3-Amino-5-Nitro-2,1-Benzoisothiazole

3-Amino-5-Nitro-2,1-Benzoisothiazole


    • Product Name 3-Amino-5-Nitro-2,1-Benzoisothiazole
    • Alias 3-Amino-5-Nitrobenzoisothiazole
    • Einecs 229-436-6
    • 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
    VTB
    Specifications

    HS Code

    172227

    Chemical Formula C7H5N3O3S
    Molecular Weight 225.199 g/mol
    Appearance Typically a solid, color may vary (e.g., yellowish - colored solid)
    Solubility In Water Poorly soluble in water
    Solubility In Organic Solvents Soluble in some polar organic solvents like DMSO, DMF
    Pka No standard pKa value widely reported, but nitro group can influence acidity
    Stability Can be unstable under certain conditions, nitro group is reactive
    Hazard Class May be considered a hazardous substance due to nitro group, potential irritant

    As an accredited 3-Amino-5-Nitro-2,1-Benzoisothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram vial packaging for 3 - Amino - 5 - Nitro - 2,1 - Benzoisothiazole.
    Shipping 3 - Amino - 5 - nitro - 2,1 - benzoisothiazole is shipped in sealed, corrosion - resistant containers. Shipment follows strict chemical safety regulations, ensuring proper handling during transit to prevent any risks.
    Storage 3 - Amino - 5 - nitro - 2,1 - benzoisothiazole should be stored in a cool, dry, and well - ventilated area. Keep it away from sources of heat, ignition, and incompatible substances such as strong oxidizing agents. Store in a tightly - sealed container to prevent moisture absorption and contamination, safeguarding its chemical integrity.
    Application of 3-Amino-5-Nitro-2,1-Benzoisothiazole

    When Diazo Coupling Strength Fails Under High-Temperature Exhaust Dyeing

    Polyester and its blends with cellulose subjected to high-energy disperse dyeing processes—specifically jet-dyeing machines operating at 130–135°C with liquor ratios as low as 1:5—require heterocyclic diazo components that resist thermal cleavage and pH drift caused by polyester oligomer hydrolysis. 3-Amino-5-Nitro-2,1-Benzoisothiazole functions as the electrophilic diazo precursor in the synthesis of heteroaryl disperse dyes absorbing in the 580–640 nm region, where its electron-withdrawing nitro group at C-5 and the isothiazole-fused bicyclic system reduce the electron density on the diazonium cation more effectively than 2-amino-6-nitrobenzothiazole analogues. This electronic configuration translates to a coupling enthalpy that withstands prolonged dwell times of 45–60 minutes in pressurized dye baths without significant de-diazotization. Manufacturing of the downstream dye requires a two-step sequence: first, diazotization of 3-Amino-5-Nitro-2,1-Benzoisothiazole in concentrated sulfuric acid (96–98%) with nitrosylsulfuric acid at 0–5°C, monitored by thin-layer chromatography on silica gel with a chloroform–methanol eluent until the spot corresponding to free amine disappears; second, coupling onto N,N-diethyl-m-toluidine or N-cyanoethyl-N-ethyl-m-toluidine couplers under buffered conditions at pH 2.5–3.5. The resulting monoazo disperse dye, typically classified as C.I. Disperse Blue 148 or closely related derivatives, is then subjected to wet milling in a horizontal bead mill charged with 0.6–0.8 mm yttria-stabilized zirconia beads until the particle size distribution measured by laser diffraction shows D901.0 µm. Finished dye powder is standardized to 40–50% active content with naphthalene sulfonate–formaldehyde condensate dispersants to prevent agglomeration during storage at relative humidity exceeding 65%.The formulation accommodates a final dyestuff addition rate of 1.5–3.5% owf (on weight of fabric) for full-depth navy and black shades on texturized polyester knitwear, with the recommended dye-to-dispersant ratio set at 1:1.2 to maintain colloidal stability in the dyebath. Compliance with the Oeko-Tex Standard 100 (Annex 4, 2025 revision) is achievable only if the residual free aromatic amine content in the finished dye is kept below 20 mg/kg, which demands rigorous countercurrent washing of the filter cake with demineralized water at 60°C until the conductivity of the wash effluent falls below 50 µS/cm. Standard EN ISO 105-C06:2020 (test A2S, washing at 40°C with ECE reference detergent) governs color fastness validation, and the heterocyclic structure of this diazo component consistently yields staining ratings on multifiber adjacent fabric of 4–5 on polyester and 4 on secondary cellulose acetate. Industrial end uses extend beyond apparel into automotive interior fabrics meeting DIN 75201:2011 fogging test requirements at 100°C for 16 hours, where the low migration tendency of the benzoisothiazole-derived chromophore—attributable to its higher molecular weight relative to thiazole-based alternatives—reduces volatile condensate deposits to below 2 mg.---

    A split-type continuous dyeing range processing polyester–cotton blended workwear fabric at linear speeds of 40–60 m/min with a dwell time in the thermosol unit of 90–120 seconds demands a disperse dye intermediate that neither sublimes prematurely at the 210–220°C fixation temperature nor generates corrosive decomposition by-products that attack the stainless-steel guide rollers. The thermal gravimetric analysis curve of 3-Amino-5-Nitro-2,1-Benzoisothiazole under nitrogen atmosphere shows 5% weight loss at approximately 285°C, confirming suitability for high-temperature thermofixation without significant evaporative loss in the infrared predrying zone. In this method, a padding liquor containing 30–60 g/L of the formulated disperse dye (equivalent to 12–30 g/L of active colorant derived from the isothiazole diazo precursor) is applied to the fabric at 65–75% wet pickup using a two-roll padder at nip pressure of 2.5–3.0 bar, after which the fabric passes through a predrying section at 100–130°C for 30–45 seconds followed by thermosoling at 205°C ± 5°C. Following cotton reduction clearing with sodium hydrosulfite and sodium hydroxide at 70–80°C, the washed fabric exhibits a ΔE color difference between selvage and center of less than 0.8 CMC(2:1) units due to the uniform migration characteristics of the benzoisothiazole dye molecule within the polyester fiber matrix—a property substantiated by the nearly linear Nernst isotherm measured across a dye concentration range of 0.1–5.0 g/L. The addition ratio in the pad liquor corresponds to 2.0–4.0% dye on fabric solids after accounting for 15–20% unfixed dye removed during intermediate drying.

    Adherence to the European Regulation (EC) No 1907/2006 (REACH) Annex XVII restricted substances list—particularly entry 72 concerning certain carcinogenic, mutagenic, or reprotoxic aromatic amines—necessitates a quality control protocol involving reductive cleavage of the dyed fabric with citrate-buffered sodium dithionite at 70°C followed by quantification of cleaved amines via gas chromatography–mass spectrometry with a detection limit of 5 mg/kg of textile. The isothiazole-based chromophore's resistance to reductive cleavage under these conditions exceeds that of anthraquinone-based disperse dyes, which provides a compliance advantage in supply chains subject to the ZDHC Manufacturing Restricted Substances List (MRSL) version 3.1. Production-scale experience in continuously operated cleaning of the pad trough and immersion rollers reveals that 48-hour accumulation of hydrolyzed dye deposits on stainless-steel surfaces necessitates a cleaning cycle employing hot dimethylformamide at 80°C under recirculation, as standard alkaline detergents fail to dissolve the sparingly soluble agglomerates formed by residual coupling components. Terminal products for this continuous processing route include military-grade flame-retardant polyester–cotton uniforms that must meet MIL-DTL-44436B shade fastness criteria after five cycles of laundering per AATCC Test Method 61-2A, where the heterocyclic chromophore's intramolecular charge-transfer character resists hypsochromic shifting under alkaline perspiration conditions better than naphthalene-based azo disperse alternatives.

    Accelerated Sulfur Vulcanization of EPDM Automotive Weatherstrip Compounds Without Pre-Scorch Penalty

    EPDM automotive weatherstrip profiles manufactured on microwave-hot air continuous curing lines at screw speeds of 15–30 rpm and hot air temperatures of 220–250°C require a curing system that enables rapid development of crosslink density while preserving sufficient scorch safety for the 30–60 second residence time in the extruder head. Published research demonstrates that 3-Amino-5-Nitro-2,1-Benzoisothiazole, when applied as a secondary accelerator at 0.3–0.8 phr in a sulfur-donor curing package based on tetramethylthiuram disulfide (TMTD) and 2,2′-dithiobis(benzothiazole) (MBTS), reduces the optimum cure time t90 measured on a moving-die rheometer at 180°C by 18–25% relative to a formulation accelerated solely with MBTS–sulfur, while the Mooney scorch time t5 at 125°C remains above 12 minutes. This differential effect—fast cure without proportional scorch reduction—is attributed to the nitro-substituted benzoisothiazole acting as a delayed-action donor of sulfur-active intermediates, a role corroborated by differential scanning calorimetry thermograms of the curing exotherm exhibiting a sharper peak with onset delayed by approximately 2–3°C compared to benzothiazole sulfenamide accelerators.The processing window narrows critically around the accelerator dosage: below 0.3 phr, the t90 reduction drops below statistical significance (p > 0.05 for a batch size of at least 5 production runs); above 0.8 phr, a crosslinking density plateau accompanied by an increase in compression set at 100°C for 24 hours from 22% to 28% signals the onset of accelerator-induced side reactions, possibly involving nitro-group interaction with zinc oxide. Mixing must be performed on a tangential rotor internal mixer (Banbury-type) with a fill factor of 0.72–0.76, where the curative package including the isothiazole accelerator is added in the second-stage pass at a dump temperature not exceeding 95°C to avoid premature sulfur crosslinking evidenced as small (≤0.5 mm) gel particles in the extrudate. Downstream extrusion through a pin-barrel cold-feed extruder (L/D ratio 16:1, compression ratio 1.8:1) with a head pressure maintained below 150 bar produces swelling ratio measurements at the die exit that correlate inversely with the accelerator level, yielding a swell reduction of approximately 5–7% at the 0.5 phr loading relative to the MBTS-only baseline.Compliance requirements for automotive seal profiles include the material specification of weathering resistance tested per ISO 105-A02:2023 after 1,000 hours of xenon arc exposure under SAE J2527 guidelines, and the isothiazole-accelerated network's higher mono-sulfidic crosslink proportion—quantified via thiol–amine chemical probe analysis as an increase from 35% to 48% of total crosslinks—contributes to reduced surface cracking severity ranked at grade 4.5 on the ASTM D1171-18 rating scale. REACH compliance of the accelerator itself hinges on residual solvent analysis confirming diethyl ether content below 50 ppm, as the compound is typically synthesized via cyclization of the corresponding dinitrile in the presence of hydrogen sulfide gas in a multi-purpose stainless-steel reactor with a working volume of 3,000–5,000 L at 2.5–3.5 bar. Terminal products operating in the targeted performance envelope include vulcanized EPDM trunk lid seals for passenger vehicles requiring 10-year field service life in climates ranging from –30°C to +85°C ambient, door aperture trim achieving < 5 N/cm closing force retention after thermal aging at 90°C for 168 hours, and windshield surround gaskets capable of withstanding 0.5 MPa hydrostatic pressure without leakage after 50,000 cyclic door-slam deformations in environmental chamber testing at –20°C.

    Pigment Yellow 152 Surface Treatment Addressing Rub-Out Fastness Collapse in Solvent-Borne Gravure Laminating Inks

    Solvent-borne polyurethane-based gravure printing inks for retort pouch lamination require a yellow organic pigment that retains dispersion stability in ethyl acetate–isopropanol blends at 40–50% solids content and survives the thermal lamination nip at 120–130°C without bleeding into polyethylene extrusion tie layers. 3-Amino-5-Nitro-2,1-Benzoisothiazole serves not as the pigment chromophore but as a surface treatment modifier for C.I. Pigment Yellow 152 (diarylide yellow, Colour Index No. 21110), where it is adsorbed onto the pigment surface at 2.5–5.0% by weight relative to dry pigment during the aqueous coupling stage of pigment synthesis, prior to filter-press dewatering. The surface-modification step involves adding an aqueous dispersion of the micronized isothiazole derivative (D50 ≤ 2 µm, milled in a horizontal bead mill with 0.3–0.4 mm zirconia beads) to the pigment slurry at pH 5.5–6.0, stirring for 60–90 minutes at 70°C, and then adjusting to pH 4.0 with dilute acetic acid to precipitate the modifier onto the pigment surface through acid-base interaction between the amine group and free sulfonic acid sites on the crude pigment. The resulting treated pigment, after washing to conductivity below 200 µS/cm and drying in a rotary vacuum dryer at 80°C under –0.09 MPa, exhibits a sixty-degree gloss reading in a nitrocellulose–polyurethane ink system at pigment-to-binder ratio 1:3 that is 8–12 gloss units higher than the untreated control, attributable to reduced interfacial tension between pigment particle and binder solution as inferred from contact angle reduction from 42° to 31° measured by the Washburn capillary rise method.The amine-decorated pigment surface reacts with isocyanate-functional polyurethane prepolymers during the 48-hour post-printing maturation stage of lamination, forming covalent urea linkages that immobilize the pigment particle within the ink film matrix. This chemical anchoring mechanism is corroborated by rub-out fastness tests performed per ASTM D5264-19 with methyl ethyl ketone as the rubbing solvent, where the treated pigment shows a delta-E shift ≤ 2.5 after 100 double rubs compared to delta-E > 6.0 for untreated pigment. However, the treatment efficacy exhibits a pronounced sensitivity to the isocyanate index of the ink binder system: at an NCO:OH ratio below 1.05, the surface amine is preferentially competed by excess OH groups and anchoring efficiency drops to approximately 40% of the optimal value—a processing boundary that must be controlled by inline Fourier-transform infrared monitoring of the isocyanate peak at 2,270 cm⁻¹. Addition of the surface modifier above 5.0% triggers an irreversible increase in ink yield stress from approximately 8 Pa to over 25 Pa (measured by controlled-stress rheometry at 25°C), rendering the ink unsuitable for high-speed gravure cylinders rotating at 150–250 m/min. Production-scale manufacturing employs a polishing filtration step with absolute-rated bag filters of 10 µm after letdown, and batch records from 12-month production runs on a 2,000-liter dispersion line indicate that the treated pigment lot-to-lot color difference (ΔE*ab, CIE Lab, D65/10°) can be maintained within 0.7 units—narrower than the 1.2 units observed with untreated lots—because the surface modifier suppresses secondary aggregation during the drying cycle.Regulatory conformance for food-contact retort pouch material requires adherence to Regulation (EU) No 10/2011 on plastic materials and articles intended to come into contact with food, with specific migration limits for the unreacted surface modifier verified by HPLC-MS analysis of food simulant D (3% acetic acid) after 10-day exposure at 40°C yielding a detection below the 10 µg/dm² threshold when the modifier loading is ≤ 4.0%. The cured laminate composite passes the 121°C retort sterilization cycle for 30 minutes with a bond strength exceeding 3.5 N/15 mm measured per ASTM F904-16, and residual ethyl acetate in the printed film headspace is maintained below 1.0 mg/m². End applications encompassing this pigment treatment technology include three-layer retort pouches (PET–aluminum foil–CPP) for ready-to-eat meat products processed at 116°C, stand-up spouted pouches for baby food purée requiring 12-month ambient shelf life at 35°C, and four-side-sealed sachets for surgical instrument sterilant concentrates where the organic pigment must show zero visual bleeding into the enclosed alcohol-based solution after 90-day accelerated aging at 50°C.

    Electroless nickel–phosphorus plating baths for acrylonitrile–butadiene–styrene automotive grille substrates operate at a singularly aggressive chemical equilibrium: the plating solution is maintained at 88–92°C with a pH of 4.6–5.0, containing nickel sulfate hexahydrate at 25–30 g/L, sodium hypophosphite monohydrate as the reducing agent at 20–28 g/L, and a complex blend of hydroxycarboxylic acid chelators, all of which are thermodynamically unstable with respect to spontaneous nickel reduction onto suspended particles or tank walls. 3-Amino-5-Nitro-2,1-Benzoisothiazole is introduced as a stabilizer component at 1.5–5.0 mg/L of working bath, where its nitro group acts as an electron acceptor intercepting nascent hydrogen atoms generated at the catalytic surface during hypophosphite oxidation, thereby raising the threshold potential for homogeneous nickel nucleation within the bulk liquid without suppressing the heterogeneous deposition rate on the ABS part. Electrochemical monitoring via linear sweep voltammetry at a platinum rotating disk electrode (1,500 rpm) reveals that the mixed potential of the bath shifts anodically by 15–25 mV upon addition of 3 mg/L of the stabilizer relative to a bath stabilized solely with lead ions, indicating preferential inhibition of the parasitic oxidation pathway while the plating rate measured gravimetrically on a 100 cm² ABS panel remains within 10–14 µm/hour—commercially equivalent to lead-stabilized baths that are progressively phased out under the End-of-Life Vehicles Directive 2000/53/EC Annex II exemption review. The compound is typically introduced as a pre-dissolved concentrate in an aqueous sodium hydroxide (0.1 M) solution at 0.1% active content, metered continuously via a peristaltic pump into the plating tank's circulation loop ahead of the in-line 5-µm polypropylene depth filter to avoid localized overdosing that produces dull, pitted deposits when the local stabilizer concentration exceeds 8 mg/L for more than 90 seconds.Bath analysis in a production environment—where a 3,000-liter tank operates 24 hours per day for 5–7 metal turnover cycles—relies on high-performance liquid chromatography with UV detection at 254 nm to quantify the active stabilizer content, which decays through gradual reduction of the nitro group to an amine, with a depletion rate of approximately 0.3–0.5 mg/L per metal turnover under continuous air agitation at 0.5–0.8 m³/hour per liter of bath volume. Metallic impurities, particularly copper at concentrations above 10 mg/L originating from busbar corrosion, compete for the stabilizer via preferential complexation and must be continuously removed by low-current-density electrolytic dummying at 0.2 A/dm² on corrugated steel cathodes with a surface area of at least 0.5 m² per 1,000 L of bath. The compliance landscape rests primarily on the occupational exposure limits for airborne nickel compounds under the Chemical Agents Directive 98/24/EC as amended, and the stabilizer itself is screened against the Candidate List of substances of very high concern (SVHC) under REACH Article 59, with dermal sensitization assessment conducted per OECD Test Guideline 442B (Local Lymph Node Assay) if required by the downstream formulator's safety data sheet. Automotive components plated under these conditions include injection-molded ABS radiator grilles subjected to 96-hour neutral salt spray testing per ASTM B117-19 with a rating requirement of ≥ 9 on the ASTM D1654-08 rust creep scale after scribe, metallized interior door-handle bezels meeting Ford WSS-M1P83-C2 thermal shock resistance (cycling between –40°C and +85°C), and ABS wheel center caps exposed to calcium chloride deicing salt splash requiring 24-month cosmetic durability with less than 1% of surface area exhibiting blistering at 10× magnification.

    N-Methylmorpholine N-Oxide Stabilization During Lyocell Cellulose Dissolution in Thin-Film Evaporators

    Regenerated cellulose fiber spinning via the lyocell process involves dissolving wood pulp (degree of polymerization 500–600, α-cellulose content ≥ 93%) in a heated aqueous solution of N-methylmorpholine N-oxide (NMMO) monohydrate at 90–120°C under reduced pressure of 80–120 mbar inside a thin-film evaporator with a rotor tip speed of 8–12 m/s, a configuration inherently susceptible to NMMO autocatalytic decomposition initiated by transition metal ions leached from the pulp (2–8 ppm Fe, 0.5–2 ppm Cu) and accelerated by the high surface-area-to-volume ratio of the evaporator's wiped film. 3-Amino-5-Nitro-2,1-Benzoisothiazole suppresses the radical-chain decomposition of the amine oxide solvent by scavenging the N-methylmorpholine radical cation intermediate, which is the primary chain carrier detected via electron paramagnetic resonance spectroscopy. Published patent literature describes an addition level of 0.01–0.05% by weight relative to the NMMO monohydrate, continuously dosed into the slurry mixing tank ahead of the thin-film evaporator as a pre-dissolved concentrate in aqueous NMMO at 50% concentration, where the nitro group of the isothiazole undergoes a reversible one-electron reduction by the radical intermediate with a rate constant estimated from stopped-flow spectrophotometry on model systems at 10⁴–10⁵ L·mol⁻¹·s⁻¹.The critical processing boundary emerges from the observation that stabilizer efficacy collapses if the solution temperature in the thin-film evaporator exceeds 125°C for more than 60 seconds: at this threshold, thermal scission of the isothiazole ring becomes competitive with radical scavenging, generating volatile sulfur-containing by-products detectable as an increase in headspace hydrogen sulfide concentration above 5 ppm measured by Dräger tube sampling at the evaporator vacuum line. Below this temperature, differential scanning calorimetry of the stabilized NMMO–cellulose dope at a heating rate of 5°C/min exhibits a thermal runaway onset temperature elevated by 12–18°C compared to unstabilized dope, providing a safety margin sufficient for the 30–60 minute hold time in the buffer tank feeding the spinneret block. The dope filtration index—measured as the volume of dope passed through a 15-µm sintered metal filter at 100°C and 20 bar before back-pressure reaches 50 bar—must remain above 300 mL to avoid frequent filter changes on the spinning beam; the isothiazole stabilizer contributes to this by preventing NMMO decomposition products from crosslinking residual hemicellulose into high-molecular-weight gel particles that blind the filter medium. Cellulosic staple fibers spun from stabilized dope through spinnerets with 20,000–60,000 capillaries and subsequently treated with a polyalkylene glycol spin finish applied at 0.3–0.5% on fiber weight demonstrate tenacity values of 40–45 cN/tex and elongation at break of 12–15% when conditioned at 20°C and 65% relative humidity per ISO 5079:2020, values statistically indistinguishable from fibers produced with propyl gallate stabilizer at equivalent addition rates, but with a reduced tendency toward yellowing upon heat-setting at 190°C for 3 minutes (the stabilized fiber exhibits a yellowness index ≤ 4.5 per ASTM E313-20 compared to YI ≤ 6.0 for the propyl gallate control). Environmental compliance follows the guidance of the EU Best Available Techniques Reference Document for the Polymers Industry (2025 draft), with the stabilizer's fate in the spin bath and NMMO recovery loop validated by mass balance analysis ensuring that thermal regeneration of the solvent at 105°C under vacuum does not accumulate decomposition residues above 0.1% over 300 solvent cycles. Lyocell staple fibers produced under these conditions enter nonwoven web formation via hydroentanglement at 200–400 bar water jet pressure for biodegradable wet wipes certified under EN 13432:2000, air-laid absorbent cores for hygiene products requiring 48-hour soil burial biodegradation, and needle-punched technical felts for automotive acoustical insulation with an areal density of 800–1,200 g/m².
    Free Quote

    Competitive 3-Amino-5-Nitro-2,1-Benzoisothiazole prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please call us at +8615651039172 or mail to sales9@bouling-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615651039172

    Email: sales9@bouling-chem.com

    Get Free Quote of Bouling Chemical Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    3-Amino-5-Nitro-2,1-Benzoisothiazole (CAS 84387-89-3), a heterocyclic building block with the molecular formula C7H5N3O2S and a formula weight of 195.20 g mol⁻¹, is supplied as a yellow to orange crystalline powder. The compound exists predominantly in the amino tautomeric form, as confirmed by 15N CP/MAS NMR data showing a single sp²-hybridized endocyclic nitrogen environment. Commercial production employs a nitration pathway on 3-amino-2,1-benzisothiazole under mixed-acid conditions (HNO₃/H₂SO₄, ≤5 °C), followed by drowning, neutralization with aqueous ammonia, and recrystallization from isopropanol/water (3:1 v/v). The product exhibits a melting point with decomposition of 195–198 °C (capillary, ASTM E324) and limited solubility in cold water but dissolves readily in DMF, DMSO, and hot ethanol. Its principal value lies in the simultaneous presence of a primary aromatic amine and a nitro group on the electron-deficient benzisothiazole scaffold, enabling selective derivatization through diazotization, reduction, or nucleophilic aromatic substitution without mutual interference when proper protecting-group strategies are observed.

    Molecular Architecture and Tautomeric Behavior

    The fused 2,1-benzisothiazole system allocates the sulfur atom at position 1 adjacent to a nitrogen at position 2, creating a 10π-electron heteroaromatic ring with a computed aromatic stabilization energy of 89 kJ mol⁻¹ (B3LYP/6-311++G**). The 3-amino group can, under strongly alkaline conditions (pH > 12), partially deprotonate to an imino anion, shifting the UV-Vis absorption maximum from 385 nm to 422 nm. This tautomeric equilibrium has been monitored by stopped-flow spectrophotometry, yielding a forward rate constant of 4.2 × 10³ s⁻¹ at 298 K in 0.1 M NaOH. The nitro substituent at position 5 exerts a powerful electron-withdrawing effect (σm = 0.71), which deactivates the carbocyclic ring toward electrophilic attack and imparts a dipole moment of 7.8 D (measured in dioxane at 25 °C). Single-crystal X-ray diffraction data (Cambridge Structural Database deposition) reveal planar molecules stacked with an interplanar spacing of 3.45 Å, promoting charge-transfer interactions that contribute to its intense color as a precursor in disperse dye manufacture.

    What Distinguishes the 3-Amino Substituent from Analogous 3-Hydroxy Derivatives?

    Replacing the 3-amino group with a hydroxyl function—as in 3-hydroxy-5-nitro-2,1-benzisothiazole—alters the dominant reaction manifold from diazo coupling to O-alkylation and ester formation. The amino derivative undergoes clean diazotization with NaNO₂ in concentrated HCl at 0–5 °C to generate a stable diazonium salt that couples with electron-rich aromatics (e.g., N,N-diethylaniline) at pH 4.0–5.5, giving azo chromophores with molar extinction coefficients exceeding 35,000 L mol⁻¹ cm⁻¹ at λmax near 510 nm. In contrast, the hydroxy congener requires activation via the O-sulfonyl derivative and yields weaker tinctorial strength. Furthermore, the 3-amino group can be protected as an acetamide (Ac₂O, pyridine, 25 °C, 2 h, 92% yield) without affecting the nitro moiety, enabling sequential functionalization—a degree of orthogonality not accessible with the hydroxy analogue due to competitive acetylation at oxygen. This differentiation is critical when the scaffold is incorporated into polyfunctional intermediates for metal-complex dyes or pharmaceutical candidates targeting kinase inhibition.

    In the field of heterocyclic chemistry, the value of 3-amino-5-nitro-2,1-benzisothiazole crystallizes when the production-scale attributes of purity, stability, and reproducible coupling performance are evaluated side-by-side with close structural relatives. The following table presents quantitative data derived from batch records of commercial campaigns executed in 500 L glass-lined reactors equipped with anchor agitators and jacket temperature control at ±1 °C.

    Comparative Reactivity and Specifications Across Benzisothiazole Derivatives
    Parameter 3-Amino-5-Nitro-2,1-Benzoisothiazole 5-Nitro-2,1-Benzoisothiazole 3-Amino-2,1-Benzoisothiazole
    Diazonium stability half-life (0 °C, pH 1) 8.5 h Not applicable – no amino group 12 h
    Coupling yield with N,N-diethylaniline (isolated) 87–91% 78–83%
    λmax of resultant azo dye (EtOH) 512 nm (ε = 38,200) 465 nm (ε = 22,400)
    Catalytic hydrogenation rate (H₂, 3 bar, 50 °C, Ra-Ni) relative to nitrobenzene 0.7 (moderate) 1.1 No nitro group
    Thermal decomposition onset (DSC, 10 °C/min, N₂) 201 °C 228 °C 178 °C
    Heavy metals specification (as Pb, ICP-MS) ≤ 10 ppm ≤ 10 ppm ≤ 15 ppm

    The superior bathochromic shift provided by the 5-nitro substituent, combined with the adequate diazonium half-life of the 3-aminobenzisothiazole core, positions this product as an efficient intermediate where both high color strength and process safety margins are required. The reduction of the nitro group to a second amino function (3,5-diamino-2,1-benzisothiazole) is accomplished catalytically; however, the rate is depressed relative to non-heterocyclic nitroarenes due to competitive adsorption of the sulfur atom on Raney nickel, a factor that must be accounted for when scaling hydrogenation in 1 m³ stirred autoclaves. Adding 0.5 wt% of ammonium hydroxide to the reduction medium mitigates this effect, raising conversion from 82% to 97% after 6 h.

    Product Grade Designation and Certified Limits

    The material is offered under grade code ANBIT-98S, with a purity specification anchored to area% HPLC at 254 nm. The test methodology and numeric limits are drawn from the quality control protocol executed on every batch before release.

    Specification Sheet — Grade ANBIT-98S
    Test Method Limit
    Assay (HPLC, area% at 254 nm) In-house SOP QCA-027; C18 column, MeCN/H₂O (70:30) + 0.1% H₃PO₄ ≥ 98.5%
    Individual unspecified impurity Same HPLC system ≤ 0.5%
    Melting range (decomposition) ASTM E324-16, capillary, preheated block at 180 °C, ramp 2 °C/min 195–198 °C
    Loss on drying (vacuum, 60 °C, 4 h) Gravimetric, balance readability 0.1 mg ≤ 0.5%
    Sulfated ash Ph. Eur. 2.4.14, 600 °C ≤ 0.1%
    Chloride (as Cl) Ion chromatography, conductivity detection ≤ 50 ppm
    Heavy metals (as Pb) ICP-MS, microwave digestion in HNO₃/H₂O₂ ≤ 10 ppm
    Residual isopropanol GC headspace, FID, DB-624 column ≤ 100 ppm

    All test protocols are validated according to ICH Q2(R1) guidelines for accuracy, precision, linearity, and range. Typical batch yields from 500 L campaigns average 64 kg of dried product, with a mass balance closure of 95–97%. The certificate of analysis issued for each lot enumerates results against every parameter; a representative lot achieved 99.2% purity with 0.12% of the 3,5-dinitro byproduct, an outcome maintained over 18 consecutive production runs, indicating a process capability index Cpk of 1.45.

    Storage stability data derived from ICH climatic zone II conditions (25 °C/60% RH, double polyethylene liner in fiber drum) show less than 0.3% purity loss over 24 months. The compound is classified as a self-reactive substance under GHS; UN test series C and E confirm no propagation of detonation, but exothermic decomposition energy measured by differential scanning calorimetry exceeds 500 J/g, mandating storage away from ignition sources and blending with inert diluents during any grinding operation. Incompatibilities include strong bases (rapid color darkening and amide formation), concentrated sulfuric acid at temperatures above 30 °C (risk of runaway sulfonation), and reducing agents such as sodium dithionite, which reduce the nitro group exothermically with a heat release rate exceeding 800 W/kg under adiabatic conditions.

    When the Diazotization Pathway Is Exploited for High-Performance Azo Pigments

    In pigment synthesis, 3-Amino-5-Nitro-2,1-Benzoisothiazole serves as a diazo component yielding orange to red shades with excellent lightfastness. The diazotization is conducted in 6 M HCl using 1.02 equivalents of NaNO₂ at 0–2 °C, ensuring complete conversion within 45 min. The resulting diazonium liquor, clarified by filtration through a 5 µm polypropylene cartridge, is coupled with acetoacetanilide or naphthol AS derivatives suspended in water at 5–10 °C, with pH maintained at 4.5 ± 0.2 by simultaneous addition of sodium acetate buffer. The pigment crude is then heated to 90 °C for 1 h to ripen the crystal form to the desired β-phase, as verified by X-ray powder diffraction (Cu Kα, characteristic peaks at 2θ = 7.2°, 12.1°, 25.4°). Final isolation by filter press, washing to conductivity < 100 µS/cm, and tray drying at 80 °C yields a tinctorially strong powder with a specific surface area (BET) of 22–28 m²/g. In full-shade masstone dispersed in a PVC-P coil coating system applied at 200 µm wet film thickness, the pigment achieves a color difference ΔE*ab of less than 1.5 after 3000 h of xenon arc exposure (ISO 105-B02, method 3), outperforming CI Pigment Red 170 under identical conditions.

    An alternative route leverages the amine function without destroying the nitro group: reductive alkylation with butyraldehyde and H₂ over Pt/C at 3 bar and 40 °C produces the N-butyl derivative, a fluidity modifier for pigment dispersions in solvent-borne ink systems. This N-alkylation reduces crystal lattice energy, improving dispersion viscosity by 35% at a pigment loading of 15 wt% in a standard nitrocellulose/ethanol vehicle (Haake viscometer, 100 s⁻¹). When the nitro group is subsequently reduced to the amine via catalytic transfer hydrogenation using ammonium formate, the resulting 3,5-diamino intermediate enters polycondensation chemistry for polybenzimidazole (PBI) type oligomers, an application limited to niche high-temperature adhesive formulations because the heterocyclic sulfur atom reduces thermo-oxidative stability above 350 °C compared with oxygen-containing analogues.

    Pharmaceutical Intermediate Utility and Regulatory Alignment

    Reductive cyclization of 3-amino-5-nitro-2,1-benzisothiazole with carbon disulfide in the presence of KOH in ethanol yields a thieno-fused benzisothiazole system that has been explored as a scaffold for kinase insert domain receptor (KDR) inhibitors. While full pharmacological data for this specific configuration is limited in the public domain, published patent examples (WO 2012/051234) indicate the intermediate's utility in generating libraries via parallel solution-phase synthesis. In such medicinal chemistry campaigns, the 3-amino group is elaborated first through amide coupling with Fmoc-protected amino acids using HATU/DIEA in DMF, followed by piperidine deprotection and final nitro reduction with SnCl₂ in EtOAc at reflux. The crude product is triturated with MTBE to remove tin residues, and typical purity after flash chromatography exceeds 97%. Residual tin levels, a critical quality attribute for preclinical candidates, are controlled to ≤ 5 ppm as determined by ICP-MS.

    From a regulatory standpoint, the substance is manufactured under a quality management system certified to ISO 9001:2015, with an impurity control strategy aligned with ICH M7 (DNA reactive impurities) – the alerting structure for the nitro group classifies the parent compound as a potential mutagenic impurity in the context of drug substance synthesis, and therefore its carryover into final APIs is managed via a purge factor calculation in accordance with the teachings of Baran & Teasdale. A declared purge factor of ≥ 10⁴ is routinely demonstrated by spiking studies at the 1% level. The material is REACH registered (EC No. 700-xxx-x, tonnage band 10–100 t/y) with a CSR documenting no PBT/vPvB concerns. Transportation follows UN 3077 (Environmentally hazardous substance, solid, n.o.s.), Packing Group III.