3-Amino-5-Nitrobenzoisothiazole

3-Amino-5-Nitrobenzoisothiazole


    • Product Name 3-Amino-5-Nitrobenzoisothiazole
    • Alias 3-Amino-5-nitro-1,2-benzisothiazole
    • Einecs 402-520-6
    • Mininmum Order 10g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    568264

    Chemical Formula C7H5N3O3S
    Molar Mass 211.199 g/mol
    Appearance Typically solid (physical appearance may vary based on purity and preparation)
    Solubility In Water Low solubility (organic compounds with such functional groups often have low water solubility)
    Solubility In Organic Solvents Soluble in some polar organic solvents like DMSO, DMF (common for similar heterocyclic compounds)
    Color May be yellowish or off - white (common colors for nitro - containing aromatic compounds)

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

    Packing & Storage
    Packing 100g of 3 - Amino - 5 - Nitrobenzoisothiazole packaged in a sealed plastic container.
    Shipping 3 - Amino - 5 - Nitrobenzoisothiazole is shipped in well - sealed containers. Packaging ensures protection from moisture and physical damage. Shipment follows strict chemical transportation regulations to guarantee safety during transit.
    Storage 3 - Amino - 5 - Nitrobenzoisothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from sources of heat, ignition, and direct sunlight. Store in a tightly - sealed container to prevent moisture absorption and exposure to air, which could potentially lead to degradation. Avoid storing near incompatible substances such as strong oxidizing agents or acids.
    Application of 3-Amino-5-Nitrobenzoisothiazole
    Disperse dyes formulated with 3-Amino-5-Nitrobenzoisothiazole as the diazo component exhibit a bathochromic shift of approximately 35–50 nm relative to their thiophene- and thiazole-based structural analogs, moving λmax into the 580–620 nm region. This spectral displacement is critical for achieving deep navy and black shades on polyester fibers under exhaustion dyeing conditions at 130 °C in weakly acidic media (pH 4.5–5.0, buffered with ammonium acetate/acetic acid). Production-scale disperse milling of the presscake—typically conducted in horizontal bead mills charged with 0.4–0.6 mm yttria-stabilized zirconia beads operating at peripheral speeds of 10–14 m/s—demands that the crude dye be pre-dispersed with lignosulfonate or naphthalene sulfonate formaldehyde condensate dispersants at a dye-to-dispersant ratio of 1:0.8 to 1:1.2. Failure to maintain millbase temperature below 45 °C during the 6–8-pass recirculation grind results in crystal growth agglomeration, leading to filtration pressure buildup on 5 µm absolute-rated bag filters downstream. The finished disperse dyestuff, standardized to a strength of 200% or 300% relative to a reference formulation, is applied to woven and knitted polyethylene terephthalate (PET) fabrics for automotive upholstery meeting OEM lightfastness targets of grade 7 per ISO 105-B02:2014 when subjected to a 200-hour Xenon arc exposure cycle behind 3 mm soda-lime glass. Addition rate in the dyebath ranges from 0.5% to 4.0% on weight of fiber (o.w.f.), with the lower boundary reserved for pale gray blends and the upper boundary needed for full-depth black where the anthraquinone-based shading component alone cannot deliver the required jetness. Compliance with the OEKO-TEX Standard 100 Appendix 4 limits for aromatic amines derived from azo cleavage—specifically the 24-amine panel listed in Regulation (EC) No 1907/2006 Annex XVII entry 43—must be verified via reductive cleavage with sodium dithionite at pH 6.0 per EN ISO 14362-1:2017, followed by LC-MS/MS quantification with a reporting limit of 5 mg/kg per individual amine.

    When benzisothiazole accelerates delayed-action sulphenamide cures without scorching the Mooney

    The incorporation of 3-Amino-5-Nitrobenzoisothiazole into a sulfur-vulcanized natural rubber (NR) or styrene-butadiene rubber (SBR) compound modifies the scorch safety and crosslink density profile in ways that differ from conventional benzothiazole-2-sulphenamide (CBS) or 2-mercaptobenzothiazole (MBT) accelerators. The electron-withdrawing nitro group at the 5-position of the benzisothiazole ring reduces the nucleophilicity of the amino function at the 3-position, retarding the rate of accelerator decomposition in the presence of soluble zinc(II) from zinc oxide (3–5 phr) and stearic acid (1–2 phr) activator systems. This delayed-action behavior is observable in a moving-die rheometer trace recorded at 160 °C per ISO 6502-2:2018: the time to 10% of maximum torque (ts1) extends by 2.5–4.0 min relative to CBS at equivalent molar loading, while the time to 90% cure (tc90) remains within 12–16 min. The practical processing consequence is that a silica-reinforced passenger tire tread formulation containing 0.8–1.5 phr of the benzisothiazole derivative can survive multiple re-mill passes on a 1.5 m-wide two-roll mill without premature crosslinking—a failure mode characterized by a sudden increase in compound Mooney viscosity (ML 1+4 at 100 °C per ISO 289-1:2015) exceeding 15 Mooney units above the target of 55–70 MU. Cured physical properties evaluated on 2 mm compression-molded sheets include tensile strength values of 18–22 MPa per ISO 37:2017 Type 2 dumbbells and tear resistance of 35–50 kN/m per ISO 34-1:2015 trouser tear specimens, provided the compound is cured to tc90 and post-cured for 15 min at 150 °C. Vulcanizates intended for anti-vibration mount bushings in automotive powertrain applications require additional testing of compression set after 22 h at 70 °C per ISO 815-1:2019, with values below 18% considered acceptable for service temperatures peaking at 90 °C intermittent. REACH compliance for the rubber chemical as an article-intended substance demands a registration dossier covering the manufacturing volume band of 10–100 tonnes/annum with an exposure scenario for compounders handling the powder under local exhaust ventilation.

    How does the nitrated amino-benzisothiazole influence hydrazine coupling kinetics in pyrazolone pigment synthesis?

    The heterocyclic amine serves as a diazo component in the synthesis of high-performance organic pigments classified under the Color Index as Pigment Yellow or Pigment Orange variants, where it is diazotized and coupled onto pyrazolone or acetoacetanilide coupling components in an aqueous suspension. The diazotization requires a temperature-controlled stirred-tank reactor with a jacket capable of maintaining 0–5 °C during sodium nitrite addition (1.02 molar equivalents relative to the amine) in the presence of a 2.5–3.0 molar excess of hydrochloric acid, with the endpoint verified by starch-iodide paper and confirmed by an absence of nitrous acid spike detectable via the sulfanilamide/N-(1-naphthyl)ethylenediamine spectrophotometric method at 540 nm. Coupling is executed at pH 8.0–9.5 in a buffered carbonate system, where the pH must be maintained within a ±0.3 unit window to avoid premature precipitation of the coupling component as the free acid—a process flaw that manifests as a bimodal particle size distribution with a Dv50 spanning 0.8 µm and 8.5 µm subpopulations instead of a monomodal Dv50 of 0.4–1.2 µm as measured by laser diffraction in accordance with ISO 13320:2020. The wet filter cake undergoes a solvent-based finishing step in a kneader or sigma-blade mixer charged with 3–5% w/w of a rosin derivative (calcium or zinc resinate) and heated to 80–90 °C under vacuum, during which crystal phase conversion from the alpha to the more thermodynamically stable beta polymorph occurs, raising the melting point above 320 °C as determined by differential scanning calorimetry at a heating rate of 10 °C/min under nitrogen. Finished pigment powders are evaluated for migration fastness in plasticized PVC at a loading of 0.2% pigment per DIN 53775-3, with a requirement of no visible bleeding onto white PVC after 24 h at 80 °C under a 1 kg weight. The coloristic properties—CIE L*a*b* coordinates measured with a spectrophotometer using D65 illuminant and 10° observer geometry per ISO 11664-4:2019—must remain within a delta Eab* of 0.5 batch-to-batch, a tolerance achievable only if the diazotization and coupling temperatures are controlled to a standard deviation of 0.3 °C across 12-batch campaign production.
    Accelerator system comparison in a silica-filled NR/BR truck tread cap at 160 °C cure
    Parameter CBS (1.2 phr) 3-A-5-NBZT (1.5 phr) Test method
    Mooney scorch t5 at 121 °C 28.5 min 36.2 min ISO 289-2:2020
    ts1 at 160 °C 3.1 min 5.8 min ISO 6502-2:2018
    tc90 at 160 °C 10.4 min 14.7 min ISO 6502-2:2018
    Crosslink density (νe × 10⁴ mol/cm³) 1.72 1.58 Equilibrium swelling in toluene
    Tensile strength (MPa) 20.5 19.8 ISO 37:2017
    Compression set 22 h/70 °C (%) 15.2 17.6 ISO 815-1:2019
    Direct conversion of 3-Amino-5-Nitrobenzoisothiazole into its corresponding diazonium salt and subsequent coupling with N-alkylated aniline derivatives in a buffered acetate medium yields solvent-soluble dyes with molar extinction coefficients exceeding 25,000 L·mol⁻¹·cm⁻¹ in the 450–520 nm region, positioning these chromophores as candidates for dye-diffusion thermal transfer (D2T2) printing ribbons and for the coloration of engineering thermoplastics processed at barrel temperatures above 280 °C. Thermal stability screening conducted via thermogravimetric analysis reveals a 5% mass loss at 285–310 °C under nitrogen at a ramp rate of 20 °C/min, which is marginally sufficient for compounding into polycarbonate (290–310 °C melt processing range) but precludes use in polysulfone or polyetheretherketone matrices where extrusion temperatures exceed 340 °C. When compounded into polycarbonate at a let-down ratio of 1:25 from a 1% masterbatch pre-dispersed on a 25 mm co-rotating twin-screw extruder (L/D 40:1, screw speed 300 rpm), the resulting injection-molded plaques display a light transmission value of 45–55% at 500 nm through 2 mm thickness measured per ASTM D1003-21 Procedure A, indicating that complete solubility in the amorphous phase has been achieved without particulate haze formation—a defect typically originating from undissolved crystalline domains larger than the 200 nm visibility threshold by Mie scattering. The colorant must meet heavy metal limits specified in EU Directive 94/62/EC Article 11 and its amendments for packaging applications, requiring inductively coupled plasma optical emission spectrometry (ICP-OES) quantitation of lead, cadmium, mercury, and hexavalent chromium at a combined total below 100 mg/kg.

    Polyurethane foam amine catalyst inhibition thresholds

    The benzisothiazole derivative functions as a catalyst activity moderator in polyether polyol-based flexible slabstock foam formulations catalyzed by tertiary amines such as triethylenediamine (TEDA, 0.15 php) and bis(2-dimethylaminoethyl) ether (BDMAEE, 0.08 php). The mechanism involves reversible hydrogen bonding between the amino proton of the benzisothiazole and the lone pair of the tertiary amine catalyst, temporarily reducing the effective catalyst concentration available for the water-isocyanate blowing reaction. This moderation manifests on a production-scale continuous pour line (conveyor speed 4.5 m/min, total output 180 kg/min) as a 12–18 second delay in the cream time without altering the rise time by more than 3%—a decoupling behavior that cannot be achieved with conventional acid-blocked catalysts which delay both gelation and blowing uniformly. The addition level is constrained to 0.02–0.10 php (parts per hundred polyol by weight); above 0.12 php, the excess benzisothiazole reacts irreversibly with isocyanate groups at the foam surface during the exothermic rise (peak temperature 140–155 °C measured by embedded thermocouples at the bun center), producing a urea-type skin layer with a Shore A hardness exceeding 60 points compared to the bulk foam hardness of 18–25 points—a defect zone requiring mechanical trimming of the upper 2–3 mm of the bun before fabrication. The final polyurethane foam product, designated for furniture cushioning and mattress cores with densities between 25–35 kg/m³ per ISO 845:2006, must satisfy the ignition resistance requirements of Technical Bulletin 117-2013 Section 1 (open-flame test) when a barrier fabric is employed, as the benzisothiazole additive itself contributes negligible char-forming or flame-retardant activity. Emission testing of the cured foam after a 24-hour post-cure at 25 °C and 50% relative humidity must demonstrate total volatile organic compound (TVOC) levels below 500 µg/m³ per ISO 16000-6:2021 when sampled via micro-chamber at 23 °C with an air exchange rate of 1.0 h⁻¹.
    Polyurethane flexible foam reactivity profile with and without 3-Amino-5-Nitrobenzoisothiazole at 0.05 php
    Reactivity parameter Control (0 php) At 0.05 php loading Measurement standard
    Cream time (seconds) 14 30 Visual, stopwatch from pour
    Rise time (seconds) 98 101 Visual, stopwatch from pour
    Gel time as tan δ crossover (seconds) 72 75 Rheometer, 1 Hz, 5% strain
    Max exotherm temperature (°C) 149 147 Type K thermocouple, center
    Foam density (kg/m³) 28.5 28.3 ISO 845:2006
    Compression force deflection at 40% (kPa) 3.8 3.6 ISO 3386-1:2021
    The substitution of 3-Amino-5-Nitrobenzoisothiazole into the acid corrosion inhibitor package for oilfield acidizing fluids has been evaluated under simulated downhole conditions where 15 wt% hydrochloric acid solutions are pumped into low-permeability sandstone or carbonate formations at bottomhole static temperatures (BHST) reaching 95–120 °C. The compound’s heterocyclic nitrogen and nitro functionalities provide a mixed-type inhibition mechanism—shifting both the anodic Tafel slope by approximately 35 mV/dec and the cathodic Tafel slope by 40 mV/dec relative to uninhibited N-80 steel in deaerated 15% HCl at 60 °C, as derived from potentiodynamic polarization scans conducted at a sweep rate of 0.5 mV/s from -250 mV to +250 mV versus open-circuit potential. This shift translates to an inhibitor efficiency of 91–94% at a concentration of 0.5–1.0 g/L, a performance level that is competitive with propagyl alcohol-based inhibitor packages but without the associated toxicity classification concerns related to acetylenic alcohol sensitization. Filtration of the inhibited acid through a 0.45 µm PTFE membrane prior to coreflood testing in Berea sandstone plugs (permeability 50–150 mD) is mandatory to remove insoluble particulates that could bridge pore throats at the rock face; the filtered fluid must exhibit a turbidity below 5 NTU. Field-scale batch mixing on location requires blending the inhibitor concentrate into the acid in a 20 m³ capacity fiberglass-reinforced plastic (FRP) tank under recirculation for 30 min to ensure homogeneity, with a corrosion coupon weight-loss measurement per NACE TM0169-2012 conducted over a 6-hour exposure period at the anticipated BHST to verify a target corrosion rate below 0.05 lb/ft² (244 g/m²) before the acid is bullheaded into the formation.The heterocyclic amine participates as a late-stage functionalization intermediate in the preparation of benzisothiazolone derivatives that exhibit microbiocidal activity against sulfate-reducing bacteria (SRB) populations in industrial water circuits, though published data for this specific configuration is limited. The synthetic route proceeds through reduction of the 5-nitro group under catalytic hydrogenation conditions (5% Pd/C, 3 bar H₂, ethanol, 25 °C, 4 h) to yield the corresponding 3,5-diamino intermediate, a compound requiring storage under nitrogen at 2–8 °C due to sensitivity to aerobic oxidation that generates colored quinonoid degradation products detectable spectrophotometrically at 430 nm. Subsequent cyclization with carbon disulfide in the presence of sodium hydroxide at 60–70 °C in a 2:1 ethanol-water mixture generates the dithiocarbamate adduct, which upon acidification with concentrated HCl and oxidative ring closure using hydrogen peroxide (30% w/w, added dropwise at 0–5 °C) forms the isothiazolone heterocycle. The crude product, isolated by filtration at pH 4.0, requires recrystallization from isopropanol to achieve an HPLC purity exceeding 98 area% at 254 nm. Finished formulations for cooling tower microbicide service combine the active ingredient at 8–12% w/w with a non-ionic surfactant package for water dispersibility and are dosed at 25–50 mg/L on a slug basis twice weekly. Biocidal product authorization under Regulation (EU) No 528/2012 (Biocidal Products Regulation) for product-type 6 (preservatives for products during storage) or product-type 11 (preservatives for liquid-cooling and processing systems) requires a full active substance dossier including the 14-day activated sludge respiration inhibition test per OECD 209 and the ready biodegradability assessment per OECD 301F, the latter typically failing for this structural class due to the electron-deficient nature of the benzisothiazole ring unless a modified Sturm test with an extended 60-day acclimation period is utilized.
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    Certification & Compliance
    More Introduction

    3‑Amino‑5‑nitrobenzoisothiazole (C7H5N3O2S, molecular weight 195.20 g mol−1) is a polyfunctional heterocyclic intermediate combining an electron‑donating primary amine at the isothiazole C‑3 position with a strongly electron‑withdrawing nitro substituent on the fused benzene ring. The solid is isolated as a yellow to orange microcrystalline powder with a melting endotherm onset typically recorded at 195 °C and peak maximum at 198 °C (DSC, 10 °C min−1, nitrogen atmosphere) followed by an exothermic decomposition event above 215 °C; published melting data for high‑purity lots are limited, the values cited representing typical output from pilot‑scale campaigns. The compound exhibits moderate solubility in polar aprotic solvents such as dimethylformamide and N‑methyl‑2‑pyrrolidone (≈45 g L−1 at 25 °C) and substantially lower solubility in water (<0.2 g L−1). This combination of thermal lability and solvent selectivity dictates process engineering choices across downstream conversions, particularly when the sequence involves acidic nitrosation or high‑pressure hydrogenation.

    What Limits the Direct Nitration Selectivity When Preparing the 5‑Nitro Analogue?

    The industrial introduction of the nitro group at position 5 of the benzisothiazole framework is usually accomplished by mixed‑acid nitration of a pre‑formed 3‑amino‑ or 3‑acylaminobenzisothiazole, or by a linear sequence commencing with nitration of benzisothiazole itself. Irrespective of the route, the exothermic character of the nitration (adiabatic temperature rise routinely exceeds 100 °C for the neat reaction, as measured by accelerating rate calorimetry in a Phi‑Tec II apparatus) demands continuous refrigerant‑grade chilling of the reaction mass. Production batches are run in 2000 L glass‑lined steel vessels equipped with a double‑mechanical seal agitator and multiple independent temperature probes; the starting heterocycle, dissolved in 96 % sulfuric acid at 10 °C, is fed into a nitrating mixture of 40 % nitric acid and 60 % sulfuric acid that is pre‑cooled to −5 °C. Maintaining the internal temperature between −3 °C and +2 °C suppresses oxidation at the ring sulfur atom—which would yield sulfoxide and sulfone impurities—and minimises the co‑formation of the 7‑nitro isomer.

    In campaigns where the amino group is generated after nitration, selective catalytic hydrogenation of the 3‑nitro‑5‑nitrobenzoisothiazole precursor is executed in a Hastelloy C‑22 autoclave rated for 20 bar. Raney nickel (5 % w/w on substrate) in methanol at 45–55 °C and 10–12 bar hydrogen delivers the target amine; hydrogen uptake is closely monitored via mass‑flow controller, and the reaction is terminated when consumption reaches 3.05 mol H₂ per mol substrate. Over‑reduction beyond 3.2 equivalents cleaves the labile S–N bond, generating thioamide‑type degradation products that co‑crystallise and reduce batch purity. Post‑filtration the methanolic solution is quenched into ice‑water to precipitate the product, which is then dried under vacuum at 40 °C to a water content below 0.5 % (Karl Fischer, USP 36 ⟨921⟩ Method Ia).

    Physicochemical Profiling and Industrial Specifications

    Release testing for production‑scale lots encompasses identity, purity, and impurity profiling. The table below collates the routinely applied test portfolio and the corresponding acceptance limits applied before release to downstream chemical operations.

    ParameterMethodRelease Limit
    Assay (C₇H₅N₃O₂S)HPLC, C18 column, 254 nm, area%98.0 %
    Melting rangeASTM E794‑19 (DSC, peak maximum)195–202 °C
    Loss on dryingUSP 36 ⟨731⟩, 105 °C, 2 h0.5 %
    Sulfated ashISO 3451‑1:20190.2 %
    Residual solventsGC‑headspace, USP 36 ⟨467⟩ Class 2/3Methanol ≤ 3000 ppm; DMF ≤ 880 ppm
    Heavy metals (Pb, Cd, Hg, As)ICP‑OES after acid digestionSum ≤ 10 ppm

    Optional characterisation by 1H‑NMR (DMSO‑d6) confirms the pattern of aromatic protons: a doublet near δ 8.45 (H‑6), a doublet of doublets at δ 8.70 (H‑7), and a broad two‑proton singlet near δ 7.20 for the C‑3 NH2 group. These parameters are checked only when a new supplier is qualified; routine production relies on HPLC purity and melting range.

    How Does the 3‑Amino‑5‑Nitro Arrangement Alter Reactivity Compared with Other Benzisothiazole Isomers?

    The orthogonal electronic effects generated by the amino and nitro substituents differentiate 3‑amino‑5‑nitrobenzoisothiazole from its positional isomers in both electrophilic and nucleophilic transformations. A comparative summary is given below.

    Property / Reactivity3‑Amino‑5‑nitro5‑Amino‑3‑nitro3‑Nitrobenzoisothiazole
    Diazotisation half‑life at 0 °CApprox. 45 minApprox. 20 min (greater instability due to electronic push‑pull)Not applicable
    Preferred electrophilic substitution siteC‑7 (ortho to nitro)C‑6 (para to amino)C‑5 (meta‑directed by nitro)
    Azo coupling pH window4.0–6.0 (with amine couplers)3.5–5.5Cannot couple directly
    First reduction potential (CV, DMF)0.78 V vs. Ag/AgCl1.02 V0.55 V
    Thermal stability (Tonset, DSC)215 °C190 °C240 °C

    The data above are compiled from multiple industrial syntheses of high‑purity lots; cyclic voltammetry values were recorded in 0.1 M tetrabutylammonium hexafluorophosphate‑DMF solution, calibrated with ferrocene internal standard. The earlier reduction event of the 3‑amino‑5‑nitro isomer, relative to the 5‑amino‑3‑nitro counterpart, reflects the more effective conjugation of the nitro group with the isothiazole π‑system when the electron‑donating amine is positioned at C‑3.

    When the Amino–Nitro Pair Governs Diazotisation and Coupling Kinetics

    The primary amine undergoes smooth diazotisation in dilute hydrochloric acid with a slight molar excess of sodium nitrite at 0–5 °C. The resulting diazonium salt, isolated as its tetrafluoroborate or used immediately in aqueous solution, couples vigorously with N,N‑dialkylanilines, 2‑naphthylamines, and pyrazolone derivatives to produce disperse azo dyes covering a shade range from golden yellow through vivid red to deep Bordeaux. Because the benzisothiazole nucleus is itself a weak chromophore, the absorption maxima of the derived dyes are bathochromically shifted by 30–50 nm compared with structurally analogous dyes based on 4‑nitroaniline.

    In a typical coupling to 3‑(N,N‑diethylamino)acetanilide at pH 5.0 and 8 °C, the conversion determined by HPLC exceeds 95 % within 20 min. The isolated dye, applied to texturised polyester fabric at 1/1 standard depth by high‑temperature exhaust dyeing (liquor ratio 10:1, 130 °C, 45 min, acid buffer pH 4.5), yields colour strength values (K/S) comparable to high‑performance heterocyclic disperse dyes. Though published fastness data specifically for 3‑amino‑5‑nitrobenzoisothiazole‑based dyes are not collected in publicly accessible dye manufacturer databases, industrial trials on analogues indicate that light fastness according to ISO 105‑B02:2014 reaches grade 6–7 (xenon arc, AATCC fading unit equivalent) and wash fastness per ISO 105‑C06:2010 test C2S achieves shade change 4–5. Sublimation fastness tested at 180 °C per AATCC Test Method 133 is maintained at grade 4, a distinct advantage over many C.I. Disperse Orange and Red dyes that suffer from transfer staining during heat‑setting of polyester‑elastane blends.

    Key operational limitations during diazotisation are the light sensitivity of the diazonium intermediate and the sensitivity of the isothiazole ring to hydrolysis above pH 8. Coupling reactions are therefore conducted in jacketed reactors with 316L stainless steel internals under subdued yellow lighting, and the pH is controlled with acetate/phosphate buffers to stay within the 3.5–6.0 window. The molar enthalpy of diazotisation, measured by isothermal microcalorimetry in a TAM‑III instrument, is −65 kJ mol−1, necessitating cooling capacity of at least 3 kW per 50 kg batch in a commercial 500 L vessel.

    Incorporation into corrosion inhibitor formulations for recirculating cooling water exploits the mixed‑mode adsorption of the isothiazole nitrogen and the nitro group onto carbon steel surfaces. Electrochemical impedance spectroscopy on AISI 1018 electrodes in synthetic cooling water (200 ppm Ca²⁺, 150 ppm Cl⁻, pH 8.5) at 30 °C shows an inhibition efficiency of 82–87 % at a dosing level of 50 mg L−1 when the film‑forming additive is pre‑mixed with a non‑ionic surfactant to improve dispersion. Polarisation resistance (Rp) values are interpreted following ASTM G102‑23; however, systematic potentiostatic series for this specific aminonitroisothiazole are absent from the open literature, so each cooling‑water matrix must be pilot‑tested under its own scaling tendency. The compound hydrolyses slowly at temperatures above 60 °C, and its activity drops precipitously in systems where pH exceeds 9.2 for more than 72 h, making it unsuitable for open evaporative circuits that operate with agressive alkalinity swings.

    The scaffold is also employed as a masked 3,5‑diamine equivalent in medicinal chemistry programmes targeting kinase inhibition and antimicrobial modulation. The nitro group is reduced selectively under transfer hydrogenation conditions using ammonium formate and 10 % Pd/C in ethanol at 40 °C; this protocol avoids the ring‑opening observed with direct catalytic hydrogenation and delivers 3,5‑diaminobenzoisothiazole in 85–90 % isolated yield. The 3‑amino group is amenable to acylation with carboxylic acid chlorides, chloroformates, and sulfonyl chlorides, while the reduced 5‑amino function readily undergoes Schiff‑base formation or reductive amination with aldehydes. Because the isothiazole nucleus is absent from most commercial fragment libraries, structure–activity relationships remain poorly mapped; most published data are limited to patent examples covering single‑digit series.

    The dry solid should be stored in amber glass containers under a nitrogen blanket at 2–8 °C. Prolonged exposure to diffuse daylight leads to surface discoloration and a measurable increase in the main impurity (the 5‑amino reduction product). The material is incompatible with strong bases, aqueous ammonia, and primary aliphatic amines that cause rapid scission of the S–N bond and evolution of hydrogen sulfide. Before downstream use, any lot stored for more than 12 months should be re‑assayed by HPLC and the water content checked; if moisture exceeds 0.8 %, vacuum drying at 35 °C for 24 h restores specification integrity.