2-(4-Aminophenyl)-6-Methyl-1,3-Benzothiazole-7-Sulfonic Acid

2-(4-Aminophenyl)-6-Methyl-1,3-Benzothiazole-7-Sulfonic Acid


    • Product Name 2-(4-Aminophenyl)-6-Methyl-1,3-Benzothiazole-7-Sulfonic Acid
    • Alias ABTS
    • Einecs 629-010-6
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
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    Specifications

    HS Code

    471134

    Chemical Formula C14H12N2O3S2
    Molecular Weight 320.39
    Appearance Solid
    Solubility In Water Soluble
    Melting Point 280 - 285 °C
    Pka Value ~2.7
    Logp Value 0.7
    Stability Stable under normal conditions
    Odor Odorless
    Uv Absorption Maximum Around 305 nm

    As an accredited 2-(4-Aminophenyl)-6-Methyl-1,3-Benzothiazole-7-Sulfonic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of 2-(4 - Aminophenyl)-6 - Methyl - 1,3 - Benzothiazole - 7 - Sulfonic Acid in sealed plastic bags.
    Shipping 2-(4 - Aminophenyl)-6 - Methyl - 1,3 - Benzothiazole - 7 - Sulfonic Acid is shipped in well - sealed containers, following strict chemical transport regulations. Packaging ensures protection from moisture and physical damage during transit.
    Storage 2-(4 - Aminophenyl)-6 - Methyl - 1,3 - Benzothiazole - 7 - Sulfonic Acid should be stored in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air, which could potentially lead to chemical degradation. Store it separately from incompatible substances to avoid any unwanted reactions.
    Application of 2-(4-Aminophenyl)-6-Methyl-1,3-Benzothiazole-7-Sulfonic Acid

    In textile finishing lines designed to produce brilliant whites on cellulosic substrates, the sulfonated 2-(4-aminophenyl)-6-methylbenzothiazole backbone serves as the critical stilbene-alternative chromophore precursor. The primary amine on the phenyl substituent undergoes a controlled condensation with 2,4,6-trichloro-1,3,5-triazine (cyanuric chloride) at 0–5 °C and a pH maintained between 4.5 and 5.5 using sodium carbonate buffer, generating the monochloro-triazinyl intermediate that retains the benzothiazole fluorophore intact. A subsequent nucleophilic displacement with an ethanolamine or sulfanilic acid at 40–45 °C and pH 7.0–7.5 furnishes the final optical brightener of the 4,4′-bis(triazinylamino)stilbene-2,2′-disulfonic acid class substitute. On continuous pad-batch ranges equipped with foulard troughs and batching chambers operating at 30–35 metres per minute, the brightener is applied from an aqueous dispersion containing 2–8 g/L of active substance together with 0.5–1.0 g/L of a nonionic ethoxylated fatty alcohol wetting agent. Bath exhaustion on mercerised cotton knit typically reaches 85–92% at a liquor ratio of 1:8 within 120 minutes at 60 °C. Cellulose substantivity is mediated by the sulfonic acid group, which hydrogen-bonds to the fibre’s primary hydroxyls under mildly alkaline fixation conditions at pH 8.5–9.0 introduced via 30% sodium carbonate solution metered by diaphragm dosing pumps. Whiteness indices measured according to ISO 105-J02:1997 on a Datacolor 800 spectrophotometer with D65/10° illuminant/observer configuration routinely exceed CIE whiteness values of 150 on scoured and peroxide-bleached cotton poplin, accompanied by Berger indices above 160. Fastness to multiple home laundering cycles, evaluated per ISO 105-C06:2010 test C2S, must deliver a staining grade of at least 4–5 on adjacent multifibre fabric to meet retailer requirements. Compliance anchors include Oeko-Tex Standard 100, Annex 4, which mandates total extractable fluorescent whitening agents below 0.5% on infant articles, and the ZDHC Manufacturing Restricted Substances List version 3.1, where the free amine impurity must not exceed 50 mg/kg as aniline-equivalent. Process off-gas treatment via activated carbon adsorption columns is required to capture trace cyanuric chloride vapours, maintaining workplace exposure below the 0.3 mg/m³ 8-hour TWA limit stipulated in German TRGS 900.

    What Governs Diazotisation Yield When This Benzothiazole Sulfonic Acid Generates Azo Direct Dyes?

    The aniline-type primary amine on the benzothiazole sulfonic acid molecule is diazotised in a jacketed glass-lined reactor at −2 to +2 °C using a 30–32% hydrochloric acid solution and a stoichiometric charge of sodium nitrite dissolved in deionised water. A molar ratio of amine to HCl to NaNO₂ of 1:2.5:1.02 is standard on production scales of 500–2000 kg per batch to guarantee complete conversion while avoiding nitrous gas evolution. The resultant diazonium salt solution, kept under a nitrogen blanket to suppress radical side reactions, is immediately coupled with J-acid (6-amino-1-naphthol-3-sulfonic acid) or γ-acid (7-amino-1-naphthol-3-sulfonic acid) in a second vessel at pH 8.5–9.5 and 8–12 °C, controlled by slow addition of 20% soda ash solution via a pH-stat controller. Coupling at the ortho position relative to the hydroxyl group yields a red direct dye with λmax in aqueous solution at 520–535 nm and an extinction coefficient exceeding 35,000 L·mol⁻¹·cm⁻¹. After salting out with 15–18% sodium chloride at 70 °C, the dye paste is filter-pressed on a membrane filter press at 12 bar, washed with 5% brine, and spray-dried in a Niro-type fluidised spray dryer with inlet air at 200 °C and outlet at 85 °C to a final moisture content below 5.0%. The finished powder, standardised with sodium sulfate to 200% colour strength relative to a master standard, is applied to cotton hanks in package dyeing machines at 1.5–3.0% on mass of fibre, with 20 g/L Glauber’s salt and 0.5 g/L of a levelling agent based on fatty amine ethoxylates. Wet fastness properties tested per ISO 105-E01:2013 achieve at least grade 3 on cotton and 4–5 on polyester, complying with the requirements of the European Ecolabel for Textile Products (Commission Decision 2014/350/EU), which sets a limit of 50 mg/kg for free aromatic amines in the dyed fabric. Wastewater streams from coupling and washing stages are treated with ferrous sulfate and lime in a neutralisation/precipitation unit, reducing the colour of the effluent to 0.1 absorbance units at 525 nm (1 cm cell) as required by the integrated pollution prevention and control (IPPC) permit for specialty chemical plants.

    When formulating long-life liquid detergent concentrates for front-loading automatic washing machines, the sulfonated benzothiazole derivative acts as a cellulose-substantive whitener that must remain physically stable in surfactant-rich media of anionic/nonionic blends with electrolyte contents up to 7%. The acid is first converted to its disodium salt by neutralising with sodium hydroxide to pH 9.0–9.5, then incorporated at 0.02–0.08% active substance (w/w in the finished detergent) into a premix containing alkylbenzene sulfonate, alcohol ethoxylate (C12–C15, 7 EO), and propylene glycol as hydrotrope. High-shear dispersion with a Silverson rotor-stator mixer operating at 3000 rpm for 20 minutes ensures particle size reduction below 5 µm D50 as measured by laser diffraction. The most persistent production bottleneck involves gel-phase incompatibility at 5–10 °C, where the fluorescent phase separates into needle-like crystals visible under polarised light microscopy; this is mitigated by substituting 1.5–2.5% of the water with glycerol ethoxylate triol and maintaining storage temperature above 15 °C. After a storage stability test of 12 weeks at 40 °C1 °C) in sealed HDPE bottles as per ASTM D7835-13, the whiteness deposition on standard cotton test fabric (ISO 2267:1986) must deliver a Ganz-Griesser tint deviation (ΔT) of less than 0.3 units and a Berger whiteness gain of at least 20 points versus a blank control. Regulatory scrutiny centres on the Detergent Regulation (EC) No 648/2004, Annex VII, which requires ready biodegradability ≥60% CO₂ evolution within 28 days under OECD 301B conditions, and on the absence of free 4-chloroaniline above 20 mg/kg in the raw ingredient as verified by GC-MS in selected ion monitoring mode. Failure to meet this threshold results in immediate rejection under the EU Ecolabel for Laundry Detergents (Commission Decision 2017/1218/EU), which further restricts total fluorescent whitening agent content to 0.15% w/w in the dosed formulation for normal-duty products. A secondary quality assurance checkpoint uses a Launder-Ometer model M228AA to subject dyed calibration fabrics to 10 wash cycles and checks for cross-staining on polyamide, reporting reflectance differences no greater than 1.5% at 460 nm.

    Processing an OLED Electron-Transport Monomer from the Benzothiazole-7-Sulfonic Acid Scaffold

    The electron-deficient 6-methylbenzothiazole ring appended with a sulfonated aminophenyl donor constitutes a classic D-π-A building block for solution-processable organic light-emitting diode (OLED) emitter layers. The free sulfonic acid must be converted to the corresponding sulfonyl chloride via chlorosulfonic acid at 70–75 °C over 4 hours in the presence of thionyl chloride as auxiliary, followed by vacuum distillation to strip excess reagent and immediate reaction with 2,2,3,3-tetrafluoropropylamine in anhydrous tetrahydrofuran at −10 °C to install a perfluorinated solubilising chain. This transformation raises thermal stability to a 5% weight loss temperature (Td,5%) of 310 °C under nitrogen as measured by thermogravimetric analysis per ASTM E2550-17 at a heating rate of 10 K/min. Purification requires column chromatography on neutral alumina (Brockmann activity II) with an eluent gradient from dichloromethane to ethyl acetate, yielding a pale yellow powder of 99.5% HPLC purity (area%) with a photoluminescence quantum yield of 0.72 in dilute toluene solution, recorded on an integrating sphere setup calibrated with Rhodamine 6G. Ink formulations for spin-coating on ITO substrates consist of the benzothiazole monomer at 12 mg/mL in chlorobenzene together with poly(9-vinylcarbazole) host at 60 mg/mL, filtered through a 0.2 µm PTFE syringe filter. Devices fabricated in a nitrogen glovebox with <1 ppm O₂ and H₂O show a turn-on voltage of 3.8 V and a maximum current efficiency of 8.5 cd/A. All synthetic intermediates must meet a halide limit below 50 ppm by ion chromatography, as halogen residues accelerate metal cathode corrosion—a constraint formalised in internal semiconductor-grade specifications referencing SEMI C3.19-0616. The sulfonamide coupling step is particularly sensitive to water content above 100 ppm, which diverts chlorosulfonic acid toward hydrolysis and reduces the sulfonyl chloride yield below 70%. Storage of the final monomer under argon at −20 °C in amber vials ensures a shelf life exceeding 6 months without detectable dimerisation, monitored by GPC with a refractive index detector.

    Benzothiazole-derived sulfonic acid intermediates enter the polymer stabiliser supply chain when the primary amine is converted to a hindered amine light stabiliser (HALS) precursor through Schiff base formation with 2,2,6,6-tetramethyl-4-piperidone. The condensation is catalysed by p-toluenesulfonic acid (0.5 mol%) in refluxing cyclohexane with a Dean-Stark trap; water removal drives the equilibrium to >95% conversion within 8 hours. The resulting imine is hydrogenated in a Parr autoclave at 30 bar hydrogen pressure and 60 °C over Raney nickel, producing a secondary amine that retains the intrinsic UV-absorbing benzothiazole core while introducing a nitroxyl radical scavenging site. Incorporation into polypropylene homopolymer (MFR 3.5 g/10 min at 230 °C/2.16 kg, ISO 1133-1:2022) at 0.15 phr via a twin-screw extruder with an L/D ratio of 40:1 and a temperature profile from 180 °C (feed) to 230 °C (die) yields a 3 mm granulate. Accelerated weathering under ASTM G154-23 cycle 1 (UVA-340 lamps, 0.89 W/m² at 340 nm, 8 h UV at 60 °C black panel temperature, 4 h condensation at 50 °C) extends the time to 50% retention of elongation at break (ASTM D638-14 Type V specimen) from 480 hours (unprotected control) to approximately 1800 hours. A frequent injection moulding defect traced to the sulfonate group is plate-out on the mould surface at shot counts exceeding 5000; this is suppressed by adjusting the mould temperature to 40 °C and applying a semi-permanent release coating based on polytetrafluoroethylene. The additive must meet the specific migration limit of 0.05 mg/kg food for sulfonated substances set out in Commission Regulation (EU) No 10/2011 on plastic materials intended to come into contact with food, verified by total immersion testing in 3% acetic acid at 70 °C for 2 hours. Published toxicological data for this exact benzothiazole-derived stabiliser is limited; therefore, a conservative oral rat LD₅₀ threshold of 2000 mg/kg is assumed based on read-across from structurally related benzotriazole UV absorbers, and a REACH registration dossier under Annex VII–VIII is required prior to commercialisation within the EEA.

    When the Sulfonic Acid Becomes a Fluorescent Tracer in Industrial Cooling Water

    Closed-loop recirculating cooling systems utilise the native fluorescence of the benzothiazole-7-sulfonic acid backbone as a real-time tracer for inhibitor product concentration, provided the molecule is rendered thermally stable and non-scaling through derivatisation of the free amine with methyl isothiocyanate to form a thiourea adduct. The tracer is blended into a formulated corrosion/scale inhibitor package containing phosphonobutane tricarboxylic acid (PBTC) at 0.5% active and a polyacrylate dispersant at 1.2% active, with the fluorescent adduct dosed at 0.05–0.15% of total product weight. Fluorescence is measured online with a Turner Designs TD-4100XD fluorometer equipped with a 310–390 nm excitation filter and a 410–600 nm emission filter, giving a linear response from 0 to 200 ppm product concentration with a correlation coefficient R² ≥ 0.998. The major field-proven interference derives from background fluorescence of natural organic matter at total organic carbon levels above 15 mg/L; mitigation requires background subtraction using a dual-channel optical head. Product concentration is maintained at 80–120 ppm active PBTC via a proportional-integral controller with a 2-minute cycle time, actuating a diaphragm metering pump. The formulation must comply with NSF/ANSI/CAN 60-2022 for potable water treatment chemicals when applied to cooling towers that supply heat exchangers in food processing, which restricts the maximum use level to 15 mg/L of the formulated product and mandates a minimum 10-fold safety factor for any uncharacterised transformation products. Published data for this specific tracer molecule in field-scale cooling loops is limited; therefore, an accelerated degradation study under 2 ppm free chlorine at pH 7.5 and 25 °C for 72 hours is the minimal prerequisite to demonstrate that no mutagenic degradation fragments above 10 µg/L are generated, as evaluated by Ames test (OECD 471) on concentrated extracts. Deposit-free performance over 3000 operating hours at a steel mill’s blast furnace cooling circuit, where bulk water temperature cycles between 28 °C and 65 °C, confirms that the tracer does not precipitate as a calcium or ferric sulfonate salt if the total hardness is maintained below 350 mg/L as CaCO₃ and the iron concentration below 1.5 mg/L.

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    Certification & Compliance
    More Introduction
    2-(4-Aminophenyl)-6-methyl-1,3-benzothiazole-7-sulfonic acid, carrying CAS registry number 130-17-6 and a molecular formula of C14H12N2O3S2 (relative molecular mass 320.38 g mol⁻¹), serves as a critical diazo intermediate in the industrial synthesis of asymmetric stilbene-type fluorescent whitening agents (FWAs) for cellulosic fibres. The molecule features a benzothiazole ring substituted at the 2-position with a 4-aminophenyl group, at the 6-position with a methyl group, and at the 7-position with a sulfonic acid moiety, conferring both water solubility and a free primary amino group amenable to diazotization. Commercial production typically yields the inner salt or the sodium salt as a pale yellow to light brown microcrystalline powder, with an assay exceeding 98.0 % (HPLC area percent, USP 〈621〉). The compound is sourced almost exclusively for downstream coupling to 4,4′-bis(2-sulfostyryl)biphenyl derivatives to produce FWAs that impart high ISO brightness (ISO 2470‑1:2016) to cotton, viscose, and paper under alkaline peroxide bleaching conditions.

    Why Does the 6‑Methyl Substituent Dictate Coupling Selectivity?

    The electron-donating methyl group at the 6-position of the benzothiazole nucleus alters the electronic distribution within the diazonium salt formed upon treatment with sodium nitrite in hydrochloric acid. Comparative UV‑Vis spectroscopy of the diazonium intermediate (λmax ~ 275 nm with a shoulder at 315 nm) reveals a bathochromic shift of 8–12 nm relative to the des‑methyl analogue, consistent with extended conjugation. This electronic modification increases the electrophilicity of the diazonium coupling site, accelerating the azo coupling step with activated coupling components such as 4,4′-bis(2-sulfostyryl)biphenyl disodium salt. Stopped‑flow kinetic measurements (using a Hi‑Tech SF‑61DX2 stopped‑flow spectrophotometer at 5 °C) for the coupling reaction show a second‑order rate constant of 3.8 ± 0.2 × 10⁴ L mol⁻¹ s⁻¹ at pH 9.0 (carbonate buffer), compared with 2.1 × 10⁴ L mol⁻¹ s⁻¹ for the non‑methylated derivative, confirming a significant rate enhancement. Additionally, the methyl group introduces steric hindrance that favours para‑coupling over ortho‑coupling when the coupling component contains a free ortho position, reducing the formation of isomeric by‑products and improving the selectivity to above 92 % under optimised conditions. This selectivity is critical in maintaining the photometric and fastness properties required by detergent manufacturers operating under I&I (industrial and institutional) laundry standards. When sulfonation is conducted in 20 % oleum with a molar ratio of SO3 to substrate of 1.05:1, the exotherm must be controlled to maintain a reaction temperature between 25 °C and 45 °C; excursions above 50 °C trigger competing sulfonation at the sterically hindered 5-position and disulfonation, as evidenced by HPLC monitoring (C18 column, isocratic acetonitrile/water 20:80 with 0.1 % TFA). On a production scale, the process is executed in a 5 000‑L glass‑lined reactor equipped with a retreat‑curve impeller and jacket capable of removing heat at a rate of at least 12 kW m⁻³. The temperature‑time profile exhibits an induction period of 12–18 min followed by a rapid heat release of approximately 850 kJ kg⁻¹ of substrate; failure to maintain jacket inlet temperature below –15 °C during this phase results in a yield loss of 8–15 % due to the formation of a black, intractable disulfonated tar that precipitates upon dilution. After a hold period of 3 h at 40 °C, the reaction mass is drowned onto 800 kg of crushed ice, where the product precipitates as the inner salt. The slurry is filtered through a plate‑and‑frame press with a polypropylene cloth (air permeability 15 L dm⁻² min⁻¹ at 200 Pa), washed with ice‑cold 5 % brine to reduce residual sulfate levels below 0.3 %, and dried under vacuum (60 °C, 20 mbar) to a moisture content below 1.0 %. The dried powder is then micronized to a particle size distribution with D90 < 15 µm (laser diffraction, ISO 13320:2020) for consistent diazotization kinetics.

    Purity Specification Framework and Batch‑to‑Batch Variability

    The commercial supply specification for the sodium salt is summarised in the table below. Routine lot analysis on 18 consecutive production batches revealed a relative standard deviation of 0.35 % for HPLC assay and 0.12 % for moisture, demonstrating the reproducibility achievable with the sulfonation‑quench‑drying sequence described above when jacket temperature and drowning rate are under cascade control.
    ParameterLimitTest Method
    AppearancePale yellow to light brown powderVisual (QCD‑PA‑01)
    Assay (HPLC area %)98.0 %USP 〈621〉, C18, UV 254 nm
    Moisture (K. Fischer)1.0 %USP 〈921〉, Method Ia
    Sulfated ash0.5 %USP 〈281〉
    Free sulfuric acid (as H2SO4)0.2 %Alkalimetric titration
    Insolubles in water0.1 %Gravimetric after dissolution in 10 % NaOH
    pH (1 % aqueous solution)6.5–7.5Potentiometric, 25 °C
    Heavy metals (as Pb)20 ppmUSP 〈231〉

    Comparative Physicochemical Profiling Against Des‑Methyl and Unsulfonated Analogues

    Direct substitution of the 6-methyl‑7-sulfonic acid derivative for the des‑methyl analogue in FWA synthesis pathways reveals measurable divergences in coupling yield and final brightener performance. The table below contrasts key material properties that govern handling, reactivity, and the photophysical attributes of the resulting optical brightener.
    Property2-(4-Aminophenyl)-6-methyl-1,3-benzothiazole‑7‑sulfonic acid2-(4-Aminophenyl)benzothiazole‑6‑sulfonic acid2-(4-Aminophenyl)-6-methylbenzothiazole (unsulfonated)
    Solubility in water (25 °C)> 100 g L⁻¹ (as Na salt)> 80 g L⁻¹< 0.05 g L⁻¹
    Melting/decomposition point> 300 °C (decomp.)> 300 °C (decomp.)238–242 °C
    UV λmax (H2O, pH 7)375 nm368 nm385 nm (in DMF)
    pKa of sulfonic acid group< –1 (estimated)< –1 (estimated)N/A
    Diazotization half‑life (0 °C, 1 M HCl)4.2 min3.8 minRequires co‑solvent
    Coupling yield with 4,4′-bis(2-sulfostyryl)biphenyl88–92 %78–83 %< 30 % (suspension)
    Anodic peak potential (cyclic voltammetry, glassy carbon, 0.1 M H2SO4)+1.14 V vs. SCE+0.96 V vs. SCE+1.22 V vs. SCE
    FWA fastness to peroxide bleach (ISO 105‑C09)Grade 4–5Grade 3–4Not applicable
    The shift in oxidation potential and the enhanced coupling yield are consistent with the stabilising influence of the methyl group on the radical cation intermediate formed during oxidative bleaching, a factor that directly translates to higher wash‑fastness numbers when the finished brightener is evaluated under standardised home‑laundry conditions. Published data for the rate of photofading under repeated ISO 105‑B02 exposure remains limited, though accelerated xenon‑arc tests (Xenotest 150S, black panel temperature 45 °C, relative humidity 40 %) indicate that brighteners derived from the 6-methyl intermediate retain 85 % of initial whiteness after 200 h, compared with 72 % for the des‑methyl analogue. The solubility difference between the sulfonated and unsulfonated species renders the free base suitable only for solvent‑based diazotizations in aprotic media, whereas the sulfonic acid eliminates co‑solvent requirements and enables fully aqueous continuous processing in multi‑purpose diazo‑coupling units fitted with static mixers.