDS and shipping documents.
    Shipping Kraton™ MD SEBS MD6953 MU is a non-hazardous thermoplastic elastomer supplied as pellets. Ship in clean, dry containers at ambient temperature, protected from moisture, heat, and direct sunlight. No UN number or dangerous goods classification is assigned.
    Storage Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and oxidizing agents. Keep containers tightly closed and protect from moisture, dust, and contamination. Avoid prolonged storage at elevated temperatures, maintain good housekeeping, and follow the supplier’s SDS and local regulations.
    Shelf Life Typical shelf life is 2 years from date of manufacture when stored in original unopened packaging under dry, cool conditions.
    Application of Kraton Kraton™MD SEBS MD6953 MU

    Kraton™ MD6953 MU is a linear styrene-ethylene/butylene-styrene block copolymer with a nominal styrene content of 33 wt%, density of 0.91 g/cm³ per ISO 1183-1:2019, and uncompounded Shore A hardness in the 60–70 range per ASTM D2240-15e1. Production-scale compounding of PVC-free infusion tubing compounds from this grade is normally executed on a co-rotating twin-screw extruder with an L/D ratio of 44:1 to 52:1. A starting-point formulation comprises 40–55 wt% Kraton™ MD6953 MU, 20–35 wt% medical-grade white oil, 10–20 wt% polypropylene homopolymer, 5–10 wt% high-density polyethylene, and 0.1–0.3 wt% of a phenolic-phosphite antioxidant package. The regulatory boundary for this compound falls under FDA 21 CFR 177.1810, with additional biocompatibility screening per ISO 10993-5:2009, ISO 10993-10:2010, ISO 10993-11:2017, and USP <88> Class VI. During compounding, low-molecular-weight hydrocarbon oil can phase-separate if screw speed exceeds 450 rpm on a 40 mm co-rotating twin-screw due to shear heating that drives melt temperature beyond 230 °C; this produces batch-to-batch Shore A variation greater than 3 points and is controlled with distributive mixing elements in zones 4–6 and vacuum devolatilisation at −0.08 MPa. Tube extrusion downstream uses a single-screw extruder with an L/D of 30:1, die temperature 210–220 °C, and cooling water at 10–15 °C. Terminal products include IV administration tubing, peristaltic pump tubing, and jacketing for dialysis lines. Compounds must be pre-dried at 80 °C for 2–4 h if exposed to ambient relative humidity above 60 %. Co-storage with DEHP-containing PVC line components is not recommended because plasticizer migration can lower tensile strength and generate tacky surfaces on coiled tubing.

    What Changes When SEBS Replaces Thermoset Rubber in Prefilled Syringe Plunger Seals?

    Injection molding of prefilled syringe plunger seals from Kraton™ MD6953 MU removes the sulfur-vulcanization and post-cure steps associated with halogenated butyl rubber. A production-validated starting composition uses 100 parts by mass Kraton™ MD6953 MU, 0.1–0.3 parts phenolic antioxidant, and optionally 10–20 parts polypropylene homopolymer when higher dimensional stability is required. The material is processed on a reciprocating-screw injection molding machine with a shot-residence ratio above 20 % of barrel capacity, barrel temperatures from 200 °C to 230 °C, and a cold-runner mold held at 30–50 °C. Holding pressure is set at 50–70 % of injection pressure, with injection pressure in the range 60–90 MPa. Plunger seal wall thicknesses of 1.2–3.0 mm require cooling times of 15–30 s. Regulatory expectations are defined by USP <381>, USP <88> Class VI, ISO 10993-5:2009, ISO 10993-10:2010, and ISO 11040-5:2012. Because SEBS contains no sulfur, accelerator, or zinc oxide cure system, extractable profiles differ from thermoset rubber closures; residual peroxide and amine crosslinker by-products are absent. The main process risk is void formation at the gate when melt temperature exceeds 240 °C, producing visual rejects under 2.5× magnification and irregular compression set. Maintaining melt temperature below 235 °C and installing a heated sprue bushing reduce reject rates. Terminal products include plunger seals, needle shields, and vial stopper liners for injectable drug packaging.

    Compliance verification matrix for Kraton™ MD6953 MU downstream applications
    Regulatory/standard referenceMethod or clauseBoundary applicationTypical acceptance target
    21 CFR 177.1810Indirect food additive: styrene block copolymersInfusion tubing, closure linersEnd-testing with food simulants per FDA guidance
    USP <88> Class VIBiological reactivity tests in vivoTissue/blood contactNo systemic toxicity
    USP <381>Elastomeric closures for injectionsPlunger seals, vial stoppersPhysicochemical and biological panel
    ISO 10993-5:2009In vitro cytotoxicityAll skin/mucosa contactGrade ≤2
    ISO 10993-10:2010Skin irritation and sensitizationOstomy pouches, wound filmsNo erythema/oedema grade >1
    ASTM E96/E96M-22Water vapour transmission rateBreathable backsheet filmLot-specific MVTR validated

    When Coextruded with Random Copolymer Polypropylene in Ostomy Barrier Film

    In a three-layer cast film configuration, the sealant layer contains 70–85 wt% Kraton™ MD6953 MU, 10–20 wt% random copolymer polypropylene, and 5–15 wt% medical-grade white oil. The skin-contact layer is coextruded with a tie layer and an outer layer of polypropylene random copolymer at layer ratios of 60/10/30 to 75/5/20, depending on heat-seal strength and moisture vapour transmission targets. Standards governing this construction include ISO 10993-5:2009, ISO 10993-10:2010, and FDA 21 CFR 177.1520 for the polypropylene component, while ASTM E96/E96M-22 is used for water vapour transmission testing. Cast film processing is performed on a three-extruder line with screw diameters of 25 mm/35 mm/25 mm, die temperature 220–235 °C, and a polished chill roll held at 12–18 °C. Heat-seal activation occurs at 150–165 °C for 1.0–2.5 s; above 170 °C the sealant layer begins to thin and creates channel leakers. In production, migration of low-molecular-weight oil to the film surface is monitored by Fourier transform infrared spectroscopy at 7-day intervals because oil bloom above a surface concentration of 0.3 mg/100 cm² reduces pouch weld strength. Terminal products include ostomy pouch barrier films, wound drainage pouch inner liners, and faecal management devices. This film structure is not recommended for repeated autoclave sterilization because layer delamination occurs after more than 30 cycles at 134 °C.

    Insert molding of soft-touch grips onto polypropylene-based surgical instrument handles uses a two-shot injection cell with a vertical rotary platen. The soft-touch compound is prepared from 45–60 wt% Kraton™ MD6953 MU, 10–25 wt% polypropylene homopolymer, and 20–30 wt% medical-grade white oil; the exact ratio within this envelope is adjusted to a target Shore A of 45–65 measured per ASTM D2240-15e1. The substrate is injection molded from polypropylene homopolymer at a melt temperature of 210–230 °C, transferred to the second cavity, and overmolded at 190–215 °C with a mold temperature of 30–45 °C. Because unmodified SEBS does not develop structural bond strength to polycarbonate, polyamide, or polyester substrates, adhesion is restricted to polyolefin substrates or else a maleic anhydride-grafted tie-layer must be used. Compliance verification for the overmolded assembly includes ISO 10993-5:2009, ISO 10993-10:2010, and 21 CFR 177.1810 for the styrenic block copolymer phase. Terminal products include ergonomic grips on powered surgical instruments, vibration-damping pads on diagnostic analyzers, and bumper components on wearable insulin pumps. Process audits on production lines show that cavity-pressure sensors reading below 35 MPa during overmold injection correlate with short shots at the distal tool end, and this is corrected by increasing holding pressure by 10–15 %.

    Sterilisation Dose Mapping Identifies Tensile Retention Limits in Wound Care Film Laminates

    Before release of wound dressing film laminates, dose mapping across 25 kGy, 40 kGy, and 50 kGy electron-beam or gamma irradiation is performed because phenolic antioxidant depletion changes tensile retention and yellowing. A cast film formulation for wound care backings uses 60–80 wt% Kraton™ MD6953 MU, 10–20 wt% polypropylene random copolymer, and 5–15 wt% aliphatic hydrocarbon oil. Film is cast at 220–240 °C onto a matt steel chill roll at 15–20 °C, with thickness controlled to 50–200 μm for incise drapes and wound-contact layers. Tensile strength and elongation are measured according to ASTM D882-18 before and after sterilization; supplier-published data for this specific Kraton™ MD6953 MU film configuration is limited, so lot-specific validation is required. Biocompatibility requirements include ISO 10993-5:2009, ISO 10993-10:2010, and ISO 11137-1:2006 for radiation sterilization validation. The main processing risk occurs when film thickness exceeds 300 μm, where electron-beam dose penetration becomes non-uniform and hard spots develop. Terminal products include wound dressing backing films, incision drape laminates, and medical tape backing layers.

    Breathable Elastic Backsheet Film for Negative-Pressure Wound Therapy Dressing Systems

    Microporosity in breathable elastic backsheet films is generated by machine-direction orientation of calcium carbonate-filled Kraton™ MD6953 MU compounds at stretch ratios between 2.5:1 and 4.0:1. The starting compound comprises 30–45 wt% Kraton™ MD6953 MU, 15–25 wt% polypropylene homopolymer, 30–50 wt% treated calcium carbonate, and 5–10 wt% medical-grade white oil. The filled compound is pelletized on a twin-screw extruder with an L/D of 44:1, then extruded as cast film with a die gap of 500–800 μm at 210–230 °C and oriented in-line through an MDO unit with roll temperatures ramped from 70 °C to 95 °C. This creates elongated micropores that increase moisture vapour transmission while maintaining hydrostatic head resistance. Compliance references for NPWT dressings include ISO 10993-5:2009, ISO 10993-10:2010, EN 13726-1:2002, and ASTM E96/E96M-22 for MVTR verification. Terminal products are microporous backsheet layers in negative-pressure wound therapy dressings, surgical fenestration films, and breathable cover layers for wearables. The operational boundary is that calcium carbonate loading above 50 wt% combined with orientation ratios above 4.0:1 produces film fibrillation, pinholes, and loss of bacterial barrier function. Batch-to-batch variation in calcium carbonate particle size distribution measured by laser diffraction must remain within ±0.5 μm of the specified D50 to maintain consistent pore dimensions.

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    Certification & Compliance
    More Introduction

    Kraton™ MD SEBS MD6953 MU is introduced as a neat, clear, linear styrene-ethylene/butylene-styrene block copolymer supplied in free-flowing pellet form. The MD prefix is typically associated with medical-industry packaging and lot control, while the MU suffix is a manufacturer-specific designation; neither suffix substitutes for end-use regulatory testing. Because the midblock is fully hydrogenated, the material shows greater oxidative, ozone, and UV resistance than unsaturated styrene-butadiene-styrene grades when evaluated under ASTM D1148 and ASTM G154. Representative values for this high-styrene SEBS place bound styrene in the 30–33 mass % band, specific gravity near 0.91 per ISO 1183-1, and compression-molded Shore A hardness in the 70–80 range under ASTM D2240. Published independent data for this exact MD6953 MU configuration are limited, so the supplier technical data sheet and certificate of analysis remain the binding source for lot-specific melt flow, gel count, ash content, and residual styrene levels. The material is not oil-extended, which shifts formulation control for hardness, extractables, and process viscosity to the downstream compounder.

    How Does a Non-Oil-Extended High-Styrene SEBS Change Compounding Economics and Performance?

    An oil-extended SEBS compound arrives with mineral oil already dispersed in the polymer matrix; MD6953 MU does not. This increases melt viscosity, raises shear heat during plastication, and requires the formulator to select oil type and dosage. With oil addition at 30–50 phr, Shore A hardness can be reduced by 10–20 points, but the relationship is not linear and depends on oil kinematic viscosity at 100°C, naphthenic versus paraffinic character, and mixing intensity. The saturated ethylene/butylene midblock provides better compression set resistance and UV ageing behavior than SBS at equal oil loading, although ultimate tensile strength may be lower than an SBS compound with comparable hardness. The absence of pre-dispersed oil also permits use of high-purity hydrocarbon fluids for lower extractables under ISO 10993-12 extraction protocols. The economic trade-off is higher shear energy input and a narrower stable processing window if the compound is under-plasticized during twin-screw compounding.

    The morphological behavior of MD6953 MU governs these effects. At rest, the polystyrene endblocks phase-separate into glassy domains with a glass transition temperature reported near 95–100°C; these domains act as physical crosslinks and dissolve only when heated above their softening range. The ethylene/butylene midblock retains low-temperature flexibility with a loss tangent maximum near -55°C under ISO 6721-1 dynamic mechanical analysis. Paraffinic process oils selectively partition into the midblock; the high bound-styrene content therefore limits equilibrium oil uptake relative to low-styrene SEBS grades but raises room-temperature hardness and tensile strength. In comparative oil-absorption evaluations, a 33 mass % bound-styrene SEBS can require 10–20 phr less oil to achieve a given Shore A hardness than a 20 mass % bound-styrene grade, although the exact delta depends on aromatic content and screw residence-time distribution.

    When Twin-Screw Compounding of Neat SEBS Must Deliver a Low-Gel Medical Compound

    On a production-scale co-rotating twin-screw extruder with an L/D 40 barrel, neat high-styrene SEBS is typically processed with early barrel temperatures of 180–200°C and die temperature near 200°C. The feed throat should remain water-cooled to prevent pellet surface softening and bridging; if the feed zone exceeds 120°C, pellet clumping can cause feed instability and torque oscillation. Oil injection is staged downstream of the melt seal, usually after zone 5 of a 10-zone barrel, to avoid worm-hole slip and to improve distributive mixing. Field experience on production-scale twin-screw extruders indicates that melt temperature excursions above 215°C can produce melt pressure variation at the die plate and gel formation, although published kinetic data for MD6953 MU are limited. A gear pump or melt filtration unit with screen packs of 100–250 μm is used to stabilize die pressure and remove agglomerates. Vacuum venting at -80 kPa or lower is applied in the devolatilization zone to remove residual moisture and volatile oil fractions without foaming the melt pool.

    Blown film and tubing lines using MD6953 MU compounded with polyolefins typically require a melt temperature of 190–210°C and a blow-up ratio below 3.0 to avoid melt fracture. For casting and flat-die extrusion, die lip gaps of 0.5–1.0 mm are common, with haul-off speed set to produce 100–300 μm thick film without orientation-induced crinkle. In injection molding of finished MD6953 MU-based compounds, barrel temperatures from 190°C to 210°C, a mold temperature of 20–40°C, and injection speeds that maintain apparent shear rates below 10,000 s⁻¹ are used to avoid surface melt fracture. Hold pressures of 30–60 MPa are typical for hardness-controlled parts, but gate geometry and wall thickness require rheological simulation. Mold release may require non-amine external release agents because amine-based additives can accelerate oxidative degradation of SEBS at elevated temperature. Regrind of fully compounded scrap can be reincorporated at 20–30 wt% in non-critical applications, but each heat history shifts molecular weight distribution and must be validated against ASTM D638-14 tensile and ASTM D2240 hardness.

    Comparison parameterMD6953 MU neat SEBSOil-extended SEBS compoundUnsaturated SBS
    Midblock chemistryEthylene/butylene, saturatedEthylene/butylene plus process oilButadiene, unsaturated
    Typical melt processing window180–210°C neat; higher viscosity160–200°C depending on oil type150–190°C; less thermally stable
    Ozone resistanceHigh retention under ASTM D1148High, but dependent on oil migrationLow unless antiozonant added
    Oil addition latitudeCustom oil type and level; requires high shearPre-dispersed oil; limited flexibilityGood but with lower oxidative stability
    Extractables controlHigh-purity oil selected by compounderFixed oil; verify ISO 10993-12Higher unsaturation; antioxidant residues possible

    Heat, Radiation, and Ethylene Oxide Sterilisation Boundaries

    For ethylene oxide sterilization, molded TPE parts should be aerated at 50–55°C until residual ethylene oxide meets ISO 10993-7 action levels. SEBS midblock saturation generally provides better resistance to oxidative degradation than SBS during gamma irradiation, but gamma dose mapping per ISO 11137-1 is required. Dose fractionation above 50 kGy may induce detectable crosslinking or chain scission depending on the antioxidant package; published data for MD6953 MU under high-dose gamma exposure are limited. Steam autoclave cycles at 121°C can soften the ethylene/butylene midblock and alter dimensions or peel force, so repeated-cycle validation is necessary. The grade should not be processed with chlorine-containing cleaning agents or with peroxide masterbatches without checking peroxide half-life at processing temperatures because uncontrolled free-radical activity can alter molecular weight distribution. Storage should avoid direct UV exposure and condensation; although SEBS is not markedly hygroscopic, condensed moisture on cold pellets can introduce steam sections during processing.

    Regulatory positioning requires separation of resin certification from finished device validation. FDA 21 CFR 177.1810 covers styrene block copolymers in food-contact articles; a medical device manufacturer must verify that the chosen stabilizer package and processing conditions meet intended-use conditions. USP <661.1> sets biological reactivity expectations for plastic packaging materials; ISO 10993-5 and ISO 10993-10 address cytotoxicity and irritation for medical devices. REACH Article 33 communication duties and RoHS Directive 2011/65/EU Annex II restrictions may apply depending on additive content. A raw resin supplier statement cannot be transferred to the finished component without formulation-specific testing. For exact extractables profiles, gel-count specifications, and migration limits in finished devices, published data for this specific configuration remain limited; validation should be performed on the compounded formulation rather than on the neat resin alone.

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