5-Methylbenzothiazole

5-Methylbenzothiazole


    • Product Name 5-Methylbenzothiazole
    • Alias 5-Methyl-1,3-benzothiazole
    • Einecs 212-236-7
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
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    • Manufacturer Bouling Chemical Co., Limited
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    VTB
    Specifications

    HS Code

    409206

    Chemical Formula C8H7NS
    Molecular Weight 149.21 g/mol
    Appearance Solid (usually white to off - white powder)
    Odor Typical benzothiazole - like odor
    Melting Point 56 - 58 °C
    Boiling Point 238 - 240 °C
    Solubility In Water Slightly soluble
    Solubility In Organic Solvents Soluble in common organic solvents like ethanol, chloroform
    Density 1.23 g/cm³ (approximate)
    Stability Stable under normal conditions

    As an accredited 5-Methylbenzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 5 - Methylbenzothiazole packaged in 500 - gram bottles for chemical use.
    Shipping 5 - Methylbenzothiazole is shipped in well - sealed, corrosion - resistant containers. Adequate cushioning and labeling indicating its chemical nature are ensured. Shipment follows strict safety regulations for chemical transportation.
    Storage 5 - Methylbenzothiazole should be stored in a cool, dry, well - ventilated area away from sources of ignition. Keep it in a tightly closed container to prevent evaporation and contamination. Store it separately from oxidizing agents and incompatible substances. Avoid storage near heat or direct sunlight to maintain its chemical stability.
    Application of 5-Methylbenzothiazole

    The synthesis of 2-mercapto-5-methylbenzothiazole proceeds via thiolation of 5-methylbenzothiazole with sodium hydrosulfide under pressure in an aqueous medium at 140–160°C. The reaction is carried out in a Hastelloy C-276 autoclave with anchor-type agitation at 60–90 rpm to ensure sufficient gas-liquid contact, as the rate-limiting step is dissolution of H₂S into the molten organic phase. The molar ratio of NaHS to 5-methylbenzothiazole is maintained at 1.08:1; excess hydrosulfide shifts the equilibrium toward the thiolate but levels above 1.15:1 generate polysulfide byproducts that reduce the melting point of the crude product and cause filtration difficulties in the downstream isolation step. After a hold time of 5–6 hours, the batch is cooled to 80°C, acidified to pH 4.5–5.0 with dilute sulfuric acid, and the precipitated 2-mercapto-5-methylbenzothiazole is collected by vacuum belt filtration. The wet cake is washed with deionized water until the conductivity of the filtrate drops below 50 μS/cm and dried in a conical vacuum dryer at 45°C and 5 kPa to a moisture content of ≤0.15 wt%, which is critical because residual moisture promotes dimerization during subsequent pelletizing and storage. The final accelerator is blended with ethylene-propylene-diene monomer (EPDM) binder and paraffinic process oil in a co-rotating twin-screw extruder (L/D ratio 48:1) at a screw speed range of 180–220 rpm and barrel temperature profile 50°C→65°C→70°C→65°C→50°C to produce dust-free cylindrical pellets of 2.0–2.5 mm diameter. In a natural rubber compound formulation based on RSS-1 (ribbed smoked sheet) filled with N330 carbon black at 50 phr, the dichloromethane-extractable 2-mercapto-5-methylbenzothiazole content measured by HPLC must fall within 0.35–0.50 wt% of total compound mass to balance scorch safety and crosslink density. At loading of 0.8 phr in a sulfur cure system with 2.0 phr sulfur and 4.0 phr zinc oxide, the compound exhibits a Mooney scorch time (MS-t5 at 121°C, per ISO 289-1:2022) of 18–22 minutes and a cure rate index (per ISO 3417:2008, MDR at 150°C) of 8.5–9.5 dN·m/min. Methyl substitution on the benzothiazole ring reduces the nucleophilicity of the mercapto group relative to unsubstituted MBT, decelerating sulfidic crosslink insertion and thereby widening the safe-processing plateau by 3–5 minutes compared to formulations employing an equimolar sulfur mass fraction of MBT. This delay is exploited in the manufacture of large rubber-to-metal bonded anti-vibration mounts, where full mold filling before the onset of scorch requires a compound flow distance exceeding 600 mm in transfer molding presses with clamp force above 800 tonnes. Compliance with EU Directive 2005/69/EC (PAH restriction) is maintained via post-vulcanization acetone extraction that confirms benzo[a]pyrene content below the 1.0 mg/kg threshold. Accelerator migration into polyamide overmolding layers is suppressed when the cure temperature is limited to 145°C to avoid the exudation threshold of 150–155°C observed in TGA isothermal mass loss experiments.

    Textile-grade 4,4′-bis[(4-anilino-6-morpholino-1,3,5-triazin-2-yl)amino]stilbene-2,2′-disulfonic acid derivatives are synthesized by cyanuric chloride mediated coupling, where 5-methylbenzothiazole-2-sulfonic acid serves as the anilino-group building block that extends the conjugation length and shifts the fluorescence emission maximum from 435 nm to 448 nm. Sulfonation of 5-methylbenzothiazole is performed with 20% oleum at 25–30°C, yielding the 2-sulfonic acid isomer in excess of 92% selectivity as verified by ion chromatography with conductivity detection. The condensation with cyanuric chloride is carried out in a jacketed glass-lined reactor at 0–2°C and pH 7.0–7.5, controlled by simultaneous metering of 10% sodium carbonate solution, using a mole ratio of 5-methylbenzothiazole-2-sulfonic acid to cyanuric chloride of 1.00:1.02. After the first condensation step, the second chlorine on the triazine ring is substituted with aniline-2,5-disulfonic acid at 35–40°C and pH 6.5–7.0, followed by the third chlorine displacement with morpholine at 80–85°C. The resulting triazine-stilbene fluorescent whitening agent (FWA) is isolated as a disodium salt by spray drying at an inlet temperature of 190°C and outlet of 90°C, yielding free-flowing microspheroids with a bulk density of 0.45–0.55 g/cm³. In laundry powder application at 0.08–0.15 wt% of detergent mass, the CIE whiteness index of cotton poplin fabric after 25 wash cycles at 60°C in water of 250 ppm CaCO₃ hardness is increased by 18–22 points relative to unwhitened control, as determined by a spectrophotometer with d/8° geometry per ISO 105-J02:1997. The critical aggregation concentration of the FWA in the wash liquor, measured by fluorescence polarization, is 8×10⁻⁶ mol/L; above this value the quantum yield plateaus because of excimer self-quenching. Therefore, the dosing pump stroke length on the detergent post-dosing station must be calibrated to maintain an anionic surfactant to FWA ratio of 120:1 to 150:1 to prevent precipitation as a surfactant-FWA complex. Registration for detergent use under EU Ecolabel Decision (EU) 2017/1218 requires ready biodegradability demonstrated by >70% DOC removal in a 28-day OECD 301B test, a criterion that the morpholine-substituted structure satisfies when the dissolved oxygen uptake curve shows a lag phase not exceeding 3 days.

    Table 1. Cure characteristics of NR/BR blend with mercapto-accelerator systems at 150°C (MDR per ISO 3417:2008)
    Parameter2-Mercapto-5-methylbenzothiazole (0.8 phr)MBT (0.8 phr)Test method
    Min. torque ML (dN·m)1.8–2.01.7–1.9ISO 3417
    Max. torque MH (dN·m)14.2–14.815.1–15.7ISO 3417
    ts2, scorch safety (min)11.0–12.57.5–8.5ISO 3417
    t90, optimum cure (min)22.0–24.018.5–20.0ISO 3417
    Tensile strength, MPa (cured to t90)24.5–25.525.0–26.0ISO 37:2017 (dumbbell type 2)

    Where solubility parameters dictate that the benzothiazole mesogenic core must exhibit a dipole moment between 2.8 and 3.2 D to achieve the desired dielectric anisotropy for twisted nematic (TN) and super-twisted nematic (STN) electro-optical cells, 5-methylbenzothiazole is converted to 2-(4-alkylphenyl)-5-methylbenzothiazole via a palladium-catalyzed Suzuki coupling. The cross-coupling employs Pd(PPh₃)₄ at a loading of 0.5 mol% relative to 5-methylbenzothiazole-2-boronic acid pinacol ester, with potassium carbonate (2.0 equiv.) in a degassed toluene/ethanol/water ternary mixture (volume ratio 5:1:1) at reflux for 8 hours. The boronate ester precursor is obtained by lithiation of 5-methylbenzothiazole with n-butyllithium at -78°C in anhydrous THF, followed by quenching with 2-isopropoxy-4,4,5,5-tetramethyl-1,3,2-dioxaborolane at -70 to -65°C. After aqueous work-up and chromatography over silica gel (eluent: hexane/ethyl acetate 95:5 v/v), the 2-(4-alkylphenyl)-5-methylbenzothiazole intermediates are hydrogenated over 5% Pt/C at 0.3 MPa to saturate the alkyl chain to a trans-cyclohexyl unit when low birefringence is targeted. The nematic phase range of the homologous series with alkyl chain lengths C₃ to C₇ spans from 42°C to 118°C (clearing point), as determined by differential scanning calorimetry at a scan rate of 5°C/min. Voltage holding ratio (VHR) measurements at 25°C and 1 Hz frame rate, following IEC 61747-5-3:2020, demand that the mesogen exhibit a resistivity >5×10¹³ Ω·cm after silica gel filtration and vacuum degassing at 2 Pa for 24 hours to eliminate ionic impurities below the 10⁻⁸ mol/L threshold. Blends containing 8–12 wt% of this benzothiazole dopant in a base mixture of alkylcyanobiphenyls and alkylterphenyls reduce the threshold voltage (V₁₀) of a 90° TN cell from 1.85 V to 1.58 V while the optical response time (τ_on+τ_off) at ±3 V driving remains below 45 ms. The methyl substituent at the 5-position suppresses the formation of the smectic A phase that otherwise appears with unsubstituted benzothiazole derivatives at temperature ranges overlapping the nematic operating window, a critical processing requirement for injection-filling of 4–6 μm cell gaps on production lines operating with a fill-speed of 1.5–2.5 mm/s.

    The cyanine dye chromophore 3-ethyl-2-[3-(3-ethyl-3H-benzothiazol-2-ylidene)-propenyl]-5-methylbenzothiazolium iodide, used as a spectral sensitizer in silver halide tabular-grain emulsions for green-light recording layers, is assembled by condensation of 5-methyl-2-methylthiobenzothiazole with 2-(2-acetanilidovinyl)-3-ethylbenzothiazolium iodide in acetic anhydride at 120°C in the presence of triethylamine (1.1 eq.). The key intermediate 5-methyl-2-methylthiobenzothiazole is prepared by S-alkylation of the corresponding 2-mercapto derivative with dimethyl sulfate at 55°C in aqueous sodium bicarbonate, the exothermicity requiring controlled reagent addition over 45 minutes to keep the temperature below 60°C. After the dye condensation, the reaction mass is drowned into ice water, and the precipitated dye is collected, washed with methanol until the filtrate is colorless, and vacuum-oven dried at 40°C. The absorption maximum in methanol is 512 ± 2 nm (log ε = 4.92), which shifts to 535 nm in the J-aggregate state adsorbed onto AgBrI (3 mol% iodide) tabular grains of 1.2 μm equivalent circular diameter. Coating formulations for negative-working graphic arts film employ a dye loading of 0.35–0.50 mmol per mole of silver halide to achieve a spectral sensitivity of 3.2×10⁻³ J/m² at 530 nm (exposure required for an optical density of 1.0 above fog), evaluated in a 21-step sensitometric wedge exposure through a 530 nm interference filter. The residual methylthiobenzothiazole precursor must be <0.05% area by HPLC (UV 254 nm) because it functions as a desensitizer on the grain surface, elevating the intrinsic fog level by displacing the cyanine dye from its adsorption sites. Manufacturing specifications for the finished dye, aligned with ISO 18921:2008 (silver image stability), require that a forced-aging test at 70°C and 80% RH for 7 days produces a change in optical density of dye-only extraction solvent of less than 0.03 units, confirming that the 5-methyl substitution imparts sufficient oxidative stability by blocking the benzothiazole ring position most susceptible to photo-Fenton discoloration.

    When the benzothiazole core is incorporated as a heterocyclic substituent on the triazolopyrimidine scaffold of the fungicide 5-chloro-7-(4-methylpiperidin-1-yl)-6-(2,4,6-trifluorophenyl)-[1,2,4]triazolo[1,5-a]pyrimidine, 5-methylbenzothiazole-2-carbaldehyde functions as the key building block that introduces a hydrogen-bond-acceptor motif to the ATP-binding pocket of succinate dehydrogenase. The aldehyde is generated by Vilsmeier-Haack formylation of 5-methylbenzothiazole using POCl₃ and DMF at 80°C, with the mole ratio of POCl₃ to substrate set at 2.5:1 to drive complete conversion within 6 hours. After quenching onto crushed ice and neutralization to pH 7.0, the crude aldehyde is purified by vacuum distillation at 2.5–3.0 mm Hg (boiling range 148–152°C) and stored under nitrogen at –20°C to suppress auto-oxidation to the corresponding carboxylic acid, which would otherwise exceed a specification limit of 0.2 wt% as measured by acid-base titration. The subsequent Knoevenagel condensation with ethyl cyanoacetate in toluene with piperidine acetate catalyst at reflux, followed by cyclization with aminoguanidine bicarbonate, yields a benzothiazole-triazolopyrimidine intermediate in 65–70% overall yield after recrystallization from methyl tert-butyl ether. Pesticide registration under Regulation (EC) No 1107/2009 requires an impurity profile demonstrating that the 5-methylbenzothiazole-2-carbaldehyde intermediate contains less than 0.1 mg/kg of mutagenic benzothiazole-derived nitrosamines, as verified by LC-MS/MS with a method detection limit of 0.02 mg/kg. The commercial wettable powder formulation (500 g/kg active ingredient) is obtained by jet-milling the active substance with sodium lauryl sulfate (2.0 wt%) and precipitated silica (8.0 wt%) to a particle size distribution with D₉₀ <5 μm (laser diffraction, Malvern Mastersizer 3000), ensuring suspension stability of >90% after 30 minutes in a 2.0% aqueous dilution per CIPAC MT 184.

    Table 2. Key physical properties of 5-methylbenzothiazole derivatives for polymerization of photosensitive resin
    PropertyValue/rangeAnalytical technique
    Melting point of 5-methylbenzothiazole10–12°C (b.p. 237°C/760 mm Hg)DSC, heating rate 10°C/min
    Assay purity (typical supplier specification)≥99.0% (area%, GC-FID)Capillary GC, DB-5 column, 30 m × 0.25 mm
    Water content (Karl Fischer, coulometric)≤0.10%ISO 760:1978
    Iron content<2 mg/kgAAS or ICP-OES
    Storage stability (dark, 25°C)24 months without color change >50 APHAVisual comparison per ASTM D1209

    The amine-catalyzed condensation of 5-methylbenzothiazole-2-sulfonamide with 2-chloro-4,6-dimethoxy-1,3,5-triazine in a two-phase water/toluene system produces a sulfonylurea herbicide safener that upregulates glutathione S-transferase in maize. The sulfonamide intermediate is synthesized by chlorosulfonation of 5-methylbenzothiazole with chlorosulfonic acid at –5 to 0°C, followed by ammonolysis with 25% aqueous ammonia at 10–15°C. The addition rate of ammonia is controlled so that the pH of the reaction mixture does not exceed 10.5 to avoid ring-opening of the thiazole via nucleophilic attack at the 2-position. After filtration, the sulfonamide is recrystallized from isopropanol to a melting point of 184–186°C. In the triazine coupling step, the stoichiometry of sulfonamide to 2-chloro-4,6-dimethoxy-1,3,5-triazine is 1:1.1, with tetrabutylammonium bromide phase-transfer catalyst at 3 mol% and aqueous NaOH as acid scavenger to maintain the interphase pH at 8.0–8.5. The reaction completes in 12–14 hours at 30°C, after which the organic layer is separated, dried over sodium sulfate, concentrated, and the safener precipitated by addition of n-heptane. The safener is typically coated onto corn seed at a rate of 30–50 g a.i. per 100 kg seed in combination with a film-forming polymer binder (polyvinyl alcohol, hydrolysis degree 88%) to ensure adhesion and controlled release. Efficacy testing according to Council Directive 76/116/EEC methodology, as amended, demonstrates that the safener reduces the phytotoxicity of sulfonylurea herbicides such as nicosulfuron by >85% at the 2-leaf stage of maize, measured by chlorophyll fluorescence parameter Fv/Fm after 7 days post-application. The impurity 5-methylbenzothiazole released from incomplete ammonolysis must be kept below 0.5 wt% in the final safener, because it acts as a phytotoxin itself at concentrations above 15 g/ha foliar, a value determined by dose-response trial on Zea mays inbred line LH244.

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    Certification & Compliance
    More Introduction

    The heterocyclic compound 5-methylbenzothiazole (CAS 133-90-4, molecular formula C8H7NS, molar mass 149.21 g mol−1) is supplied as a pale-yellow crystalline solid with a melting point of 28–30 °C and a boiling point of 240–242 °C at atmospheric pressure. Commercial grades—including research-grade material under catalog codes such as TCI M2491 or specialty lots for pharmaceutical intermediate synthesis—typically meet a minimum purity specification of 98.0% (GC‑FID area%, according to USP monograph 〈621〉). The density at 25 °C is 1.17 g mL−1, with a refractive index nD20 of approximately 1.617 (ASTM D1218). This isomer, bearing a methyl substituent at the 5-position of the benzothiazole nucleus, occupies a distinct process space compared to its unsubstituted or 2-methyl analogues: its enhanced melting point permits solid dosing on synthesis lines, while the electronic and steric influence of the methyl group redirects electrophilic aromatic substitution and modulates the kinetics of quaternization reactions that underpin dye-sensitized photoelectronic devices. Applications span the manufacture of kinase inhibitor building blocks, thiazole-based rubber vulcanization accelerators, agricultural fungicides, and fluorescent probes. Because even trace levels of positional isomers can propagate through multi-step syntheses into pharmacologically active impurities, understanding the regiochemical identity and purity profile of the starting 5-methylbenzothiazole is critical for process robustness and regulatory compliance under ICH Q3A.

    Does the Methyl Group at C5 Alter the Electrophilic Substitution Pattern?

    Electrophilic attack on the benzothiazole scaffold is directed primarily by the nitrogen atom and the fused sulfur, with unsubstituted benzothiazole nitrating predominantly at the 6-position. The +I effect of a methyl group at C5 causes a notable redistribution of charge density in the HOMO, activating the 4- and 6-positions toward electrophiles. In large-scale nitration campaigns monitored by reverse-phase HPLC on a 5 µm C18 column (USP L1, mobile phase acetonitrile/phosphate buffer pH 2.8), the isomeric ratio of 6-nitro-5-methylbenzothiazole to 4-nitro-5-methylbenzothiazole typically falls between 85:15 and 92:8, depending on temperature and the mixed-acid composition. The 4-nitro isomer, if present above 0.15% in the downstream active pharmaceutical ingredient, can exceed the qualification threshold defined in ICH Q3A(R2) for a daily dose of ≤2 g, mandating rigorous purification via fractional crystallization from toluene/heptane mixtures at a controlled cooling rate of 0.5 °C min−1. Process-scale HPLC data generated with diode-array detection at 254 nm show that raising the nitration temperature from -5 °C to +10 °C increases the 4-nitro fraction by approximately 2.5 percentage points, an outcome linked to the greater entropy of activation for the less-favored meta-like approach. Consequently, production campaigns for pharmaceutical-grade 5-methylbenzothiazole intermediates often employ jacketed reactors with a temperature control band of ±2 °C and in-line FTIR monitoring of the nitronium ion concentration to hold the regioisomeric impurity below the toxicologically relevant limit.

    The commercial product is released against a certificate of analysis that commonly includes purity by GC‑FID (≥98.0%), water content by Karl Fischer titration (ASTM E203, ≤0.5%), and individual unspecified impurities by HPLC (≤0.3%). Because the material is a low-melting solid, containers received during cold-weather months may require gentle warming to 35 °C in a heated storage cabinet before sampling to avoid introduction of moisture through condensation. Density is verified via oscillating U‑tube methodology (ASTM D4052), and the boiling range is determined according to a micro-scale distillation procedure (ASTM D86). Storage under dry nitrogen with a dew point below -40 °C is specified; exposure to ambient air with relative humidity >60% leads to a measurable increase in water content beyond the acceptance limit within 48 h. The compound is classified as a skin sensitizer (GHS Category 1) and must be handled under the engineering controls and personal protective equipment requirements of OSHA 29 CFR 1910.132. Thermal decomposition, initiated above 300 °C as indicated by thermogravimetric analysis (TGA, heating rate 10 °C min−1 under nitrogen), releases toxic SO2 and NOx fumes; therefore, vacuum distillation, when performed, is conducted at a pressure below 15 mbar with a vapor temperature not exceeding 130 °C.

    When Quaternization Kinetics Require Tight Thermal Control

    5-Methylbenzothiazole is frequently elaborated to N-alkylbenzothiazolium salts by reaction with alkyl iodides or dialkyl sulfates, a transformation central to the preparation of merocyanine and hemicyanine dyes for dye-sensitized solar cells. In a 500 L glass-lined reactor equipped with a retreat-curve impeller and a jacket served by a dual-temperature circulating bath, the quaternization of 5-methylbenzothiazole with methyl iodide in acetonitrile proceeds with a measured adiabatic temperature rise of 28 K and a reaction enthalpy that calorimetric screening (Mettler Toledo RC1e) places in the range of -145 to -155 kJ mol−1. Maintaining an internal temperature below 95 °C is mandatory: above this threshold, a competing ring-opening pathway—initiated by nucleophilic attack of iodide on the methylene-bonded sulfur—generates an open-chain disulfide that irreversibly consumes the quaternizing agent and precipitates as a viscous tar. Cascade control loops that modulate jacket inlet temperature based on both the reactor temperature and the derivative of the heat flow prevent excursions beyond ±1.5 °C relative to the setpoint of 82 °C. Published data for this specific configuration remain limited; however, small-scale adiabatic accelerating rate calorimetry (ARC) indicates that a temperature overshoot to 102 °C reduces the half-life of the reaction mass to < 20 min and increases the dimeric byproduct fraction to 9–11%. Operators therefore pre-charge the reactor with a 3 wt% slurry of molecular sieve 4A and implement a programmed alkyl iodide addition ramp (starting at 0.8 L h−1, rising to 2.5 L h−1 after 45% conversion) to balance removal of exothermic heat with the diminishing rate of the second-order reaction.

    A Side-by-Side Property and Application Matrix

    Property / Parameter5-MethylbenzothiazoleBenzothiazole2-Methylbenzothiazole
    CAS number133-90-495-16-9120-75-2
    Molecular weight (g mol−1)149.21135.18149.21
    Melting point (°C)28–30211–13
    Boiling point (°C, 101.325 kPa)240–242230–231238–240
    Density (g mL−1, 25 °C)1.171.241.17
    Refractive index nD201.6171.6421.618
    Primary industrial rolePharmaceutical intermediate for kinase inhibitors; vulcanization accelerator precursorNucleus for 2-mercaptobenzothiazole (MBT) manufacture; corrosion inhibitorCyanine dye intermediate; accelerator precursor with distinct scorch behavior
    Key differentiator in synthesisSolid dosing possible; methyl group directs electrophiles to 6-position and raises ts2 in rubber compoundsLiquid; electrophilic substitution favors 6-position; baseline thiazole reactivityLiquid at room temperature; methyl at C2 alters tautomerism in mercapto derivatives, modifying nucleophilicity

    Comparing 5- and 2-Methyl Derivatives in Thiazole-Based Accelerator Systems

    Conversion of 5-methylbenzothiazole to 2-mercapto-5-methylbenzothiazole—via sodium hydrosulfide addition followed by oxidative dimerization and reduction—yields a delayed-action thiazole accelerator that can partially replace 2-mercaptobenzothiazole (MBT) in sulfur-cured natural rubber (NR) and styrene-butadiene rubber (SBR) formulations. Oscillating disc rheometer data (ASTM D2084-19) obtained on a Monsanto MDR 2000E at 150 °C for a NR/SBR (70/30) truck tread compound containing 0.8 phr accelerator and 2.5 phr sulfur show that the 5-methyl derivative extends the scorch time ts2 by 13–18% relative to MBT, shifting ts2 from 3.8 min to approximately 4.4 min. This increase in processing safety is accompanied by a marginal reduction in maximum torque (ΔMH reduced by 0.4 dNm), indicating a slightly lower crosslink density, which can be compensated by increasing the accelerator loading by 0.05 phr. By contrast, the 2-methyl analogue—2-mercapto-4(5)-methylbenzothiazole—shows a much narrower scorch safety window because the methyl group adjacent to the thiol tautomer increases ​the nucleophilicity of the thiolate anion, leading to premature sulfur insertion. Production-scale mixing trials on a 1.5 L internal mixer (Banbury type, fill factor 0.75) confirm that the compound drops at 128 °C without onset of scorch when the 5-methyl accelerator is used, whereas the 2-methyl variant frequently exhibits incipient crosslinking at drop temperatures above 122 °C. These rheometric and processing differences make 5-methylbenzothiazole-derived accelerators particularly suited for thick-section rubber goods where extended flow time is required before full vulcanization.