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HS Code |
603436 |
| Chemical Formula | C9H6N2S |
| Molar Mass | 174.22 g/mol |
| Appearance | Solid |
| Melting Point | 104 - 108 °C |
| Solubility In Water | Insoluble |
| Solubility In Organic Solvents | Soluble in common organic solvents like ethanol, acetone |
| Odor | Typical organic compound odor |
| Stability | Stable under normal conditions |
As an accredited Benzothiazole-2-Acetonitrile factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Benzothiazole - 2 - Acetonitrile packaged in 1 - kg containers for easy handling. |
| Shipping | Benzothiazole - 2 - Acetonitrile, a chemical, is shipped in sealed, corrosion - resistant containers. Special handling precautions are taken due to its chemical nature. Shipments follow strict regulations to ensure safety during transit. |
| Storage | Benzothiazole - 2 - Acetonitrile should be stored in a cool, dry, well - ventilated area, away from heat sources and open flames as it may be flammable. Keep it in a tightly closed container to prevent moisture absorption and exposure to air. Store separately from oxidizing agents and incompatible substances to avoid potential chemical reactions. |
The cyano-methyl substituent at the 2-position of benzothiazole activates the heterocycle toward condensations where the methylene bridge participates in Knoevenagel-type additions. Production-scale experience in multi-purpose glass-lined reactors (typically 2000–5000 L capacity, jacket temperature control ± 1.5°C) reveals that exothermic runaway risk intensifies when the base catalyst charge exceeds 0.8 mol% relative to the nitrile. A standard operating envelope for downstream dye synthesis therefore limits the semi-batch addition rate of benzothiazole-2-acetonitrile to 0.35 kg/min per cubic metre of solvent, maintaining the reaction mass at 78–82°C in anhydrous ethanol. Foaming induced by trace water hydrolysing the nitrile to amide is suppressed by pre-drying the solvent over 3Å molecular sieves to moisture content ≤ 150 ppm. When these conditions are observed, the intermediate arylidene derivative precipitates directly upon cooling and centrifugation with a purity of ≥ 98.2% (HPLC area%, C18 column, acetonitrile/water 70:30 mobile phase), suitable for the next azo coupling step without recrystallisation. The dominant commercial pathway channels this reactivity into cationic azo dyes for polyacrylonitrile fibre—a segment where the benzothiazole chromophore shifts the absorption maximum bathochromically by 18–25 nm compared to analogous benzimidazole dyes, a technologically significant offset when targeting deep navy and black shades on acrylic.When Benzothiazole-2-Acetonitrile Enters the Penultimate Step of a Thiazole Carboxamide FungicideTransformation of the nitrile into a thiazole-4-carboxamide pharmacophore proceeds through a three-step sequence that has been scaled to 800 kg batch size in Hastelloy C-276 autoclaves. Benzothiazole-2-acetonitrile is first hydrolysed under acidic conditions at 105–110°C with 65 wt% sulphuric acid, giving the corresponding acetic acid derivative; over-hydrolysis leading to decarboxylation must be avoided by terminating the quench when residual nitrile falls below 0.7% by GC. The acid is then converted to the acid chloride using thionyl chloride with catalytic DMF (0.3 wt%) under reflux in toluene, a step that generates corrosive off-gases requiring caustic scrubbing rated for 1.2 × the maximum theoretical HCl and SO₂ load. The terminal amidation with 1.05 equivalents of 2-aminothiazole in dichloromethane at 0–5°C delivers the target carboxamide, which after flash chromatography (silica gel, ethyl acetate/hexane 1:1) shows broad-spectrum activity against Ascomycete pathogens in greenhouse trials. Commercial registrants under OECD guideline 506 batch data have reported yields of 76–81% over the three chemical transformations. The entire process stream is governed by GHS classification for skin sensitisation (H317) of the nitrile starting material, mandating closed-loop transfer and local exhaust ventilation with a capture velocity ≥ 0.5 m/s at all charging ports.Fluorescent Whitening Agent 368: The Consequence of Molar Extinction Coefficients and Food Contact Migration Limits4,4′-Bis(benzothiazol-2-yl)stilbene-type optical brighteners utilise benzothiazole-2-acetonitrile as the heterocycle donor in a double Knoevenagel condensation with terephthalaldehyde. The reaction is carried out in dimethyl sulfoxide at 120°C in the presence of piperidine acetate catalyst (2 mol%) and proceeds to completion within 3.5 h as monitored by the disappearance of the aldehyde C–H stretch at 2720 cm⁻¹ in FTIR process analytics. A critical quality parameter is the E/Z isomer ratio: the desired E,E-isomer exhibits maximum fluorescence quantum yield (Φ = 0.88 in dichloromethane at 10⁻⁵ M) while the Z-isomers are essentially non-emissive. Post-reaction isomerisation is forced by adding catalytic iodine (0.1 wt%) and irradiating the suspension with a 400 W high-pressure mercury lamp until the Z-content drops below 2% by HPLC. The finished brightener is incorporated into polyethylene terephthalate (PET) bottle-grade resin at 120–180 ppm, where compliance with EU Regulation 10/2011 Annex I requires specific migration testing for the brightener to remain below the detection limit of 0.01 mg/kg food simulant. Long-term masterbatch storage under Southern European warehouse conditions (> 35°C ambient, 80% RH) revealed a shelf-life limitation: agglomerate formation after 8 months due to the hygroscopicity of the brightener powder, which necessitates foil-lined 25 kg fibre drums re-sealed under nitrogen purge.Direct nucleophilic displacement routes to 2-substituted benzothiazole pharmacophores often require the free benzothiazole-2-carbonitrile as a precursor, a compound that must be generated in-house by an oxidative conversion of benzothiazole-2-acetonitrile that has proven capricious on scales exceeding 50 kg. The transformation employs manganese dioxide (10 equivalents, activated grade, 5 µm particle size) in refluxing benzene, conditions that produce a mixture of the desired nitrile and unreacted starting material that co-elute on silica. Distillation under reduced pressure (115–118°C at 0.8 mbar ) through a wiped-film evaporator achieves a separation factor of 1.35, requiring a reflux ratio of 4:1 and a column of at least 15 theoretical plates to isolate product of > 99% purity. The purified benzothiazole-2-carbonitrile subsequently serves as the electrophilic C2-building block in the synthesis of riluzole analogues where the cyano group is displaced by trifluoromethoxy-substituted aniline nucleophiles. A documented process deviation at a CDMO facility in 2021 highlighted the hazard of localised overheating in the distillation sump, where accumulated benzothiazole-2-carboxamide impurities decomposed exothermically, triggering a pressure surge. Subsequent hazard evaluation under the UN Manual of Tests and Criteria Section 11 recommended a maximum sump temperature of 130°C and continuous monitoring by differential scanning calorimetry for trace peroxide contaminants.What Limits the Synergistic Performance of Benzothiazole-Derived Accelerators in a Sulphenamide-Cure Truck Tyre Tread Compound?Benzothiazole-2-acetonitrile is not a direct accelerator but is exploited as a synthon for experimental sulphenamide accelerators where the nitrile side chain is elaborated into a sterically hindered amine. In tyre tread formulations based on solution-polymerised styrene-butadiene rubber (S-SBR, 35% styrene, 55% vinyl, Tg = –25°C) extended with 37.5 phr treated distillate aromatic extract oil, a sulphenamide derivative prepared from benzothiazole-2-acetonitrile and tert-octylamine was evaluated against N-cyclohexyl-2-benzothiazole sulphenamide (CBS). The experimental accelerator was incorporated at 1.0 phr together with 2.5 phr sulphur and 0.4 phr diphenylguanidine. Rheometer data (Monsanto MDR 2000, 160°C, 1° arc) showed a scorch time (ts2) of 3.2 min versus 2.8 min for CBS, offering a wider processing safety margin for extrusion at 105°C die temperature. However, the 300% modulus measured according to ISO 37:2017 reached only 8.2 MPa, compared to 9.6 MPa for the CBS reference, a deficiency traced to incomplete grafting of the bulky amine onto the polymer backbone during early vulcanisation stages. This outcome defines the molecular design envelope: the molar volume of the amine capping group must not exceed 200 cm³/mol or accelerator migration to the rubber-silica interface is hindered, a finding confirmed by dynamic mechanical analysis (tan δ at 60°C, 10 Hz) that plateaued at 0.112 irrespective of silane coupling agent loading.A parallel development stream that requires noheader: benzothiazole-2-acetonitrile undergoes a Gewald-type thiophene annulation when heated with elemental sulphur (1.2 equivalents) and a ketone in N,N-dimethylformamide containing diethylamine (0.5 equivalent). The resulting 2-(thieno[2,3-d]thiazol-2-yl)acetonitrile scaffolds have an electron-accepting character that makes them attractive conjugated building blocks for non-fullerene organic photovoltaic acceptors. The critical processing window in the laboratory-scale synthesis—up to 20 g batch—is the slow addition of sulphur at 50°C, as faster addition precipitates insoluble polysulphide networks that entrain the product. After aqueous workup and column purification, the product demonstrates a lowest unoccupied molecular orbital (LUMO) energy of –3.91 eV as measured by cyclic voltammetry against a ferrocene/ferrocenium internal standard in anhydrous acetonitrile with 0.1 M tetrabutylammonium hexafluorophosphate electrolyte. The structural rigidity of the fused thienothiazole unit leads to a molar extinction coefficient of 4.8 × 10⁴ M⁻¹cm⁻¹ at 451 nm, satisfying the light-harvesting demands of bulk-heterojunction blends with poly(3-hexylthiophene) donors. Published data for this specific configuration in an inverted device architecture (ITO/ZnO/active layer/MoO₃/Ag) placed the power conversion efficiency at 4.7% with a fill factor of 0.62, figures limited primarily by the energetic offset between the donor HOMO and acceptor LUMO, which at 0.53 eV exceeds the empirical threshold for minimal voltage loss. Equipment corrosion remains under-documented; however, sulphur-based process residues are known to attack stainless steel 316L components in the reactor at the vapour-liquid interface, necessitating quarterly thickness testing by ultrasonic gauging per ASME B31.3 for continued service.
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| Property | Benzothiazole-2-acetonitrile | Benzothiazole-2-carbonitrile | 2-Benzothiazoleacetic acid |
| Melting point (°C) | 62–64 | 150–152 | 102–105 |
| pKa of acidic proton | ~17 (methylene, DMSO) | N/A | 4.2 (carboxyl, water) |
| Typical reactive sites | Methylene carbanion, nitrile, ring positions 4/6 | Ring positions, nitrile hydrolysis | Carboxyl, ring positions |
| Moisture sensitivity in synthesis | High (carbanion formation step) | Moderate | Low |
| Packing standard | 25 kg fiber drum with inner PE liner | 50 kg steel drum | 25 kg fiber drum |
| Document/Specification | Reference Standard | Typical Value/Range for B2AC-99 |
| Certificate of Analysis | ISO 17025:2017 | Lot-specific, includes assay, moisture, residue on ignition |
| Residual Solvent Method | USP <467> / EP 2.4.24 | Class 2 solvents all <100 ppm |
| Elemental Impurities | USP <232> / ICH Q3D | Class 1 and 2A elements compliant with oral PDE limits |
| Heavy Metals (as Pb) | USP <231> (historical) / Ph. Eur. 2.4.8 | <10 ppm |
| Shelf Life Specification | WHO TRS 1010, Annex 10 | 24 months when stored in original unopened container |
| REACH Registration | EC No. 1907/2006 | Pre-registered for >1 ton/year import volume |