2-Amino-6-Nitrobenzothiazole

2-Amino-6-Nitrobenzothiazole


    • Product Name 2-Amino-6-Nitrobenzothiazole
    • Alias 2-amino-6-nitro-1,3-benzothiazole
    • Einecs 221-540-7
    • 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

    890463

    Chemical Formula C7H5N3O2S
    Molar Mass 195.199 g/mol
    Appearance Yellow solid
    Melting Point 175 - 177 °C
    Solubility In Water Insoluble
    Solubility In Organic Solvents Soluble in some organic solvents like ethanol, chloroform
    Odor Odorless or very faint odor
    Stability Stable under normal conditions but may react with strong oxidizing agents

    As an accredited 2-Amino-6-Nitrobenzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2 - Amino - 6 - Nitrobenzothiazole packaged in a sealed plastic bag.
    Shipping 2 - Amino - 6 - Nitrobenzothiazole is shipped in sealed, corrosion - resistant containers. Adequate cushioning is used to prevent damage. Shipments follow strict hazardous material regulations, ensuring safe transportation.
    Storage 2 - Amino - 6 - Nitrobenzothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, flames, and oxidizing agents. Store in a tightly - sealed container to prevent moisture absorption and potential reactions. Avoid storing near incompatible substances to ensure safety and maintain its chemical integrity.
    Application of 2-Amino-6-Nitrobenzothiazole
    When 2-amino-6-nitrobenzothiazole is introduced into a diazotization coupling sequence for disperse blue azo dyes, reaction control pivots on maintaining the exotherm below 5°C via jacketed glass-lined vessels with brine circulation capable of extracting −10°C thermal load. The compound functions as a heterocyclic diazo component, where the electron-withdrawing nitro group at position 6 intensifies the electrophilicity of the diazonium intermediate, accelerating coupling with N,N-disubstituted aniline derivatives. A typical milled formulation for C.I. Disperse Blue 79:1 incorporates 2.8–4.2 wt% of the downstream dye derived from this intermediate, dispersed with lignosulfonate or naphthalene sulfonate formaldehyde condensate dispersants at a pigment-to-dispersant ratio of 1:1.2 to 1:1.8. Post-synthesis, the crude dye cake undergoes wet milling in horizontal bead mills packed with 0.4–0.6 mm yttria-stabilized zirconia beads at 1,200–1,500 rpm impeller tip speeds until particle size distribution reaches D901.0 µm measured by laser diffraction (ISO 13320:2020). Spray drying at inlet temperature 190–210°C and outlet 85–95°C converts the aqueous dispersion into non-dusting granular powder. Exhaust dyeing of polyester staple fiber on high-temperature beam or jet machines proceeds at 130°C with a liquor ratio of 1:8 to 1:15, followed by reduction clearing with sodium dithionite and caustic soda at 80°C for 20 minutes to remove surface loosely bound colorant. The competitive advantage of the 6-nitro-substituted benzothiazole chromophore over aminoanthraquinone analogues lies in its 30–40% higher molar extinction coefficient, translating to deeper shades at reduced dyestuff loadings, with lightfastness ratings meeting ISO 105-B02:2014 minimum grade 6 on polyester and sublimation fastness under ISO 105-P01:1993 achieving grade 4–5 at 180°C. Compliance with the ZDHC Manufacturing Restricted Substances List v3.1 and OEKO-TEX Standard 100 Annex 4 requires confirmation that residual arylamine levels from reductive cleavage remain below the 20 mg/kg detection threshold via GC-MS analysis per EN 14362-1:2017.

    What governs coupling pH profiling when this intermediate reacts with pyridone-based coupling components?

    Disperse yellow to greenish-yellow azo dyes synthesized from 2-amino-6-nitrobenzothiazole and 2,6-dihydroxypyridine or N-methylpyridone derivatives exhibit pronounced sensitivity to coupling medium pH, with optimal yield and hue purity constrained within a narrow window of pH 4.0–5.5 buffered by sodium acetate-acetic acid systems. Deviation below pH 3.8 protonates the pyridone ring oxygen, retarding nucleophilic attack at the coupling position, while excursion above pH 6.2 promotes hydrolysis of the diazonium salt to the corresponding hydroxybenzothiazole, a non-chromophoric byproduct detectable as a 2–5% impurity peak at Rf 0.12 on silica TLC developed with toluene-ethyl acetate 3:1. Industrial coupling protocols deploy inline pH probes with automated acetic acid dosing pumps in 5,000–10,000 L stainless steel coupling vessels, where the diazonium liquor is fed under surface into a chilled coupling component suspension at a controlled addition rate of 0.8–1.2 L/min to prevent localized pH spikes. The resultant dye, structurally analogous to C.I. Disperse Yellow 56 but with a bathochromic shift of 12–18 nm attributable to the benzothiazole sulfur atom’s contribution to the π-conjugated system, requires oven milling at 60°C for 8–12 hours with dispersant premixes before final standardization. Polyester automotive upholstery fabrics dyed with this chromophore must satisfy the SAE J1885:2012 interior weathering standard, retaining at least 80% breaking strength after 225.6 kJ/m² xenon arc exposure, a specification that pre-selects for the nitrobenzothiazole scaffold over lower-photostability pyrazolone-based yellows. The addition level in the final ink formulation for transfer printing paper can reach 7.5 wt% dispersed dye content when combined with 12–15 wt% ethylene glycol and 0.05 wt% biocide, viscosity adjusted to 3.5–5.0 cP for continuous inkjet printhead compatibility at 45 kHz drop ejection frequency.
    Formation of a mercerized cotton-reactive disperse dye hybrid requires synthesizing an intermediate that couples the benzothiazole chromophore to a sulfatoethylsulfone or monochlorotriazine reactive anchor through an ethylamino bridging group. 2-Amino-6-nitrobenzothiazole diazotized and coupled to m-toluidine, followed by reduction of the nitro group to an amine and subsequent condensation with 2,4,6-trichloro-1,3,5-triazine at 0–5°C and pH 6.5–7.0, yields a hetero-bifunctional chromophore capable of covalent fixation to cellulosic hydroxyl groups under alkaline exhaust conditions. The reactive dye intermediate is isolated at ≥94% purity (HPLC area percent, detection at λmax 490–510 nm) and formulated with 25–35 wt% inert diluent (sodium sulfate or dextrin) to standardize strength to 100% relative to a master calibration standard traceable to ISO 105-A05:1996. Exhaust application on cotton knitgoods in soft-flow dyeing machines proceeds at a liquor ratio of 1:10 with 40–60 g/L sodium sulfate and 15–20 g/L sodium carbonate dosed incrementally over 45 minutes at 60°C, fixation efficiency reaching 82–88% determined by stripping unbound dye with 25% aqueous pyridine at reflux. The resultant dyeings, after soaping with a nonionic surfactant at boil for 15 minutes, exhibit wet rubbing fastness of grade 3–4 under ISO 105-X12:2016 and wash fastness of grade 4 under ISO 105-C06:2010 test C2S (60°C, with perborate), values that position this chemistry for medium-depth shades on apparel where azoic coupling methods are displaced. However, the published data for long-term hydrolytic stability of the triazine linkage in the presence of residual perborate bleaching agents at concentrations above 1.0 g/L available oxygen remain limited, warranting accelerated aging validation at 70°C and 90% relative humidity for 500 hours before qualifying specification-grade lots. Compliance with the EU Ecolabel for textile products (Commission Decision 2014/350/EU) mandates that the sum of adsorbable organically bound halogens (AOX) in the discharge from synthesis and application does not exceed 40 mg Cl/kg finished fabric, requiring that the triazine condensation step employ rigorous stoichiometric control to minimize unreacted chlorinated intermediates.

    When this benzothiazole scaffold is exploited in solution-dyed regenerated cellulose filament production

    Spun-dyeing of viscose or lyocell filaments with pigment dispersions prepared from 2-amino-6-nitrobenzothiazole-derived insoluble azo colorants introduces rheological challenges absent from textile immersion processes because the pigment particle size distribution must remain below 0.8 µm D99 to avoid spinneret hole blockage in 13,000–18,000 hole platinum-rhodium alloy spinnerets with orifice diameters of 50–70 µm. The pigment is milled in a recirculating horizontal media mill charged with 0.3 mm cerium-stabilized zirconium oxide beads until Hegman gauge readings exceed 7.5 (ASTM D1210-05:2020), then injected into the viscose dope at a concentration of 0.5–2.0 wt% relative to cellulose content immediately before the spinning pump, with static mixers of 24 elements installed downstream to ensure distributive mixing uniformity. Coagulation in a bath containing 100–120 g/L sulfuric acid, 280–320 g/L sodium sulfate, and 12–18 g/L zinc sulfate at 48–52°C proceeds with no pigment migration into the coagulation medium because the particle size exceeds the 10 nm threshold for molecular diffusion, confirmed by spectrophotometric analysis of spent bath liquor showing absorbance below 0.005 AU at λmax. The resulting colored filament, after washing, desulfurization with sodium sulfide, bleaching, and finishing, delivers lightfastness superior to vat-dyed equivalents, with ISO 105-B02:2014 ratings of grade 7 at 1.0% pigment loading. The operational boundary for pigment addition rate is defined by a viscosity ceiling: dope containing more than 2.5 wt% pigment exhibits a 15–25% increase in falling-ball viscosity at 20°C, which destabilizes the spin bath stretch ratio due to elevated die swell and filament tension variability exceeding ±0.12 cN/dtex on the first godet roller.
    Incorporation of 2-amino-6-nitrobenzothiazole-based azo pigments into polyolefin masterbatch for thin-gauge film fiber extrusion leverages the thermal stability of the benzothiazole moiety, which withstands processing temperatures up to 280°C without significant chromophore degradation as verified by thermogravimetric analysis showing <5% weight loss at 300°C under nitrogen (ASTM E1131-08:2020). The pigment presscake is flushed with low-density polyethylene wax at 120–140°C in a sigma-blade kneader to displace water and encapsulate primary particles within the hydrophobic carrier resin, achieving a pigment loading of 40–50 wt% in the intermediate flushed chip. Let-down ratio into polypropylene homopolymer at 25:1 to 50:1 on a co-rotating twin-screw extruder with L/D ≥ 40 and screw speed 400–600 rpm produces a final masterbatch containing 1.5–2.0 wt% active pigment, which is metered into a spunbond nonwoven line at 2–4 wt% addition rate to yield filaments with a titer of 1.5–2.2 dtex. The technical challenge during high-speed unwinding of the pigmented filament arises from migration of low-molecular-weight processing aids co-formulated in the masterbatch to the filament surface, forming a skin layer of thickness 50–200 nm detectable by time-of-flight secondary ion mass spectrometry that alters the filament’s coefficient of friction and can generate oligomer deposition on draw rolls operating at 3,500–5,000 m/min. Migration kinetics follow a Fickian diffusion model with an apparent diffusion coefficient of 8×10⁻¹³ m²/s at 25°C, accelerating to 3×10⁻¹¹ m²/s at 70°C, mandating that post-extrusion heat-setting ovens not exceed 120°C for accumulative residence beyond 6 seconds. The colorfastness of the spunbond fabric to rubbing under ISO 105-X12:2016 achieves dry grade 4–5 and wet grade 4, while resistance to hypochlorite bleaching per ISO 105-N01:1993 is limited to grade 2–3 due to oxidative attack at the benzothiazole sulfur atom, an inherent limitation requiring explicit disclosure on technical data sheets distributed to converters servicing hygiene and medical disposables markets where chlorine-based sanitization protocols are prevalent.

    Solvent-soluble dye preparation for engineering thermoplastic coloration

    When 2-amino-6-nitrobenzothiazole undergoes diazotization and coupling with N-ethyl-N-cyanoethylaniline, the resulting monoazo dye exhibits solubility in polar aprotic solvents including dimethylformamide, dimethylacetamide, and N-methylpyrrolidone at 15–25 g/L at 25°C, enabling direct dissolution into polyacrylonitrile spinning dope for wet-spun acrylic fiber coloration without particulate dispersion steps. The dye solution is filtered through 5 µm absolute rated polypropylene depth cartridges and metered into the dimethylacetamide-cellulose acetate dope stream at a rate calculated to deliver 0.3–0.8 wt% dye-on-polymer, with static in-line mixing followed by deaeration under vacuum (−0.95 bar gauge) to eliminate air bubbles that nucleate filament voids during solvent-non-solvent coagulation. Coagulation in a 60:40 DMAc-water bath at 30°C yields a gel filament that is subsequently drawn 5–8× in a hot water cascade at 95–98°C, dried on perforated drum dryers, and relaxed in steam at 130°C to develop final tensile properties satisfying ISO 2076:2021 specifications for acrylic staple. The dye displays a partition coefficient between the solvent-rich coagulation bath and the polymer phase that determines dye retention in the filament; at equilibrium, 88–92% of the dosed dye remains within the polymer matrix, measured spectrophotometrically in dimethylformamide extracts of the dried tow against calibration curves constructed at the absorbance maximum of 530–540 nm. Avoidance of exposure to reducing agents during any stage of dope preparation, spinning, and downstream fiber processing is mandatory because the nitro group is susceptible to reduction to an amino group under the action of residual sulfites or thiosulfates carried over from acrylonitrile monomer production, forming a less intensely colored amino derivative with an 80–90 nm hypsochromic shift and compromised lightfastness. Testing per ISO 105-B02:2014 on knitted panels from fully drawn tow yields grade 6–7 at 1/1 standard depth, a value that degrades to grade 4 when the reduced amino analog comprises more than 8% of the total dye content, a threshold detectable via HPLC with diode-array detection at the ratio of absorbance at 440 nm and 535 nm.
    2-Amino-6-nitrobenzothiazole serves as an accelerator precursor in sulfur vulcanization systems by reacting with mercaptobenzothiazole disulfide (MBTS) during the induction period to generate in situ 2-mercapto-6-nitrobenzothiazole, a species exhibiting 15–20% faster scorch delay reduction than unsubstituted 2-mercaptobenzothiazole in natural rubber compounds loaded with 45 phr N330 carbon black. The accelerator is pre-dispersed in ethylene propylene diene monomer binder at 80°C on a two-roll mill with a friction ratio of 1:1.2 and formed into 3–5 mm pellets containing 70 wt% active substance, suitable for automatic weighing and feeding systems on intermix internal mixers. The addition level of the accelerator powder, calculated on 100 parts rubber hydrocarbon, ranges from 0.8 to 1.5 phr for truck tire tread compounds where the balance between processing safety and rapid cure at 150–160°C press temperatures determines cycle time economics; moving die rheometer cure curves (ISO 6502:2020) at 160°C and 0.5° arc amplitude demonstrate a ts2 scorch time elongation of approximately 45 seconds relative to mercaptobenzothiazole control formulations, affording wider processing latitude during extrusion of complex tread profiles with thin gauge wing sections prone to scorch from frictional heat buildup. The critical incompatibility in this application domain is co-formulation with secondary amine-based antidegradants such as N-phenyl-N′-isopropyl-p-phenylenediamine (IPPD) at loadings exceeding 2 phr, which can extract the labile proton alpha to the nitro group at process temperatures above 140°C, prematurely deprotecting the latent accelerator and triggering crosslinking within the internal mixer before the dump step, a fault diagnosed by a Mooney viscosity (ISO 289-1:2015) increase of 15–25 MU above the target plasticity retention index. Activator formulations including 3–5 phr zinc oxide and 1.5–2.5 phr stearic acid are required to solubilize the zinc-accelerator complex and promote its nucleophilic attack on elemental sulfur rings, opening S8 to generate active sulfurating species that form crosslink precursors with allylic positions on polyisoprene chains. Vulcanizate mechanical properties after optimum cure show tensile strength of 22–26 MPa (ISO 37:2017, Type 2 dumbbells) and elongation at break of 480–520%, values statistically indistinguishable from sulfenamide-accelerated controls but with a reversion resistance improvement measurable as a 6–9% lower torque loss over 30 minutes over-cure at 180°C, a property attributable to the electron-withdrawing nitro substituent stabilizing the sulfur crosslinks against thermal anaerobic decomposition.
    Vulcanization accelerator performance comparison: benzothiazole sulfenamide vs. 2-amino-6-nitrobenzothiazole derived system in NR/BR tread compound at 160°C
    Parameter (ISO 6502:2020)TBBS Control (1.2 phr)6-Nitro BT Derivative (1.0 phr)
    Minimum torque ML (dNm)2.11.9
    Maximum torque MH (dNm)15.815.2
    Scorch time ts2 (min:sec)2:353:10
    Optimum cure t90 (min:sec)4:505:05
    Reversion at t90+30 min (% MH loss)12.33.8
    Concentrated sulfuric acid dissolution of 2-amino-6-nitrobenzothiazole followed by oxidative ring closure with sodium dichromate dihydrate at 35–40°C generates a benzothiazole-fused polycyclic chromophore absorbing in the near-infrared region, a transformation exploited in the synthesis of organic photoconductor undercoat layer materials for laser printer drums. The nitrated intermediate’s electronic structure positions the lowest unoccupied molecular orbital at −3.4 eV (determined by cyclic voltammetry in acetonitrile with tetrabutylammonium hexafluorophosphate supporting electrolyte, referenced to ferrocene/ferrocenium), which aligns with the charge generation layer’s conduction band in dual-layer organic photoconductors operating at 780 nm diode laser wavelength. The material is vacuum-deposited at 1×10⁻⁵ Pa base pressure with a deposition rate of 0.3–0.5 nm/s onto anodized aluminum substrates pre-coated with a 0.5–1.0 µm solvent-cast polyamide blocking layer, forming a uniform film of 200–350 nm thickness verified by stylus profilometry. The purity specification for this electronic-grade application mandates metal ion content below 1 ppm for each of iron, copper, and nickel as determined by inductively coupled plasma mass spectrometry, because trace transition metals catalyze dark decay of the photogenerated charge, increasing residual potential above the −50 V threshold that causes print background fog. Synthesis lot qualification includes measurement of dark conductivity, which must remain below 1×10⁻¹² S/cm at an applied field of 30 V/µm (ASTM D257-14), and photosensitivity, expressed as the energy required to discharge half the initial surface potential, with acceptance criterion E1/20.8 µJ/cm² at 780 nm. REACH Annex XVII restrictions apply to the dichromate oxidation step, requiring substitution with manganese(III)-based oxidants or electrochemical ring closure at a carbon felt anode in methanesulfonic acid electrolyte to eliminate hexavalent chromium from the synthetic pathway, a modification currently at pilot-scale validation in 200 L divided electrolytic cells operating at 4.5 V and 60 A/m² current density with 68–72% isolated yield.

    When 2-amino-6-nitrobenzothiazole participates in formulating latent fingerprint detection reagents

    The nitrobenzothiazole scaffold reacts with ninhydrin under mild alkaline conditions in methanol to produce a Schiff base adduct exhibiting fluorescence emission at 580 nm when excited at 440 nm, a Stokes shift of 140 nm that facilitates imaging on porous substrates (paper, cardboard, raw wood) with minimal background autofluorescence interference from optical brighteners emitting in the 420–460 nm region. The working solution is prepared by dissolving 0.5 g of 2-amino-6-nitrobenzothiazole and 0.3 g of ninhydrin in 100 mL absolute methanol with 1.0 mL glacial acetic acid as catalyst, allowed to stand for 24 hours in darkness at 22°C to permit complete imine formation before filtration through 0.2 µm PTFE syringe filters. The reagent is applied by dipping or spraying in a fume hood exhausted at 0.5 m/s face velocity, then the specimen is heated at 80°C in a humidity-controlled oven at 65% relative humidity for 10 minutes to develop ridge detail. Fluorescence imaging under forensic light source excitation at 450 nm with a 550 nm long-pass barrier filter yields ridge contrast exceeding 120:1 signal-to-background ratio on white photocopy paper twenty-year-aged specimens, as quantified by pixel intensity histogram analysis of 12-megapixel RAW-format images captured with a monochrome CCD camera thermoelectrically cooled to −20°C. The primary operational limitation is the shelf life of the working solution, which due to the hydrolytic susceptibility of the imine bond, declines to 50% fluorescence intensity after 14 days at 4°C in amber borosilicate bottles, requiring fresh preparation biweekly and quality control by fluorescence spectrophotometry against a rhodamine B standard (quantum yield 0.65 in ethanol). The reagent is incompatible with plastic substrates containing phthalate ester plasticizers, which leach into the methanol carrier and quench fluorescence through collisional energy transfer, a mechanism confirmed by Stern-Volmer analysis yielding a quenching constant KSV of 120 M⁻¹ for dioctyl phthalate.
    Fingerprint development reagent performance on porous substrates after 10-minute development at 80°C, 65% RH
    SubstrateRidge Contrast Ratio (S/B)Emission λmax (nm)Detectable Latency Period (days)*
    White copy paper, 80 gsm128:158245
    Brown kraft envelope95:158030
    Newsprint72:158518
    Cotton check paper (currency grade)140:157860

    * Latency period defined as maximum time between fingerprint deposition and reagent application yielding contrast ratio ≥ 10:1 under standardized imaging conditions with 450 nm excitation and 550 nm long-pass barrier filter.

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    Certification & Compliance
    More Introduction
    The heterocyclic building block 2-amino-6-nitrobenzothiazole (CAS 6285-57-0), empirical formula C₇H₅N₃O₂S, molecular weight 195.20 g mol⁻¹, is supplied as a yellow to ochre crystalline powder with a characteristic faint thiazole odor. Standard industrial-grade specifications set a minimum purity of 98.5% by HPLC area normalization (UV detection at 254 nm, external standard method per USP <621>), a melting interval of 248–253 °C with decomposition (capillary tube, USP <741>), loss on drying ≤0.5% at 105 °C for 2 h, and sulfated ash ≤0.2% ( 800 °C, 1 h). Moisture-sensitive applications may additionally require water content by Karl Fischer titration ≤0.3% (USP <921>, Method Ia). The electron-withdrawing nitro substituent at the 6-position fundamentally separates this intermediate from unsubstituted 2-aminobenzothiazole (CAS 136-95-8) and from the 4-nitro isomer (CAS 6285-56-9), reordering the reactivity of the amino group, the stability of derived diazonium salts, and the thermal behaviour of downstream fine chemicals.

    What Distinguishes 2-Amino-6-Nitrobenzothiazole From Unsubstituted Benzothiazole Amines?

    The presence of the 6-nitro function depresses the pKa of the conjugate acid by roughly 1.5–2.0 units relative to the parent 2-aminobenzothiazole (measured potentiometrically in acetonitrile/water mixtures, referenced to ISO 17025 calibration). This deactivation retards diazotization with sodium nitrite in mineral acid, requiring continuous-flow processing for scalable, safe production. In a jacketed tubular reactor of 6 mm internal diameter, 1.2 m length, and residence time of 30–60 s, the diazonium salt of 2-amino-6-nitrobenzothiazole remains processable at 0–5 °C without precipitation-induced clogging; by contrast, the salt of the unsubstituted amine may begin to crystallise within 15 s under identical conditions, leading to pressure excursions exceeding 3 bar. This behaviour forces a segmented feed strategy—one pump delivering amine/HCl slurry, another nitrite solution, merging at a T-mixer with 10 ms contact time—to keep the local nitrogen dioxide fugacity below the threshold for decomposition. Beyond handling, the electronic difference manifests in downstream dyes. When coupled to N,N-diethylaniline, the 6-nitro diazonium component produces a bathochromic shift of the principal absorption band, typically Δλmax 25–45 nm relative to the unsubstituted analogue, as recorded in DMF solution with a double-beam spectrophotometer following ASTM E1164. The resulting azo chromophore exhibits enhanced photostability on polyester, attributed to a lowered HOMO energy that resists singlet-oxygen-mediated fading. Accelerated weathering in a xenon-arc apparatus (ISO 105-B02:2014, blue wool reference) on PET woven fabric dyed at 2.0% on-weight-fiber via high-temperature exhaust (130 °C, 60 min) consistently yields a rating advantage of 1–2 grades for the 6-nitro-derived dye over the non-nitrated benchmark. In the synthesis of heterocyclic disperse dyes for automotive polyester textiles, the filtered diazonium solution is reacted with tertiary aniline couplers in a jacketed vessel equipped with cascade PID control holding pH at 2.5–3.5 through automatic addition of sodium acetate buffer. Coupling temperature is maintained at 0–3 °C by a recirculating chiller with ±0.5 °C stability. Continuous monitoring of unreacted diazonium by spot-test with resorcinol (limit of detection 10 ppm) terminates the batch at residual diazonium content <50 ppm before isolation by filtration and washing with 0.5% acetic acid. The differential performance over dyes from 2-aminobenzothiazole is most apparent in high-energy disperse red shades where the nitro substituent lifts light fastness into the range required for OEM fabric specifications (minimum grade 6 on the blue wool scale). Published data for dyed film light-stability at 120 °C (interior automotive testing per DIN 75202) are limited, but retained strength after 100 h is routinely > 85% for the 6-nitro derivative on polyester, compared to 70–75% for the unsubstituted control.

    When the 6-Nitro Substituent Modulates Scorch Safety in Accelerator Synthesis

    2-Amino-6-nitrobenzothiazole serves as the immediate precursor to the corresponding sulfenamide, N-cyclohexyl-2-(6-nitrobenzothiazolesulfenamide), a delayed-action vulcanisation accelerator. Electron depletion at the benzothiazole thiol-derived sulfur strengthens the S–N bond, raising the activation energy for homolytic scission and thus deferring the onset of crosslinking. In a two-stage mixing procedure on a 1.5 L intermeshing laboratory internal mixer (fill factor 0.75, rotor speed 60 rpm, dump temperature 140 °C for the masterbatch and 100 °C for the accelerator/sulfur pass, in accordance with ASTM D3182), the 6-nitro sulfenamide yields a Mooney scorch time t5 at 121 °C (ASTM D1646) between 24 and 28 min. The unsubstituted analogue CBS (CAS 95-33-0) under the same formulation (NR RSS1 100 phr, N330 50 phr, ZnO 5 phr, stearic acid 2 phr, sulfur 2.5 phr, accelerator 0.7 phr) typically registers t5 in the range 17–21 min. The widened processing safety window—roughly 30–40% longer than CBS—allows injection molding of thick-walled technical rubber goods (e.g., bushings with cross-section >20 mm) without risk of premature centre scorch during mould filling at injection pressures up to 100 MPa. A moving die rheometer trace per ISO 6502 at 160 °C further shows that t90 (time to 90% of maximum torque) increases by approximately 1.2–1.8 min, which must be compensated by small additions of a secondary booster (e.g., DPG at 0.1 phr) to meet cure cycle targets of 3–4 min on high-speed presses. The primary limitation observed in production-scale trials on a 270 L tangential internal mixer is an increased sensitivity to batch-to-batch particle size variation of the accelerator. Nitro substitution elevates the softening point such that pastilles aged at relative humidity >60% for more than 48 h show delayed dispersion, detectable as undispersed agglomerates in microtome sections under dark-field microscopy. Producers specifying this intermediate for sulfenamide synthesis therefore impose a maximum particle size of 98% < 75 µm (sieving, ASTM D1921 dry method) and mandate sealed, desiccated packaging in foil-lined drums. Unlike the non-nitrated pathway, the thiolation of 2-amino-6-nitrobenzothiazole to form the mercaptan must be conducted under sodium hydrosulfide at a strictly limited temperature of 115–120 °C; excursion to 130 °C leads to reduction of the nitro group and the formation of intractable amino-thiol polymeric residues that foul the reactor wall.

    Regulatory and Purity Differentials Across Supplier Grades

    Typical grade specifications for 2-amino-6-nitrobenzothiazole
    ParameterTechnical gradePharmaceutical intermediate gradeTest method reference
    Assay (HPLC area%)≥98.0%≥99.2%USP <621>, 254 nm
    Melting range246–253 °C249–252 °CCapillary method, USP <741>
    Loss on drying (105 °C, 2 h)≤1.0%≤0.5%USP <731>
    Sulfated ash≤0.2%≤0.1%USP <281>
    Water (Karl Fischer)≤0.5%≤0.2%USP <921>, Method Ia
    Heavy metals (as Pb)≤20 ppm≤10 ppmUSP <231> Method II
    Insolubles in 1N HCl≤0.3%≤0.1%Gravimetric, 0.45 µm membrane
    Residual nitrobenzothiazole isomers≤1.0% total≤0.3% totalGC-FID after derivatisation
    Isomeric purity is a critical differentiator when comparing products sourced from different synthetic routes. Nitration of 2-aminobenzothiazole in concentrated sulfuric acid at 0–10 °C yields primarily the 6-nitro isomer, but the mononitration mixture invariably contains 3–6% of the 4-nitro isomer and trace 5-nitro species. For pharmaceutical side-chain elaboration—where the nitro group is later reduced to a primary amine—the presence of a 5-nitro isomer can generate a genotoxic impurity that must be controlled below the Threshold of Toxicological Concern (TTC) of 1.5 µg day⁻¹ per ICH M7(R1). Consequently, pharmaceutical-grade material typically undergoes a recrystallisation from a mixture of acetone and water (3:1 v/v) with a yield penalty of about 10–15%, stripping isomer content below 0.3% as verified by UPLC-MS/MS with a limit of quantitation of 0.05%. Switching from the unsubstituted 2-aminobenzothiazole to the 6-nitro congener also introduces differences in REACH-registered tonnage bands and hazard classification. While both substances are supplied as fine chemicals in volumes below 10 tonnes year⁻¹, the 6-nitro derivative carries self-classification for skin sensitisation Category 1 (H317) based on in vivo testing according to OECD 406 (Buehler method), triggering obligatory labelling with EUH208 when present above 0.1% in finished mixtures. These regulatory divergences must be factored into any substitution strategy when the nitro compound is evaluated as a more lightfast dye intermediate relative to its non-nitrated precursor.