| HS Code | 135927 |
| Manufacturer | Lucobit AG |
| Brand | Lucopren |
| Productdesignation | SBS SB 1551-60S |
| Polymertype | Styrene-butadiene-styrene block copolymer (SBS) |
| Appearance | White to off-white granules or pellets |
| Density | Approx. 0.94 g/cm³ |
| Bulkdensity | Approx. 0.45 g/cm³ |
| Hardness | Shore A 60 |
| Meltflowrate | Approx. 5–10 g/10 min at 200 °C/5 kg |
| Tensilestrength | Approx. 10–15 MPa |
| Elongationatbreak | Approx. 600–800% |
| Tearstrength | Approx. 30 kN/m |
| Compressionset | Approx. 25% at 70 °C/22 h |
| Styrenecontent | Approx. 30% |
| Volatilematter | ≤0.5% |
| Ashcontent | ≤0.2% |
As an accredited Lucobit AG Lucopren® SBS SB 1551-60S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lucopren® SBS SB 1551-60S is supplied in 25 kg sealed moisture-resistant bags, with 1,000 kg net per pallet. |
| Container Loading (20′ FCL) | A 20-foot FCL container is loaded with Lucobit AG Lucopren® SBS SB 1551-60S, properly stacked, secured, and sealed for ocean shipment. |
| Shipping | Lucobit AG Lucopren® SBS SB 1551-60S is shipped as a non-hazardous thermoplastic elastomer (SBS) in moisture-proof bags, octabins, or bulk. Transport at ambient temperature, protected from direct sunlight, heat, and moisture. It is not classified as dangerous goods for road, sea, or air transport. |
| Storage | Store Lucobit AG Lucopren® SBS SB 1551-60S in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizing agents. Keep original containers or bags tightly closed, labeled, and protected from moisture, dust, and UV exposure. Avoid prolonged high temperatures; use first-in, first-out stock rotation and follow the SDS/local regulations. |
| Shelf Life | Shelf life is typically 24 months in unopened original packaging, stored cool, dry, and away from direct sunlight. |
An injection-moulding grade of Lucobit AG Lucopren® SBS SB 1551-60S is specified for soft-touch overlays on hand tools and power tool housings when a low-hardness elastomeric surface must be combined with a rigid thermoplastic substrate. The material is processed as an overmould onto glass-filled polypropylene or PC/ABS substrates on a two-shot injection moulding machine with a rotary platen. Barrel temperature settings are typically 160–190 °C from feed throat to nozzle, with the nozzle held at 185–195 °C. Mould temperature is maintained at 20–35 °C. The substrate is pre-heated to 40–60 °C or surface-treated by plasma discharge before overmoulding because SBS 1551-60S develops only limited chemical adhesion to untreated polypropylene. Injection speed is set to 40–80 cm³/s through gates of 1.5–2.5 mm diameter. Holding pressure is kept at 300–600 bar for 2–5 s, followed by 8–15 s cooling. Colour is adjusted with 2–3 wt% styrenic colour masterbatch. A stabiliser package of 0.2–0.4 phr hindered phenolic antioxidant and 0.3–0.8 phr UV absorber is used when the tool housing is exposed to workplace lighting or intermittent outdoor use. Hardness is checked on a 6 mm plaque according to ISO 868 and is required to remain within ±3 Shore A of the nominal 60 Shore A specification. Tensile strength and elongation are determined according to ISO 37 on type 2 dumbbells at 500 mm/min. Adhesion failure is evaluated visually after 24 h at 23 °C; peeling or delamination at the SBS-substrate interface is cause for rejection. Compliance for articles placed on the EU market includes REACH Regulation (EC) No 1907/2006 Annex XVII entry 50 for polycyclic aromatic hydrocarbons in rubber or plastic parts with direct skin contact and RoHS Directive 2011/65/EU for electrical tool housings. The grade is not specified for food-contact use unless lot-specific migration testing is performed. Finished articles include overmoulded grips on cordless screwdrivers, angle grinders, and handheld power tools.
Calendered anti-fatigue mats based on SBS 1551-60S are produced on a three-roll calender in L or inverted-L configuration. Roll temperatures are set at 140–160 °C for the middle and bottom rolls and 130–150 °C for the top roll. The friction ratio between rolls is held at 1.1:1–1.3:1 to generate controlled shear heating without scorching the polybutadiene mid-blocks. The compound is pre-mixed in a tangential mixer at 110–130 °C, then passed through a strainer extruder with barrel temperatures of 120–140 °C to remove gels larger than 100 µm. For indoor industrial mats, the formulation may contain 20–35 phr calcium carbonate filler, 5–15 phr paraffinic or naphthenic oil, and 0.5–1.0 phr zinc stearate as an internal release agent. For outdoor or high-UV service, a stabiliser package of 0.3–0.8 phr UV absorber, 0.2–0.5 phr hindered amine light stabiliser and 2–3 phr carbon black is required, because residual unsaturation in the butadiene phase causes surface chalking and discolouration under xenon-arc exposure according to ISO 4892-2. Slip resistance is measured according to EN 13893 or DIN 51130. A targeted R10 rating under dry and wet conditions is achieved with an embossed surface generated by a chilled embossing roll at 30–40 °C. Thickness control is maintained within ±0.3 mm across the web, because edge thinning changes deformation under foot load. Compliance for industrial mats placed on the EU market includes REACH Annex XVII entry 50 PAH limits and, where relevant, construction products regulation requirements. Published data for this specific mat configuration is limited; lot-specific mechanical and slip tests are required before series production. Finished goods include modular anti-fatigue mats for assembly lines, commercial kitchen floors, and standing workstations.
Footwear sole production with SBS 1551-60S is carried out either by direct injection moulding or by compression moulding. In formulations where the grade is used as the elastomeric base, a typical sole compound contains 70–80 wt% SBS 1551-60S, 10–20 wt% general-purpose polystyrene for hardness and abrasion improvement, 5–10 wt% naphthenic oil, 5–20 wt% calcium carbonate filler, 0.3–0.5 phr phenolic antioxidant, and 0.5–1.0 wt% zinc stearate. Direct injection moulding uses a reciprocating screw machine with barrel temperatures of 165–190 °C and a clamp force of 800–1500 kN for multi-cavity sole moulds. Compression moulding uses pre-heated slugs at 140–160 °C and 6–10 min moulding pressure of 15–25 MPa. The processing window is narrow. Above 195 °C, oxidative degradation of the polybutadiene mid-block produces gel specks and reduces elongation. Below 160 °C, weld-line strength in multi-gate soles is insufficient and visible flow lines form. Mould release is a production bottleneck because SBS has high hot tack under ejection conditions. External mould-release agents based on 0.5–1.0 wt% zinc stearate or PTFE-coated mould surfaces are required to prevent tearing at ejection pin marks. Post-moulding shrinkage is anisotropic, measured at 1.0–1.8% in the flow direction and 0.5–1.0% transverse after 24 h at 23 °C, according to ISO 294-4. Soles are conditioned for 24 h before hardness is checked with ISO 868. The target hardness is 60 Shore A with a tolerance of ±3 points. Tensile strength is determined on ISO 37 type 2 dumbbells at 500 mm/min. Abrasion resistance is measured according to ISO 4649 method A; values above 250 mm³ are rejected for safety footwear outsoles. Flexural fatigue is evaluated according to ISO 16177:2021 for crack initiation at 30 000 cycles. Adhesive bonding to leather or textile uppers is performed with polyurethane-based cements; natural rubber latex cements are not recommended because SBS swells and loses bond strength in hydrocarbon solvents. Regulatory compliance for footwear includes REACH Annex XVII entry 50 PAH limits for skin contact. RoHS is not normally applicable to non-electrical footwear unless metallic accessories are integrated. Finished soles and midsoles are used in sandals, casual shoes, and work safety footwear.
| Process variable | Setting | Observed failure mode outside setting |
|---|---|---|
| Melt temperature | 160–190 °C | Below 160 °C: incomplete weld lines; above 195 °C: gel specks and elongation loss |
| Mould temperature | 20–35 °C | Above 45 °C: ejection marks and longer cycle time |
| Cooling time per 3 mm wall thickness | 12–18 s | Below 10 s: post-mould warpage and excessive shrink |
| Mould release | Zinc stearate 0.5–1.0 wt% or PTFE coating | No release agent: tearing at ejection pin marks |
Extruded appliance seal profiles from SBS 1551-60S are produced on a single-screw extruder with 25:1–30:1 L/D and a screw compression ratio of 2.5:1–3.0:1. The screw is cooled to 80–100 °C in the feed zone to prevent pellet bridging. Barrel zones are profiled from 160 °C at the feed throat to 180 °C at the die. The die head is held at 175–185 °C. A breaker plate and screen pack of 60/100 mesh are used to generate back pressure and remove gels. The profile is calibrated in a water trough at 15–25 °C with vacuum sizers. Post-extrusion shrinkage of 0.8–1.2% occurs within 48 h, so cutting tolerances for freezer door gaskets are set at 2–3 mm per metre. If the grade is used as supplied, additional external plasticiser is generally not required, which reduces surface bloom and migration to painted cabinet surfaces. Compression set is measured by ISO 815-1 at 70 °C for 22 h; values above 50% indicate insufficient recovery for sealing. Low-temperature flexibility is measured by ISO 2921; the profile must remain flexible at −20 °C for freezer applications. Compliance for appliance seals includes Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU where electronic components are integrated. No phthalate plasticisers are used in the unmodified grade. Direct food-contact declarations are outside the specification unless migration testing under EC 1935/2004 is performed. Finished goods include freezer door gaskets, low-heat appliance bumpers, and flexible retaining strips.
When a Shore A 60 SBS compound is specified for suction cups and sealing rings, injection-compression moulding is preferred over straight injection moulding because the compression phase produces lower internal stress and improves dimensional stability. Machine parameters are barrel temperature 170–195 °C, compression stroke 2–5 mm, compression force 600–1200 kN, and venting 0.2–0.5 s. The mould is held at 25–40 °C. Cavities with polished surfaces are used because SBS develops vacuum adhesion to glass and glazed ceramic only when the contact surface is free of sink marks. Surface irregularity above 0.1 mm creates a leak path. Formulation includes 0.5–1.0 phr antioxidant and 0.3–0.6 phr mould-release lubricant to reduce ejection tack. No external plasticiser is needed, so migration to the contact interface is minimal. Air permeability through the butadiene phase limits long-term holding force; published data for this specific configuration is limited and product-specific holding-force tests are required. Product qualification includes tensile strength by ISO 37, hardness by ISO 868, and compression set by ISO 815-1 method A at 23 °C for 72 h. The finished part must recover to 80–90% of original height within 60 s after unloading. Compliance for suction cups placed on the EU market includes REACH Annex XVII entry 50 PAH limits and RoHS Directive 2011/65/EU. Food-contact and medical suction devices are outside the grade boundary unless specific migration and biocompatibility testing are completed. Finished articles include automotive dashboard suction mounts, household hooks, and vacuum-fixture sealing rings.
Compounding of SBS 1551-60S with recycled general-purpose polystyrene is carried out on a co-rotating twin-screw extruder with 30:1–40:1 L/D and a barrel profile of 180–200 °C. SBS is fed as 5–20 wt% into the first barrel section. A distributive mixing section with kneading blocks at 45°–60° staggering is used to generate dispersion without excessive shear heating. Screw speed is set to 250–400 rpm. A vacuum vent at 0.08–0.09 MPa removes volatiles from recycled PS. The extrudate is strand-pelletised after water cooling to 30–40 °C. Impact performance is measured on injection-moulded specimens according to ISO 180/A notched Izod at 23 °C. Addition of 10 wt% SBS 1551-60S typically moves the failure mode from brittle crack to hinge break in thin-wall parts; published data for this specific recycled feedstock is limited. Melt flow index is determined by ISO 1133-1:2022 at 200 °C/5 kg. SBS addition reduces MFR, so gate size and injection pressure must be increased by 10–20% compared with unmodified recycled PS. Processing temperature must not exceed 200 °C, because recycled PS may contain residual contaminants that accelerate SBS degradation. Compliance for electrical appliance housings includes RoHS Directive 2011/65/EU. PAH restrictions under REACH Annex XVII entry 50 apply if the final article is sold in the EU and sustains direct skin contact. Finished goods include appliance housings, coat hangers, and office accessories.
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Lucopren® SBS SB 1551-60S is a pelletized thermoplastic elastomer compound based on styrene-butadiene-styrene triblock copolymer architecture. The 60 in the grade designation is consistent with a nominal hardness of 60 Shore A measured to ISO 868:2003. Because the polystyrene end-blocks function as thermoreversible physical crosslinks, the material can be processed on conventional thermoplastic injection-moulding and extrusion lines without vulcanization. The unsaturated butadiene midblock provides low-temperature flexibility and elastomeric recovery, but it also establishes the principal boundary condition: thermo-oxidative degradation accelerates above 210 °C, and long-term exposure to ozone or UV is not recommended without a protective topcoat or externally compounded stabilizer system.
Conditioning for mechanical testing follows the procedure common to SBS compounds of this hardness class: test plaques are stored for 24 h at 23±2 °C and 50±5 % relative humidity before measurement. The compound is not a thermoset rubber; properties depend on the re-formed polystyrene domain network and therefore on cooling rate, mould temperature, and thermal history after processing.
Injection moulding of Lucopren SBS SB 1551-60S is performed with a general-purpose thermoplastic screw having an L/D ratio of 20:1 to 25:1 and a compression ratio of 2.5:1 to 3.0:1. Barrel temperature settings from feed throat to nozzle are typically arranged as 150 °C, 165 °C, 175 °C, 185 °C, and 190 °C; the nozzle should not exceed 200 °C. Melt temperatures above 210 °C increase the rate of butadiene midblock chain scission. Residence time at melt should therefore be held below 10 min, and production interruptions longer than 15 min should be followed by purging before restart. This is an operational boundary, not a lab-scale recommendation, because barrel hold-up in a 100-tonne class injection-moulding machine can expose material in the compression zone to elevated temperature for longer than the nominal setpoint indicates.
Injection pressure is commonly set between 400 bar and 800 bar hydraulic depending on flow length and gate size. Holding pressure is maintained at 50 % to 75 % of peak injection pressure, with hold time selected as the gate-seal time determined by part-weight stabilization. Mould temperature is maintained between 15 °C and 40 °C; the lower end of this range reduces cycle time but can increase frozen orientation and reduce weld-line strength. Higher mould temperatures improve surface replication and allow more complete re-formation of the polystyrene domains before ejection.
Batch-to-batch viscosity should be monitored on incoming lots because melt flow rate can shift with extender oil content and molecular architecture. A shift of more than ±15 % from the established baseline is often sufficient to alter fill balance in multi-cavity tools on production-scale equipment. The material’s melt flow rate is typically in the range 5–20 g/10 min at 190 °C/5 kg when measured to ISO 1133-1:2022; the manufacturer’s lot certificate governs for release purposes.
Pre-drying is not mandatory when pellet surface moisture is below 0.1 %. However, if pellets are stored in cold warehousing and transferred into a production hall where relative humidity exceeds 60 %, condensation can produce surface moisture sufficient to cause surface splay. In that case, drying for 2 h at 60–70 °C in a desiccant dryer is applied before processing.
For extrusion profiling, a single-screw extruder with 24:1 L/D and compression ratio of 2.5:1 is adequate. Temperature zones should rise from 150 °C at the feed throat to 180–190 °C at the die. Screw speed is adjusted to maintain melt pressure below 250 bar; screen packs of 40/80 mesh are acceptable but will raise melt temperature if fines accumulate during long runs. The compound exhibits pseudoplastic flow behaviour and supports thin-wall profile sections, although sharp internal corners and narrow die lips can generate shear heating sufficient to exceed the 210 °C degradation threshold if screw speed is not reduced.
Regrind addition from sprues and reject parts may be incorporated up to 20 % by weight when the regrind is clean, dried, and generated from the same lot. Higher regrind fractions increase the risk of surface streaking and lower tensile elongation because of cumulative thermal history. Production-scale trials on multi-cavity hot-runner tools have shown that inconsistent regrind particle size is a more common cause of viscosity variation than the regrind level itself.
The values below describe the general envelope for SBS compounds of similar hardness and block copolymer architecture. They are not a certificate of analysis for the specific Lucobit lot and should not be used as acceptance criteria without consulting the manufacturer’s released specification.
| Property | Test method | Typical envelope for 60 Shore A SBS compounds |
|---|---|---|
| Hardness | ISO 868:2003, 3 s reading | 55–65 Shore A |
| Density | ISO 1183-1:2019 | 0.95–1.10 g/cm³ |
| Tensile strength at break | ISO 37:2017, Type 2 dumbbell | 6–14 MPa |
| Elongation at break | ISO 37:2017, Type 2 dumbbell | 450–750 % |
| Tear strength, trouser | ISO 34-1:2022, Method B | 15–30 kN/m |
| Compression set, 24 h at 70 °C | ISO 815-1:2019, Method A | 30–55 % |
| Melt flow rate | ISO 1133-1:2022, 190 °C/5 kg | 5–20 g/10 min |
Mechanical response is controlled by the microphase-separated morphology. The styrene end-blocks form dispersed glassy domains that act as physical crosslinks at service temperatures below approximately 70–80 °C. The butadiene midblock phase provides the low-temperature flexibility; flexibility retention at sub-zero temperatures is therefore better than plasticized PVC grades of equivalent room-temperature hardness, but the unsaturated backbone limits continuous high-temperature service when compared with SEBS or TPV materials.
Overmoulding on polypropylene or ABS substrates is generally feasible without primer when the substrate surface is heated above the re-crystallization onset of the SBS midblock. Adhesion to polypropylene requires an interface temperature above 120 °C; for ABS, mould temperatures of 40–60 °C improve interdiffusion and peeling resistance. However, published data for this specific configuration is limited, and adhesion must be evaluated on production tooling because part geometry, gate position, and substrate grade dominate the failure mode.
Compared with plasticized PVC, Lucopren SBS SB 1551-60S contains no phthalate or ester plasticizer. Plasticizer migration into lacquers, adhesives, and adjacent polymers is therefore not a failure mode under the same conditions that cause PVC soft-touch parts to become stiff or tacky over time. The lower density relative to plasticized PVC offers a mass reduction at equal wall thickness. The SBS compound also retains flexibility at temperatures where many plasticized PVC grades stiffen, but it does not match the inherent flame retardance of PVC and may need additional flame-retardant treatment where regulatory fire performance is required.
In sealing and damping applications, the material can be used as a replacement for solid rubber in parts that require repeated assembly and disassembly or two-shot moulding with thermoplastics. The main differences from thermoset rubber are that SB 1551-60S does not require a curing step, can be reground and reprocessed, and can be processed at lower cycle times. This comes at the cost of compression set, which is higher than a vulcanized EPDM or NBR compound under identical temperature and time conditions.
| Criterion | SBS SB 1551-60S class | SEBS compound | TPV |
|---|---|---|---|
| Room-temperature hardness | 60 Shore A | 55–65 Shore A | 60–70 Shore A |
| Continuous service temperature, typical | 70–80 °C | 90–110 °C | 110–135 °C |
| Low-temperature flexibility | Good to approximately -40 °C | Good to approximately -50 °C | Moderate; depends on PP phase |
| UV/ozone resistance | Poor unless stabilized; not for outdoor use | Good due to saturated midblock | Good to moderate; EPDM phase resists ozone |
| Compression set at 70 °C | Higher than SEBS/TPV | Lower; better recovery | Lowest typically |
| Melt processability | Easy flow; lower melt temperature | Higher viscosity; higher processing temperature | Higher processing temperature; shear-sensitive |
| Recyclability | Regrind can be reused within limits | Regrind reused; more stable | Regrind reused; high thermal stability |
The principal advantage of SEBS over SBS is outdoor weathering and heat resistance. The principal advantage of SBS over SEBS is lower processing temperature and often lower compound cost at equivalent hardness. TPV grades are selected where compression set and hot-oil resistance are critical, but they require higher processing temperatures and can exhibit more shear-dependent melt behaviour. The choice between these materials is therefore governed by the upper service temperature, exposure to UV or ozone, and the acceptable level of compression set in the application.
Chemical resistance is moderate. The compound resists water, dilute acids, dilute bases, and many polar organic solvents only under short-term contact. Aliphatic hydrocarbon oils, aromatic solvents, chlorinated solvents, and strong oxidizing agents swell or degrade the butadiene phase. Applications involving continuous immersion in oil or fuel require either a different chemistry such as TPV or nitrile rubber, or a barrier layer. For indoor consumer goods, appliance feet, grips, mats, and damping elements, these limitations are generally acceptable if the part is not in prolonged contact with aggressive media.
Regulatory documentation should be obtained directly from Lucobit AG for REACH SVHC status, RoHS recast 2011/65/EU, and any applicable food-contact or medical statements. The statements in this document do not establish food-contact, medical, or toy-use compliance. Any material substitution in a regulated article requires verification against the exact grade formulation and lot-specific documentation.