3-Chloro-1,2-Benzoisothiazole

3-Chloro-1,2-Benzoisothiazole


    • Product Name 3-Chloro-1,2-Benzoisothiazole
    • Alias 3-Chlorobenzothiazole
    • Einecs 220-529-0
    • Mininmum Order 25g
    • 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

    490190

    Chemical Formula C7H4ClNS
    Molar Mass 169.63 g/mol
    Appearance Typically a solid
    Color May be colorless to light - colored
    Odor Characteristic, potentially pungent
    Solubility In Water Low solubility
    Solubility In Organic Solvents Soluble in some organic solvents like dichloromethane
    Melting Point Data varies, specific value needed from reliable source
    Boiling Point Data varies, specific value needed from reliable source
    Stability Stable under normal conditions, but may react with strong oxidizing agents

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

    Packing & Storage
    Packing 500 - gram bottles containing 3 - Chloro - 1,2 - Benzoisothiazole, well - sealed for safety.
    Shipping 3 - Chloro - 1,2 - Benzoisothiazole is shipped in well - sealed containers, compliant with chemical transportation regulations. Packaging ensures protection from external factors during transit to prevent leakage and maintain its integrity.
    Storage 3 - Chloro - 1,2 - Benzoisothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, open flames, and oxidizing agents. Store in a tightly sealed container to prevent moisture and air exposure, which could potentially lead to degradation. Ensure storage is in a location inaccessible to unauthorized personnel.
    Application of 3-Chloro-1,2-Benzoisothiazole

    In the synthesis of the atypical antipsychotic active pharmaceutical ingredients lurasidone and ziprasidone, 3-chloro-1,2-benzisothiazole functions as the electrophilic coupling partner in a nucleophilic aromatic substitution with anhydrous piperazine. The hydrochloride salt of the resulting 3-(piperazin-1-yl)-1,2-benzisothiazole constitutes the penultimate intermediate and must conform to monograph specifications governed by ICH Q7 Good Manufacturing Practice for Active Pharmaceutical Ingredients and enforced through FDA 21 CFR Part 211 current good manufacturing practice for finished pharmaceuticals. Residual solvent limits are set according to ICH Q3C (e.g., toluene class 2 limit 890 ppm, methylene chloride class 2 limit 600 ppm), and single impurity thresholds are reported under ICH Q3A guidelines with identification thresholds at 0.10% and qualification thresholds at 0.15% for a 2 g daily dose. The molar feed ratio of 3-chloro-1,2-benzisothiazole to anhydrous piperazine is controlled in the range 1:1.12 to 1:1.20 to compensate for azeotropic loss of piperazine during cyclohexane or toluene reflux; the substrate concentration in toluene is maintained at 0.8–1.2 M. In production-scale batches executed in 2000–5000 L glass-lined reactors equipped with jacketed temperature control and paddle agitators, the reaction mixture is heated to 110–112°C under Dean‑Stark water removal for 8–14 hours until in-process HPLC analysis (column: C18, mobile phase acetonitrile/phosphate buffer pH 3.0) shows residual 3-chloro-1,2-benzisothiazole below 0.5 area%. A critical process alarm is set at 115°C because thermal ring-opening of the isothiazole produces 2-mercaptobenzamide derivatives that are difficult to purge and raise the total impurity burden above the 0.3% acceptance criterion specified for the downstream API. After completion, the batch is cooled to 0–5°C and hydrochloric acid in ethanol (15–20 wt% HCl) is metered in while maintaining a nitrogen blanket to precipitate 3-(piperazin-1-yl)-1,2-benzisothiazole hydrochloride. The slurry is centrifuged in a bottom-discharge basket centrifuge, the wet cake is washed with pre-cooled isopropanol, and drying proceeds under vacuum (≤10 mbar) at 50°C to a loss-on-drying value below 0.5%. Final product typical purity exceeds 99.7% (HPLC, 230 nm) with the des-chloro dimeric impurity capped at 0.10%. Production experience has documented batch-to-batch colour variability from white to pale yellow requiring ion-chromatographic verification of iron content below 10 ppm to avoid discolouration in the final dosage form; this has necessitated the exclusive use of glass-lined or Hastelloy C-276 piping from the filtration skid onward. The terminal dosage forms are lurasidone hydrochloride tablets (20 mg, 40 mg, 80 mg strengths) and ziprasidone hydrochloride capsules (20 mg, 40 mg, 60 mg, 80 mg), with the benzisothiazole-derived intermediate accounting for approximately 42–48% of the molecular weight of the active moiety.

    Comparative Process Parameters for Lurasidone vs. Ziprasidone Intermediate Manufacture
    ParameterLurasidone RouteZiprasidone Route
    Solvent systemToluene, 5.0 volumesCyclohexane/methyl ethyl ketone 4:1 v/v, 7.0 volumes
    Reaction temperature110 ± 2°C80 ± 2°C
    Reaction duration10–14 h6–9 h
    Isolated yield (free base equiv.)82–88%76–83%
    Primary impurity thresholdDes-chloro dimer ≤ 0.10%Oxidised piperazine adduct ≤ 0.15%
    Drying endpoint (LOD)0.5%0.3%

    A consolidated compliance cross-reference that maps the regulatory frameworks applicable across all downstream domains where 3-chloro-1,2-benzisothiazole is industrially consumed is presented in the following matrix; it spans pharmaceutical, agrochemical, colourant, and advanced material quality systems.

    Regulatory Compliance Matrix by Downstream Application
    Application DomainPrimary Regulatory FrameworkKey Standards / CertificationsTypical Analytical Grade Requirement
    Antipsychotic API intermediatesICH, FDA, EMAICH Q7, FDA 21 CFR Part 211, ISO 9001:2015Purity ≥ 99.5%, single unknown impurity ≤ 0.10%
    PPO-inhibitor herbicide intermediatesEPA, FAOEPA 40 CFR Part 158, FAO Spec. 2019, CIPAC HandbookPurity ≥ 98.0%, water ≤ 0.5%, batch-to-batch consistency
    Disperse dye intermediatesREACH, OEKO-TEX, ZDHCOEKO-TEX Standard 100 (Annex 4), ZDHC MRSL v3.1Amine release below detection limit (30 ppm), purity ≥ 97.0%
    Organic photovoltaic materialsRoHS, IECIEC 61215:2021, RoHS 2011/65/EUPurity ≥ 99.9% by sublimation, halogen residues ≤ 50 ppm
    Kinase inhibitor librariesISO, Institutional EthicsISO 9001:2015, OECD GLP (where pre-clinical)Purity ≥ 95.0%, characterisation by ¹H NMR, MS
    Automotive coating UV-absorber monomersREACH, ASTMREACH Article 33, ASTM D4587-11Purity ≥ 98.5%, inhibitor level 250 ± 50 ppm MEHQ

    Does the 3-Chloro Substituent Enable a Convergent Route to Protoporphyrinogen Oxidase Inhibitors?

    Protoporphyrinogen oxidase (PPO, EC 1.3.3.4) inhibitor herbicides belonging to the pyrimidinedione and triazolinone families can be accessed by nucleophilic displacement of the chlorine atom on 3-chloro-1,2-benzisothiazole with substituted phenols or heterocyclic amines that carry the pro-herbicidal pharmacophore. The electron-withdrawing character of the fused sulfoximine-like heterocycle activates the C–3 position sufficiently for reaction under mild conditions, permitting a convergent late-stage coupling that avoids protecting-group chemistry. The synthesis complies with the data requirements for registration under EPA 40 CFR Part 158 and with the FAO Specifications for Agricultural Pesticides (2019 revision), particularly regarding the identity of the active ingredient, physico-chemical properties, and five-batch analysis conducted according to Collaborative International Pesticides Analytical Council (CIPAC) methods. In the synthetic scheme, 3-chloro-1,2-benzisothiazole is combined with a substituted phenol in a mole ratio of 1:1.02 to 1:1.10, using anhydrous potassium carbonate (1.5 equivalents) as acid scavenger in dimethylacetamide (DMAc) at 80–100°C for 4–6 hours. The benzisothiazole fragment typically accounts for 18–30 wt% of the final herbicide active molecule, conferring flatness and π-stacking affinity for the enzyme’s FAD cofactor. On a 2000 L scale, the crude product is precipitated by controlled addition of water (3 volumes) at 50°C, isolated on a centrifuge, and purified by recrystallisation from methanol to achieve a purity of ≥ 98.0% (HPLC area%, 254 nm). A recognised operational limitation is the generation of dimethylamine from high-temperature decomposition of DMF when it is used as a substitute solvent; the resulting amine undergoes nucleophilic aromatic substitution to form the dimethylamino-benzisothiazole impurity, requiring a solvent switch to DMAc and a nitrogen sparge to keep dimethylamine below 100 ppm in the headspace. The resulting PPO-inhibitor active ingredient is formulated as a suspension concentrate (SC, typically 240–480 g/L) or water-dispersible granule (WDG, 70–80% active ingredient) for pre-emergence and post-emergence application on soybean, maize, and sugarcane. The formulated end-use product must pass storage stability testing per CIPAC MT 46.3, with no more than 5% decomposition after 14 days at 54°C.

    Disperse Dye Chromophore Extension via Diazo Coupling on the Benzisothiazole Scaffold

    The conversion of 3-chloro-1,2-benzisothiazole to 3-amino-1,2-benzisothiazole via Buchwald-Hartwig amination or ammonia substitution yields a diazo component that can be tetrazotised and coupled onto tertiary-amine-capped aniline couplers, producing red-shifted monoazo disperse dyes for polyester fibre. Environmental compliance for textile auxiliaries is governed by OEKO-TEX Standard 100 Annex 4, which sets a detection limit of 20 ppm for each of the listed carcinogenic arylamines cleavable from azo structures, and by the Zero Discharge of Hazardous Chemicals (ZDHC) Manufacturing Restricted Substances List v3.1, which adds restrictions on chlorinated solvents and heavy metal residues. In the coupling protocol, the diazonium salt derived from 3-amino-1,2-benzisothiazole is added dropwise to a solution of the coupling component at a molar ratio of 1:0.98 to 1:1.02, while the pH is continuously adjusted to 3.5–4.5 with sodium acetate buffer and the temperature held at 0–5°C. The resulting azo dye is salted out, filtered, and dried in a tray dryer at 80°C. The terminal products are high-energy disperse dyes suitable for exhaust and thermosol dyeing of polyethylene terephthalate; they are supplied as press cakes (solids content 35–45%) or after standardisation with lignin sulfonate dispersants. A process hazard arises when coupling pH exceeds 6.0, at which point the diazonium salt undergoes rapid decomposition and the released nitrogen causes foaming in the precipitation vessel.

    When Electron-Deficient Heterocycles Are Required for Non-Fullerene Acceptors in Organic Photovoltaics

    In the design of A-D-A-type non-fullerene acceptors for bulk heterojunction organic photovoltaics, the benzisothiazole nucleus delivers a deeper lowest unoccupied molecular orbital (LUMO) compared to benzothiadiazole analogues, an attribute that raises open-circuit voltage when paired with high-lying donor polymers such as PBDB-T. 3-Chloro-1,2-benzisothiazole is incorporated as the halogenated electrophile in Stille or Suzuki cross-coupling polymerisations with distannyl-thiophene or diboronic ester comonomers. The process is conducted under strict oxygen-free conditions (glovebox O₂ < 1 ppm) using Pd₂(dba)₃/P(o-tolyl)₃ catalyst systems. The molar feed of the benzisothiazole monomer is adjusted to 10–50 mol% to tune the acceptor crystallinity. Following polymerisation, crude products are subjected to sequential Soxhlet extraction with methanol, acetone, and chloroform, and the chloroform fraction exhibiting Mn 25–45 kDa (by GPC) is retained. Device qualification follows IEC 61215:2021 for terrestrial photovoltaic modules, with material purity specifications mandating sublimed-grade intermediates having purity ≥ 99.9% and total halogen residues below 50 ppm to avoid charge trapping. Final demonstrator cells are fabricated as inverted architectures (ITO/ZnO/active layer/MoO₃/Ag) and are encapsulated with a barrier film having a water vapour transmission rate below 10⁻³ g/m²/day.

    Benzisothiazole-based targeted covalent inhibitors (TCIs) demand high-purity 3-chloro-1,2-benzisothiazole as the hinge-binding motif electrophile for irreversible inhibition of non-receptor tyrosine kinases, including Bruton’s tyrosine kinase (BTK) and certain epidermal growth factor receptor (EGFR) mutants. The compound serves as a starting material in parallel medicinal chemistry libraries where the chlorine atom is displaced by a diverse set of aliphatic and aromatic amines under mild conditions (25–40°C, acetonitrile, 3.0 equivalents of N,N-diisopropylethylamine). The typical addition ratios in library synthesis use 1.3 equivalents of amine nucleophile relative to 3-chloro-1,2-benzisothiazole to drive the reaction to completion within 12 hours, after which the crude compound is purified by automated flash chromatography (Biotage® system, gradient ethyl acetate/heptane) to achieve purity ≥ 95%. Quality assurance for research-grade material is aligned with ISO 9001:2015 and, where data are intended for IND-enabling studies, with OECD Principles of Good Laboratory Practice. Because the free base of unsubstituted 3-amino-benzisothiazole is susceptible to aerial oxidation forming sulfoxide degradants, laboratory handling protocols specify storage under argon at −20°C and the addition of 50 ppm butylated hydroxytoluene for solutions stored longer than 24 hours. This application does not produce a commercial pharmaceutical directly; the terminal outputs are milligram-to-gram quantities of structure-activity relationship compounds that are screened in biochemical kinase assays (e.g., IC₅₀ determination using HTRF technology) and subsequently profiled in selectivity panels.

    The Heterocycle Serves as a Core for Polymerisable UV Absorbers in Automotive Clearcoats

    Benzisothiazole esters equipped with a terminal methacrylate or acrylate handle are co-polymerised into acrylic polyols for two-component polyurethane clearcoats used in automotive OEM and refinish applications, where long-term ultraviolet (UV) durability is required. The 3-chloro substituent is employed to attach a hydroxy-functional spacer via etherification, after which the hydroxyl group is esterified with methacrylic anhydride. Statutory compliance for the cured coating falls under REACH Article 33 communication duties for substances of very high concern and the performance benchmark is ASTM D4587-11 (Standard Practice for Fluorescent UV-Condensation Exposures of Paint and Related Coatings). The polymerisable UV absorber is dosed into the acrylic monomer feed at 1.5–3.0 wt% and subjected to free-radical solution polymerisation in butyl acetate with an initiator level of 1.5 mol% azobisisobutyronitrile at 85°C. The resulting polyacrylate has a glass transition temperature near 45°C and a weight-average molecular weight of 8 000–12 000 g/mol. After crosslinking with hexamethylene diisocyanate trimer, accelerated weathering tests show less than 10% gloss reduction after 3000 hours of QUV-B exposure. A noted formulation restriction is the incompatibility with strong Lewis acid catalysts such as dibutyltin dilaurate at concentrations above 0.05 wt%, which can de-coordinate the benzisothiazole heteroatom and trigger undesirable chromophore bleaching, so catalyst levels must be kept in the 0.01–0.03 wt% range and chelated titanate alternatives evaluated before factory-scale deployment.

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    Certification & Compliance
    More Introduction

    The heterocyclic intermediate 3-chloro-1,2-benzoisothiazole (CAS 3042-06-8; molecular formula C₇H₄ClNS; molecular weight 169.63 g/mol) is produced as a pale yellow to off-white crystalline solid with a melting range of 38–41°C determined by capillary method per ASTM E324-16. Its primary industrial significance lies in its role as a near-stoichiometric precursor to 1,2-benzisothiazolin-3-one (BIT), a broad-spectrum biocide employed in metalworking fluids, latex paints, adhesives, and papermaking. Unlike the finished biocide, 3-chloro-1,2-benzoisothiazole exhibits no intrinsic antimicrobial activity; the chlorine substituent at the 3-position of the fused thiazole ring serves as a leaving group that must be displaced by hydroxide ion to generate the active isothiazolinone pharmacophore. Commercial grades are supplied with a minimum purity of 98.5% (GC-FID area%, internal method based on ISO 17025), a moisture content below 0.2% (ISO 760), and a sulfated ash residue of less than 0.1%. These specifications are critical because residual moisture or ionic impurities can catalyse premature hydrolysis during storage or compromise the yield of subsequent BIT synthesis in aqueous alkaline media.

    Representative Specification for Industrial-Grade 3-Chloro-1,2-Benzoisothiazole
    ParameterMethodSpecification
    AppearanceVisualPale yellow crystalline solid
    Purity (GC-FID)GC, 30 m DB-5, FID, area%98.5%
    Melting rangeASTM E324-16 (capillary)38–41°C
    Moisture (Karl Fischer)ISO 7600.2% w/w
    Sulfated ashISO 3451-10.1%
    Chloride (as Cl⁻)Ion chromatography after hydrolysis0.05%
    Storage lifeSealed under N₂, 2–8°C12 months

    Why Hydrolysis to BIT Demands Strict Temperature Control

    The conversion of 3-chloro-1,2-benzoisothiazole to 1,2-benzisothiazolin-3-one involves dosing the solid into aqueous sodium hydroxide at 20–25% w/w in a glass-lined reactor. The reaction is exothermic; while published enthalpy data for this specific configuration are limited, estimates from analogous chloroisothiazole hydrolyses place ΔH near -130 kJ/mol. At pilot scale, the reaction mass must be held between 0°C and 10°C to suppress formation of the ring-opened by-product 2-mercaptobenzamide, which consumes base and reduces BIT purity below 99%. If the internal temperature exceeds 15°C, hydrolysis accelerates autocatalytically through liberated chloride acting as a nucleophilic catalyst; a mandatory overflow line to a chilled secondary containment vessel is then activated. All wetted parts are restricted to PTFE or glass, as the HCl-laden vapor phase corrodes 316L stainless steel at rates exceeding 0.1 mm/year. In campaigns surpassing 500 kg batch size, solid addition is regulated by a load-cell-controlled screw feeder with a jacket brine temperature setpoint of -15°C and a maximum dosing rate of 3.5 kg/min. Post-reaction, the BIT slurry is acidified to pH 4–5 and dewatered in a centrifuge fitted with polypropylene cloth. Residual 3-chloro-1,2-benzoisothiazole content is quantified by HPLC (C18, UV 280 nm) with an accept/reject limit of ≤ 0.1% area. The resulting BIT’s conformity to ISO 11930 preservative efficacy protocols is directly linked to this purity threshold. Under EU REACH Regulation (EC) No 1907/2006, the substance is registered as an intermediate handled under strictly controlled conditions within a tonnage band of 10–100 t/a.

    Storage instability in humid environments cannot be overstated. When exposed to relative humidity above 60%, the solid undergoes surface hydrolysis to BIT, leading to caking and a purity decline to below 97% within 48 hours. Transfer operations are therefore confined to glove boxes purged with dry nitrogen (dew point ≤ -40°C). Drums are double-bagged in aluminium barrier laminate with a humidity indicator card placed on each pallet. Out-of-specification material can be reprocessed by recrystallization from anhydrous toluene (water content <50 ppm by coulometric KF) at a concentration of 200 g/L, achieving typical recovery rates of 85–90%. The recrystallized product must be re-qualified against all specification parameters before release for BIT manufacturing.

    Chlorine Displacement Reactivity: A Comparison with 2-Chlorobenzothiazole

    The S–N bond in the 1,2-benzisothiazole ring system imparts a significantly higher reactivity toward nucleophilic aromatic substitution compared to benzothiazole congeners. Under identical conditions (0.1 M piperidine in DMF, 25°C), the half-life for chloride displacement from 3-chloro-1,2-benzoisothiazole is on the order of minutes, while 2-chlorobenzothiazole requires prolonged heating above 80°C for a comparable extent of conversion. This disparity influences hybrid process designs where one-pot cascade reactions are employed for pharmaceutical intermediates; the high reactivity of the benzisothiazole halide must be managed through programmed temperature ramps or protection-deprotection strategies. Beyond mere kinetics, the toxicity profiles diverge: both BIT and its chloro precursor are classified as skin sensitizers (GHS07, H317), but the intermediate carries a higher acute aquatic hazard, with 96‑h LC50 values for fish falling in the range 1–10 mg/L, whereas BIT typically lies in the 10–100 mg/L band. This demands dedicated wastewater pre-treatment—usually inline neutralization followed by activated carbon adsorption— before discharge, in accordance with an ISO 14001-certified environmental management plan. A further distinction exists with methylisothiazolinone (MIT) and its chlorinated analogue CMIT: those molecules possess an N-methyl group that permits direct dehydrogenase inhibition, whereas 3-chloro-1,2-benzoisothiazole is a pro-biocide, exhibiting antimicrobial activity only after hydrolysis to the unsubstituted isothiazolinone.

    Comparative Nucleophilic Displacement Reactivity (Conditions: 0.1 M piperidine in DMF, 25°C)
    Substratet₁/₂ for chloride displacementApprox. relative rate
    3-Chloro-1,2-benzoisothiazole<5 min1 (reference)
    2-Chlorobenzothiazole> 600 min (requires heating)<0.008
    3,5-Dichloro-1,2-thiazole~ 120 min~ 0.04

    When Pre-Dried Solvent is Non-Negotiable in Grignard Reactions Using This Intermediate

    Beyond hydrolysis, 3-chloro-1,2-benzoisothiazole serves as an electrophile in cross-coupling reactions that install carbon-based substituents on the benzisothiazole scaffold for agrochemical and pharmaceutical discovery. In a typical Negishi protocol, the chloride undergoes oxidative insertion with magnesium turnings in THF to form the corresponding Grignard reagent. Rigorous anhydrous conditions are mandatory: THF must be distilled from sodium/benzophenone ketyl until a persistent blue colour is obtained, with final water content verified below 50 ppm by coulometric Karl Fischer titration (ISO 760). Schlenk-line techniques or an inert-atmosphere glovebox (O₂ < 5 ppm) are employed throughout. Published yields of the coupled product exceed 85% when moisture is controlled, but drop to less than 20% if THF contains more than 50 ppm water, as the intermediate organomagnesium species is immediately protonated. The stark sensitivity contrasts with the behaviour of 2-chlorobenzothiazole, which tolerates trace moisture more readily in Grignard formation, albeit with slower initiation. For process-scale work, the THF distillate is stored over activated 4 Å molecular sieves and the magnesium is activated by iodine or dibromoethane prior to addition. Batch records from multi-kilogram campaigns document an induction period of 15–20 minutes with an exotherm that plateaus at 45–50°C; exceeding 55°C initiates homocoupling side-reactions that reduce the yield of the desired benzisothiazole adduct.

    In the context of BIT manufacturing, process water generated after hydrolysis is typically saturated with sodium chloride (≈ 26% w/w) and carries residual levels of the chlorinated precursor. Direct disposal without treatment is precluded by local consent limits that commonly set a chronic toxicity threshold (NOEC) for the parent compound at <0.01 mg/L in receiving waters. Skid-mounted treatment units incorporating a pH adjustment stage to 6–8, a multi-media filtration step, and two granular activated carbon columns in series reduce total organic halogen (AOX) to below 0.5 mg/L, allowing discharge compliance under the Industrial Emissions Directive (2010/75/EU). Spent carbon is thermally regenerated off-site, and the process is audited bi-annually against ISO 14001 objectives. When the chlorinated intermediate is used outside of BIT synthesis—for instance, in medicinal chemistry scaffolds—the aqueous waste stream must be quenched with sodium sulfite to destroy residual electrophilic species before release to biological treatment, as standard activated sludge consortia are inhibited at concentrations above 20 mg/L of the halide, measured by HPLC-MS.