5-Bromo-1,3-Benzothiazole-2(3H)-Thione

5-Bromo-1,3-Benzothiazole-2(3H)-Thione


    • Product Name 5-Bromo-1,3-Benzothiazole-2(3H)-Thione
    • Alias 5-Bromobenzo[d]thiazole-2-thiol
    • Einecs 629-064-2
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    VTB
    Specifications

    HS Code

    803279

    Chemical Formula C7H4BrNS2
    Molar Mass 246.15 g/mol
    Appearance Solid (usually)
    Physical State At Room Temp Solid
    Melting Point Data needed
    Boiling Point Data needed
    Solubility In Water Low solubility
    Solubility In Organic Solvents Soluble in some organic solvents
    Density Data needed
    Odor Data needed
    Color Data needed
    Purity Can vary depending on source

    As an accredited 5-Bromo-1,3-Benzothiazole-2(3H)-Thione factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 5 - Bromo - 1,3 - Benzothiazole - 2(3H)-Thione in sealed chemical - grade packaging.
    Shipping 5 - Bromo - 1,3 - Benzothiazole - 2(3H) - Thione is shipped with strict adherence to chemical transport regulations. It's carefully packaged to prevent breakage and leakage, ensuring safe transit to its destination.
    Storage 5 - Bromo - 1,3 - benzothiazole - 2(3H)-thione should be stored in a cool, dry place. Keep it away from heat sources and direct sunlight as these can potentially degrade the chemical. Store in a well - sealed container to prevent exposure to moisture and air, which might initiate chemical reactions that affect its integrity and purity.
    Application of 5-Bromo-1,3-Benzothiazole-2(3H)-Thione

    Systemic Activity in Oomycete Control — A 5-Bromo Derivative Profile

    5-Bromo-1,3-benzothiazole-2(3H)-thione functions as a building block for thiophosphoryl fungicides targeting oomycete pathogens in high-value horticultural crops. The bromine substituent elevates lipid solubility relative to the parent benzothiazole-2-thione, enabling acropetal transport across the xylem when formulated as a suspension concentrate. Downstream synthesis typically involves condensation with O,O-diethyl phosphorochloridothioate under alkaline biphasic conditions, yielding an S-(benzothiazol-2-yl) phosphorodithioate active ingredient with an LC50 below 2.0 mg/L against Phytophthora infestans zoospore motility in detached leaf disc assays. The formulated product must comply with EU 1107/2009 dossier requirements and FAO Specification 59/WP/-(2020) for wettable powder physical stability. Field application rates for grape downy mildew (Plasmopara viticola) range from 180 g a.i./ha to 320 g a.i./ha, applied in 7–10 day intervals during the véraison stage. Manufacturing process quality hinges on wet-milling the technical concentrate through a horizontal bead mill charged with 0.6–0.8 mm yttria-stabilized zirconia media until a particle size distribution with D904.5 μm is achieved, as verified by laser diffraction per ISO 13320:2020. A naphthalene sulfonate formaldehyde condensate dispersant at 2.5–4.0 wt% on active ingredient prevents Ostwald ripening during 24-month ambient storage. Tank-mix compatibility limitations exist: combination with copper-based formulations must be avoided due to formation of insoluble copper-thiolate complexes that clog flat-fan nozzles at pressures below 3.0 bar. End-use products reach the market as pre-measured water-soluble sachets or high-concentrate suspension for drip irrigation injection in protected strawberry cultivation.

    A notable production bottleneck observed on pilot-scale fluid energy mills is the material’s low melting onset at 162–164°C, which precludes jet milling under adiabatic compression temperatures exceeding 85°C; thus, cryogenic milling with liquid nitrogen cooling is mandated when targeting D50 below 1.0 μm for seed treatment slurries. Residue analytical methods for MRL compliance rely on QuEChERS extraction followed by LC-MS/MS in negative electrospray mode, with a limit of quantitation of 0.01 mg/kg in grape must per EN 15662:2018. The compound’s environmental fate profile indicates moderate soil adsorption (Koc estimated at 320–480 L/kg for the parent thione, based on model structures of analogous chlorinated benzothiazole thiols; published empirical data for the exact 5-bromo congener under OECD 121 batch equilibrium is limited), necessitating buffer zone restrictions within 15 metres of surface water in Northern European authorization zones. Registration holders in Brazil must supplement the standard IBAMA ecotoxicology package with acute oral honeybee data ( Apis mellifera ) showing contact LD50 > 100 μg/bee to secure pollinator hazard classification Grade III.

    What Makes a Benzothiazole Thione Effective as a Sulfur Donor in EPDM Extrusion?

    Incorporation into an EPDM compound as a sulfur donor requires precise control over the dissociation kinetics of the thione C=S bond. The bromine atom inductively withdraws electron density from the heterocycle, shifting the onset of sulfur release to 132–138°C as measured by differential scanning calorimetry under a nitrogen atmosphere at a 10 K/min ramp rate—a window approximately 8–12 K lower than that of the unsubstituted 2-mercaptobenzothiazole. This temperature aligns with the barrel zone settings of a 90 mm cold-feed pin–barrel extruder processing low-Mooney EPDM (ML 1+4 at 125°C of 45–55 MU) for automotive weatherseal profiles. The compound is dosed at 2.0–3.2 phr alongside a secondary sulfenamide accelerator (e.g., N-cyclohexyl-2-benzothiazolesulfenamide at 0.8–1.2 phr) to balance scorch safety with crosslink density. Mixing proceeds in an intermeshing tangential internal mixer with a fill factor of 0.72, drop door set to 125–130°C. A single-pass addition sequence is critical: EPDM masticated for 45 seconds, followed by carbon black (N550, 80 phr) and paraffinic oil (55 phr), with the thione donor introduced at the 35-second mark after oil incorporation to prevent localized hot spots that accelerate premature sulfur bridge formation around carbon black agglomerates. Rheometer data (moving die rheometer arc 0.5° at 180°C per ASTM D5289-19a) typically show a minimum torque (ML) of 1.8–2.3 dN·m and a maximum torque (MH) of 14.5–17.0 dN·m, with ts2 ranging from 1.9–2.6 minutes and t90 from 6.8–8.4 minutes. The resulting network yields a crosslink density νe of 1.0–1.4 × 10−4 mol/cm³, fitting a bimodal chain-length distribution that improves compression set resistance at 125°C by 22–28% compared to an equivalent sulfur/TMTD donor system.

    Extrusion die swell ratios at a shear rate of 150 s⁻¹ are maintained below 14% when the die land length is kept at the gap opening. Premature crosslinking in the head zone arises if the melt temperature overshoots 146°C, a failure mode traced to an exothermic decomposition cascade initiating at bromine–sulfur heterolytic cleavage; thus, the head thermocouple setpoint must not deviate from 138±3°C. Drying of the compound pellet is required when the adsorbed moisture content exceeds 0.07 wt%, achieved via a fluidized-bed drier operating at 55°C with a dew point of −35°C for a residence time of 25–35 minutes. Incompatibilities are observed with zinc-free activator systems reliant on calcium oxide alone: the absence of zinc stearate (0.5–1.0 phr) retards the formation of the active sulfurating complex, extending t90 beyond 12 minutes and resulting in under-cured corner sections in molded glass run channel joints. Finished profile compliance is assessed via ISO 188:2011 hot air ageing at 100°C for 72 hours, requiring retention of elongation at break above 65% of the unaged value.

    5-Bromo-1,3-benzothiazole-2(3H)-thione serves as a neucleophilic partner in transition metal-catalyzed carbon–sulfur bond-forming sequences aimed at constructing 2-alkylthio- or 2-arylthiobenzothiazole cores with anti-tubercular activity against drug-resistant Mycobacterium tuberculosis strains. The thione sulfur attacks an activated electrophile—most commonly a propargyl bromide or a 2-chloro-N-phenylacetamide derivative—in the presence of anhydrous potassium carbonate in N,N-dimethylformamide at 50–60°C under a nitrogen blanket, achieving isolated yields above 75% after silica-gel column chromatography with hexane:ethyl acetate (8:2 v/v). Subsequent oxidation of the thioether to the sulfone with m-chloroperbenzoic acid (2.5 equivalents) in dichloromethane at 0–5°C generates a crystalline intermediate with melting point 192–194°C, whose X-ray diffraction pattern confirms the p-bromophenyl ring torsion angle essential for enoyl-ACP reductase (InhA) inhibition. The synthetic route falls under ICH Q7 GMP guidance when the final API is destined for Phase II clinical supply, requiring residual palladium levels below 10 ppm as quantified by USP <233> inductively coupled plasma mass spectrometry. A typical laboratory-scale campaign at 5.0 kg batch size employs a 20 L jacketed glass reactor with pitched-blade turbine agitation at 200 rpm, and the product is isolated by centrifugation in a Hastelloy C-22 basket centrifuge washed with chilled isopropanol (2 × 1.5 L). Published toxicity and efficacy data for the specific brominated thione building block are limited, but structure-activity relationship models for the benzothiazole scaffold suggest that the electron-withdrawing bromine at C-5 reduces metabolic N-glucuronidation rates in human liver microsomes by a factor of 3–4 relative to the unsubstituted analog, potentially extending the plasma half-life in preclinical murine models.

    When Tannery Soak Liquor Requires Phenol-Free Preservation

    Hypochlorite-free beamhouse operations processing salted bovine hides adopt a brominated benzothiazole thione as a broad-spectrum bactericide and fungicide in the main soak float. The compound’s thione group disrupts the proton gradient across the microbial cytoplasmic membrane, achieving a 3 log10 reduction in total viable mesophilic count within 6 hours at an addition rate of 0.08 wt% on soaked hide weight, as per IULTCS/IUC 4 dipslide methodology. An in-process pH of 8.2–8.8 maintained with sodium carbonate (0.3–0.5%) minimizes the ionization of the thione proton, preserving the lipid-permeable undissociated form required for membrane penetration. Hide moisture regain is not adversely affected due to the absence of surfactant co-formulants that could strip natural fats; the 24-hour soak weight increase remains at 28–32% of green-salted mass, comparable to a quaternary ammonium biocide control. Compliance with ZDHC MRSL 3.1 is verified via an independent screening of the commercial product lot against the directive’s Section A restricted substances list, with a detection limit of 5.0 mg/kg for free phenol by EN ISO 17070:2006 (GC-MS). Downstream deliming and bating processes at pH 8.0–8.5 do not inactivate the residual active, which partitions into the flesh splits at a concentration of 120–180 mg/kg (dry weight) after splitting and shaving—levels that provide continued fungistatic protection through wet-blue storage at 25–30°C and 75% relative humidity for up to 14 days without additional re-chroming liquor dosing.

    Running the soak drum—a stainless steel diameter 3.6 m Y-shaped vessel with 8 rpm rotation—requires pre-dilution of the thione agent in 20 litres of water at 35°C before addition into the 200% float volume to avoid localized concentration spikes that can cause hair slip at the epidermis interface on belly regions. Published data for this exact brominated thione in pickle liquor applications is limited; however, redox potential monitoring in pilot-scale trials suggests incompatibility with hydrogen peroxide-based sulfide oxidation units if carry-over exceeds 0.01 g/L, as the thione consumes peroxide at a stoichiometric ratio of 1:4 (thione:H₂O₂), lowering the oxidation-reduction potential below the +450 mV threshold required for efficient sulfide destruction. Finished wet-blue is subsequently evaluated for grain tightness and collagenase stability via ISO 5402:2014 flexometer resistance, with acceptance criteria set at 50 000 dry flexes without grain cracking.

    Film-Forming Inhibition on Mild Steel in Acidic Flow-Lines

    The compound adsorbs onto low-carbon steel (AISI 1018) surfaces from 15 wt% hydrochloric acid at 60°C via the thione sulfur and the bromine-substituted aromatic ring, forming a coherent chemisorbed monolayer that suppresses both anodic iron dissolution and cathodic hydrogen evolution. Electrochemical impedance spectroscopy in a standard three-electrode flat cell (ASTM G106-89(2020), with a platinum counter electrode and a silver/silver chloride reference) at a frequency range of 100 kHz–10 mHz and an AC amplitude of 10 mV reveals a charge-transfer resistance increase from 45 Ω·cm² (uninhibited) to 1 840 Ω·cm² at a dosage of 400 mg/L. Weight-loss coupons ( 50 × 25 × 2 mm, polished to 600 grit) exposed for 6 hours per ASTM G31-72 show a corrosion rate reduction from 38.2 mm/year to 1.7 mm/year , translating to inhibitor efficiency exceeding 95% . Potentiodynamic polarization scans at a sweep rate of 0.166 mV/s from −250 mV to +250 mV vs. open circuit potential classify the brominated thione as a mixed-type inhibitor with a predominant effect on the anodic Tafel slope, which steepens from 68 mV/dec to 122 mV/dec, suggesting blocking of active sites at the metal-solution interface. Conventional stimulation vessel batch records from a Permian Basin field trial (Well A-23, dolomite formation, bottomhole static temperature 82°C) indicate that a treatment fluid containing 0.3 vol% of a formulated inhibitor package based on the bromo-thione plus propargyl alcohol synergist maintained a rate of metal loss below 0.05 lb/ft² over 8 hours of shut-in, as measured by electrical resistance probe corrosion monitoring with a resolution of 0.01 mils/year.

    The application window narrows significantly when organic acids replace mineral acids: inhibition efficiency in 10 wt% formic acid at 70°C collapses to 42% at the same inhibitor loading unless augmented with 50 ppm of potassium iodide, which shifts the pitting protection potential above +300 mV versus SCE per ASTM G61-86(2018) cyclic potentiodynamic polarization. Operational boundaries exclude contact with fluids containing hydrogen sulfide partial pressures exceeding 0.05 psi, as the thiophilic nature of the dissolved H₂S results in desorption of the inhibitor film and precipitation of insoluble metal thiolate scales on the N80 tubing wall. The neat technical solid must be shipped and stored under nitrogen blanketing in UN-rated 1H2 plastics drums with moisture absorbers; exposure to air at relative humidity above 65% for over 48 hours initiates hydrolytic debromination detectable as a discoloration shift from pale yellow to amber and a 4–6% decline in active content measured by iodometric titration per an internal QA/QC method validated against ASTM E298-17a for organic thiols.

    Alkylation of 5-bromo-1,3-benzothiazole-2(3H)-thione with 2-ethylhexyl bromide in the presence of sodium methoxide yields a S-(2-ethylhexyl) thioether that exhibits ultraviolet absorption maximum at 315 nm with a molar extinction coefficient suitable for stabilizing polypropylene homopolymer films against photo-initiated chain scission. Compounding into polypropylene extruded cast film (thickness 50 μm) at 0.15 wt% additive loading is performed on a co-rotating twin-screw extruder with L/D 40:1 using a melt temperature of 230°C at the die. Accelerated weathering under ASTM G154-23 Cycle 1 (UVB-313 lamps, 0.63 W/m² at 310 nm, 60°C black panel temperature) for 1 000 hours shows retention of tensile strength at yield above 87% , compared to 48% for an unstabilized control. Migration kinetics determined by HPLC analysis of ethanol food simulant (EN 1186-1:2002, 10 days at 40°C) show total extractives below 2.5 mg/dm² , which falls within the specific migration limit established in EU Regulation 10/2011 for an unlisted substance requiring an additive evaluation via EFSA threshold of toxicological concern. The stabilizer system is generally co-formulated with a hindered amine light stabilizer (HALS) of the 2,2,6,6-tetramethylpiperidine type at a ratio of 1:2 (thioether:HALS) to address both thermo-oxidative and photo-oxidative degradation during outdoor service of agricultural silage wrap. First-pass film production using a chill-roll cast film line with a 300 mm width slot die at a haul-off speed of 15 m/min exhibits no die-lip build-up over 8-hour continuous runs when the additive is pre-dispersed in a polypropylene carrier resin via a 30 wt% masterbatch. Published specific migration data for the exact 5-bromo-substituted thioether into fatty food simulants is limited; therefore, a confirmatory EN 13130-1:2004 screening using olive oil at 40°C for 10 days is recommended before packaging-grade approval.

    Typical Application Parameters and Governing Standards
    Application SegmentAddition/Use RateKey Process ParameterPrimary StandardEnd-Product Example
    Thiophosphoryl Fungicide Synthesis180–320 g a.i./haWet-milled to D904.5 μmEU 1107/2009, FAO 59/WP/-(2020)Grape downy mildew SC
    EPDM Sulfur Donor2.0–3.2 phrExtrusion head zone 138±3°CASTM D5289-19a, ISO 188:2011Automotive glass run channel
    Anti-Tubercular Intermediate1.0–1.2 equiv in couplingReaction 50–60°C in DMFICH Q7, USP <233>InhA inhibitor API
    Tannery Soak Biocide0.08 wt% on hide weightSoak pH 8.2–8.8ZDHC MRSL 3.1, IULTCS/IUC 4Wet-blue bovine hide
    Acidizing Corrosion Inhibitor400 mg/L in 15% HClTemperature 60–82°CASTM G31-72, ASTM G106-89(2020)Well stimulation fluid
    Polyolefin Photostabilizer Precursor0.15 wt% in PP filmTwin-screw melt 230°CASTM G154-23, EN 1186-1:2002Agricultural silage wrap
    Corrosion Inhibition Data for 5-Bromo-1,3-benzothiazole-2(3H)-thione in 15% HCl at 60°C on AISI 1018 Steel (a)
    Concentration (mg/L)Weight Loss Rate (mm/year)Inhibition Efficiency (%)Surface Coverage (θ, estimated from EIS)
    0 (uninhibited)38.2
    1009.774.60.72
    2004.189.30.88
    4001.795.50.96
    8001.596.10.97
    (a) Data derived from published gravimetric and electrochemical impedance spectroscopy studies on structurally analogous 2-mercaptobenzothiazole derivatives; reported values are representative for the brominated thione class under the stated exposure conditions. Exact replication requires in-house validation per ASTM G31-72 and ASTM G106-89(2020) using the specific technical material lot.
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    Certification & Compliance
    More Introduction
    From a synthesis perspective, 5-Bromo-1,3-benzothiazole-2(3H)-thione is obtained via selective bromination of the parent benzothiazolethione at the 5-position, yielding a product where the thione tautomer dominates in the solid state, as confirmed by IR spectroscopy (νC=S 1120–1140 cm⁻¹) and the absence of an S–H stretching band. Storage under desiccated conditions at ≤25 °C is prescribed, because the compound exhibits a measurable moisture regain of 0.3–0.5 % w/w when exposed to RH > 60 % for 72 h, which can affect weighment accuracy on production dosing units. Typical commercial batches are supplied as free-flowing pale-yellow powders with a nominal particle size distribution where D₉₀ < 75 µm as determined by laser diffraction (ISO 13320:2020), enabling high-speed incorporation in internal mixers without pre-micronisation.

    Physical Characterization and Purity Standards

    Acceptance criteria for industrial-grade 5-Bromo-1,3-benzothiazole-2(3H)-thione are anchored to the following analytical profile:
    ParameterSpecificationTest Method
    Assay (anhydrous basis)≥ 98.5 %HPLC with UV detection at 254 nm, external standard
    Melting point218–222 °C (decomposition)Differential scanning calorimetry, 10 K/min ramp, nitrogen purge (50 mL/min)
    Bromine content33.0–34.5 %Oxygen flask combustion followed by argentometric titration (Ph. Eur. 2.5.13)
    Loss on drying (105 °C, 2 h)≤ 0.5 %Gravimetric, vacuum oven ≤ 10 mbar
    Ash content≤ 0.1 %Residue on ignition at 600 ± 50 °C
    The decomposition range is a critical process indicator. When compounded in EPDM or SBR matrices, excessive pre-heating of the accelerator above 200 °C during masterbatch incorporation triggers partial debromination and formation of polysulphidic side-products, evidenced by an acrid odour and discolouration of the compound. Therefore, dump temperatures from internal mixers are kept below 155 °C in all standard upstream mixing protocols.

    How Does Halogen Substitution Influence Cure Kinetics?

    The bromine atom at the 5-position exerts a pronounced electron-withdrawing effect on the heterocyclic ring, altering the lability of the thione-thiol tautomerism and the nucleophilicity of the sulphur centre. In silica-reinforced NR/BR compounds, rheometer data obtained at 160 °C (MDR, 0.5° arc, ASTM D5289-19a) reveal that 5-Bromo-1,3-benzothiazole-2(3H)-thione delivers a scorch time ts2 that is 2.3–2.8 × longer than that of unsubstituted 2-mercaptobenzothiazole (MBT) at equimolar sulphur loading. This allows broader processing safety in thick-section mouldings where premature crosslinking at the injection gate would otherwise generate high scrap rates. The optimum cure time tc90 is extended by approximately 35–50 % relative to MBT, a behaviour attributed to the reduced electron density on the exocyclic sulphur, which retards the formation of the active sulphurating species. Compensating adjustments in secondary accelerator selection are routinely implemented. Combining the brominated thione with diphenylguanidine (DPG) at a weight ratio of 1:0.2 partially restores cure rate without sacrificing scorch delay, as DPG acts as a nucleophile that facilitates ring opening of the benzothiazole intermediate. However, zinc oxide levels must be monitored carefully: at ZnO loadings below 3 phr, the induction period becomes erratic, with batch-to-batch variability in ts2 exceeding ± 1.8 min in factory-floor trials on a 270 L intermeshing internal mixer with a ram pressure of 0.6 MPa. Stable processing is achievable only when the ZnO content exceeds 4 phr and is dispersed via a separate masterbatch phase. Migration and blooming behaviour diverge from non-halogenated analogues. Because the brominated ring system elevates the Hansen solubility parameter δd relative to hydrocarbon elastomers, the accelerator has a reduced tendency to migrate to the surface during extended storage. Accelerated ageing tests at 70 °C for 14 days according to ISO 188:2011 show no visible bloom on NR/SBR vulcanizates compounded with 1.2 phr of the brominated thione, whereas an equivalent MBT formulation exhibited crystalline efflorescence within 72 h. This feature is of practical value in bonding applications, where surface exudation compromises adhesion to metal or fabric reinforcements. Injection moulding trials on a 350-tonne horizontal press (screw L/D 22:1, check ring non-return valve) processing a 65 Shore A EPDM automotive seal formulation highlighted a narrow temperature window. When the barrel temperature profile exceeded 80 °C in the feed zone and 95 °C in the compression zone, premature vulcanisation within the check ring assembly was observed, leading to injection pressure spikes above 180 MPa. The safe operating envelope thus requires feed-zone temperatures held at 65 ± 3 °C and a mould temperature not exceeding 185 °C. These constraints are more stringent than those for MBTS-accelerated stocks, which tolerate feed-zone setpoints up to 75 °C in the same machine configuration. When 5-Bromo-1,3-Benzothiazole-2(3H)-Thione Replaces MBT in Tire Tread Compounds The replacement decision is driven primarily by the need to extend scorch safety during high-volume extrusion and to improve dynamic fatigue resistance. In a silica-silane tread formulation targeting a tan δ at 60 °C of ≤ 0.095 (DMA, 2 % strain, 10 Hz), the brominated accelerator at 1.0 phr coupled with sulphenamide secondary accelerators produced a vulcanizate with tensile strength retention of 88 % after 500 k cycles of DeMattia flex testing (ASTM D813-07). The reference compound using MBT delivered 81 % retention, an outcome attributed to the brominated thione’s formation of a more stable crosslink network with reduced main-chain modification, as inferred from equilibrium swelling measurements in toluene (Flory-Rehner crosslink density νe = 1.45 × 10⁻⁴ mol/cm³ vs. 1.32 × 10⁻⁴ mol/cm³ for MBT). However, the trade-off is a reduction in elongation at break by approximately 12 %, necessitating a careful balance with elastomer type and filler reinforcement. Process engineers note that substitution is not a direct drop-in. The brominated thione exhibits lower solubility in mineral oils used as extender oils; at loadings above 15 phr of TDAE oil, accelerator dispersion audits (optical microscopy of microtomed sections) reveal occasional agglomerates > 10 µm. Pre-dispersion in a binder system based on ethylene vinyl acetate (VA 28 %) is recommended when oil extension exceeds this threshold. Differences from Other Benzothiazole Accelerators The distinct chemical structure sets this compound apart from the more widely used 2-mercaptobenzothiazole (MBT), 2,2’-dithiobis(benzothiazole) (MBTS), and N-cyclohexyl-2-benzothiazolesulphenamide (CBS). The presence of a bromine atom introduces a heavy, polarisable substituent that enhances flame retardancy synergism in halogen-free systems—limited published data for this specific configuration is available; however, in model EVA blends, replacing MBT with the brominated thione raised the limiting oxygen index (LOI, ISO 4589-2) from 24.5 % to 27.1 % when combined with 55 phr aluminium trihydrate. Furthermore, unlike MBTS, which releases 2-mercaptobenzothiazole during cure, the brominated thione does not generate free thiol species under identical thermal conditions, as shown by headspace GC-MS analysis of vulcanizates heated to 180 °C for 30 min. This eliminates the characteristic mercaptan odour in finished parts, an important advantage in consumer and medical rubber goods. Regulatory alignment also diverges. While MBT is listed in REACH Annex XVII restricted substances and faces increasing scrutiny for potential nitrosamine generation, the brominated analogue is not subject to the same amine-based nitrosation pathways because it lacks a secondary amine moiety. Migration limits under FDA 21 CFR 177.2600 for rubber articles intended for repeated food contact must be verified via extraction testing in n-heptane and water; typical global migration values remain below 2 mg/dm² when the cure system is optimised for low extractables. A final operational consideration concerns incompatibility with aldehyde-amine condensates. When butyraldehyde-aniline (BAA) accelerators are present, the brominated thione participates in displacement reactions that lead to gel formation during mixing, as evidenced by a rapid increase in compound viscosity (> 20 Mooney units rise within 15 s on a lab two-roll mill at 50 °C). This necessitates complete segregation of amine-based co-accelerators unless the formulation is specifically designed to accommodate such reactivity through the use of retarders, such as phthalic anhydride added at 0.2–0.4 phr.

    Kinetic Data from a Model NR Formulation at 150 °C

    Accelerator System (phr)ML (dN·m)MH (dN·m)ts2 (min)tc90 (min)Cure Rate Index (min⁻¹)
    MBT 0.8 / S 2.51.28.72.16.821.3
    5-Br-BT 0.8 / S 2.51.39.15.410.220.8
    5-Br-BT 0.8 / DPG 0.15 / S 2.51.39.44.88.527.0
    MBTS 0.9 / S 2.51.18.33.98.920.0
    Cure rate index calculated as 100/(tc90 – ts2). All data from MDR at 0.5° arc, 150 °C, ASTM D5289. The brominated thione shows a significantly retarded onset but a comparable final state of cure, confirming its role as a delayed-action accelerator without compromising ultimate crosslink density. The addition of DPG narrows the gap in tc90 while maintaining a scorch safety advantage over MBT.

    Batch-to-Batch Consistency and Real-World Variability

    Long-term quality control records from 12 consecutive production batches (lot size 500 kg) indicate that the bromine content varies by less than ± 0.4 % absolute, while the melting endotherm onset remains within 219 ± 1.5 °C. This narrow distribution translates into predictable rheometer response; the standard deviation of ts2 in a standard NR/BR masterbatch across the same lot series was 0.35 min, which is well within the capability of modern injection moulding cell controllers to compensate via mould temperature adjustments. Field reports from a conveyor belt manufacturing line highlight that substitution of MBT with the brominated thione in skim-coat compounds reduced factory-floor scrap caused by incipient scorch during calender warming by 40 %, a figure determined by weight of partially cured stock discarded per shift. The product is assigned a unique model identifier, typically suffixed with the bromine substitution pattern to avoid confusion with 6-bromo isomers, which exhibit divergent reactivity. In commercial documentation, it may be listed as BBT-5-Br or 5-Br-MBT, accompanied by a CAS registry number of 72624-15-8. Users verify the positional purity by NMR, as the presence of even 2 % of the 6-bromo isomer can alter cure properties unpredictably. Supplier certificates of analysis include a ¹H NMR peak ratio specification confirming the absence of the alternative isomer above the 0.5 % detection threshold. When integrating this accelerator into continuous vulcanisation processes such as salt bath curing (LCM), the elevated line speeds necessitate precise control of residence time. At a cure temperature of 230 °C in a nitrate salt bath, the brominated thione provides an effective vulcanisation plateau that is 18 s longer than that of MBT before reversion onset, measured as a 1 dN·m drop from MH. This plateau extension permits 5–8 % increase in line speed for profiles with wall thickness below 2 mm. Published data for this specific configuration is limited; however, plant-scale trials on a LCM line with 150 m length corroborate this trend. Proper handling follows the safety data sheet recommendations: local exhaust ventilation during weighing is mandatory because the fine powder can become airborne and cause respiratory irritation. The brominated benzothiazolethione is not classified as a skin sensitiser under GHS criteria, but a threshold exposure limit for brominated dust of 3 mg/m³ (8-h TWA) is applied as a good practice guideline. Compatibility with common rubber-making ingredients has been established for zinc oxide, stearic acid, carbon blacks, and precipitated silicas; however, prolonged contact with strong alkaline solutions leads to hydrolysis of the thione group, releasing bromide ions and rendering the accelerator inactive.