| HS Code | 784020 |
| Polymer Type | SEBS compound |
| Appearance | Natural-colored pellets |
| Density | 0.91 g/cm³ |
| Hardness Shore A | 42 |
| Tensile Strength | 7.6 MPa |
| Elongation At Break | 600% |
| 100 Modulus | 2.1 MPa |
| 300 Modulus | 3.0 MPa |
| Tear Strength | 30 kN/m |
| Compression Set 23 C 22 H | 20% |
| Melt Flow Rate 230 C 2 16 Kg | 10 g/10 min |
| Specific Gravity | 0.91 |
As an accredited Kraton Kraton™G SEBS-Comp. G7720-1001-01 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Kraton G7720-1001-01 is supplied in 25 kg moisture-resistant bags, palletized for safe handling, storage, and transport. |
| Container Loading (20′ FCL) | A 20′ FCL container loaded with palletized Kraton™G SEBS-Comp. G7720-1001-01, properly secured, labeled, and sealed for chemical transport. |
| Shipping | Shipping description (typical): Kraton™ G SEBS-Comp. G7720-1001-01, styrene-ethylene-butylene-styrene block copolymer compound pellets; non-hazardous, not regulated as dangerous goods by DOT/IMDG/IATA. Ship in closed original packaging; protect from moisture, heat, UV, and direct sunlight; store cool, dry, well-ventilated. Confirm classification against current SDS. |
| Storage | Store Kraton™ G SEBS-Comp. G7720-1001-01 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly closed in original packaging to prevent moisture and contamination. Avoid extreme temperatures and humidity. Follow first-in, first-out practices and consult the SDS for specific storage requirements. |
| Shelf Life | Shelf life is 24 months from manufacture when stored dry, cool, and in original unopened packaging. |
In ISO Class 8 cleanroom injection molding where post-mold capture of volatile oligomers is at issue, Kraton G SEBS-Comp. G7720-1001-01 is processed as a neat elastomer or as a polypropylene-alloyed thermoplastic elastomer for medical device components. The grade-specific melt flow rate and Shore A hardness require confirmation against the supplier certificate of analysis before tooling is finalized; published data for this exact subgrade in open literature is limited, so the following numerical windows are conservative engineering estimates for SEBS compounds within the Kraton G family and must be verified on first article qualification. Biocompatibility documentation for medical parts is governed by ISO 10993-1:2018, with cytocompatibility assessed under ISO 10993-5:2009 and sensitization under ISO 10993-10:2021; material-level testing may be filed under USP Class VI protocols and supported by FDA 21 CFR Part 58 GLP data. Formulation for a syringe gasket or fluid-path seal typically incorporates the SEBS compound at 55–85 wt% as the elastomer matrix, homopolymer polypropylene at 15–45 wt% to raise hardness, a hindered phenolic antioxidant at 0.1–0.3 wt%, and optionally medium-viscosity white mineral oil at 0–10 phr only where lower Shore A values below 35 are required. On production-scale equipment, the material is pre-dried at 70–80°C for 2–4 h if silo residence time exceeds 48 h at 60% RH; the melt is injected on a closed-loop electric injection molding machine with a compression ratio between 2.0:1 and 2.5:1, barrel temperatures staged from 170°C near the feed throat to 210°C at the nozzle, and holding pressure held between 40 MPa and 60 MPa. Mold temperature is controlled at 20–40°C, and post-mold annealing at 80°C for 120–180 min stabilizes dimensional tolerances and reduces residual stress before gamma or electron beam sterilization. Terminal finished product types include elastomeric tubing segments, syringe seals, peristaltic pump elements, and fluid-path gaskets; exposure to amine-based additives is avoided where gamma irradiation at 25–40 kGy is planned, because free primary amines accelerate post-irradiation yellowing.
Thermoplastic elastomer systems based on styrene-ethylene/butylene-styrene triblock copolymers are used in automotive interior skins because the hydrogenated mid-block limits unsaturated chain scission during high-shear extrusion; however, fogging is governed by the migration of low-molecular-weight processing oils and additives, not by the SEBS mid-block itself. Compliance with OEM specifications is demonstrated through DIN 75201-B or ISO 6452:2007 fogging tests, VDA 270 odor evaluation, and DIN EN ISO 1183-1:2019 density verification; typical automotive limits require fogging condensate below 2 mg per 10 g sample and reflectance retention above 80%, although individual OEM standards such as GMW 15651 may impose narrower limits. A soft-touch instrument panel skin formulation typically loads G7720-1001-01 at 25–40 wt%, homopolymer polypropylene at 20–35 wt%, ethylene-octene copolymer at 10–20 wt%, high-molecular-weight paraffinic oil at 5–15 wt%, antioxidant at 0.2–0.4 wt%, and release modifier at 0.1–0.2 wt%. The dry blend is compounded on a co-rotating twin-screw extruder with an L/D of 36:1 to 48:1 using a temperature profile that does not exceed 220°C at the die; the melt is then slot-die extruded into sheet of 0.5–1.5 mm thickness and embossed on a three-roll calender stack before negative-pressure thermoforming onto a soft-touch carrier. Airbag cover components are injection molded at 190–215°C melt temperature and 35–50°C mold temperature, with low-temperature ductility verified by ASTM D3763-18 impact testing at -35°C; insufficient SEBS content or excessive oil loading produces brittle fracture at the hinge line. Terminal finished product types include instrument panel skins, door panel soft-touch inserts, airbag outer covers, and center console armrests. Process stability issues appear as die lip plate-out when low-molecular-weight oil fractions are used above 10 wt%, which increases scrap rate and reduces leather-grain transfer fidelity on the embossing roll.
When magnesium dihydrate and melamine polyphosphate are dispersed into a styrenic elastomer matrix for halogen-free flame-retardant cable sheathing, the dispersion quality of the inorganic phase, rather than the SEBS content alone, governs elongation-at-break retention in vertical flame tests and heat-aged tensile strength. This scenario treats G7720-1001-01 as the base elastomer in a zero-halogen wire and cable compound, with associated compliance under UL 1581 for vertical flame propagation, UL 758 for appliance wiring material, IEC 60332-1-2 for flame spread, RoHS Directive 2011/65/EU Article 4, and REACH Candidate List restrictions. A robust cable sheathing formulation uses the SEBS compound at 35–50 wt%, magnesium hydroxide at 40–55 wt% with a median particle size of 0.8–1.5 µm, melamine polyphosphate at 5–12 wt%, zinc borate at 3–8 wt%, processing aid at 0.5–1.0 wt%, and hindered phenolic antioxidant at 0.2–0.5 wt%. The compounded pellet is manufactured on a co-rotating twin-screw extruder with an L/D of 40:1, a side-stuffer positioned after the kneading block, and vacuum venting at -0.08 MPa to remove moisture; barrel temperatures are staged from 150°C at the feed zone to 190°C at the die, because magnesium hydroxide releases water only above 330°C but processing oils may begin to crack above 210°C under extended residence time. Melt pressure exceeding 12–14 MPa at constant screw speed is an early indicator of agglomerated flame-retardant filler and requires adjusting side-stuffer feed rate or increasing the number of dispersion kneading discs. The final wire coating operation uses a 90 mm single-screw extruder with an L/D of 24:1, a barrier screw, a screen pack of 80/120/80 mesh, and a draw-down ratio between 1.5:1 and 3.0:1; conductor preheat at 100–120°C prevents surface condensation and improves insulation adhesion. Terminal finished product types include EV charging cable sheathing, industrial robotics flexing cables, and building wire insulation for cold environments; accelerated aging is assessed by elongation retention after 168 h at 136°C under UL 1581 reference methods.
A polypropylene-supported SEBS compound containing G7720-1001-01 is used for closure liners and sealing gaskets subject to repeated contact with aqueous and fatty foods; compliance is demonstrated under EU Regulation (EC) No 10/2011 with overall migration limits of 10 mg/dm² per EN 1186-1:2002, and for US markets under FDA 21 CFR 177.1810 for styrene block copolymers in repeat-use articles, with the finished liner tested in simulated food environments by FDA 21 CFR 177.2600. The seal formulation adds G7720-1001-01 at 70–100 wt%, homopolymer polypropylene at 0–30 wt%, high-molecular-weight white mineral oil below 10 wt% to minimize extractable low-molecular-weight species, and antioxidant at 0.05–0.15 wt%. Production is by injection-compression molding of annular liners at 190–215°C melt temperature and 20–40°C mold temperature, followed by closure insertion on high-speed capping lines; terminal finished product types include beverage closure liners, jar gaskets, tamper-evident seals, and dairy container sealing rings.
The adhesion window of SEBS overmold grades onto polypropylene is sufficiently wide that the substrate surface temperature alone is the controlling variable, while polycarbonate adhesion requires a maleic anhydride-grafted SEBS coupling interlayer or a pre-primed surface because the hydrogenated mid-block is non-polar. Compliance for consumer articles includes EN 71-3:2019 for toys, EU Regulation (EC) No 1935/2004 for kitchen utensils, and FDA 21 CFR 177.1810 where repeat food contact applies. The overmold compound is used at 90–100 wt%, with color masterbatch at 1–3 wt%, and where polycarbonate is the substrate, a maleated SEBS tie layer is added at 3–8 wt% within the overmold or as a separate 0.1–0.3 mm layer. Two-shot injection molding is performed at 180–200°C melt temperature, 25–50°C mold temperature, and holding pressure of 40–60 MPa; terminal finished product types include power-tool soft grips, toothbrush handles, and kitchen utensil overmolded grips.
Elastomeric closures in parenteral packaging are not tested as final materials but as finished components under compendial requirements that include residual moisture, volatile loss, and extractables after steam autoclaving; SEBS compounds offer low compression set and low extractables when oil loading is constrained. The G7720-1001-01 grade is incorporated at 80–100 wt% of the elastomeric fraction, with polypropylene at 0–20 wt%, white mineral oil at 0–5 wt%, and optionally barium sulfate radiopaque filler at 0–10 wt% where radiographic detection is specified. Compliance is established under USP <381> for elastomeric closures, USP <87> and USP <88> cytotoxicity and systemic injection tests, Ph. Eur. 3.2.9, and ISO 8871-1:2003; terminal steam sterilization is performed at 121°C for 30 min or 134°C for 10 min, after which compression set is evaluated by ISO 815-1:2019 at 70°C for 22 h. Injection-compression molding is used on a multi-cavity cleanroom tool at 185–210°C melt temperature and 20–35°C mold temperature, followed by washing in filtered water and silicone-free lubrication where required; terminal finished product types include vial stoppers, syringe plunger tips, infusion ports, and lyophilization stoppers.
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Kraton™ G SEBS-Comp. G7720-1001-01 is a compounded styrene-ethylene-butylene-styrene thermoplastic elastomer formulated for melt-processable applications requiring a saturated midblock. The designation “SEBS-Comp.” separates the material from neat SEBS polymer grades; the “G7720-1001-01” suffix encodes the base grade, formulation version, and packaging/lot identifier rather than a separate polymer composition. Published single-point specification data for this exact suffix is limited. The controlling documents are the lot certificate of analysis and the manufacturer’s material data sheet for the G7720-1001 series. In general, SEBS compounds of this class contain a hydrogenated ethylene/butylene midblock that replaces the unsaturated butadiene segment of SBS, increasing thermo-oxidative stability and the safe melt-processing ceiling while retaining thermoplastic reprocessability. Unlike vulcanized EPDM or cured silicone, the material can be reprocessed by injection molding, extrusion, or blow molding without a second crosslinking step. The saturated EB midblock also reduces ozone susceptibility relative to unsaturated SBS and lowers density relative to TPU, although solvent resistance, abrasion performance, and creep behavior differ from those polymer classes.
For soft-touch overmolding, medical device components, and food-contact articles, the product is evaluated against relevant biological and physicochemical test programs. Cytotoxicity data are developed under ISO 10993-5; physicochemical conformance for drug packaging is evaluated against USP 661.1 and USP 661.2. Food-contact use requires lot-specific confirmation under 21 CFR 177.1810 and EU Regulation 10/2011 migration testing. These designations do not constitute an automatic compliance declaration for this specific suffix.
Dynamic mechanical analysis for similar SEBS compounds shows an EB midblock glass transition near −50 °C and a polystyrene end-block transition near 95 °C. The low-temperature transition governs flexibility at refrigeration temperatures, while the high-temperature transition defines the softening point and upper service limits for shape retention.
For injection molding, a general-purpose reciprocating-screw machine with a screw L/D of at least 20:1 is used. Barrel temperature profiles for compounded SEBS of this class typically begin at 170 °C in the rear zone, rise to 190–210 °C in the middle and front zones, and maintain nozzle temperature at 200–220 °C. Mold temperature is controlled between 20 °C and 50 °C for fast solidification, although textured surfaces may require higher mold temperature to replicate grain. Melt temperature measured at the nozzle should not exceed 240 °C for extended residence times; above this limit the styrenic end-blocks may undergo chain scission, producing viscosity loss and transfer of degraded material to molded parts.
Continuous compounding on a co-rotating twin-screw extruder with L/D 40:1 and modular screw elements is performed with barrel set points from 160 °C to 220 °C. High-shear kneading blocks are placed downstream of the feed zone to disperse additives; distributive mixing elements are positioned near the die to homogenize melt temperature. Screw speeds of 200–400 rpm are typical, but specific energy input must be monitored because shear heating can raise melt temperature by 10–30 °C above barrel set point. A vacuum vent at −0.06 MPa to −0.08 MPa is applied downstream of the kneading section to strip volatiles.
On production-scale twin-screw compounding lines, liquid plasticizer addition is placed downstream of the first kneading block. Feeding liquid into the feed throat can cause screw slip, lower melt conveying, and a 15–20% reduction in output. Batch-to-batch variation in melt flow rate may exceed 10% when loss-in-weight feeders for polymer and additives are not synchronized. These observations are not grade-specific but establish the sensitivity of the compounding step.
Residual moisture is controlled by desiccant drying at 80 °C for 2–4 hours when ambient relative humidity exceeds 60%. Moisture-related defects include splay, surface chatter, and tensile property loss in extruded profiles.
When capillary rheometry is applied to similar SEBS compounds, pseudoplastic behavior is observed with shear thinning above 100 s⁻¹. Melt shear viscosity may range from 100 Pa·s to 800 Pa·s at 230 °C and 1000 s⁻¹ depending on oil content and styrene content; lot-specific data by ISO 11443 is required before gate and runner sizing.
In thin-wall molding trials, gate freeze time is evaluated by cavity pressure transducers. A gate diameter below 1.0 mm may cause premature gate freeze and high residual stress, while an edge gate thickness of 1.2–2.0 mm with land length of 0.8–1.0 mm is commonly used for soft SEBS compounds. Cavity pressure at switchover is held between 300 bar and 600 bar; holding pressure decay is monitored to avoid sink marks. The product is also processed by profile extrusion, where screw L/D of 24:1 to 30:1 and a breaker plate with mesh packs of 40/60/80 are used to build back pressure.
The G7720-1001-01 compound is supplied as pellets and is molded with a metering stroke of 1.5–2.5 D and back pressure of 5–15 bar to avoid excessive shear heating. Screw recovery speed is set to fill the shot without exceeding 80% of available cooling time. Because SEBS compounds exhibit compressibility in the barrel, decompression after rotation is limited to 3–5 mm; excessive decompression draws air into the melt and creates silver streaks.
For hot-runner systems, internal runner diameters above 4.0 mm and open-pipe nozzles are required. Valve gates are preferred for large parts to prevent stringing. Cold-runner sprue and runner systems use full-round runners with diameters of 4.0–6.0 mm and cold slug wells of at least 1.5 times runner diameter.
Part ejection is affected by the low flexural modulus of the compound. Draft angles of 1.5°–3.0° are used on deep cores, and air blow-off or poppet valves are applied to prevent vacuum sticking. Shrinkage allowance in the range of 1.2%–2.0% is used in the mold design phase, but final shrinkage must be determined by pilot mold trials because orientation and packing pressure shift the value.
The choice between G7720-1001-01 and a high-styrene neat SEBS such as Kraton G1650 or G1651 is governed by hardness, melt flow, and oil tolerance. High-styrene neat SEBS grades typically exhibit Shore A hardness above 70 and melt mass-flow rates below 1 g/10 min at 230 °C/5 kg under ISO 1133-1:2022, whereas compounded grades in the G SEBS-Comp. series are formulated for lower hardness and higher flow. The exact MFR of G7720-1001-01 must be confirmed by lot documentation.
In overmolding onto polypropylene, adhesion depends on the compatibility of the EB midblock with the PP amorphous phase and on melt contact temperature. Preheating the PP substrate to 70–100 °C before overmolding improves mechanical interlock and interfacial diffusion. Cohesive failure within the SEBS layer rather than adhesive delamination is the target failure mode. Peel strength is evaluated by ASTM D903 or ISO 8510-2.
When replacing plasticized PVC, G7720-1001-01 avoids ortho-phthalate plasticizer migration but may exhibit higher gas permeability and lower tear strength than plasticized PVC. Tear resistance is assessed by ASTM D624 die C; compression set is assessed by ISO 815-1:2022.
Relative to a TPV such as PP/EPDM vulcanizate, the SEBS compound has a lower continuous-use temperature limit and lower compression set resistance at 100 °C, but offers better melt stability and lower hardness at equivalent flow. These differences are measured by ISO 815-1:2022 compression set and ISO 188:2023 aging.
Incoming quality control for this class of compounded SEBS uses the following test designations. Target ranges are established by the manufacturer’s certificate of analysis; the table lists the method and parameter without fabricated numerical limits.
| Test | Method | Parameter |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 / ASTM D1238 | 230 °C / 5 kg; compare to CoA |
| Density | ISO 1183-1:2019 / ASTM D792 | specific gravity at 23 °C |
| Shore A hardness | ISO 48-4:2018 / ASTM D2240 | 15 s reading |
| Tensile stress at break | ISO 37:2017 / ASTM D638 | MPa |
| Elongation at break | ISO 37:2017 / ASTM D638 | % |
| Compression set | ISO 815-1:2022 / ASTM D395 Method B | 23 °C/22 h and 70 °C/22 h |
| Oxidative aging | ISO 188:2023 / ASTM D573 | retention of tensile after 70 °C/168 h |
| UV weathering | ISO 4892-2 Method A / ASTM G155 | comparative gloss and tensile retention |
Storage is controlled at 5–40 °C in sealed original packaging, protected from UV and moisture. Bags opened beyond 24 h and exposed to relative humidity above 60% require re-drying. The material is incompatible with aromatic hydrocarbon solvents and strong oxidizing acids; aromatic hydrocarbons can solvate the polystyrene end-blocks and cause swelling. High loadings of mineral oil reduce tensile strength and require recompounding rather than dry blending at the press. Processing machinery is purged with polypropylene after shutdown to prevent oxidative gel formation in the barrel.
For steam sterilization at 121 °C, compatibility testing under ISO 17665-1 is required. Oxidative disinfectants such as hydrogen peroxide plasma may alter surface tack and color. Gamma irradiation above 25 kGy can crosslink or chain-scission the EB midblock depending on dose rate and antioxidant package; lot-specific dose mapping is required. Published data for this specific configuration is limited; all processing boundaries are verified on the production line using lot-specific documentation.