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Non‑functionalized SSBR Grades
- Product Name: Non‑functionalized SSBR Grades
- Factroy Site: Yudu County, Ganzhou, Jiangxi, China
- Price Inquiry: sales3@ascent-chem.com
- Manufacturer: Ascent Petrochem Holdings Co., Limited
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- Non‑functionalized SSBR Grades is a solution-polymerized styrene-butadiene elastomer in solid bale form, commonly used in tire tread compounding, where a balance of low rolling resistance and high wet grip is required.
| HS Code | 151556 |
| Styrene Content | 25 wt% |
| Vinyl Content 1 2 Butadiene | 40 wt% |
| Mooney Viscosity Ml 1 4 100 C | 50 MU |
| Glass Transition Temperature | -50 °C |
| Density | 0.93 g/cm³ |
| Number Average Molecular Weight Mn | 300,000 g/mol |
| Polydispersity Index Mw Mn | 2.5 |
| Tensile Strength Cured Compound | 20 MPa |
| Elongation At Break Cured Compound | 450 % |
| Shore A Hardness Cured Compound | 60 |
| Volatile Content | 0.5 wt% |
| Ash Content | 0.2 wt% |
As an accredited Non‑functionalized SSBR Grades factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Non-functionalized SSBR grades are supplied as 25 kg polyethylene-wrapped bales, palletized and stretch-film wrapped for safe handling and storage. |
| Container Loading (20′ FCL) | Non-functionalized SSBR grades are loaded into 20-foot FCL containers, secured on pallets, protected from moisture and contamination. |
| Shipping | Non‑functionalized SSBR grades are shipped as bales, pellets, or crumb, typically in heat‑sealed polyethylene bags within palletized cartons or FIBCs. They require dry, ventilated storage away from heat, oxidizers, and direct sunlight. Transport is safe via standard freight, with no hazardous classification under most regulations. |
| Storage | Store non-functionalized SSBR grades in a cool, dry, well-ventilated area, ideally below 30°C. Keep away from heat, flames, direct sunlight, and oxidizing agents. Maintain original sealed packaging to prevent moisture absorption and contamination. Avoid floor storage; use pallets. Under proper conditions, shelf life is typically six months to one year. |
| Shelf Life | Non-functionalized SSBR grades typically have a shelf life of two years when stored in original, sealed packaging under cool, dry conditions. |
What Limits Silica Dispersion in Non‑functionalized SSBR Tread Compounds?
In high‑performance passenger car and sport utility vehicle tire tread compounds, non‑functionalized solution styrene‑butadiene rubber is introduced at 60–85 phr of the hydrocarbon rubber phase, with the remaining elastomer typically being high‑cis BR at 15–40 phr. Because the absence of terminal alkoxysilane or amino groups reduces hydrogen bonding between polymer chain ends and precipitated silica surfaces, bound rubber formation after the first internal mixer pass is consistently lower than for functionalized grades; compounders compensate by raising the silane coupling agent addition to 6–10 phr of bis(triethoxysilylpropyl)tetrasulfide or disulfide on a filler‑weight basis. The filler system generally includes precipitated silica at 70–100 phr with carbon black N234 or N330 at 5–15 phr for electrical conductivity and processing stability, while TDAE or treated naphthenic oil is present at 10–37.5 phr depending on whether the selected SSBR grade is oil‑extended. Curatives include zinc oxide at 2–4 phr, stearic acid at 1–2 phr, sulfur at 1.5–2.5 phr, and a mixed sulfenamide/guanidine accelerator system at 1.5–3.0 phr to maintain a stable cure plateau at 155–170 °C. Mixing is performed in an intermeshing internal mixer with a 270–320 L net chamber volume and a fill factor of 0.70–0.75; the silica masterbatch drop temperature is held between 140 °C and 150 °C to drive the silanization reaction without pre‑scorch, while the final stage with curatives is discharged below 110 °C. Tread profiles are formed by a pin‑barrel extruder with an L/D ratio of 10:1–16:1, then cut to length and cured in a bladder press under nitrogen at 155–170 °C for 10–18 min. Regulatory compliance for the finished tire includes Regulation (EU) 2020/740 label classes, UN ECE R117.02 for rolling resistance, wet grip, and rolling sound, and measurement methods ISO 28580:2018, ISO 23671:2021, and ISO 13325:2019. The resultant tread compounds are used for UHP, touring, and electric vehicle tire treads in size ranges including 195/65R15 through 245/45R19. A process boundary is the high vinyl content of certain SSBR grades; above 65 wt% vinyl, the glass transition temperature can exceed −35 °C, and the processing window narrows to approximately ±5 °C during extruder barrel temperature control, with scorch risk rising if the extruder head temperature exceeds 120 °C.
In tire sidewall compounds for radial passenger and commercial tires, non‑functionalized SSBR is employed at 20–35 phr alongside natural rubber at 30–45 phr and high‑cis BR at 25–40 phr, a blend that shifts compound dynamic stiffness without requiring functionalized chain ends. The carbon black system is dominated by N550 and N660 at 45–60 phr, with an aromatic or TDAE oil loading of 5–10 phr; antiozonant 6PPD and antioxidant TMQ are present at 2–4 phr and 0.5–1.5 phr respectively. The cure package comprises sulfur at 1.5–2.2 phr and CBS or TBBS at 0.8–1.5 phr, producing a state of cure consistent with a reversion‑resistant plateau at 150–160 °C cure temperature. Production‑scale mixing normally uses a two‑stage cycle in a tangential internal mixer: the first stage discharges at 135–150 °C after carbon black incorporation, and the second stage adds curatives below 100 °C. Following mixing, the sidewall compound is extruded through a single‑screw extruder with a 12:1–18:1 L/D ratio into flat profiles of 6–10 mm thickness, then calendered onto carcass components before curing in a segmented bladder press at 150–160 °C. Relevant test methods include ASTM D412‑16 tensile properties, ASTM D624‑00(2020) tear strength, ASTM D1149‑18 ozone resistance under 50 pphm and 40 °C, and ASTM D4482‑11(2021) fatigue crack growth, with acceptance limits defined by each tire manufacturer due to the absence of a single harmonized sidewall standard. The resulting sidewall and shoulder insert components are fitted to radial passenger car, light truck, and truck bus tires; reduced SSBR loadings above 35 phr are avoided in sidewalls where cyclic flex fatigue under 10–30% local strain can initiate crack growth, because the higher vinyl fraction increases heat build‑up under repeated deformation compared with BR‑rich control compounds.
Underground Mining Conveyor Cover Compounds with Carbon Black Reinforcement
Underground mining conveyor belt cover compounds based on non‑functionalized SSBR are formulated with 30–60 phr SSBR and 40–70 phr natural rubber to balance cut resistance, tear strength, and black‑filled abrasion resistance. Carbon black N220 is added at 40–60 phr, plasticized by TDAE oil at 5–10 phr, and protected with TMQ and 6PPD at a total antioxidant loading of 1.5–3.0 phr. Zinc oxide at 3–5 phr and stearic acid at 1–2 phr are used as activators; sulfur at 1.8–2.5 phr with TBBS at 0.9–1.6 phr provides a balance between scorch safety during calendering and modulus development during continuous press curing. The mixing operation is conducted as a two‑stage internal mixer cycle, with the first stage discharged at 140–160 °C and the final stage discharged below 105 °C, followed by a two‑roll mill warm‑up at 70–80 °C to feed a calender. Cover sheets of 3–8 mm gauge are calendered onto polyester/nylon or steel breaker fabric treated with RFL dip, and the entire belt is vulcanized in a continuous hot press at 140–160 °C for 25–45 min depending on belt thickness. The finished belt is tested under ISO 14890:2013 safety requirements, ISO 4649:2021 rotary drum abrasion, ISO 34‑1:2022 tear strength, and ISO 15236‑1:2016 for steel cord conveyor belts, while flame‑resistant grades are assessed under ISO 340:2022 or EN 14973:2018 depending on the market. End products include abrasion‑resistant cover rubber for underground coal and aggregate belts with widths from 800 mm to 2200 mm, where the SSBR fraction reduces groove wear under wet abrasive ore handling relative to high‑BR control compounds, but comparative wear data must be validated through production‑scale trials rather than a single laboratory pass value. The upper SSBR addition is limited to 60 phr because higher loadings reduce green strength required for open‑mill handling and can raise calender shrinkage beyond 3% after cooling.
During compression molding of vulcanized footwear outsoles for safety boots and work shoes, non‑functionalized SSBR is introduced at 25–50 phr in a blend with standard Malaysian natural rubber at 30–50 phr and high‑cis BR at 20–40 phr to modify wet‑slip performance while retaining low‑temperature flexion. Silica is used at 30–55 phr in combination with carbon black N330 at 10–20 phr, and the silane coupling agent is added at 2–5 phr relative to silica to avoid excessive compound viscosity; polyethylene glycol is added at 0.5–1.5 phr to reduce silica adsorption of the accelerator system. The cure system uses sulfur at 1.8–2.4 phr, MBTS at 1.0–1.8 phr, and TMTD at 0.2–0.6 phr, giving a compression set below 30% after 24 h at 70 °C when tested under ASTM D395‑18 method B. Mixing is completed in a 75–160 L internal mixer at a dump temperature of 110–130 °C, followed by sheeting on a two‑roll mill and curing in a multi‑platen compression press at 145–155 °C for 8–15 min, or by injection molding in a 200–350 tonne clamp force machine with barrel temperatures of 80–95 °C and mold temperatures of 150–165 °C. Compliance requirements include ISO 20345:2021 for safety footwear, ISO 20871:2018 outsole abrasion resistance, ISO 868:2003 Shore A hardness, and ASTM D2240‑15(2021) durometer verification; slip resistance is evaluated under EN ISO 13287:2019 or ASTM F2913‑19. Finished components include direct‑vulcanized unit soles, Blake‑stitched sole sheets, and replaceable sole layers for slip‑rated work boots, outdoor walking shoes, and oil‑free leather footwear; published data for non‑functionalized SSBR‑specific outsole abrasion under ceramic‑grit protocols is limited, so formulation approval is generally based on internal rotary drum abrasion screening combined with production‑scale wear trials rather than a single harmonized pass value.
When SSBR Replaces Emulsion SBR in High‑Loss Anti‑Vibration Mounts
When non‑functionalized SSBR replaces emulsion SBR in high‑loss anti‑vibration mounts for stationary machinery and engine cradle applications, the blend is frequently specified at 40–70 phr SSBR with the balance being natural rubber or BR depending on the required dynamic stiffness ratio. High vinyl SSBR grades with vinyl contents of 50–65 wt% are selected because the loss factor tan δ at 60 °C can be maintained between 0.18 and 0.30, although non‑functionalized chain ends provide less filler networking than terminal‑modified types. Carbon black N330 or N550 is loaded at 30–60 phr, with process oil at 5–12 phr, zinc oxide at 3–5 phr, stearic acid at 1–2 phr, sulfur at 1.5–2.5 phr, and CBS/TMTD accelerator at 0.8–2.0 phr. The compound is mixed in a two‑stage cycle in a tangential internal mixer, with the masterbatch discharged at 140–150 °C and the final stage below 100 °C; the stock is then calendered or preformed into blanks and compression‑molded with bonded steel or aluminum inserts. Cure is carried out at 150–165 °C for 10–25 min, depending on insert thickness and mold thermal conductivity. Dynamic characterization is performed under ISO 10846‑1:2008 for dynamic stiffness and damping in the frequency range 20–200 Hz, while static and fatigue validation follows ISO 7743:2017 compression properties and ASTM D5992‑96(2018) dynamic properties of rubber isolators. The resulting anti‑vibration mounts, suspension bushings, generator set isolators, and rail pad segments are intended for dry, non‑oil‑exposed installations; contact with mineral oil or diesel fuel is not recommended because the SSBR/NR blend lacks the oil resistance of NBR or CR and can swell beyond 15% by volume when immersed in IRM 903 oil under ASTM D471‑16a for 70 h at 100 °C. A further operational boundary is the low‑service‑temperature limit: high vinyl SSBR compounds can exhibit a glass transition near −30 °C to −25 °C, so installation below −25 °C requires low‑vinyl SSBR grades with a demonstrated brittle point below −45 °C.
Precure tread rubber for retreaded commercial vehicle tires is a separate downstream segment in which non‑functionalized SSBR is used at 40–70 phr in combination with BR at 20–40 phr and NR at 10–30 phr, depending on traction, abrasion, and compound cost targets. The filler package consists of carbon black N234 or N220 at 50–70 phr, with TDAE oil at 5–15 phr, zinc oxide at 2–4 phr, stearic acid at 1–2 phr, sulfur at 1.5–2.5 phr, and TBBS/CBS accelerator at 0.9–1.8 phr. Mixing is performed in an internal mixer with the first non‑productive stage dropped at 140–155 °C and the productive stage dropped below 100 °C; the compound is then extruded through a roller‑head extruder with an 8:1–12:1 L/D ratio into a hot strip of 3–6 mm thickness, embossed with a tread pattern, and precured in a continuous press or autoclave at 150–165 °C for 15–35 min. Product compliance is governed by UN ECE R108 for retreaded passenger car tyres and UN ECE R109 for retreaded commercial vehicle tyres, with abrasion measured under ISO 4649:2021, hardness under ASTM D2240‑15(2021), and tensile properties under ASTM D412‑16. The cured strips are applied to buffed tire casings with a cushion gum and vulcanized in an enveloped curing chamber at 95–125 °C for 3–6 h to form retreaded truck and bus tires with rim diameters from 17.5 in to 24.5 in. The main processing constraint is adhesion to the buffed casing: non‑functionalized SSBR with high vinyl content exhibits higher shrinkage and lower green tack than NR‑rich cushion gum layers, so the precure tread strip must be cooled below 40 °C before buffing and stored under controlled relative humidity below 60% to prevent condensation‑induced adhesion loss during application.
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- Non‑functionalized SSBR Grades is manufactured under an ISO 9001 quality system and complies with relevant regulatory requirements.
- COA, SDS/MSDS, and related certificates are available upon request. For certificate requests or inquiries, contact: sales3@ascent-chem.com.
Non-functionalized solution-polymerized styrene-butadiene rubber (SSBR) is an anionic-polymerized copolymer of styrene and 1,3-butadiene produced in a hydrocarbon solvent without deliberate introduction of silica-reactive chain-end groups such as alkoxysilane, amine, epoxy, or hydroxyl moieties. Commercial grades are specified by bound styrene content, 1,2-vinyl content of the butadiene fraction, Mooney viscosity, oil type and loading, and glass transition temperature. Non-oil-extended grades typically span bound styrene 15 wt% to 35 wt%, vinyl content 8% to 65%, ML(1+4)100 °C 45 MU to 75 MU, and dry Tg by differential scanning calorimetry -85 °C to -25 °C. Oil-extended grades are commonly supplied with 37.5 phr treated distillate aromatic extract (TDAE) or mildly extracted solvate (MES) oil; the oil-free polymer Mooney value is proportionally higher. Grade designations are producer-specific and may encode styrene percentage, vinyl percentage, and oil loading, but the same numerical field is not transferable between suppliers. A suffix indicating non-functionalized status may appear as a blank field, a zero, or a producer-specific code, so the supplier certificate of analysis and technical data sheet remain the only reliable identifiers.
How Do Anionic Polymerization Variables Map to SSBR Microstructure?
Solution polymerization of SSBR is conducted with organolithium initiators in aliphatic or cycloaliphatic solvents. The living anionic chain ends permit controlled molecular weight and narrow molecular weight distribution, typically Mw/Mn 1.05 to 2.5 depending on coupling method. Styrene and butadiene are copolymerized in the presence of a randomizer such as tetrahydrofuran, tetramethylethylenediamine, or 2,2-bis(2-oxolanyl)propane. The randomizer concentration controls the 1,2-vinyl content of the butadiene units by shifting the addition mode from 1,4 to 1,2. Higher randomizer levels raise vinyl content and increase the copolymer glass transition temperature at constant styrene. A low-vinyl grade with 8% to 15% vinyl may show a Tg near -80 °C, whereas a high-vinyl grade with 55% to 65% vinyl may approach -25 °C to -20 °C; the exact Tg depends on both styrene and vinyl mass fractions and is measured by ISO 22768. Coupling with tin tetrachloride or silicon tetrachloride may be used to broaden molecular weight distribution and reduce cold flow, but this chain-end coupling is not equivalent to silica-specific functionalization; the chain ends remain nonpolar after steam stripping and drying.
Because the polymerization is living, molecular weight is set primarily by the monomer-to-initiator ratio rather than by transfer reactions. The absence of functional groups simplifies storage stability relative to moisture-sensitive chain-end-modified grades. However, low-Mooney linear grades may exhibit cold flow in bales at warehouse temperatures above 40 °C, and suppliers typically recommend flat pallet stacking and controlled ambient humidity below 60% RH to limit surface moisture pickup. For non-oil-extended grades, the Mooney viscosity is determined by ISO 289-1 or ASTM D1646 after the sample has been sheeted and stored under controlled conditions.
Silica Mixing and Dynamic Hysteresis in Non-functionalized Grades
In silica-filled tire tread compounds, non-functionalized SSBR does not form covalent or strongly ionic bonds with silanol groups on precipitated silica. Filler-filler networking therefore dominates unless an organosilane coupling agent is added. The standard coupling agent is bis[3-(triethoxysilyl)propyl]tetrasulfide (TESPT), typically added at 6–8 phr per 80 phr precipitated silica, or mercaptosilane at lower dosage in formulations where sulfur donor effects must be minimized. Without adequate silanization, the compound exhibits a high Payne effect, measured as the difference in storage modulus between 0.1% and 100% strain under ISO 4664-1 or ASTM D5992; this manifests on a production line as higher die swell, poorer extrudate surface quality, and increased mixing energy. Functionalized SSBR grades reduce silane demand and lower the strain dependence of storage modulus, but non-functionalized grades remain processable when mixing discipline is maintained.
Production-scale mixing of non-functionalized SSBR with high-surface-area silica requires internal mixers with intermeshing or tangential rotors and controlled dump temperature. In a typical non-productive pass, the polymer is masticated, half of the silica and silane are added, the ram is swept, the remaining silica and silane are added, and the batch is dumped at 145–155 °C. Exceeding 160 °C in the first pass can prematurely degrade TESPT and release sulfur, causing scorch in the subsequent productive pass. A second non-productive pass at 140–150 °C is often required to complete silanization. The productive pass with sulfur, accelerator, and zinc oxide is dumped below 110 °C. Failure modes observed on mixing lines include silica agglomeration when first-pass dump temperature is too low, and scorch or lump formation when the productive pass exceeds 110 °C. These are detected by a rising minimum torque in an MDR cure curve, shortened ts2, and elevated low-strain storage modulus.
Compared with silane-functionalized SSBR, the non-functionalized counterpart typically yields a higher tan δ at 60 °C at equal silica loading, meaning higher rolling resistance in the cured tire tread. The wet grip indicator tan δ at 0 °C can be maintained by selecting a higher-vinyl grade, because vinyl content raises the rubber Tg and the temperature location of the dynamic loss peak. The trade-off is that high-vinyl non-functionalized SSBR compounds may have lower abrasion resistance and higher heat build-up unless the vulcanization system is adjusted. In carbon black-filled compounds, the functionalization difference is less significant; both non-functionalized and chain-end-functionalized SSBR rely mainly on physical adsorption and mechanical interlocking with carbon black.
When TDAE Oil Extension Becomes the Principal Processing Variable
Oil extension is a production-scale method to supply high-molecular-weight non-functionalized SSBR in a processable bale form. The base polymer is polymerized to a Mooney viscosity that would be too high for ordinary downstream mixing, then extended with 37.5 phr TDAE or MES oil during finishing. The oil is not a diluent only; it reduces the uncured storage modulus, lowers mixing energy, and assists wetting of precipitated silica. In the European Union, extender oils for tires must meet the PAH restrictions of REACH Annex XVII, with benzo[a]pyrene below 1 mg kg−1 and the sum of eight listed PAHs below 10 mg kg−1 by IP 346. Oil-extended non-functionalized SSBR grades are therefore specified by both the final Mooney viscosity and the aromatic oil type. A compounder who replaces a non-oil-extended grade with an oil-extended grade must account for the oil as part of the total plasticizer loading; failure to do so results in lower cured modulus and reduced tensile properties under ISO 37 or ASTM D412.
Oil-extended grades also exhibit different cold-flow behavior. The TDAE oil lowers bale hardness but can promote blocking under high pallet load at temperatures above 35 °C. In contrast, some non-oil-extended high-styrene grades are less prone to cold flow but require higher shear for dispersion. Neither oil-extended nor dry grades should be exposed to strong oxidizers, and storage near ozone-generating equipment should be avoided because unsaturation in the butadiene units remains sensitive to ozone attack unless protected by antiozonant in the final compound.
For non-tire mechanical goods, hoses, belts, and footwear, non-functionalized SSBR is selected when lower solution-polymerized ash content, narrower molecular weight distribution, or specific low-temperature flexibility is required relative to emulsion SBR. It is compounded with carbon black at 40–80 phr, naphthenic or paraffinic oil, zinc oxide 3–5 phr, stearic acid 1–2 phr, and sulfur-donor or conventional sulfur cure systems. The cure system is adjusted by moving die rheometer; a typical sulfur/sulfenamide formulation at 160 °C may show t90 between 8 min and 15 min, but exact t90 depends on accelerator ratio and sulfur content. Non-functionalized SSBR can be blended with natural rubber or polybutadiene to improve tear strength and flex fatigue. In injection molding, low-Mooney grades are preferred for thin sections, while high-Mooney oil-extended grades may require larger screw channels and lower back pressure; published data for grade-specific plastication settings is limited.
Compared with emulsion SBR, non-functionalized SSBR contains lower non-rubber residue and is produced with a narrower molecular weight distribution. For equal styrene content, SSBR can be designed to a wider range of vinyl content and therefore a wider range of wet grip and low-temperature properties. Emulsion SBR grades are often specified by Mooney viscosity and bound styrene only, whereas SSBR requires simultaneous specification of vinyl microstructure. Compared with polybutadiene, non-functionalized SSBR has lower resilience but higher wet grip and better tensile strength retention after oil extension. These differences are formulation-dependent; published data for specific commercial grade comparisons is limited, and selection should be made using laboratory compound results and bench abrasion tests.
The Certificate of Analysis Does Not Encode Silica Interaction
The table below lists the specification envelope typically shown on a commercial certificate of analysis for unmodified linear SSBR grades. The ranges are supplier-dependent and should not be used as purchase limits without a technical datasheet.
| Property | Test method | Typical unmodified SSBR range |
|---|---|---|
| Bound styrene | ISO 2453 | 15–35 wt% |
| Vinyl content of butadiene fraction | ISO 12965 | 8–65% |
| Mooney viscosity ML(1+4)100 °C | ISO 289-1 | 45–75 MU |
| Glass transition temperature | ISO 22768 | -85 °C to -25 °C |
| Ash | ISO 247 | ≤ 0.2 wt% |
| Volatile matter | ISO 248 | ≤ 0.5 wt% |
| Specific gravity | ISO 2781 | 0.93–0.95 |
The certificate confirms composition and rheology but does not quantify filler interaction. Two grades with identical bound styrene, vinyl, and Mooney viscosity may differ in silica compound performance because of chain-end structure, coupling, and molecular weight distribution; these differences are resolved only through compound testing.
Functionalized SSBR Benchmarks Against the Same Silica Tread Matrix
When a silane-functionalized SSBR replaces a non-functionalized grade at the same silica loading, the bound rubber content generally increases, the Payne effect decreases, and tan δ at 60 °C moves lower. The functionalized chain ends condense or adsorb onto silanol groups, reducing silica aggregate re-agglomeration during storage and after mixing. This permits lower TESPT dosage in some formulations, but the extent depends on the functional group type, chain-end concentration, and mixing temperature. Silane-terminated and amine-functionalized grades can be moisture-sensitive before compounding, while non-functionalized SSBR does not exhibit the same humidity-driven viscosity drift. In carbon black compounds, the functionalization advantage is smaller, and non-functionalized grades can match processability when the mixing cycle is adjusted.
Operational boundaries for non-functionalized SSBR are defined by mixing temperature and silane dosage rather than by the polymer itself. The grades are unsuitable as drop-in replacements for silane-functionalized polymers in low-silane silica tread formulations where mixer temperature cannot be sustained above 145 °C. Published data for specific commercial grade comparisons at equal tire rolling resistance is limited; compound development therefore requires dynamometer rolling loss, wet braking, and abrasion testing under the relevant tire test conditions.
