| HS Code | 468691 |
| Grade | Denka Asaflex SBC 815 |
| Chemical Composition | Styrene-butadiene block copolymer |
| Polymer Type | SBC |
| Form | Pellets |
| Appearance | Transparent |
| Density | Approx. 1.01 g/cm³ |
| Styrene Content | Approx. 30 wt% |
| Melt Flow Rate | Approx. 8 g/10 min at 200°C/5 kg |
| Shore A Hardness | Approx. 75 |
| Tensile Strength | Approx. 20 MPa |
| Elongation At Break | Approx. 700% |
| Vicat Softening Temperature | Approx. 70°C |
| Haze | Low haze / transparent |
| Refractive Index | Approx. 1.53 |
As an accredited Denka Asaflex SBC 815 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Denka Asaflex SBC 815 is supplied in 25 kg moisture-resistant paper sacks, palletized for industrial handling and storage. |
| Container Loading (20′ FCL) | Denka Asaflex SBC 815 is loaded palletized in a 20′ FCL container, dry, secured, and compliant with shipping requirements. |
| Shipping | Denka Asaflex SBC 815 is typically shipped as thermoplastic pellets in moisture-resistant bags or bulk containers. Store in a cool, dry, ventilated area away from direct sunlight, heat, and ignition sources. Keep packaging sealed to prevent moisture contamination and follow local transport regulations. |
| Storage | Store Denka Asaflex SBC 815 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed to prevent moisture and contamination. Avoid contact with strong oxidizing agents. Maintain moderate temperatures, protect from UV exposure, and use proper grounding to prevent static buildup. Follow local regulations and SDS recommendations. |
| Shelf Life | Denka Asaflex SBC 815 typically has a 24-month shelf life when stored dry and cool in original unopened packaging, away from sunlight. |
Compounding Denka Asaflex SBC 815 with general-purpose polystyrene for transparent thermoformed food-service sheet is carried out on a co-rotating twin-screw extruder with a screw diameter of 35 mm and L/D ratio of 40:1. The screw profile uses two high-shear kneading blocks after the melting zone followed by distributive mixing and a vacuum devolatilization port at -0.08 MPa. Melt temperature at the die is maintained between 190°C and 210°C. Drying in a desiccant dryer at 70°C for 2 h is recommended when ambient relative humidity exceeds 60%. The compounding let-down range is 15 wt% to 35 wt%. Below 15 wt%, notched impact resistance improves but cold-chain pack-out trials do not reliably show a reduction in cracked-clamshell defects. Above 35 wt%, flexural modulus drops to a level that causes stack-load deformation in automated distribution. The compounded pellets are re-processed through a vented single-screw extruder with a 38D barrel for sheet casting. The three-roll stack is operated with roll temperatures of 60°C, 70°C, and 50°C, and nip pressure is set between 20 N/mm and 40 N/mm to limit machine-direction orientation. Formed trays are tested for haze according to ASTM D1003-13, notched Izod impact according to ASTM D256-23, and flexural strength according to ISO 178:2019. Food-contact suitability is evaluated under US FDA 21 CFR 177.1810 for styrene block copolymers and under EU Regulation 10/2011/EC. Edge trim regrind is re-introduced at 20%. Because the first heat history is compounding, the second is sheet extrusion, and the third is thermoforming regrind, the regrind fraction is kept at 20% or lower to avoid a measurable increase in micro-gel counts when melt temperature exceeds 220°C during start-up.
| Standard or provision | Scope | Testing requirement |
| US FDA 21 CFR 177.1810 | Styrene block copolymers in food-contact articles | End-testing for extractives appropriate to food type and temperature of use |
| US FDA 21 CFR 177.1640 | Polystyrene and rubber-modified polystyrene in food-contact articles | End-testing for extractives in the blended polymer system |
| EU Regulation 10/2011/EC | Plastic materials intended to contact food | Overall migration limit of 10 mg/dm² or 60 mg/kg depending on article geometry |
| EC Regulation 2023/2006 | Good manufacturing practice for food-contact materials | Process validation and batch traceability records |
Asaflex SBC 815 is compounded with general-purpose polystyrene at loadings between 30 wt% and 60 wt% for cast film that is subsequently oriented in the transverse direction on a tenter-frame unit. The polybutadiene midblock phase in this grade is not crosslinked, so orientation is a physical stretching process. The cast film edge temperature before the orientation zone is monitored by infrared pyrometry with a tolerance of ±5°C. Differential scanning calorimetry per ISO 11357-2:2020 is used to identify the styrene-domain glass transition and the lower-temperature relaxation of the butadiene-rich phase. The orientation zone setpoint is positioned 5°C to 10°C above the butadiene-phase relaxation onset. If the film temperature is too low, transverse stretching creates micro-tears that appear as haze bands across the sleeve. If the film temperature is too high, orientation memory is lost and shrink tensile stress measured by ISO 14616:2019 falls below the level required to hold the label in place through the shrink tunnel. Free shrink after immersion is reported according to ASTM D2732-21. Slitting edge trim from this oriented film contains pre-stretched molecules and increases die swell when re-fed into the cast layer; therefore trim re-use is limited to 10 wt%. Published data for the exact transverse-direction orientation window of Asaflex SBC 815 in this film configuration is limited, so pilot trials on a tenter frame with a width of 1.2 m are required to set infrared panel output for a given film gauge.
Thin-wall injection moulding of Asaflex SBC 815-modified polystyrene for clear dispenser closures is performed with a valve-gated hot-runner mould and a clamp force of 120 metric tons for an eight-cavity arrangement. Melt temperature is kept at 200°C to 220°C. The fill time is held below 0.8 s to prevent flow-front freeze-off in 0.8 mm nominal wall sections. The hot-runner channels are purged after each shift because the butadiene phase degrades under extended residence; degradation appears first as a yellowness shift measured by ASTM E313-20 before mechanical property loss is detected. Mould temperature is controlled between 35°C and 45°C. Vent depth is limited to 0.015 mm because the low-viscosity melt flashes at deeper vent channels. Notched Izod impact of the moulded closure is measured by ASTM D256-23. Snap-fit retention is evaluated on a motorised torque stand after 100 assembly cycles. When the closure wall falls below 0.6 mm, the melt temperature must be raised to 225°C, but only if hot-runner residence time is kept below 15 s. Longer residence at this temperature generates gel specks that collect in the valve-gate seat and produce short shots or gate blemishes.
| Operation | Melt temperature range | Critical equipment setting | Test standard |
| Twin-screw compounding with GPPS | 190–210°C | Vacuum vent -0.08 MPa | ISO 1133-1:2022 |
| Cast film for sleeve labels | 200–220°C | Orientation zone controlled to ±5°C | ISO 14616:2019 |
| Injection moulding of thin-wall closures | 200–225°C | Hot-runner purging after each shift | ASTM D256-23 |
High-gloss cosmetic packaging sheet produced with Asaflex SBC 815 and general-purpose polystyrene requires a single-screw extruder with a homogeneous melt-temperature profile and a screen pack configuration of 60/80/100 mesh. The screen pack traps gel particles formed from thermal history and edge-trim contamination. Pressure drop across the screen pack rises from approximately 3 MPa to 8 MPa over an eight-hour run when regrind content is present; operators replace the screen pack at 10 MPa to prevent excessive shear heating. Barrel zones are set at 160°C, 180°C, 190°C, 200°C, and 205°C. The die zone is held at 200°C. Sheet surface gloss is measured with a 20° gloss meter according to ASTM D2457-21. Values below 90 GU on calendered sheet indicate melt fracture, roll roughness, or a degrading butadiene phase. A polished chrome roll with surface roughness of 0.01 μm Ra is required to maintain gloss. Because the butadiene phase is shear-sensitive, screw speed is limited to 60 rpm on a 45 mm extruder. Higher screw speeds lower haze but increase gel formation in the melt stream. The sheet is printed with solvent-based flexographic inks, and ink adhesion is checked by cross-cut testing according to ASTM D3359-23. Printed sheet is thermoformed into cosmetic inserts at surface temperatures between 120°C and 140°C. At the upper end of that range, surface gloss decreases slightly, but the lower in-plane stress reduces ink delamination after high-speed die cutting.
Post-industrial polystyrene regrind from mixed HIPS and GPPS sources is compounded with Asaflex SBC 815 at 10 wt% to 20 wt% to restore impact resistance lost during previous heat histories. The regrind is collected from thermoforming skeletons and injection runner scrap. It often contains residual mineral oil, antistatic additives, and print ink residues that reduce the thermal stability of the styrenic phase. Melt temperature is therefore reduced to 180°C to 190°C. The extruder is operated with a vacuum vent at or below 25 mbar absolute and a nitrogen purge on the feed throat to limit oxidative chain scission. Melt flow stability is monitored by ISO 1133-1:2022 using the 200°C/5 kg condition. Batches with melt flow rate variation above ±0.5 g/10 min are segregated because that level of drift indicates non-uniform regrind composition. Published data for long-term performance of Asaflex SBC 815 in post-industrial mixed regrind matrices is limited; plant trials on a 52 mm co-rotating twin-screw line are used to qualify each recovered feedstock lot before production release.
Asaflex SBC 815-modified polystyrene parts joined by ultrasonic welding behave differently from unmodified general-purpose polystyrene at the joint interface because the butadiene phase alters acoustic energy dissipation. A 20 kHz ultrasonic press with amplitude of 35 μm and weld time of 0.15 s is effective for a wall thickness of 1.0 mm. The reduced stiffness of the SBC-rich phase requires a triangular energy director with a height of 0.3 mm to localise melt formation. Amplitudes above 45 μm cause localised thermal degradation at the joint and visible white marks on the transparent surface. The welded assembly is tested for gross leak according to ASTM F2096-11. For food-contact applications, the weld line is included in extractives testing evaluated under US FDA 21 CFR 177.1810. Fixture alignment must be maintained within 0.05 mm across the nest because warpage in thin SBC-modified walls shifts the energy-director contact position and produces variable weld strength.
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Denka Asaflex SBC 815 is a styrene-butadiene block copolymer supplied by Denka Company Limited as a transparent, high-styrene-content thermoplastic. The material is produced by sequential anionic polymerization, resulting in a phase-separated morphology in which polystyrene end-blocks form discrete glassy domains that act as reversible physical crosslinks, while the butadiene midblock provides impact-energy dissipation and low-temperature ductility. The product is typically supplied in pellet form for injection moulding, sheet extrusion, and blow moulding. Because the grade is formulated for optical clarity and rigidity rather than soft-elastomer behaviour, its property profile occupies a different quadrant from oil-extended SBS thermoplastic elastomers. Published numerical data for this specific Denka grade are limited; the property envelope in Table 1 is therefore compiled from supplier-typical transparent SBC values and must be verified against the current certificate of analysis for the purchased lot.
Sequential anionic polymerization controls the block molecular weights and the styrene-to-butadiene ratio. Gel-permeation chromatography with polystyrene calibration is used to measure number-average molecular weight and dispersity of the soluble fraction; for commercial SBC resins of this class, number-average molecular weight is typically in the range of 60 000–150 000 g/mol, with dispersity of 1.05–1.20. The butadiene midblock contains 1,4-cis, 1,4-trans, and 1,2-vinyl microstructures; the 1,2-vinyl content influences the glass transition temperature of the polybutadiene phase. In transparent SBC grades, vinyl content is often controlled between 7–12 mol% to suppress crystallinity and maintain optical clarity. The polystyrene domain glass transition temperature is near 95–105 °C, while the polybutadiene phase glass transition temperature is near −80 to −60 °C. These two transitions produce the low-temperature impact resistance observed in notched impact testing at −30 °C.
Transmission electron microscopy of ruthenium-tetroxide-stained ultrathin sections shows the hard polystyrene domains as dark, dispersed rods or lamellae depending on styrene content. In high-styrene SBCs such as the 815 grade, the morphology is typically a co-continuous or lamellar arrangement rather than discrete spherical domains. Interdomain spacing is in the tens-of-nanometre range, below the wavelength of visible light, which preserves transparency. Stress-whitening occurs only when local tensile dilation voids the polybutadiene phase; higher styrene content reduces overall stress-whitening compared with lower-hardness SBC grades, but weld lines remain susceptible because of unfavourable domain orientation.
The following values define the expected performance envelope for transparent styrene-butadiene block copolymers of this type when conditioned at 23 °C ± 2 °C and 50 % ± 10 % relative humidity in accordance with ISO 291:2008. The ranges are suitable for preliminary material selection and mould-filling simulation but are not batch-release limits. For acceptance sampling, the supplier’s certificate of analysis and the specified test method versions govern.
| Property | Test method | Typical value or range |
|---|---|---|
| Density | ISO 1183-1:2019 | 1.00–1.02 g/cm³ |
| Melt mass-flow rate, 200 °C/5 kg | ISO 1133-1:2022 | 4–12 g/10 min |
| Tensile yield stress | ISO 527-2:2012 | 18–25 MPa |
| Tensile elongation at break | ISO 527-2:2012 | 200–400 % |
| Flexural modulus | ISO 178:2019 | 800–1300 MPa |
| Notched Izod impact, 23 °C | ASTM D256-23 | 30–70 J/m |
| Shore D hardness | ISO 868:2003 | 60–68 |
| Vicat softening temperature, A50 | ISO 306:2022 | 68–88 °C |
| Light transmittance, 2 mm plaque | ASTM D1003-21 | >88 % |
| Haze, 2 mm plaque | ASTM D1003-21 | <3 % |
The hardness and flexural modulus values place the 815 grade at the rigid end of the transparent SBC spectrum. Users should not use the lower bound of the elongation range for safety-critical snap-fit design; ISO 527-2 tensile bars cut from injection-moulded plaques may overestimate ductility relative to moulded parts with weld lines or gate blush. For tensile property comparison, specimen geometry is critical. ISO 527-2 type 1A bars machined from annealed plaques may yield higher elongation at break than ASTM D638-14 type I bars moulded with end-gated tools because of orientation differences. Notched Izod data on 3.2 mm specimens should not be used alone to predict drop-impact performance on thin-wall containers; instrumented puncture testing at 2.0 m/s impact speed gives more relevant failure-energy data.
General-purpose polystyrene typically exhibits a notched Izod impact of 12–20 J/m under ASTM D256-23 and fails through craze propagation. Transparent styrene-butadiene block copolymers of this class shift the failure mode toward shear yielding because the polybutadiene domains cavitate and terminate crazes before catastrophic crack growth. Asaflex SBC 815 is therefore positioned as a transparent, ductile replacement for general-purpose polystyrene in thin-wall parts that must survive drop impacts. Soft SBS thermoplastic elastomers, by contrast, contain lower styrene content and are supplied with Shore A hardness values below 90; they are oil-extended or compounded for elastic recovery. The 815 grade is not an elastomer but a rigid thermoplastic with Shore D hardness in the 60–68 range, giving it closer affinity to styrene-butadiene copolymers and methyl methacrylate-butadiene-styrene grades. Direct numerical comparison with lower-numbered Asaflex grades is limited; selection between the 800-series grades should be made on the basis of side-by-side moulding trials using ISO 294-1:2023 multi-cavity tools and the current supplier datasheet.
Compared with bisphenol-A polycarbonate, Asaflex SBC 815 has lower density, lower continuous-use temperature, and lower notched impact strength but provides easier thin-wall flow and lower drying burden. Polycarbonate typical density is 1.20 g/cm³ with drying at 120 °C for 4 h; SBC parts of similar thickness are approximately 15–20 % lighter. Continuous-use temperature under load is lower for SBC because polystyrene domain softening begins near 70–90 °C, while polycarbonate can tolerate 120 °C. This positions the 815 grade for non-thermal packaging and consumer goods rather than hot-fill or autoclave applications. Within the Denka Asaflex range, the numerical suffix denotes differences in melt flow and hardness. The 815 grade is typically selected where higher stiffness and surface hardness are required relative to softer grades; published quantitative differences between the 800-series grades are limited and should be confirmed by side-by-side injection moulding with the same tool and cycle.
In injection-moulding trials on polished P20 tool steel cavities, Asaflex SBC 815 produces low-haze parts only when melt temperature, mould temperature, and injection speed are controlled within narrow limits. Predrying is mandatory when pellet moisture exceeds 0.05 wt% by ISO 15512:2019 Karl Fischer titration; typical desiccant-dryer settings are 60–70 °C for 2–4 h. At relative humidity above 60 %, hopper drying with a closed-loop desiccant system and a nitrogen purge prevents surface splay and haze. These defects appear as fan-shaped silver streaks radiating from the gate and are caused by vaporisation of water absorbed on the pellet surface during plasticating.
The melt-processing window for this grade is bounded at the low end by incomplete plasticating and at the high end by thermal degradation. Barrel settings typically follow a rising profile: rear 150–170 °C, centre 170–190 °C, front 180–200 °C, and nozzle 190–210 °C. Melt temperatures above 220 °C initiate polybutadiene oxidation and gel formation, while melt temperatures below 170 °C increase apparent viscosity to the point that thin-wall sections below 1 mm may exhibit short shots. Residence time at the upper melt temperature should not exceed 5–10 min; longer residence in the barrel leads to yellowing and black specks from degraded material at the screw root and check ring.
The melt is strongly shear-thinning. For transparent SBC grades with similar styrene content, capillary rheometry per ISO 11443:2021 gives apparent viscosity in the range of 200–500 Pa·s at 200 °C and 100 s⁻¹, falling to below 100 Pa·s at 1000 s⁻¹. Mould-filling simulation should use cross-WLF or Bird-Carreau viscosity fits generated from three-temperature capillary data, not single-point melt-flow-rate values. Screw geometry on reciprocating injection machines should be a general-purpose polyolefin-type screw with L/D 20:1–25:1, compression ratio 2.5:1–3.0:1, and a check-ring radial clearance no greater than 0.05–0.10 mm. A shallow metering depth reduces overheating in the transition zone, where shear heating can locally exceed the barrel setpoint by 10–20 °C.
Injection speeds should be moderate to high, with fill times of 0.8–2.0 s for parts of 1–3 mm wall thickness; excessive shear rates above 10 000 s⁻¹ at the gate can surface-melt the polystyrene domains and create flow marks. Holding pressure is typically 20–50 MPa hydraulic pressure, depending on machine intensification ratio and part geometry. Mould temperatures of 20–40 °C are recommended; polished mould surfaces below Ra 0.1 µm are required for low haze. Gate dimensions should avoid abrupt transitions: a fan gate of 0.8–1.2 mm thickness reduces jetting and improves optical uniformity.
Additive packages in Asaflex SBC 815 must be chosen to avoid haze, migration, and regulatory non-compliance. Colour concentrates based on polystyrene or SBC carriers are added at 1–3 wt% and require predrying before blending. Slip and antiblock additives based on high-purity erucamide or silica can reduce blocking in extruded sheet at loadings of 500–2000 ppm, but excess migratory additives increase surface haze and may alter food-contact migration behaviour. For food-contact applications, the raw resin is typically supported by a supplier statement referencing FDA 21 CFR 177.1810 for styrene block polymers and Regulation (EU) No 10/2011 with specific migration limits; the converter must verify the final article under the applicable migration testing protocol. For medical device housings and fluid-contact parts, biocompatibility screening is governed by ISO 10993-5:2009 for cytotoxicity and ISO 10993-10:2021 for skin sensitisation and irritation; these tests are performed on the finished device, not on the raw pellet.
| Compliance requirement | Standard or regulation | Verification scope |
|---|---|---|
| Food contact, United States | FDA 21 CFR 177.1810 | Supplier composition statement; finished-article migration under FDA protocols |
| Food contact, European Union | Regulation (EU) No 10/2011 | Overall migration and specific migration limits |
| RoHS | Directive 2011/65/EU, Annex II | Pb < 0.1 wt%, Cd < 0.01 wt%, Hg < 0.1 wt%, PBB/PBDE < 0.1 wt% |
| REACH | Regulation (EC) No 1907/2006 | SVHC candidate list screening |
| Medical biocompatibility | ISO 10993-5:2009, ISO 10993-10:2021 | Finished device testing |
| Toys | EN 71-3:2019+A1:2021 | Migration of elements |
In transparent packaging and consumer-goods applications, Asaflex SBC 815 is processed into display cartons, cosmetic containers, and parts requiring a combination of clarity and drop-impact resistance. Sheet extrusion lines with 30:1–36:1 L/D barrier screws and polished chrome-plated chill rolls at 15–30 °C are used to produce sheet with thickness 0.3–2.0 mm; the sheet is subsequently thermoformed at 120–150 °C surface temperature. In injection moulding, the grade is used for transparent caps, lids, and housings where weld-line strength and gate blush are controlled through sequential valve gating and hot-runner manifolds with 220–240 °C nozzle setpoints. For medical diagnostic components, the material is often specified because its density of approximately 1.00–1.02 g/cm³ allows lightweight devices; however, sterilisation by ethylene oxide or gamma radiation must be validated for the specific grade and part geometry. Published data for gamma-sterilised Asaflex 815 is limited; converters should request radiation-stability data or conduct ISO 11137-1:2006 dose-setting studies.
The main operational boundary for Asaflex SBC 815 is thermal-oxidative degradation of the butadiene midblock. At melt temperatures above 220 °C, gel particles form through crosslinking of polybutadiene unsaturation; these gels appear as fisheyes in extruded sheet and as black specks in injection-moulded parts. The degradation is autocatalytic and is accelerated by dissolved oxygen, residual peroxide from colour concentrates, and stagnant material in hot-runner dead spots. The material should not be purged with cellulose-based purging compounds above 230 °C, and regrind content should be limited to 20–40 % by weight unless optical and mechanical property data for the specific regrind fraction are available. Contact with amines, strong bases, and transition-metal stearates should be avoided because these compounds can catalyse oxidative chain scission or discolouration. The grade is not recommended for continuous service above 60–70 °C under load, because the polystyrene domains soften near the Vicat softening temperature and creep resistance decreases. For outdoor applications, the butadiene segment requires UV stabilisation; unpigmented or transparent natural parts exposed to QUV-A 340 nm testing per ASTM D4329-21 may yellow before 500 h unless compounded with a suitable UV absorber and hindered amine stabiliser at loadings specified by the stabiliser supplier.