Benzothiazole,96%

Benzothiazole,96%


    • Product Name Benzothiazole,96%
    • Alias 2-Mercaptobenzothiazole
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    VTB
    Specifications

    HS Code

    772410

    Chemical Formula C7H5NS
    Molecular Weight 135.19 g/mol
    Appearance White to yellowish solid
    Odor Faintly aromatic
    Melting Point 32 - 33 °C
    Boiling Point 231 - 232 °C
    Solubility In Water Insoluble
    Solubility In Organic Solvents Soluble in many organic solvents like ethanol, ether
    Density 1.25 g/cm³
    Flash Point 101 °C
    Purity 96%

    As an accredited Benzothiazole,96% factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 25 - kg bag of 96% Benzothiazole, well - sealed for chemical protection.
    Shipping Benzothiazole, 96% purity, will be carefully packaged in suitable containers. Shipment will follow strict chemical - shipping regulations, via approved carriers, ensuring safe and timely delivery.
    Storage Store “Benzothiazole, 96%” in a cool, dry, well - ventilated area away from heat, ignition sources, and incompatible substances. Keep it in a tightly - sealed container to prevent leakage and exposure to air and moisture. This helps maintain its purity and stability, reducing the risk of chemical reactions and potential hazards.
    Application of Benzothiazole,96%

    What Specific Molar Ratio Governs the Formation of 4,4′-Bis(benzothiazole-2-yl)stilbene from Terephthaldehyde?

    Synthesis of the di-styrylbenzene-type optical brightener 4,4′-bis(benzothiazole-2-yl)stilbene (CAS 63579-02-0) from benzothiazole 96% proceeds via a high-temperature condensation with dimethyl terephthalate in a 1:0.48 molar stoichiometry, typically in a high-boiling aromatic solvent such as 1,2,4-trichlorobenzene at 210–215 °C under nitrogen blanket with 0.3–0.5 mol% antimony trioxide catalyst. This chemistry yields a bis-benzothiazole adduct with a λmax absorption at 370–375 nm and blue-violet fluorescence peaking at 435–440 nm, measured in dimethylformamide solution per ISO 2470-1:2016. Inclusion levels in polycarbonate, rigid PVC, and polystyrene range from 0.008–0.035 wt%, standardized by CIELAB b* value reduction to ≤ -6.0 at 0.02% loading in a 3 mm injection-molded plaque, evaluated under D65 illumination. Post-extrusion sheet intended for food-contact packaging must comply with EU Regulation 10/2011 Annex I and the specific migration limit for benzothiazole itself set at 0.05 mg/kg food simulant, while U.S. indirect additive clearance falls under FDA 21 CFR 178.3297 (colorants for polymers). The downstream manufacturing process involves a wiped-film evaporator to strip solvent to <150 ppm residual, followed by a pin mill micronization step to a particle size D₉₀ < 5 µm, which is critical for uniform dispersion in polyester masterbatch. Typical terminal articles include blow-molded PET water bottles, polyolefin nonwoven fibers for hygiene products, and extruded PMMA light-diffusing panels where ultraviolet-induced yellowing index increase must remain below 2.0 after 500 hours Xenon-arc exposure per ISO 4892-2:2013.

    The largest-volume application of benzothiazole 96% globally remains its conversion to 2-mercaptobenzothiazole (MBT, CAS 149-30-4), which serves as the primary accelerator in sulfur-vulcanized diene rubber goods. Production is conducted in a 316L stainless steel high-pressure autoclave rated for PN 100, charged with benzothiazole, carbon disulfide, and sulfur in a typical molar feed ratio of 1:1.08:1.25, alongside a tertiary amine catalyst at 0.8–1.2 wt% of the total organic charge. The vessel is brought to 230–240 °C under a sustained pressure of 55–68 bar for a hold time of 5–7 hours, after which hydrogen sulfide off-gas is scrubbed in a 15% sodium hydroxide packed column and the crude MBT slurry is purified via acidification to pH 3.0–3.5 with sulfuric acid, crystallized, and dried in a rotary vacuum dryer at < 80 °C to a residual moisture of < 0.3 wt%. Conforming to GB/T 11407-2013 and ISO 10398:1998, the resulting MBT powder exhibits an initial melting point of 180–182 °C and a methanol-insoluble matter below 0.15%. In a typical natural rubber passenger tire tread formulation (NR 100 phr, N330 carbon black 50 phr, zinc oxide 5 phr, stearic acid 2 phr, sulfur 2.5 phr), MBT is dosed at 0.8–1.5 phr to achieve a Mooney scorch time (t₅ at 121 °C) of 18–24 minutes per ASTM D1646 and a rheometer cure time (t₉₀ at 160 °C) of 4–6 minutes on an MDR 2000 instrument per ASTM D5289. End products include steel-belted radial tire treads, conveyor belt covers, and vibration-damping engine mounts, all subject to REACH Annex XVII entry 50 restrictions on residual free benzothiazole in the vulcanizate.

    Compliance Standards Matrix for Benzothiazole 96% Downstream Applications
    Application SegmentPrimary StandardRegulatory Body / NormTest Method / Clause
    Rubber Accelerator MBTGB/T 11407-2013Standardization Administration of ChinaMelting point, ash, methanol insolubles
    Optical Brightener OB-StilbeneFDA 21 CFR 178.3297U.S. Food & Drug AdministrationMigration testing in food simulants
    Metal Corrosion InhibitorASTM D3306-21ASTM International (engine coolant)ASTM D1384 (glassware corrosion), ASTM D4340 (aluminum heat-rejection)
    Fungicide Intermediate (Benthiavalicarb)FAO Specification 595/SCFood and Agriculture OrganizationCIPAC 456 (HPLC assay)
    Antifungal API IntermediatePh.Eur. monograph 2.2.46European PharmacopoeiaRelated substances by HPLC, residual solvents per ICH Q3C
    Wood Preservative (TCMTB)AWPA P5-14American Wood Protection AssociationAWPA A28-14 (HPLC retention analysis)

    A niche but pharmacologically critical downstream route involves the N-alkylation of benzothiazole to yield intermediates for topical imidazole antifungals such as eberconazole nitrate. In a 500-L glass-lined reactor under nitrogen, benzothiazole 96% is reacted with 1-(2,4-dichlorophenyl)-2-(chloromethyl)-1H-imidazole in anhydrous dimethylformamide at 50–55 °C in the presence of finely ground potassium carbonate (1.4 equivalents), with the benzothiazole-to-alkylating agent molar ratio maintained at 1:0.98 to limit dialkylation impurities detected by UPLC at 0.10% area threshold. After 18 hours, the mixture is drowned into purified water, extracted with toluene, and the organic layer washed to a conductivity < 5 µS/cm, then concentrated in a wiped-film evaporator at 60 °C/20 mbar to a non-volatile residue suitable for salt formation. The resulting intermediate must exhibit a purity of ≥ 99.5% by area normalization and contain benzothiazole at ≤ 0.05%, meeting the organic impurity criteria of European Pharmacopoeia monograph 2.2.46 for the final active pharmaceutical ingredient. This synthesis is executed within an ISO 14644-1 Class 8 cleanroom with differential pressure cascade maintaining −15 Pa in the reactor room relative to surrounding corridors, and all solvents used comply with ICH Q3C residual solvent class 2 limits. The final formulation, a 1% w/w eberconazole nitrate cream, incorporates the intermediate after nitrate salt precipitation and jet-milling to D₉₀ < 10 µm for consistent topical bioavailability.

    Metal Passivation in Glycol-Based Engine Coolants: Benzothiazole Concentration Thresholds

    Benzothiazole 96% is directly incorporated into heavy-duty engine coolant concentrates as a copper-corrosion inhibitor, typically at 0.15–0.40 wt% active substance in the ready-to-use fluid, representing a 3.0–8.0 g/L as-sold concentrate based on 33 vol% coolant-to-water dilution per SAE J1034. The inhibition mechanism relies on the chemisorption of the thiazole ring onto cuprous oxide surfaces, with electrochemical potentiodynamic polarization scans (ASTM G59) in 30 vol% ethylene glycol solution containing 200 ppm chloride showing a shift in corrosion potential (Ecorr) from −220 mV vs. SCE to +45 mV when 25 mg/L benzothiazole is present, accompanied by a decline in corrosion current density (icorr) from 8.5 µA/cm² to below 0.3 µA/cm². Compatibility with other inhibitors is mandatory: benzothiazole must be blended with sebacate or azelaic acid (0.5–1.5%), a carboxylate base, and a small amount of tolyltriazole (0.05–0.10%) to protect aluminum cylinder heads; the entire formulation passes ASTM D1384 (glassware corrosion test) when mass loss for copper coupons remains under 5 mg and for aluminum under 10 mg after 336 hours at 88 °C, aerated. During coolant manufacturing, benzothiazole is pre-dissolved in a 50% aqueous caustic potash solution to form its potassium salt, ensuring rapid dissolution in the glycol matrix and preventing filter-plugging crystal formation at storage temperatures as low as −25 °C. The final coolant concentrate is subject to ASTM D3147 foam tendency testing and ASTM D4340 hot-surface aluminum corrosion rate assessment, where the maximum allowable rate is 1.0 mg/cm²/week. Heavy trucks, off-highway earthmovers, and stationary natural-gas engines are typical end-use environments, reflecting an operational life of 6,000–8,000 service hours.

    When Benthiavalicarb-isopropyl Production Requires Benzothiazole 96% with Nitrile Byproduct Management

    Benzothiazole 96% supplies the heterocyclic core for the CAA fungicide benthiavalicarb-isopropyl (CAS 177406-68-7), specifically through an early-stage synthesis of 2-benzothiazol-2-yl-acetonitrile. The route in a cGMP pilot plant reacts benzothiazole with chloroacetonitrile in anhydrous tetrahydrofuran under sodium hydride dispersion (60% in mineral oil) at −5 to 0 °C, using a molar charge of benzothiazole to chloroacetonitrile of 1:1.05 to drive complete alkylation. The resulting nitrile is reduced via catalytic hydrogenation over Raney nickel at 40 psi H2 and 45 °C to the corresponding amine, which is subsequently acylated with isopropyl chloroformate in the presence of aqueous sodium bicarbonate at pH 7.5–8.0 to give the active substance. Formulators of benthiavalicarb-isopropyl 15% suspension concentrate (SC) register the product under FAO specification 595/SC (November 2014), and quality control involves CIPAC method 456 for HPLC assay with a permitted tolerance of ±2.5% of the declared active ingredient. The formulated SC must pass wet sieve analysis through a 75 µm sieve with less than 0.5% retained, and a pourability residue below 5% per CIPAC MT 148.1. Late blight (Phytophthora infestans) control on potatoes and downy mildew (Plasmopara viticola) on grapes represent the primary terminal use patterns, with a typical field application rate of 1.2–1.5 L/ha of the 15% SC. The bulk active ingredient manufacturing step itself is subject to China’s GB 9553-2016 effluent discharge limits for heterocyclic pesticide intermediates, specifically a total nitrogen cap of 15 mg/L after plant wastewater treatment.

    Pressure-treated utility pole and rail tie preservation formulations increasingly utilize benzothiazole-derived 2-(thiocyanomethylthio)benzothiazole (TCMTB, CAS 21564-17-0) to replace copper naphthenate in ground-contact applications where copper tolerance of soil microorganisms has become problematic. Synthesis of TCMTB from benzothiazole 96% proceeds in a jacketed glass-lined reactor by dropwise addition of 37% formalin (1.03 molar equivalents relative to benzothiazole) and sodium thiocyanate solution (1.05 equivalents) into a pre-formed chloromethylation mixture of benzothiazole, hydrochloric acid, and paraformaldehyde at 10–15 °C over 4 hours, then holding for an additional 2 hours at 25 °C to reach a product assay of 94–96% after phase separation and vacuum dehydration. The resulting amber oil is formulated as a 30% emulsifiable concentrate using a nonionic/anionic surfactant blend (HLB 12.5–13.0) and diluted to 0.8–2.5% active ingredient in the treating solution for vacuum-pressure impregnation of radiata pine or Southern yellow pine sapwood in a full-cell process at 1200 kPa for 60–90 minutes. Retention targets per AWPA P5-14 Use Category 4A require 0.40 kg/m³ TCMTB on an oxide basis, verified by HPLC quantification of benzothiazole derivative residues per AWPA A28-14. Treated timber in cooling tower fills and agricultural fence posts must release less than 15 mg/L total benzothiazole species in the standardized EN 84 leaching test to satisfy the EU Biocidal Products Regulation 528/2012 Annex VI common principles. End-product durability in accelerated soil-block testing (AWPA E10-16) shows mass loss below 5% after 16 weeks exposure to Gloeophyllum trabeum, a drastic improvement over untreated controls that typically lose over 45% of their dry mass in the same period.

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    Certification & Compliance
    More Introduction
    Benzothiazole (CAS 95-16-9), supplied as a pale yellow crystalline solid with a nominal purity of 96.0% (GC area normalization, Ph. Eur. 2.2.28), is a heterocyclic building block employed primarily in the industrial synthesis of rubber accelerators and specialty organic derivatives. A typical certificate of analysis lists an assay range of 95.5–96.5%, a melting point of 1.7–2.5 °C (capillary, Ph. Eur. 2.2.14), water content ≤0.2% (Karl Fischer, ISO 760), and a single maximum impurity not exceeding 1.2%. The material is packaged under nitrogen in 200 kg UN-rated steel drums with internal epoxy-phenolic linings and conditioned in accordance with DIN 50014—23/50‑2—to minimize moisture ingress. For laboratory-scale use, 1 kg and 5 kg aluminium-laminated pouches with resealable PTFE septa are available; upon opening, the container must be flushed with dry argon and re-closed within 30 seconds to hold headspace dew point below ‑40 °C.

    Why is strict exclusion of moisture and amines critical during storage of Benzothiazole 96%?

    Benzothiazole undergoes acid- or base-catalysed ring-opening in the presence of free water, forming o-aminothiophenol and its subsequent oxidative coupling products. Accelerated stability studies conducted in 40 °C / 75% RH chambers (IEC 60068‑2‑78) on material stored in unlined carbon steel containers show a decline in assay of 0.8% per week once the internal water content exceeds 0.35%. The ring-opened species further reacts with dissolved oxygen, generating polysulphide oligomers that raise the melt viscosity and can clog metering pumps in downstream continuous processes. Therefore, transfer of the molten product—maintained at 10–15 °C above its melting point in a jacketed vessel with a nitrogen blanket at 0.2 bar positive pressure—must employ 316L stainless-steel gear pumps with 10 µm in-line filtration. Any contact with primary or secondary amines must be avoided absolutely; even 50 ppm of diethylamine in the headspace has been observed to catalyse a discolouring Maillard-like condensation, visible as a shift in APHA colour from <50 to ≥200 within 48 h. For installations where amine contamination is a process risk—such as shared nitrogen lines previously used for amine curing agents—a dedicated activated‑carbon guard bed (Calgon Carbon WS‑480, 4 × 8 mesh) is installed upstream of the storage tank blanketing valve. Spillages are absorbed with dry vermiculite and disposed of via licensed high‑temperature incineration following local hazardous‑waste regulations. Blending Benzothiazole‑96% into a reactive extrusion masterbatch for a tyre-cord skim compound requires moisture management beyond the bulk specification. Despite a certificate-of-analysis water content of 0.18%, the hygroscopic nature of the recrystallised flakes means exposure to ambient air (55% RH, 23 °C) for more than 90 seconds during hopper charging raises surface moisture to 0.42%. On a ZSK‑40 Mc¹⁸ twin‑screw extruder (L/D 48, co‑rotating, 40 mm screw diameter) operating at 180 °C barrel temperature and 300 rpm, that incremental water hydrolyses a fraction of the benzothiazole within the first three barrel zones, generating thiophenolic by‑products that prematurely activate the sulphenamide‑accelerator system. The consequence is a measurable reduction in Mooney scorch time: when the same masterbatch is produced with benzothiazole pre‑dried under vacuum (40 °C, ≤10 mbar, 4 h) to a residual water level of 0.04%, the t5 at 125 °C (ASTM D1646, large rotor) increases from 21.2 min to 29.8 min, recovering a processing safety window of over 8 minutes. The pre‑drying step is therefore mandated for compounds where Mooney viscosity ML(1+4) must remain below 55 MU after 30 days of ambient‑temperature storage.

    When the Melt Crystallises in Inadequately Traced Pipework

    The freezing point of Benzothiazole‑96% is 2.0 °C ± 0.5 K. In bulk unloading operations at ambient winter conditions in northern hemisphere sites, transfer lines must be heat‑traced with self‑limiting cables maintaining a skin temperature of 18–22 °C. A documented failure on a DN 25 AISI‑316L schedule‑10 line that lost tracing for 14 hours at a site ambient of ‑8 °C resulted in complete blockage and required line replacement after mechanical cleaning caused stress‑corrosion cracking at a weld seam. The plant’s revised SOP specifies a minimum‑flow recirculation loop with a Coriolis mass‑flow meter (Endress+Hauser Promass F 300) that detects a density shift below 1.246 g·cm⁻³ (melt at 10 °C) and triggers an alarm before solidification begins. Benzothiazole‑96% is most frequently consumed as a precursor for 2‑mercaptobenzothiazole (MBT), which is produced by thiolation with sodium polysulphide. In a 500 L Hastelloy C‑276 agitated autoclave, 120 kg of Benzothiazole‑96% is combined with 58 kg of sulphur, 84 kg of 50% sodium hydroxide, and 8 kg of water. The reactor is heated to 230 °C at 2 °C·min⁻¹, generating an autogenous pressure of 18–22 bar, and held for 6 h. The yield of isolated, purified MBT is critically dependent on the water content of the incoming benzothiazole. At feed moisture ≤0.10%, MBT yield reaches 92% (basis benzothiazole). When moisture rises to 0.50%, yield drops to 81%, and gas‑chromatographic analysis of the organic layer reveals a new peak at retention index 1685 (5‑% phenyl‑methylpolysiloxane column) corresponding to bis(2‑aminophenyl) disulphide, a secondary‑accelerator species that shortens the scorch time of the final CBS‑based vulcanisation system. In a typical natural rubber / styrene‑butadiene rubber (NR/SBR 70/30) tread formulation containing 1.2 phr of the resulting CBS, the Mooney scorch at 125 °C falls from 36 min to 24 min when the MBT was prepared from benzothiazole with 0.3% moisture compared to 0.08% moisture (Table 1).
    Table 1 — Mooney scorch time (t5, min, ASTM D1646, 125 °C, large rotor) of NR/SBR 70/30 tread compound containing CBS derived from Benzothiazole‑96% at varying feed moisture levels.
    Benzothiazole feed moisture (% wt)MBT isolated yield (%)CBS scorch safety t5 (min)bis(2‑aminophenyl) disulphide in MBT (area‑%)
    0.0891.836.00.2
    0.1589.433.50.6
    0.3085.728.21.4
    0.5081.224.12.3

    Moisture Content Thresholds Versus Scorch Safety

    The data in Table 1 reveal a processing‑window cliff edge: once the benzothiazole moisture surpasses 0.20%, the scorch safety margin drops below 30 min, which is considered the minimum acceptable value for a passenger‑car tyre tread compound extruded through a 250 °C hot‑feed pin‑barrel extruder (Troester GS 90, screw diameter 90 mm, L/D 12). The rise in the disulphide by‑product acts as a pre‑vulcanisation inhibitor decomposer, accelerating the onset of crosslinking in the extruder head and raising the pressure before the screen pack by 15–20 bar over a production shift of 8 h. To maintain seal integrity and avoid scorched‑particle contamination in the final tread, the incoming benzothiazole specification is clamped at ≤0.10% moisture when destined for CBS synthesis; when the received material exceeds this limit, it is re‑dried in a conical vacuum dryer (Italvacuum Sigma 2 m³, jacket temperature 35 °C, 5 mbar) until the Karl‑Fischer value falls below the threshold, usually within 6 h. When Benzothiazole‑96% is used directly without conversion to MBT—for instance, as a precursor to benzothiazole‑2‑sulphenamide via an oxidative coupling with cyclohexylamine—the impurity profile of the 96% grade becomes performance‑defining in a different way. The major single impurity is typically 2‑methylbenzothiazole, present at 0.8–1.2%. During sulphenamide formation, 2‑methylbenzothiazole remains largely inert, but its presence dilutes the stoichiometric ratio and can lead to an excess of free amine in the finished accelerator, which is a known nitrosamine‑precursor risk under REACH Annex XVII entry 43. Consequently, for sulphenamide products intended for markets requiring nitrosamine levels below the 0.1 µg·L⁻¹ airborne limit (TRGS 552, Germany), a Benzothiazole‑99% grade with 2‑methylbenzothiazole ≤0.2% is substituted (Table 2). This substitution adds approximately €2.40 per kilogram of final sulphenamide, which is an acceptable up‑charge for production batches destined for food‑contact rubber goods regulated under EU 1935/2004 and its associated migration testing per EN 12868.
    Table 2 — Specification comparison of Benzothiazole 96% and 99% grades and their primary application domains.
    ParameterBenzothiazole 96%Benzothiazole 99%
    Assay (GC, Ph. Eur. 2.2.28)95.5–96.5%99.0–100.0%
    Water (ISO 760)≤0.2%≤0.1%
    2‑Methylbenzothiazole≤1.5%≤0.2%
    Heavy metals (as Pb, ICP‑OES)≤5 ppm≤2 ppm
    Primary useMBT, MBTS rubber acceleratorsPharmaceutical intermediates (riluzole), low‑nitrosamine sulphenamides
    Packaging200 kg steel drums25 kg HDPE pails with aluminium‑barrier inserts
    Storage conditionAmbient, N₂ blanket2–8 °C, N₂ blanket
    In polysulphide‑cured liquid polysulphide sealants (Thiokol‑type, cured with manganese dioxide), Benzothiazole‑96% has been investigated as a cure‑rate modifier to extend the application‑pot life from 45 min to greater than 90 min when added at 0.3 phr. A study conducted on a Chem‑Rex 940 two‑part system under controlled conditions of 25 °C and 50% RH found that incorporation of Benzothiazole‑96% pre‑dissolved in dibutyl phthalate at a 10% concentration delayed the onset of the Shore‑A hardness rise by 38 min compared with the unmodified control, as measured by a durometer following ISO 7619‑1. Published data for this specific configuration is limited, and the effect is highly dependent on the residual water content of the additive; reproducibility across different sealant batches requires that the benzothiazole‑DOP pre‑mix be dried over activated 3 Å molecular sieves for 24 h before use. The thermal stability of Benzothiazole‑96% under high‑temperature downstream processing is another differentiator. When a rubber masterbatch passes through a straining extruder (Berstorff GE 150 KS, 150 mm screw diameter, L/D 8) at a melt temperature of 140 °C, the conversion of residual benzothiazole (present in commercial MBT at 0.5–1.0%) to volatile 2‑mercaptobenzothiazole is negligible; headspace GC‑MS quantification shows <5 µg·m⁻³ in the extraction hood. In contrast, benzothiazole‑2‑sulphonamide residues of similar concentration can generate aniline‑type fragments above 120 °C, introducing an occupational exposure concern during downstream calendering. The choice of Benzothiazole‑96% as the starting material, rather than a pre‑formed sulphenamide, thus keeps the precursor impurity in a less‑hazardous molecular form until the point of vulcanisation, simplifying the workplace air‑monitoring protocol defined under EN 689.