|
HS Code |
795005 |
| Chemical Formula | C11H14N2S2 |
| Molecular Weight | 238.37 g/mol |
| Appearance | White to light yellow powder |
| Odor | Faint, characteristic |
| Melting Point | 105 - 108 °C |
| Solubility In Water | Insoluble |
| Solubility In Organic Solvents | Soluble in benzene, toluene, chloroform, etc. |
| Density | 1.26 - 1.32 g/cm³ |
| Flash Point | 205 °C |
| Stability | Stable under normal conditions |
| Main Use | Vulcanization accelerator in rubber industry |
As an accredited N-Tert-Butyl-2-Benzothiazolesulphenamide factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 25 - kg bags of N - Tert - Butyl - 2 - Benzothiazolesulphenamide for chemical packaging. |
| Shipping | N - Tert - Butyl - 2 - Benzothiazolesulphenamide is shipped in well - sealed containers, following strict chemical transportation regulations. Packaging safeguards against leakage, and transport is coordinated to ensure safe delivery to the destination. |
| Storage | N - Tert - Butyl - 2 - Benzothiazolesulphenamide should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, ignition sources, and incompatible substances. Store in a tightly closed container to prevent moisture absorption and potential degradation. Avoid storage near oxidizing agents and acids. Regularly check storage conditions to ensure product integrity. |
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In the formulation of radial passenger car tire treads based on natural rubber (NR) and butadiene rubber (BR) blends—typically a 70/30 to 80/20 ratio—N-tert-butyl-2-benzothiazolesulphenamide (TBBS) is metered at 0.8–1.2 phr alongside insoluble sulfur (2.0–2.5 phr), a ZnO/stearic acid activator system (3.0–5.0 phr ZnO, 1.0–2.0 phr stearic acid), and carbon black N234 at 45–55 phr. Compounding takes place in a two-stage internal mixer; masterbatch mixing in a 270 L intermeshing Banbury operating at 45–50 rpm rotor speed reaches a drop temperature of 155–165°C, after which the stock is sheeted on a twin-roll mill with a front-roll temperature set to 55–60°C and a friction ratio of 1:1.08. The second stage, where TBBS and sulfur are introduced, must rigidly cap dump temperature at 105°C; excursions above 120°C trigger decomposition of the sulfenamide into 2-mercaptobenzothiazole (MBT) and tert-butylamine, detected as a pungent amine odor and causing a drastic reduction in scorch safety that leads to micro-gel formation in the extruder head of pin-barrel cold-feed extruders used for tread profiling. Extrusion is performed through a 200 mm diameter vented extruder with an L/D ratio of 16:1, screw speed 20–30 rpm, and barrel zones controlled at 70–85°C; the head pressure must not exceed 15 MPa to avoid local overheating. Vulcanization kinetics, recorded on a moving-die rheometer (MDR) per ASTM D5289-17 at 160°C, yield a minimum torque ML of 1.8–2.5 dN·m, maximum torque MH of 14–18 dN·m, scorch time ts2 of 3.5–4.5 min, and a t90 of 9–12 min. Curing is executed in double-cavity segmented mold presses under 20–24 MPa clamp force at 150–160°C for 12–15 min. Finished treads, destined for P-metric and LT-metric PCR tires, exhibit tensile strength above 20 MPa and elongation at break exceeding 450% when tested per ASTM D412-16 die C, and DIN abrasion loss below 110 mm³ per ISO 4649:2017. Regulatory conformance requires the cured compound to meet EU 1907/2006 (REACH) Annex XVII entry 50 restrictions on eight polycyclic aromatic hydrocarbons (PAHs); the sum of benzo(a)pyrene, benzo(e)pyrene, benzo(a)anthracene, chrysene, benzo(b)fluoranthene, benzo(j)fluoranthene, benzo(k)fluoranthene, and dibenzo(a,h)anthracene must remain below 1 mg/kg as determined by GC-MS following extraction per AfPS GS 2019:01 PAK. Moreover, N-nitrosamine migration into artificial saliva measured according to EN 12868:1999 shall not exceed 10 μg/kg for materials accessible to children, a critical boundary that limits the maximum TBBS concentration in certain compound variants. What Mechanism Underpins TBBS Selection in Steel Cord Skim Compounds?Adhesion development between brass-coated steel cord and a high-modulus NR skim compound in radial tire belts relies on a delayed crosslinking onset that permits the rubber to flow and encapsulate each filament before gelation restricts conformability. TBBS at 1.0–1.5 phr is co-formulated with a resorcinol-formaldehyde donor (e.g., hexamethoxymethylmelamine, HMMM) at 4–6 phr, precipitated silica at 10–15 phr, cobalt naphthenate (0.5–1.0 phr Co content), and a sulfur loading of 4–5 phr to achieve the required crosslink density for belt reinforcement. Masterbatch mixing in an interlocking-rotor internal mixer with a rotor speed ceiling of 35 rpm limits the dump temperature to 145°C; the finalizing pass incorporating TBBS and sulfur drops at 95–100°C. Calendering onto brass-coated wire cord is performed on a 4-roll Z-calender at a nip gap of 0.35–0.55 mm, with roll temperatures balanced at 80°C top, 85°C middle, and 75°C bottom to minimize cord tension variation that would otherwise manifest as wire displacement in the cured belt. The cord is preheated to 105–115°C immediately upstream of the calender to eliminate moisture that promotes dezincification of the brass coating; residual moisture above 0.1% measurably reduces initial adhesion force. Unaged pull-out adhesion, tested according to ISO 5600:2017 on 3×0.20+6×0.35HT construction cord, returns values of 350–500 N; after humid aging at 85°C and 95% RH for 14 days, rubber coverage on the extracted cord must remain above 80%. The delayed-action profile of TBBS, giving a Mooney scorch t5 at 127°C of 18–25 min, is critical: it extends the processing window sufficiently to allow the RF–silica network to migrate and form covalent bonds with copper in the brass before vitrification of the polymer matrix. From a compliance standpoint, skim compounds fall under the same REACH Annex XVII PAH limitations as tread compounds, and additionally material intended for the North American market must satisfy the FMVSS 139 endurance test criteria that indirectly validate belt durability over 34-hour wheel testing.
Heat-Resistant Conveyor Belt Cover CompoundsCover compounds for fabric-reinforced conveyor belts handling hot clinker or sintered ores at continuous service temperatures up to 150°C are formulated on EPDM or a EPDM/NR blend, with TBBS contributing a controlled rate of cure that combats reversion in the bulk. Dosage levels reside in the 0.6–1.0 phr band, supplemented by sulfur at 0.8–1.2 phr and a secondary ultra-accelerator (e.g., tetrabenzylthiuram disulfide, TBzTD) at 0.2–0.4 phr to flatten the cure plateau and retain physical properties after extended post-cure thermal aging at 150°C for 168 hours, evaluated per ISO 188:2011. A major processing hazard is bloom of free TBBS on the uncured sheet surface, especially at ambient temperatures below 15°C when solubility in EPDM drops exponentially; mill operators mitigate this by splitting the TBBS addition into 60% in the internal mixer and 40% on a cooling batch-off mill maintained at 45°C. The cover stock is calendered to a thickness of 5–8 mm on a 4-roll inverted L calender and subsequently laminated onto a carcass comprising EP/NR skim compounds. Continuous vulcanization is performed on a Rotocure drum press with a contact pressure of 0.5–0.7 MPa and a drum temperature profile rising from 160°C at the inlet to 180°C at the midpoint, giving a residence time of 25–35 min. The finished Class 2 and Class 3 belts must conform to ISO 14890:2013, which specifies minimum tensile strength (15 MPa), elongation at break (350%), and abrasion resistance (120 mm³) before and after thermal aging. Additionally, covers intended for the European mining sector are subject to the EN 14973:2015 fire resistance classification, requiring a surface resistivity below 3×10⁸ Ω and a propane burner test according to EN 12881-1:2014. TBBS-containing EPDM covers achieve a tear strength of 35–45 N/mm by the trouser method of ISO 34-1:2015, though a documented drop of 10–15% occurs after immersion in ASTM No. 3 oil for 70 hours at 100°C, constraining the compound’s use to dry-heat applications only. Within continuous vulcanization lines for EPDM sponge and solid automotive weatherstrip profiles, TBBS functions as a secondary accelerator at 0.4–0.7 phr in conjunction with zinc dibutyldithiocarbamate (ZDBC) or zinc dimethyldithiocarbamate (ZDMC) primary accelerators to balance the blowing agent decomposition kinetics with the crosslinking rate. The compound, containing paraffinic process oil (40–60 phr), carbon black N550/N774 blends, and azodicarbonamide blowing agent at 3–5 phr, is extruded through a 90 mm pin-barrel cold-feed extruder with a vented vacuum section maintaining −0.08 MPa to eliminate porosity defects. The profile exits into a microwave-hot air hybrid curing oven: the microwave cavities operating at 2.45 GHz with adjustable power up to 12 kW raise the extrudate core temperature to 140–160°C within 120 seconds, followed by hot air modules at 220–240°C for a total residence time of 5–8 min. A persistent failure mode on line is the formation of “elephant skin” surface roughness when TBBS concentration drops below 0.4 phr, which delays melt strength build-up too much and allows the expanding gas cells to rupture the surface skin before crosslinking stabilizes the cellular structure. Compression set testing following ISO 815-1:2019 (method A, 25% compression, 70 hours at 100°C) must return values below 50% for solid profiles and below 25% for sponge profiles. Finished weatherstrip assemblies are tested for fogging according to DIN 75201:2011, with a condensable mass limit of 2 mg at 100°C for 16 hours; TBBS, having a vapor pressure of 3.2×10⁻⁴ Pa at 25°C, contributes minimally to volatile condensate provided cure conversion exceeds 95%. The material must also satisfy VDA 278:2011 VOC and FOG emission thresholds, which dictate a total VOC below 100 μg/g for the sample. Formulators are alerted that combinations of TBBS with sulfenamide accelerators containing amine moieties (e.g., N-cyclohexyl-2-benzothiazolesulphenamide, CBS) can cause synergistic nitrosamine generation under the acidic conditions of artificial sweat testing (EN 1811:2011), a restriction important for door seal surfaces routinely grasped by occupants. When EPDM-Based Radiator Hoses Require Cure Efficiency Above 150°CCoolant hose constructions with an EPDM inner tube, aramid or polyester reinforcement, and an EPDM cover demand a fast cure system that withstands post-vulcanization heat soak without reverting; TBBS is employed at 0.8–1.2 phr together with tetramethylthiuram monosulfide (TMTM) at 0.3–0.5 phr and sulfur at 1.5–2.0 phr to raise the modulus plateau and reduce compression set after prolonged exposure to a 50/50 water–glycol mixture at 130°C. The inner tube compound is extruded via a 60 mm vented cold-feed extruder with pin-conversion technology, achieving a dimensional tolerance of ±0.15 mm on a 20 mm outer diameter, after which the tube is braided on a 24-carrier Maypole braider under 45–55 N of yarn tension to prevent tube collapse. The cover is crosshead-extruded in tandem and the entire assembly is cured on a mandrel in a saturated-steam autoclave at 165°C for 25–30 min. Under these conditions, a Mooney scorch t5 at 125°C of 12–15 min is necessary to avoid scorch in the head of the crosshead die where residence time can reach 8 min during line stoppages. Adhesion between tube and reinforcement, measured by a peel test per ISO 36:2020, must exceed 2.5 N/mm before and after immersion in the coolant mixture for 1000 hours at 120°C; TBBS-based cure systems without excessive free MBT show superior adhesion retention because MBT migration to the rubber–fiber interface catalyzes thermo-oxidative degradation of the aramid finish. The final hose assemblies are certified to SAE J20:2005 Class D-3, which mandates an impulse test of 150,000 cycles at 125°C and a burst pressure greater than 2.4 MPa. A practical limitation observed on production curing presses is mold-fouling at TBBS levels above 1.3 phr after approximately 40 cure cycles, requiring ultrasonic cleaning with a 40 kHz bath, a cost factor that forces compounders to stay within the lower half of the recommended dosage range.
Microcellular rubber soling sheets for athletic footwear, constructed from SBR/BR/NR ternary blends with a specific gravity target of 0.55–0.70 g/cm³, incorporate TBBS at 0.6–1.0 phr as the primary delayed-action accelerator, paired with a benzoquinone dioxime–red lead blowing system that decomposes coincidently with the onset of crosslinking at 150–155°C. Compounding is performed in a kneader that discharges at 90–100°C, avoiding the 130°C threshold where premature blowing agent activation would create closed-cell porosity in the pre-formed slab. The stock is calendered into 4–6 mm sheets, die-cut, and compression-molded in multi-cavity hydraulic presses under 15–18 MPa clamp pressure with a cure cycle of 6–8 min. Aesthetics-driven constraints are paramount: unreacted TBBS and its cleavage product MBT contribute to pink-to-brown discoloration under UV exposure and perspiration; when white or pastel-color solings are specified, a non-staining sulfenamide such as N-cyclohexylbis(2-benzothiazolesulfen)amide (CBBS) is substituted, though at a sacrifice of 15–20% in tensile strength of the cellular network. TBBS remains the cost-performance optimum for black and dark-colored solings, where a typical compound achieves a tensile strength of 6.5–8.0 MPa and an elongation of 380–450% determined on microcellular specimens per ASTM D3574-17 Test B. The dimensional stability during processing, measured as mold shrinkage, registers 1.8–2.3% on an average 270 mm sole length, a magnitude that must be compensated in the die design. Compliance obligations include California Proposition 65 for N-nitrosamines and the CPSIA lead content limit of 90 mg/kg in accessible substrate components; extraction testing via EPA Method 3050B and subsequent ICP-AES verifies compliance at the batch level. |
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N-Tert-Butyl-2-Benzothiazolesulphenamide (CAS 95-31-8), designated industrially as TBBS, NS, or Santocure NS, is a delayed-action primary sulfenamide accelerator developed for sulfur-vulcanized diene elastomers. Its molecular structure—2-mercaptobenzothiazole substituted at the sulfenamide nitrogen with a tertiary butyl group—introduces steric hindrance that moderates amine release during the induction period. The resulting vulcanization kinetics provide an extended scorch plateau relative to N-cyclohexyl-2-benzothiazolesulfenamide (CBS) while delivering comparable crosslink efficiency and modulus development at conventional cure temperatures of 140–180°C. Commercial production of TBBS typically yields a light-cream to tan free-flowing powder or oil-coated granular form with a melting point of 104–108°C and a molecular weight of 238.37 g/mol. The compound is insoluble in water, sparingly soluble in aliphatic hydrocarbons, and fully soluble in aromatic and chlorinated solvents such as toluene and dichloromethane. Residual free tert-butylamine, a by-product of synthesis, is controlled to below 0.5 wt% in premium grades to avoid premature crosslink activation during ambient-temperature storage of rubber masterbatches. On injection molding lines equipped with hot-runner systems and clamp forces exceeding 800 kN, TBBS-containing compounds exhibit sufficient fluidity at gate temperatures up to 90°C without incurring scorch, provided residence times are kept under 3 min.
The divergence in vulcanization profiles between TBBS and CBS originates from the differing steric and electronic environments of the amine-leaving group. In natural rubber (NR) / polybutadiene (BR) tire carcass and sidewall formulations, TBBS at 0.8–1.5 phr in the presence of 2.5 phr sulfur yields a Mooney scorch time (MS at 121°C) that is 35–50% longer than an equimolar CBS loading, as recorded on shearing-disc viscometers per ISO 289-1:2015. This wider processing window allows multi-pass internal mixing cycles in intermeshing rotor mixers (e.g., L/D ratio 1.4–1.6, fill factor 0.75) where stock temperatures peak at 130–140°C during silica dispersion. The penalty for this extended scorch safety is a modest reduction in cure rate: moving-die rheometer traces per ASTM D5289 show that t90 at 150°C for TBBS in NR tread compounds is typically 8–12% longer than for CBS. Nevertheless, the maximum torque (MH) and resulting tensile strength in the cured state—tested according to ASTM D412—remain within 5% of each other when adjusted to equal hard-acid crosslink network density. Plant trials on twin-screw roller-die extruders processing CB-filled NR/BR at output rates of 1200 kg/h have documented a reduction in die-swell scrap rates of 7% when substituting TBBS for CBS, attributed to fewer incipient scorch particles propagating edge-tears at the die lip.
TBBS is hygroscopic, and hydrolytic degradation proceeds autocatalytically once free 2-mercaptobenzothiazole (MBT) accumulates above 1.0 wt%. The hydrolysis pathway cleaves the S–N bond, liberating tert-butylamine and MBT; the latter accelerates further decomposition in a positive-feedback loop. To mitigate this, manufacturers supply TBBS in oil-treated granular forms (typical oil coating 1–2 wt% of naphthenic process oil) that reduce airborne dust and limit moisture ingress during sack or supersack storage. A side-by-side evaluation under controlled temperature-humidity conditions (30°C / 80% RH over 28 days) demonstrated that granular TBBS with 1.5% oil content retained 96% primary amine assay, whereas powdered TBBS without oil coating dropped to 82% assay over the same interval. Pre-drying in a forced-air oven at 50°C for 4 hours is recommended if sack exposure to ambient RH exceeding 60% exceeds 24 h. Table 1 summarizes the typical specification parameters for commercial TBBS grades used in rubber compounding.
| Parameter | Specification Range | Test Method |
|---|---|---|
| Assay (purity) | ≥97.0% | HPLC (area normalization) |
| Melting point (initial melting) | ≥103°C | Capillary method, ASTM D1519 |
| Ash content | ≤0.30% | ASTM D4574 |
| Free tert-butylamine | ≤0.50% | GC headspace |
| Free MBT | ≤0.80% | Potentiometric titration |
| Loss on drying (65°C, 2 h) | ≤0.40% | ASTM D4571 |
| Residue on 150 μm sieve (powder) / 2 mm sieve (granular) | ≤0.10% | ASTM D4572 |
Storage silo design on compounding lines must incorporate desiccant-breather systems when TBBS is pneumatically conveyed over distances greater than 40 m. Incompatibilities arise with strong acids and oxidizing agents; accidental blending with amine-based secondary accelerators (e.g., hexamethylenetetramine) in a shared weigh-hopper can generate localized exotherms exceeding 80°C that decompose the sulfenamide to MBT, permanently altering the cure profile.
The transition from carbon black to precipitated silica in passenger-tire tread compounds—driven by rolling-resistance and wet-grip optimization under EU tyre-labeling regulations—has altered the kinetic environment in which TBBS operates. Silica surfaces possess acidic silanol groups that adsorb basic accelerator fragments, potentially deactivating a fraction of the sulfenamide. TBBS, being less basic than diphenylguanidine (DPG), exhibits lower affinity for silanol adsorption but still requires a secondary accelerator to achieve full sulfur utilization. Typical silica-tread formulations use 1.2–1.8 phr TBBS paired with 0.3–0.6 phr DPG in a 2.0–2.4 phr sulfur cure system. The silanization reaction of bis(triethoxysilylpropyl)tetrasulfide (TESPT) with silica consumes amine species and can extend the induction period further; processing data from a 1.5 L laboratory internal mixer with Banbury-type rotors show that the Mooney scorch time at 130°C increases by 15–20% when TESPT loading rises from 4 phr to 8 phr in a TBBS-cured NR/BR matrix. Mixing protocols that achieve silanization temperatures of 145–155°C in the first pass, followed by TBBS addition in a second pass below 105°C, prevent hydrolytic loss of the sulfenamide during filler coupling. Full-scale compounding on intermeshing mixer lines with 270 L chamber volume confirms that the temperature window for the second-pass addition must be held within 100–110°C to avoid scorch nucleation while permitting adequate dispersion of the accelerator across the silica agglomerate network.
Table 2 compares the relative scorch safety and cure rate of TBBS with other common sulfenamide accelerators in a model NR/BR (70/30) formulation with 50 phr N330 carbon black, 2.2 phr sulfur, 5 phr ZnO, 2 phr stearic acid, and 1.0 phr of the respective sulfenamide, tested on a MDR at 150°C per ASTM D5289. The data are normalized to TBBS values set at a reference of 100.
| Sulfenamide | Scorch Safety Index (ts2 relative) | Cure Rate Index (t90 relative) | Modulus Development Index (MH - ML relative) |
|---|---|---|---|
| TBBS | 100 | 100 | 100 |
| CBS | 78 | 112 | 98 |
| DCBS (dicyclohexyl) | 152 | 74 | 96 |
| MBS (oxydiethylene) | 85 | 107 | 99 |
The data illustrate the inverse relationship between scorch safety and cure rate. TBBS occupies a middle position, preferred where a compound must survive multiple heat histories—such as calendering of fabric-reinforced conveyor belts—before final press cure. DCBS, with its bulkier dicyclohexylamine leaving group, provides even greater delay but at the cost of a significantly slower cure, which can reduce press throughput by 10–15% if cycle times are not extended. CBS and MBS accelerate the cure but narrower scorch windows limit their use in thick-section moldings where heat transfer gradients generate internal temperature delays that can produce under-cure at the center while the surface reaches maximum crosslink density.
In injection molding of EPDM automotive profiles—door seals and coolant hose covers—TBBS at 0.8–1.2 phr combined with a thiuram or dithiocarbamate secondary accelerator delivers high vulcanizate modulus (M100 > 2.5 MPa) and compression set under 25% after 22 h at 70°C per ASTM D395 Method B. The low free-amine specification is critical here: excess tert-butylamine can migrate into coolant fluid, extract into the glycol phase, and elevate pH above 9.5, accelerating elastomer degradation. Comparative trials on a 150-ton reciprocating-screw injection machine running a 4-cavity seal mold at 190°C found that TBBS-maintained compounds exhibited a 2.8-second median injection-fill time with zero scorched cavity incidents across 5000 cycles, whereas a CBS variant showed 14 scorch-related rejects per 1000 cycles under identical processing parameters.
When TBBS-accelerated NR compounds are vulcanized at the upper end of the processing spectrum—such as in press-cure operations reaching 185°C for thin-gauge rubber diaphragms—the induction period collapses nonlinearly. MDR isothermal data at 170°C, 180°C, and 190°C demonstrate that the scorch time ts2 for a 1.2 phr TBBS / 2.0 phr sulfur NR formulation drops from approximately 2.1 min at 170°C to 1.2 min at 180°C, and further to 0.7 min at 190°C (values derived from published technical bulletins of sulfenamide kinetics). At these cure temperatures, even a ±3°C fluctuation in mold-plate temperature—common in multi-daylight presses with oil-heated platens—can shift the scorch boundary by 10–15 seconds. This variation becomes the dominant factor in scrap-rate variability on production lines that lack closed-loop platen-temperature control with thermocouple feedback loops of response time under 2 s. Molders addressing this sensitivity often pre-heat the compound sheet to 60–70°C in a hot-air oven to reduce in-mold temperature equilibration time, but such pre-heating must not exceed 10 min total exposure to avoid initiating the scorch reaction in the pre-heat tray itself. TBBS, by virtue of its sterically hindered amine, provides a slight advantage over CBS in this high-temperature regime: the activation energy for the thermal decomposition of the TBBS-sulfur complex is reported to be approximately 10 kJ/mol higher, translating to a marginally wider temperature latitude before the autocatalytic crosslink cascade initiates.