| HS Code | 641974 |
| Polymer Type | SEBS compound |
| Color | Natural |
| Form | Pellets |
| Density | 1.08 g/cm³ |
| Shore A Hardness | 75 |
| Melt Flow Rate | 20 g/10 min at 230 °C/2.16 kg |
| Tensile Strength At Break | 8 MPa |
| Elongation At Break | 600% |
| 100 Tensile Modulus | 3.5 MPa |
| 300 Tensile Modulus | 5.0 MPa |
| Tear Strength | 30 kN/m |
| Compression Set | 30% at 23 °C/72 h |
| Processing Method | Injection molding |
As an accredited Kraton Kraton™G SEBS-Comp. G7705 GI-N factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kraton Kraton™G SEBS-Comp. G7705 GI-N is supplied in 25 kg bags, typically 40 bags per pallet (1,000 kg net). |
| Container Loading (20′ FCL) | Kraton™G SEBS-Comp. G7705 GI-N is loaded into a 20-foot FCL container, palletized and secured for export shipment. |
| Shipping | Kraton™ G SEBS-Comp. G7705 GI-N is a solid thermoplastic elastomer compound normally shipped as non-hazardous pellets in bags, boxes, or octabins on pallets. It is generally not regulated as dangerous goods for road, sea, or air. Keep dry, clean, and protected from contamination; verify the current SDS and local rules. |
| Storage | Store Kraton™G SEBS-Comp. G7705 GI-N in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep in original, closed packaging on pallets to prevent moisture and contamination. Avoid prolonged UV exposure and extreme temperatures. Follow the manufacturer’s SDS and local storage regulations. |
| Shelf Life | Shelf life is typically 24 months from manufacture when stored in original, unopened packaging under dry, cool conditions. |
Pre-compounding moisture auditing constitutes the first operational gate for this compounded SEBS grade in ISO 13485-controlled production environments. Although the hydrogenated mid-block of the styrene-ethylene/butylene-styrene triblock structure confers hydrolytic stability superior to unsaturated SBS alternatives, pellet-surface hygroscopicity requires monitoring when ambient relative humidity exceeds 60%. Desiccant-bed drying at 80°C for 2–4 hours with a dew point of -40°C is documented on production lines to reduce residual moisture below 0.05 wt% prior to melt processing. On a co-rotating twin-screw extruder with a screw diameter of 25–40 mm and an L/D ratio of 40:1–48:1, the compound is processed with a barrel temperature profile of 170/180/190/200/205°C across five zones, yielding a melt temperature of 190–220°C measured at the die exit by infrared thermometry. Melt pressure at the die plate typically stabilizes between 30–60 bar, dependent on screw speed (150–300 rpm) and throughput settings. The compound is then injection molded on horizontal machines with clamp force capacities of 50–250 tonnes, using screw compression ratios of 2.5:1–3:1 and ball-type or poppet-type check rings selected to minimize melt slippage, which is a documented failure mode when processing low-viscosity SEBS compounds at high screw recovery speeds.
Biocompatibility qualification for finished medical components fabricated from compounded SEBS follows a multi-tiered assessment protocol. In vitro cytotoxicity per ISO 10993-5:2009 (extraction method using MEM elution medium) is evaluated alongside ISO 10993-10:2010 for skin irritation and sensitization potential. Devices intended for tissue contact durations exceeding 30 days require USP <88> Class VI certification encompassing systemic injection, intracutaneous reactivity, and implantation studies in accordance with the current United States Pharmacopeia compendial method. Sterilization compatibility for molded SEBS components is established through gamma irradiation at doses of 25–40 kGy or ethylene oxide exposure per ISO 11135:2014, with residual EtO testing per ISO 10993-7:2008 confirming levels below 1 µg/cm² for patient-contacting surfaces. The material is formulated to be free of vulcanization accelerators, sulfur donors, nitrosamine-generating compounds, and phthalate plasticizers, distinguishing this chemistry from thermoset rubber alternatives that frequently require leaching minimization protocols.
Formulation ratios for medical component compounds incorporating Kraton G7705 GI-N depend on the target flexural modulus and creep resistance of the end-use geometry. Blends containing 60–80 wt% of the SEBS compound with 20–40 wt% of polypropylene homopolymer (MFI 12–25 g/10 min per ISO 1133-1:2022 at 230°C/2.16 kg) produce components with Shore A hardness values in the 55–75 A range when measured per ASTM D2240-15. For softer geometries such as respiratory mask cushions, the SEBS compound content is increased to 90–100 wt% with the addition of 0.5–1.5 phr of a medical-grade silicone lubricant masterbatch to reduce coefficient of friction. Tensile properties of molded specimens tested per ASTM D638-14 (Type IV specimen, 50 mm/min crosshead speed) typically fall within 12–25 MPa for tensile strength and 400–700% for elongation at break across the formulation range. Tear strength per ASTM D624-00 (Die C) is documented between 25–45 kN/m for harder grades and 15–25 kN/m for softer formulations, a parameter frequently overlooked in gasket and valve-seat applications experiencing cyclic compression.
Downstream production processes for medical SEBS components are constrained by the narrow thermal stability window of the hydrogenated mid-block. Sustained residence times exceeding 8–10 minutes at melt temperatures above 230°C induce oxidative chain scission of the ethylene/butylene segment, measurable as an increase in melt flow rate per ISO 1133-1:2022 and a corresponding loss of tensile elongation. This kinetic limitation necessitates shot-size-to-barrel-capacity ratios between 30–60% on injection molding equipment and thermocouple placement accuracy of ±2°C in nozzle and hot-runner zones. Mold temperature control is maintained between 20–45°C via water circulation, and venting grooves of 0.01–0.03 mm depth are specified to prevent gas entrapment at flow-front convergence points. Hot-runner systems, when employed, require internally heated manifolds with tip temperatures held at ≤210°C to prevent material stagnation and gel formation. End-product categories currently produced from this material family include IV bag injection port membranes, nasogastric tube connectors, oral dose syringe plunger tips, respiratory therapy mask cushions, wound drainage bulb components, and enteral feeding adapters.
Regulatory compliance for compounded SEBS in food-contact applications is anchored to FDA 21 CFR 177.1810(a), which identifies acceptable styrene block copolymers for articles intended to contact all food types under Conditions of Use A through H as defined in 21 CFR 176.170(c). Extraction testing mandated by 21 CFR 177.1810(b) requires the use of food-simulating solvents—distilled water, heptane, and 8% or 50% aqueous ethanol—with total extractives limits established based on the intended use condition. For the European market, Regulation (EU) No 10/2011 governs plastic materials and articles intended to come into contact with food, specifying an overall migration limit of 10 mg/dm² for all food simulants. Specific migration limits for styrene monomer per the same regulation are set at 0.05 mg/kg food simulant. NSF/ANSI 51 certification is required for food equipment components used in commercial kitchen environments, encompassing material formulation review, extraction testing in distilled water at 82°C for 24 hours, and toxicological evaluation of any migration products.
Compounding ratios for food-contact applications typically employ the SEBS compound at 100 wt% or in predetermined blends with food-contact-approved polypropylene at 30–50 wt% PP loading to enhance clarity and reduce tack. The absence of oil extension in the base G7705 polymer minimizes migratory plasticizer content, though finished compounds intended for fatty-food contact may require additional extraction validation due to the affinity of any processing oils or release agents for lipophilic food simulants such as 95% aqueous ethanol or olive oil substitutes per EU 10/2011 Annex III. Production-scale molding follows injection parameters similar to those documented for medical applications, with mold temperature maintained at 15–40°C to achieve acceptable cycle times without inducing warpage in thin-walled parts. Extrusion of sheet or profile stock for downstream thermoforming requires a 75 mm or larger single-screw extruder with a barrier screw design to prevent surging associated with pellet inter-particulate slip in the feed throat.
The primary downstream product categories for food-contact SEBS compounds include infant bottle nipple collars and sealing rings, food storage container gaskets, beverage dispenser valve seals, kitchen utensil soft-grip overmolds, and conveyor belt scrapers for food processing lines. All such components are subjected to repeated thermal cycling and detergent exposure, with ASTM D573-04 accelerated aging at 100°C for 168 hours used to qualify retention of Shore A hardness within ±5 points and tensile strength retention above 80% of original value.
Two-shot injection molding and insert overmolding represent the dominant downstream processes for consumer goods incorporating compounded SEBS soft-touch surfaces. Adhesion between the SEBS compound and rigid substrates such as polypropylene, polycarbonate/ABS blends, and nylon 6 is governed by the principle of thermodynamic compatibility, with the styrenic end-blocks of the SEBS molecule exhibiting highest interfacial bond strength to substrates containing aromatic styrenic or bisphenol-A units. Peel strength testing per ASTM D903-98 on overmolded plaques quantifies adhesion values ranging from 15–35 N/cm for PP substrates and 25–45 N/cm for PC/ABS substrates, with the caveat that PP surfaces require surface activation via corona treatment (45–52 dyn/cm, per ASTM D2578-17) or plasma treatment prior to overmolding when a pre-molded insert is used in a second-shot configuration. Failure mode analysis of peel specimens reveals cohesive failure within the SEBS layer, rather than adhesive failure at the interface, at bonding temperatures above 150°C at the substrate surface.
RoHS Directive 2011/65/EU with its Amendment (EU) 2015/863 establishes restrictions on lead (0.1 wt%), mercury (0.1 wt%), cadmium (0.01 wt%), hexavalent chromium (0.1 wt%), PBB, and PBDE in electrical and electronic equipment, all satisfied by the non-halogenated SEBS compound formulation. REACH Regulation (EC) No 1907/2006 compliance requires confirmation that the compound contains no Substances of Very High Concern (SVHCs) at concentrations exceeding 0.1 wt% per article, as specified in Article 33 and Annex XVII. The compound is also evaluated under EN 71-3:2019 for migration of certain elements in toy applications, with the absence of heavy-metal-based pigments in the GI-N formulation simplifying compliance documentation.
Molding parameters for overmolded consumer goods require the SEBS melt temperature to be maintained at 195–215°C to achieve sufficient interfacial wetting of the rigid substrate without inducing thermal degradation of the thermoplastic insert. The substrate surface temperature at the moment of SEBS injection must exceed 110°C for PP and 130°C for PC/ABS substrates to permit segmental diffusion of the styrenic end-blocks across the polymer-polymer interface. Cycle times for two-shot components are governed by the cooling rate of the SEBS overlay, with mold temperatures of 25–40°C producing solidification times of 15–30 seconds for typical 2–4 mm overlay thicknesses. The end-product categories for this scenario encompass personal care device handles (toothbrushes, electric razors, hair styling tools), hand tool grips, computer mouse surfaces, remote control housings, and wearable electronic device straps, all of which require surface hardness values between 45–65 Shore A per ASTM D2240-15 and compressive set below 35% per ASTM D395-18 Method B after 22 hours at 70°C.
Within the domain of automotive interior sealing and soft-touch automotive components, compounded SEBS finds measurable application in door-check seals, gear-shift boot covers, and HVAC duct damper gaskets. Compliance in this segment is driven by IATF 16949:2016 for supplier quality management, with component-level performance validated per OEM-specific specifications that reference VDA 275 for fogging behavior and VDA 277 for total VOC emissions. Fogging test per VDA 275 (DIN 75201:2011-11) measures condensate mass on a cooled glass plate at 100°C for 16 hours, with automotive OEM acceptance thresholds typically below 1.0 mg for interior components. The SEBS compound, being free of volatile plasticizers, consistently satisfies fogging limits; the primary volatile contributors in compounded systems are residual processing aids and any silicone lubricant additives, which are controlled through steam stripping during polymer finishing. VOC emissions are quantified per VDA 277 using headspace GC-MS at 120°C for 5 hours, with OEM targets of ≤100 µg/g total VOC for interior elastomeric parts. Production processing for automotive components uses vertical clamping injection molding machines of 150–350 tonnes to accommodate insert-loaded metal or rigid plastic bases, with mold temperatures in the range of 30–50°C to balance cycle time against surface gloss and sink-mark elimination. End product scope includes gear lever gaiter covers, door inner-handle soft inserts, parking brake lever boots, interior storage bin liners, and HVAC actuator seals, all specified to withstand 100,000–200,000 cycles of operational flexing without visible cracking per OEM durability protocols.
Flexible cord and cable jacketing represents a production-intensive downstream scenario for compounded SEBS where the crystallization kinetics of the polypropylene segments within the compound, if any are present in the formulation, and the block copolymer morphology determine the balance between flexibility at low temperature and abrasion resistance at service temperature. For jacketing applications, the SEBS compound is processed on a 60–90 mm single-screw extruder with an L/D ratio of 24:1–30:1, using a PVC-compatible screw design with a Maddock mixing section to ensure consistent dispersion of any flame-retardant or mineral filler packages. Barrel temperature profiles range from 160–200°C across four zones, with a screen pack of 80/120 mesh specified to generate back pressure for homogenization. Extrusion die temperatures are held at 190–205°C, and the molten tube is quenched in a water bath at 20–30°C to lock in the microphase-separated morphology. Line speeds for thin-wall jacketing (0.5–2.0 mm wall thickness) on conductor assemblies range between 50–150 m/min, dependent on extruder throughput capacity and downstream capstan configuration. A critical process control parameter in this scenario is the die-to-quench distance, which must be maintained between 50–150 mm to prevent surface roughness from premature cooling while avoiding excessive drawdown that would produce anisotropic shrinkage in the jacket layer.
Compliance for wire and cable jackets manufactured from SEBS compounds requires UL 62 for flexible cords and cables in the North American market, with flammability classification per UL 94 HB or V-2 as dictated by the end-use configuration and the presence or absence of halogenated flame retardants. For international distribution, IEC 60227 Parts 1 through 7 govern polyvinyl chloride insulated cables of rated voltages up to and including 450/750 V, and while SEBS jackets are positioned as non-PVC alternatives, the mechanical property and abrasion resistance requirements of IEC 60227-1:2007 clauses 5.6 and 5.7 are referenced for performance benchmarking. Low-temperature flexibility is evaluated per UL 1581 Section 560 or IEC 60811-504:2012, with specimens conditioned at -25°C or -40°C for 4 hours followed by mandrel winding at a diameter specified by the cable construction. The SEBS compound, with a glass transition temperature of the ethylene/butylene mid-block below -50°C when measured by differential scanning calorimetry per ISO 11357-1:2016, retains sufficient flexibility to satisfy these cold-bend requirements without the addition of high-molecular-weight plasticizers that would compromise abrasion resistance. Abrasion resistance is quantified per ISO 6722-1:2011 Annex C (scrape abrasion test) or the sandpaper abrasion method detailed in UL 1581 Section 720, with SEBS jackets demonstrating scrape resistance at 7 N load that exceeds thermoplastic polyurethane alternatives in controlled laboratory comparisons.
Compound formulation ratios for cable jacketing typically incorporate the SEBS base compound at 70–85 wt% with the balance comprising flame-retardant additives (magnesium hydroxide or aluminum trihydrate at 10–20 wt%), processing lubricants (0.5–2.0 wt%), and color concentrates (2–5 wt%). When halogen-free flame retardancy is required per IEC 61034-2:2019 for smoke density and IEC 60754-1:2011 for acid gas emission, the flame-retardant loading is increased to 50–65 wt% in a masterbatch dilution approach, with corresponding adjustment of Shore A hardness upward by 10–20 points to the 85–95 A range. Tensile properties of the final jacket compound, measured on extruded specimens per IEC 60811-501:2012, must exceed 10 MPa tensile strength and 300% elongation at break without conditioning, with retention above 70% after 168 hours thermal aging at 100°C per IEC 60811-401:2012. End product types using SEBS jackets include appliance cord sets for household equipment, power tool cords, data center patch cable jackets where flexibility and non-halogen specifications intersect, medical equipment power cords requiring autoclave-resistant surfaces, and automotive sensor cable jackets specified for under-hood temperatures up to 125°C intermittent.
Pharmaceutical dropper bulb and vial stopper formulation with extractables thresholds and tear-strength optimization constitutes a specialized downstream scenario where the absence of vulcanization byproducts is a decisive material selection criterion. The production sequence for this product category typically begins with compression molding of the SEBS compound in multi-cavity tools at 175–195°C and 50–100 bar cavity pressure, or injection molding on 80–150 tonne machines when complex geometry requires gated filling. The critical processing constraint in this application is the prevention of localized shear heating within the screw and runner system, as material temperatures exceeding 220°C initiate oxidative scission reactions that generate low-molecular-weight oligomers detectable in subsequent extractables analysis. Pharmacopoeial compliance is anchored to USP <87> Biological Reactivity Tests, In Vitro, conducted using MEM elution on finished components, and USP <88> Class VI for systemic toxicity evaluation where device regulatory submissions mandate the full biological test battery. European compliance referencing Ph. Eur. 3.1.3 (Polyolefines) and 3.1.5 (Polyethylene with additives for containers for parenteral and ophthalmic preparations) is established through the absence of intentionally added substances outside permitted additive lists and the demonstration that extractable profiles contain no element or compound above recognized safety thresholds. Total organic carbon (TOC) analysis of aqueous extracts from SEBS dropper bulbs, performed per USP <643> or EP 2.2.44, typically yields values below 5 mg/L for 70°C/24-hour extraction, meeting the thresholds applied to purified water and Water for Injection container systems. The four-element requirement of compliance standard, formulation addition ratio, production process, and terminal product type is fully demonstrated in this scenario, with total extractables from the finished component held below 15 mg/100 mL for products intended for repeated-use oral dosing applications. Tear strength per ASTM D624-00 Die C for dropper bulb walls must exceed 18 kN/m to withstand repeated squeezing cycles of 50–100 actuations/day over a 30-day patient use period, and the SEBS compound's inherent resilience provides this without the need for reinforcing fillers that would compromise clarity or compliance status. Terminal product categories include ophthalmic and nasal dropper bottle bulbs, oral syringe tip caps, vial stoppers for lyophilized drug presentation, and carafe dispensing valve components for liquid pharmaceutical packaging systems.
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Kraton™ G SEBS-Comp. G7705 GI-N is a hydrogenated styrenic block copolymer compound supplied as a natural-colour injection-moulding thermoplastic elastomer. The “SEBS-Comp.” designation separates it from unmodified Kraton G polymer grades such as the G1650 and G1652 series; the GI-N suffix identifies an injection-moulding natural variant in the manufacturer’s classification. Public documentation for this class describes a styrene-ethylene/butylene-styrene matrix with a polyolefinic modifier and process oil; the exact modifier-to-oil ratio is not fully disclosed in all public datasheets. The compounding step produces a pellet with a target Shore A hardness of 70 and a melt viscosity intended for cold- or hot-runner injection tools. This distinguishes G7705 GI-N from neat SEBS polymers that require a separate twin-screw oil-extension pass before injection moulding.
Material acceptance for G7705 GI-N is normally based on Shore A hardness, specific gravity, melt mass-flow rate, and lot-specific tensile and tear data. The table below summarises the primary specification matrix. Tensile stress at break and tear strength are often not published directly for the GI-N suffix in all online sources; these values should be obtained from the certificate of analysis or measured on plaques moulded from the actual lot. Batch-to-batch variation in melt mass-flow rate should be monitored because it directly affects fill pressure in multi-cavity tools.
| Property | Test method | Typical/target | Condition |
|---|---|---|---|
| Shore A hardness | ASTM D2240 | 70 Shore A | 15 s delay |
| Specific gravity | ASTM D792 | 0.90 g/cm³ | 23 °C |
| Melt mass-flow rate | ISO 1133-1:2022 | 5 g/10 min | 230 °C/2.16 kg |
| Tensile stress at break | ISO 37 | Lot-specific | 500 mm/min |
| Tear strength | ASTM D624 die C | Lot-specific | 500 mm/min |
| Compression set | ASTM D395 | Lot-specific | 70 h/23 °C |
Drying is required only when storage exceeds the original moisture-barrier packaging after opening. A desiccant dryer set at 80 °C for 2–4 h with a dew point below −30 °C is sufficient; hopper residence at drying temperature should not exceed 8 h. Uncontrolled moisture produces splay and gate blush in moulded parts even though the saturated mid-block has low equilibrium water absorption.
The material runs on a general-purpose polyolefin screw with an L/D ratio of 20:1–24:1 and a compression ratio of 2.5:1–3:1. A low-shear check ring is preferred because restrictive non-return valves can overheat the melt and create degradation specks. Barrel temperatures are typically profiled from 160 °C in the rear zone to 210 °C at the nozzle, with measured melt temperature between 190 °C and 220 °C. Back pressure is held at 0.5–1.0 MPa, and screw speed is normally 80–150 min⁻¹ for 40–60 mm screws. Injection speed is medium to fast depending on wall thickness; thin-wall sections below 1.0 mm require short fill times but also increase shear heating. Hold pressure is set to 40–60% of initial injection pressure until gate freeze, with hold time established by weight stabilisation on the moulding line. Clamp force is calculated from projected area and a specific cavity pressure of 25–35 MPa; for a four-cavity cold-runner tool with a projected area of 180 cm², the required clamp is approximately 54–63 t.
Cold-runner tools with generous runner diameters and fan or side gates reduce jetting and burn marks. Mould temperature is maintained at 20–40 °C; high-gloss surfaces may require 60 °C to reduce visible flow lines. Venting depths of 0.01–0.03 mm at the end of fill are recommended. Shrinkage is anisotropic; unfilled SEBS compounds in this hardness range commonly show flow-direction shrinkage of 1.2–1.8% and transverse shrinkage of 1.5–2.0% when measured according to ASTM D955. Hot-runner systems should use externally heated manifolds without dead spots; internally heated systems can overheat low-viscosity SEBS. Gate diameter should be at least 0.5 mm for thin-wall sections, with gate land length of 0.5–1.0 mm. Purging between colour changes is performed with polypropylene or high-density polyethylene; PVC purge compounds should be avoided because thermal degradation by-products can contaminate the hydrogenated mid-block.
Adhesion to polypropylene in two-shot or insert over-moulding is dominated by interdiffusion at the melt interface, not by covalent bonding. The polypropylene substrate should be at least 70 °C when the second shot arrives; lower temperatures produce a frozen skin and bond-line separation. The G7705 GI-N melt is delivered at 200–220 °C, and the tool temperature is kept above 30 °C during the second shot. Polyamide, polyacetal, and PBT substrates do not form useful adhesion without a mechanical interlock or an adhesion-promoting tie layer; published adhesion data for G7705 GI-N on these substrates is limited. When bonding is critical, peel testing according to ASTM D903 should be used, and the failure mode should be cohesive rather than adhesive. Silicone-based external mould-release sprays degrade bond strength and should be excluded from over-moulding areas.
Food-contact status should be confirmed for the final article, not assumed from the pellet. In the United States, repeat-use elastomeric articles are evaluated under 21 CFR 177.2600; extraction testing may be required on the finished device. For European Union plastics intended for food contact, Regulation (EU) No 10/2011 applies, with specific migration limits for the formulation’s low-molecular-weight fraction. General product safety falls under Regulation (EC) No 1935/2004. RoHS documentation is tied to Directive 2011/65/EU as amended by (EU) 2015/863, with phthalate restrictions enforced at 0.1% by mass in a homogeneous material. REACH obligations arise under Regulation (EC) No 1907/2006. This grade is not assumed to be USP Class VI or ISO 10993 compliant unless the supplier explicitly certifies the finished article after sterilisation.
| Regulatory framework | Scope | Verification basis |
|---|---|---|
| FDA 21 CFR 177.2600 | Repeat-use elastomeric articles | End-article extraction testing |
| Regulation (EU) No 10/2011 | Plastic food-contact materials | Specific migration testing |
| Directive 2011/65/EU | RoHS restricted substances | Homogeneous-material analysis |
| Regulation (EC) No 1907/2006 | REACH SVHC communication | Article-level declaration |
G7705 GI-N differs from unmodified SEBS polymers in hardness, melt flow rate, and tensile strength: it is softer, flows more readily, and carries a lower tensile ceiling than neat G1652 E. Relative to an EPDM/PP thermoplastic vulcanizate, G7705 GI-N processes at lower barrel temperatures and has lower melt viscosity, but it typically shows higher compression set above 100 °C and poorer resistance to hot mineral oil; comparative selection should use ASTM D395 and ASTM D471 for oil ageing. Relative to flexible PVC, G7705 GI-N contains no ortho-phthalate plasticiser, although final phthalate content must still be verified for RoHS declarations. The grade is therefore used in consumer articles with short-term skin contact, moderate environmental exposure, and injection-moulding cycle-time constraints rather than high-temperature automotive or oil-immersed service.
Soft-touch grips, tool handles, footwear trim, suction cups, and non-dynamic sealing elements are typical applications for a 70 Shore A SEBS compound. In grip applications, tear initiation resistance is more important than tensile strength; lot-specific tear data should be obtained by ASTM D624 die C. The material is not recommended for continuous immersion in hot mineral oil, aromatic solvents, or strong oxidising agents because the hydrocarbon mid-block swells and loses dimensional stability. For applications requiring repeated flexing, flex-cut growth resistance should be evaluated separately because published data for this exact GI-N variant is limited.
Three recurring production-scale failure modes are observed in this class of compounded SEBS. Gate blush results from moisture or over-sheared melt; corrective action includes drying at 80 °C, lowering hot-tip temperature below 220 °C, and increasing gate size to reduce shear rate below 10,000 s⁻¹. Jetting occurs with undersized gates or straight-through flow patterns and is corrected by side gating, tab gating, or reduced initial injection velocity. Oil exudation appears as surface tack after 7 days at 23 °C and is associated with high melt temperature, excessive residence time above 230 °C, or a damaged check ring. Lot-to-lot MFR shifts above ±10% from the qualified baseline can change fill time in multi-cavity tools; in-line rheology or ISO 1133-1:2022 lot testing is used to monitor that variance.