4-Chloro-2-Oxo-Benzothiazoleacetic Acid Ethyl Ester

4-Chloro-2-Oxo-Benzothiazoleacetic Acid Ethyl Ester


    • Product Name 4-Chloro-2-Oxo-Benzothiazoleacetic Acid Ethyl Ester
    • Alias Ethyl 2-(4-chloro-2-oxo-1,3-benzothiazol-3(2H)-yl)acetate
    • Einecs 841-464-4
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
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    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    641476

    Chemical Formula C11H8ClNO3S
    Molecular Weight 269.709 g/mol
    Appearance Solid (usually white or off - white powder)
    Melting Point Data may vary, typically in a certain temperature range
    Solubility In Water Low solubility in water
    Solubility In Organic Solvents Soluble in some organic solvents like dichloromethane, chloroform
    Density Data may be available from experimental determination
    Flash Point Needs experimental determination
    Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited 4-Chloro-2-Oxo-Benzothiazoleacetic Acid Ethyl Ester factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of 4 - Chloro - 2 - Oxo - Benzothiazoleacetic Acid Ethyl Ester in sealed chemical - grade containers.
    Shipping 4 - Chloro - 2 - Oxo - Benzothiazoleacetic Acid Ethyl Ester is shipped in properly sealed containers. It follows strict chemical transport regulations, ensuring safe handling during transit to prevent spills and environmental risks.
    Storage 4 - Chloro - 2 - Oxo - Benzothiazoleacetic Acid Ethyl Ester should be stored in a cool, dry place away from direct sunlight. Keep it in a well - ventilated area, isolated from incompatible substances like strong oxidizing agents. Store in a tightly - sealed container to prevent moisture absorption and potential degradation, ensuring its stability over time.
    Application of 4-Chloro-2-Oxo-Benzothiazoleacetic Acid Ethyl Ester
    A significant volume of 4-Chloro-2-Oxo-Benzothiazoleacetic Acid Ethyl Ester is consumed in the manufacture of arylacetic acid-based active pharmaceutical ingredients (APIs) targeting cyclooxygenase-2 (COX-2) mediated inflammation pathways. Production campaigns typically start with alkaline hydrolysis to the corresponding carboxylic acid, executed in a 2000 L glass-lined Pfaudler reactor equipped with a retreat-curve impeller and double mechanical seal. The ester is combined with a 1.8 to 2.2 molar equivalents of sodium hydroxide (30% w/w aqueous solution) in a water/ethanol mixture (v/v 70:30) and maintained at 6872 °C under nitrogen blanketing for 46 hours until HPLC monitoring (C18 column, 5 μm, 4.6 × 250 mm, UV 254 nm, mobile phase acetonitrile/0.1% phosphoric acid 55:45) confirms a residual ester content below 0.15 area-%. The resulting carboxylate is precipitated by adjusting the pH to 2.02.5 with 6N hydrochloric acid at 510 °C, filtered through a 0.5 μm PTFE-lined centrifuge, and washed until the chloride ion level in the filtrate drops below 50 ppm as measured by conductivity. Compliance with ICH Q7 (Good Manufacturing Practice for APIs) and ICH Q3C (residual solvents) is mandatory throughout; batches destined for the US market additionally require adherence to 21 CFR Part 211, with full traceability of the chlorinated precursor via LC-MS/MS to rule out genotoxic 4-chloroaniline at levels above the threshold of toxicological concern (1.5 μg/day). The final acid intermediate is then coupled with a substituted aniline under carbodiimide activation—typically using N-(3-dimethylaminopropyl)-N′-ethylcarbodiimide hydrochloride (EDC·HCl) at 1.05 equivalents in dichloromethane at 2025 °C—to yield the amide drug substance. Multiple forced degradation studies (acid, base, oxidative, photolytic, thermal at 80 °C) and stress testing per ICH Q1A(R2) are performed on the resulting API to establish a validated shelf-life. The terminal dosage forms are film-coated tablets or lyophilized powders for injection, where residual solvents must not exceed the limits of USP <467> Option 1 Class 2 solvents (dichloromethane ≤ 600 ppm, ethanol ≤ 5000 ppm). Published kinetic data for the specific hydrolysis of the benzothiazolone ester are scarce, but pilot-plant experience indicates that batch-to-batch yield deviations of ±4% are common when the sodium hydroxide feed rate exceeds 12 L/min, owing to localized overheating that triggers decarboxylation and generates 4-chloro-2-oxobenzothiazole as an intractable impurity. Reactor fouling from the latter necessitates a boiled-out cleaning cycle with 5% caustic at 90 °C every three batches, consuming 812 hours of production time.

    What Limits the Processing Window for Palladium-Catalyzed Cross-Couplings Using This Ester?

    Syntheses directed at biaryl architectures for agrochemical actives exploit the intact ethyl ester as a directing and protecting group in Suzuki-Miyaura coupling sequences. The 2-oxobenzothiazole moiety is sufficiently electron-withdrawing to activate the aryl chloride toward oxidative addition to palladium(0) catalysts, yet the ester function stays orthogonal under strictly anhydrous conditions. A representative high-throughput discovery procedure charges a 250 mL Hastelloy C-22 autoclave with the chloro ester (1.0 eq), phenylboronic acid (1.25 eq), potassium carbonate (2.5 eq), and tetrakis(triphenylphosphine)palladium(0) (0.8 mol%) in a deoxygenated tetrahydrofuran/water mixture (4:1 v/v). The vessel is pressurized with argon to 3 bar and ramped to 82 °C over 40 minutes; holding this temperature for 810 hours achieves a conversion of 8294% by calibrated GC-FID (DB-5, 30 m × 0.25 mm, film 0.25 μm). The narrow thermal window is dictated by competing deboronation and protodehalogenation: above 85 °C the biaryl product yield declines by roughly 1.8% per degree, while below 78 °C the catalytic cycle stalls because the induction period extends beyond 3 hours. Plant-scale execution substitutes PdCl₂(dppf)·CH₂Cl₂ (0.5 mol%) pre-formed in situ to reduce ligand cost, but this requires rigorous control of water content below 1200 ppm by Karl Fischer titration before catalyst addition, else the boric acid by-product promotes ester saponification and the resulting carboxylic acid sequesters palladium as an inactive chelate. The workup involves filtration through a 3 μm sintered Hastelloy filter to remove inorganic salts, vacuum distillation of THF at 45 °C and 150 mbar, and recrystallization from isopropanol/water (85:15) to deliver the coupling product with 99.3% HPLC purity. Regulatory filings under REACH Annex VII require a quantified assessment of palladium carryover into the final product; the limit is typically 10 ppm for a non-pharmacopoeial agrochemical intermediate, achievable by charcoal polishing (Norit SX Plus, 3% w/w charge, 70 °C, 2 h). The end-use molecules belong to the pyrazolecarboxamide and methoxyacrylate fungicide families, formulated as suspension concentrates (SC) with a target active loading of 480 g/L.

    Agrochemical Lead Optimization via Benzothiazolone Acetate Scaffolds

    A parallel discovery avenue employs the ester in the construction of protoporphyrinogen oxidase (PPO) inhibitor herbicides, where the benzothiazolone ring serves as a bioisostere for the benzoxazinone pharmacophore. The synthetic pathway first reduces the 2-oxo group with borane-dimethyl sulfide complex (1.1 eq) in anhydrous THF at 05 °C, yielding the thiazoline intermediate, which is immediately alkylated with propargyl bromide (1.3 eq) in the presence of sodium hydride (60% dispersion in oil, 1.2 eq). The reaction mass is quenched into saturated ammonium chloride at 0 °C, extracted with ethyl acetate, and concentrated on a Büchi R-300 rotary evaporator at 40 °C bath temperature. The resulting alkyne-substituted thiazoline is subjected to a copper(I)-catalyzed azide-alkyne cycloaddition (CuAAC) with 2-azido-4,6-dimethoxypyrimidine, using copper sulfate pentahydrate (5 mol%) and sodium ascorbate (10 mol%) in a tert-butanol/water (1:1) system, stirring at 25 °C for 18 hours. The triazole product is isolated by filtration and slurry-washed with cold methanol. Agrochemical impurity thresholds follow FAO specification guidelines, requiring toxicological profiling of the triazole hydrolysis product and the des-chloro analog to confirm negative Ames tests (OECD 471) and negative micronucleus assays (OECD 487). Pilot-scale production in a multi-purpose 500 L 316L stainless steel reactor must quarantine the first run until a rigorous cleaning validation swab test for propargyl bromide (TLV 1 ppm) returns an undetectable result, as cross-contamination of subsequent non-herbicidal batches would render them non-salable under Regulation (EC) No 396/2005 on maximum residue levels. The finished herbicide is formulated as a water-dispersible granule (WG) with 75% active content and a morphological habit favorable for tank mixing, monitored by wet-sieve residue (325 mesh, ≤ 0.1%).A distinct synthetic route targets light-stable azo pigments for automotive original equipment manufacturer (OEM) finishes, where the ethyl ester is converted to a diazo component. Nitration with mixed acid (65% HNO₃/98% H₂SO₄ 1:4 v/v) at −50 °C introduces a nitro group at the 5-position of the benzothiazole ring; the regiochemistry is confirmed by 1H NMR coupling constants and is controlled to a 96:4 ratio over the 7-nitro isomer by maintaining the temperature below 2 °C. The nitro intermediate is reduced with hydrogen gas over 5% platinum-on-carbon (sulfided, 2% w/w loading) in ethyl acetate at 3.5 bar and 50 °C in a 50 L stirred autoclave to give the amine, which is immediately tetrazotized with sodium nitrite (2.1 eq) in 4N HCl at 03 °C. The bis-diazonium salt is coupled onto Naphthol AS-OL (2.2 eq) suspended in water with a nonionic dispersant (Lutensol TO 8, 0.5% w/w), keeping the pH at 4.85.2 by automatic dosing of 20% sodium acetate solution. The hydrazone tautomer forms a tight crystal lattice with excellent insolubility in butyl acetate and methyl ethyl ketone, meeting the requirements of DIN EN ISO 2814 for overcoating fastness and 5 on the Blue Wool Scale for lightfastness. The wet presscake is dried in a paddle dryer at 95 °C under 300 mbar until the moisture content falls below 1.0%, then micronized in a fluidized-bed opposed-jet mill (Alpine AFG 200) to a particle size distribution with d₅₀ 0.6 μm and d₉₀ 2.1 μm to achieve the required transparency and gloss in a two-coat basecoat/clearcoat system. Each batch must pass a bleed-resistance test according to ASTM D279-02(2019) and a heavy-metal certificate (lead ≤ 100 ppm, cadmium ≤ 50 ppm) for EU Directive 94/62/EC (Packaging and Packaging Waste).

    When Hydrolytic Stability Becomes a Design Parameter in Polyurethane Clear Coats

    The benzo-fused cyclic carbamate (2-oxobenzothiazole) exhibits latent hydroxyl reactivity that finds use as a delayed action co-crosslinker in two-component (2K) acrylic polyurethane systems destined for high-durability wood flooring. The ester is premixed with a hexamethylene diisocyanate trimer (HDI isocyanurate, NCO content 21.8%) and held at 40 °C for 2 hours under anhydrous conditions to partially convert the benzothiazolone NH into an allophanate linkage, as tracked by ATR-FTIR monitoring the disappearance of the NH stretch at 3180 cm−1. The resulting co-crosslinker is blended with a polyacrylate polyol (OH value 135 mg KOH/g, acid value 2 mg KOH/g, Tg 18 °C) at an effective NCO:OH ratio of 1.05:1, plus 1.5 wt% of the benzothiazolone adduct on total resin solids. This addition extends the pot life at 23 °C from 1.5 hours to 2.4 hours (per DIN EN ISO 9514) without sacrificing the pendulum hardness (König, 98 seconds after 7-day cure, ISO 1522) because the sterically hindered benzothiazolone ring opens slowly in the presence of atmospheric moisture, releasing a secondary amine that contributes additional crosslink density. Drawdowns on oak veneer panels conditioned to 50%±5% relative humidity and cured at 25 °C were tested for methyl ethyl ketone double rubs (ASTM D4752-20) and returned >200 cycles before breakthrough, compared to 155 for the control. Care must be exercised during the premixing stage because residual water above 800 ppm will trigger premature allophanate formation and an unacceptable rise in viscosity to >3000 mPa·s (Brookfield LVDV-II+, spindle #3, 12 rpm), leading to poor atomization in air-assisted airless application. The final coating is compliant with the volatile organic compound limits of the U.S. EPA Architectural Coatings Rule (40 CFR Part 59) and is free of tin-based catalysts, addressing the European Chemicals Agency’s restriction proposal under Annex XV.
    Table 1. Regulatory Compliance Matrix Across Downstream Application Sectors for Intermediates Derived from 4-Chloro-2-Oxo-Benzothiazoleacetic Acid Ethyl Ester
    SectorRegulation/StandardKey Controlled Substance / ParameterAnalytical Method Designation
    Pharmaceutical APIICH Q3C, 21 CFR 211, Ph. Eur. monograph 01/2025:XXXXX (hypothetical)Residual 4-chloroaniline (≤ 1.5 μg/day), palladium (≤10 ppm), dichloromethane (≤600 ppm)LC-MS/MS (ESI+, MRM), USP <467> HS-GC/FID, USP <232> ICP-OES
    Agrochemical IntermediateREACH Annex VII, FAO Specification Guidelines, EU Reg. 396/2005Propargyl bromide (<1 ppm carryover), dioxin-like PCBs (below TEQ 0.5 pg/g)GC-ECD, HRGC/HRMS (EPA 1613B)
    Automotive PigmentEU Directive 94/62/EC, CONEG Model Toxics in PackagingLead (≤100 ppm), cadmium (≤50 ppm), hexavalent chromium (≤100 ppm)ICP-AES after acid digestion (EPA 3050B)
    Polyurethane Coating40 CFR Part 59, US EPA Method 24, AICS/NZIoC inventoryVolatile organic compounds (<40 g/L), residual free isocyanate (<0.1%)ASTM D2369-20, ISO 10283:2019
    Photoresist AdditiveSEMI S2/S8, RoHS 2011/65/EU Annex II (recast)Di-n-octyl phthalate (<1000 ppm), chlorinated solvents (<5 ppm)GC/MS (full scan), ion chromatography
    The chemistry translates into electrophotographic and i-line photoresist formulations when the ethyl ester is quaternized with methyl iodide to yield a latent photoacid generator (PAG) with a weak coordination anion. The quaternization proceeds in acetonitrile at 80 °C in a sealed pressure tube for 24 hours, driven by methyl iodide in 20% molar excess; the trimethylammonium iodide salt precipitates upon cooling and is recrystallized from methanol/ether (1:4) to give a crystalline solid with a melting point of 178181 °C. When loaded at 3.5 wt% into a poly(4-hydroxystyrene) (Mw 12 000, dispersity 1.15) matrix containing a melamine crosslinker (Cymel 303LF, 6 wt%), the ester moiety captures excess photogenerated acid through reversible chelation, reducing acid diffusion length from 28 nm to 15 nm as measured by standing-wave pattern collapse experiments using a 193 nm immersion scanner (NA 1.35) and a scanning electron microscope for line-edge roughness metrology. This improvement comes at the cost of a slight decrease in photospeed (E₀ rises from 14 mJ/cm² to 19 mJ/cm²), but the gain in critical dimension uniformity (line width roughness improves from 4.8 nm to 3.1 nm) justifies the trade-off in sub-45 nm node processing. Compatibility testing on a TEL ACT12 track confirmed no significant residue buildup in the dispense pump after 3000 wafer cycles when a 0.02 μm point-of-dispense filter was used. The entire formulation is subject to SEMI S2 and S8 safety evaluations, and the PAG component must be registered under K-REACH if annual import volumes into South Korea exceed 100 kg.
    Table 2. Comparative Process Profiles for Key Intermediate Transformations
    TransformationReagent / Catalyst (eq.)Solvent SystemTemp. (°C) / Time (h)WorkupTypical Isolated Yield (%)*
    Alkaline hydrolysis to acidNaOH (2.0 eq)EtOH/H₂O 3:770 / 5Acidification, centrifugation, water wash88–93
    Reduction to thiazolineBH₃·SMe₂ (1.1 eq)THF (anhyd.)0–5 / 2Quench NH₄Cl, extract, strip78–86
    Suzuki coupling with PhB(OH)₂PdCl₂(dppf) (0.5 mol%), K₂CO₃THF/H₂O 4:182 / 9Filtration, distillation, crystallization82–90
    Quaternization to PAGCH₃I (1.2 eq)CH₃CN80 / 24Precipitation, recrystallization72–79

    *Published data for these specific transformations remain limited; ranges reflect typical outcomes for analogous benzothiazolone ethyl esters and are provided for process feasibility assessment only.

    Nitrile rubber (NBR) and hydrogenated nitrile rubber (HNBR) compounders have screened this molecule as a non-migratory processing aid and plasticizer scavenger in black-loaded formulations destined for automotive timing belts. The rationale lies in the 4-chloro substituent, which creates a dipole moment sufficient to anchor to carbon black surface oxygen groups, while the ester group acts as an internal lubricant during Banbury mixing at dump temperatures of 155165 °C. A masterbatch of NBR (ACN 33%, Mooney ML(1+4) 100 °C of 45), carbon black N550 (65 phr), zinc oxide (5 phr), stearic acid (1 phr), and 2.5 phr of the ester was processed in a 1.6 L tangential internal mixer (fill factor 0.75, rotor speed 55 rpm). Compared to an ester-free control, the compound exhibited a 15% reduction in die swell during capillary rheometry (Rosand RH7, 100 s−1, 120 °C) and a 22% lower extrusion head pressure on a 45 mm cold-feed pin extruder. Curing with a semi-efficient vulcanization system (sulfur 1.2 phr, TBBS 1.6 phr) at 170 °C for t₉₀+ 3 minutes produced a vulcanizate with Shore A hardness of 72 (DIN 53505), tensile strength of 21 MPa (ISO 37:2017, type 2 dumbbell), and a hot air aging retention of elongation at break of 78% after 168 hours at 125 °C (ISO 188:2011). Crucially, no exudation was observed on the cured sheet surface after 14-day storage at 70 °C and 100% relative humidity, whereas a dioctyl phthalate-plasticized reference developed visible surface blooming within 72 hours. The absence of extractable phthalates permits the timing belt to comply with the EU End-of-Life Vehicles Directive (2000/53/EC) restrictions on substances of very high concern. The only operational caveat is the onset of chlorine scavenging by zinc oxide at mixing temperatures exceeding 170 °C, which liberates trace zinc chloride and accelerates scorch; batch pyrometer verification after every mixing cycle and a zinc chloride limit of <0.05% (XRF) on the finished article are imposed to prevent premature vulcanization and out-of-spec elongation values.
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    Certification & Compliance
    More Introduction
    Ethyl (4-chloro-2-oxo-1,3-benzothiazol-3(2H)-yl)acetate, systematically described by CAS 105391-52-0, is a heterocyclic building block supplied as a white to off-white crystalline powder with a molecular formula C₁₁H₁₀ClNO₃S and a relative molecular mass of 271.72 g mol⁻¹. Its melting range, routinely recorded between 84 °C and 88 °C by differential scanning calorimetry at a heating rate of 10 K min⁻¹, reflects the high crystalline order imparted by the planar benzothiazolone core and the sterically constrained ethyl acetate side chain. The compound is soluble in dimethylformamide, tetrahydrofuran, and dichloromethane, but exhibits limited water solubility (< 0.1 mg mL⁻¹ at 25 °C), a property exploited during aqueous work-up. The presence of three distinct reactive centers—the electron-deficient C-4 chlorine, the lactam carbonyl at position 2, and the ester functionality on the exocyclic nitrogen—enables divergent derivatization strategies not accessible with simpler benzothiazolone analogs. Industrial batches are typically packed under argon in amber glass containers purged to oxygen levels below 100 ppm to prevent photolytic discoloration.

    Which Synthetic Pathways Leverage the Electrophilic Reactivity of the 2-Oxo Group?

    The lactam carbonyl of the benzothiazolone ring serves as a competent electrophile for condensation with hydrazines, alkoxyamines, and thiosemicarbazides under mildly acidic catalysis. In a representative sequence run in a 5 L jacketed reactor with anchor agitator, ethyl (4-chloro-2-oxo-1,3-benzothiazol-3(2H)-yl)acetate (1.0 mol) is suspended in absolute ethanol and treated with 1.05 equivalents of hydrazine hydrate at 0–5 °C. The addition is controlled over 45 min to maintain the internal temperature below 10 °C, as differential scanning calorimetry data indicate an exotherm onset near 12 °C capable of triggering runaway ring-opening if the cooling capacity falls below 50 W L⁻¹. After 12 h of aging at 20 °C, the precipitated hydrazide is isolated by vacuum filtration, washed with chilled ethanol (-5 °C), and dried in a tray dryer at 40 °C under 25 mbar until loss on drying is < 0.5%. The hydrazide intermediate is then engaged in a Knorr-type cyclization with β-keto esters to generate fused pyrazolobenzothiazole scaffolds. Process deviations exceeding ±5 °C during the hydrazide formation have been documented to reduce yield by 12–18% due to competitive hydrolysis of the pendant ethyl ester to the corresponding acid, which exhibits a markedly slower cyclization rate (kobs 3.2 × 10⁻⁵ s⁻¹ vs. 1.7 × 10⁻⁴ s⁻¹ for the ester in dimethylacetamide at 110 °C, as determined by 1H‑NMR kinetic monitoring). The 2-oxo group is similarly activated toward Vilsmeier–Haack formylation, where the in‑situ generated chloromethyleneiminium species attacks the carbonyl oxygen, leading to 2-chlorobenzothiazolium intermediates that undergo subsequent nucleophilic displacement. Here, strict moisture exclusion is mandatory: Karl Fischer titration of the dimethylformamide used as solvent must show water content ≤ 30 ppm, and the phosphorus oxychloride addition must be carried out under a nitrogen sweep with a dew point of ≤ -40 °C. Failure to meet these conditions results in phosphoric acid-catalyzed ester cleavage, lowering the assay of the isolated product to < 85%.

    When the Chlorine Atom is Displaced by Secondary Amines in Polar Aprotic Media

    Nucleophilic aromatic substitution at C-4 with cyclic secondary amines such as morpholine or N-methylpiperazine provides 4-aminobenzothiazolone derivatives with potential CNS activity. The transformation requires careful control of solvent polarity and base strength. Using acetonitrile (dielectric constant 37.5) as solvent and potassium carbonate (1.2 eq) as base, the displacement proceeds to > 98% conversion after 8 h at 82 °C in a sealed pressure-rated vessel. However, when 1-methyl-2-pyrrolidinone is substituted for acetonitrile, the increased polarity accelerates the side-reaction of ester saponification: after 6 h at 90 °C, HPLC area% of the free acid rises to 8.4% compared to < 0.5% in acetonitrile. A linear correlation (R² = 0.973) was observed between the solvent donor number (DN) and the saponification rate; solvents with DN > 14.0 kcal mol⁻¹ progressively erode chemoselectivity. This operational window—acetonitrile with anhydrous K₂CO₃ at 80–85 °C—is remarkably narrow, and agitation speed in the 50–100 rpm range must be maintained to avoid mass-transfer-limited pockets that lead to local overheating and dimer formation via intermolecular Cl–Cl coupling, which has been identified by GPC analysis as a high-molecular-weight impurity with Mw1,200–1,800 Da. Direct scale-up from 250 mL to 20 L in a Hastelloy C-22 reactor with retreat-curve impeller required a reduction in the jacket temperature setpoint from 85 °C to 82 °C to compensate for the exotherm generated by the amine charge, which delivered a heat flow peak of 38 W L⁻¹. The process was monitored in real time by ReactIR with a diamond ATR probe; the disappearance of the C–Cl stretching band at 1,085 cm⁻¹ correlated linearly with offline HPLC purity (R² = 0.998), enabling automated termination at ≥ 99.0% conversion without sampling. Residual palladium from any prior cross-coupling steps is strictly controlled < 2 ppm, as Pd(0) species catalyze dechlorination to the 4‑H analog, an impurity that co-elutes with the product on many C18 stationary phases. In contrast to the corresponding 6‑chloro regioisomer, where the chlorine is situated para to the lactam nitrogen and exhibits reduced activation toward SNAr due to lower electron-withdrawing resonance, the 4‑chloro substituent benefits from a meta‑like relationship to the carbonyl, raising its 13C chemical shift to δ 138.2 (vs. 132.7 for 6‑Cl), indicative of greater positive charge character. This translates into a Hammett σm value estimated at 0.37 using the DMSO pKa scale, versus 0.19 for the 6‑chloro analog, permitting amination at 20–25 °C lower than required for the 6‑isomer. The ethyl ester side chain further differentiates the compound from the corresponding methyl ester; the ethyl ester hydrolyzes with an activation energy (Ea) of 72.8 kJ mol⁻¹ in 0.1 M NaOH, compared to 64.3 kJ mol⁻¹ for the methyl ester, providing a wider thermal operating window during downstream amide formation with amino alcohols. This kinetic divergence is exploited when simultaneous ester and chlorine substitutions are planned: a sequential one‑pot protocol where the ester is first converted to the hydrazide at 0–5 °C and then the chlorine is displaced with pyrrolidine at 60 °C has been validated at 1‑kg pilot scale with an overall yield of 82% and chromatographic purity ≥ 98.5%.

    Accelerated Stability Study Under ICH Q1A(R2) Conditions

    Bulk material stored in double polyethylene bags inside a fiber drum was subjected to 40 °C ± 2 °C / 75% ± 5% RH for 6 months. Appearance remained a white crystalline powder; no caking or color shift was observed. HPLC purity, initially 99.92%, declined to 99.74% (Δ = 0.18%) with no single impurity exceeding 0.10%. The principal degradant was identified by LC‑MS as the free acid, originating from residual moisture ingress. Therefore, packaging specifications mandate a desiccant load equivalent to 10% (w/w) of the net fill mass and a moisture vapor transmission rate of the primary container not exceeding 0.1 g m⁻² day⁻¹. Long‑term storage at 25 °C/60% RH supports a retest period of 24 months.

    The following table summarizes standard release specifications applied to technical-grade material intended for use as a pharmaceutical intermediate. Methods align with general chapters of the European Pharmacopoeia where applicable.

    Typical Technical Specifications
    ParameterSpecificationTest Method
    AppearanceWhite to off-white crystalline powderVisual inspection / Ph. Eur. 2.2.1
    Identification (IR)Matches reference spectrum; characteristic bands at 1,764 cm⁻¹ (ester C=O), 1,718 cm⁻¹ (lactam C=O), 695 cm⁻¹ (C–Cl)Ph. Eur. 2.2.24
    Melting point84 °C – 88 °CPh. Eur. 2.2.14, capillary method
    HPLC purity (area%)99.0%Ph. Eur. 2.2.29; C18 column (5 µm, 250 × 4.6 mm), gradient of acetonitrile / 0.1% H₃PO₄; detection at 254 nm
    Water content0.5% (w/w)Ph. Eur. 2.5.12, Karl Fischer coulometric titration
    Residue on ignition0.1%Ph. Eur. 2.4.14
    Heavy metals (as Pb)10 ppmPh. Eur. 2.4.8, Method C
    Residual solvents: ethanol0.5%Headspace GC-FID per USP <467> Class 3
    Residual solvents: acetonitrile410 ppmHeadspace GC-FID, ICH Q3C limit
    4-Chloro-2-oxobenzothiazole (des‑ester impurity)0.15%HPLC, same conditions as purity; RRT 0.82
    For synthetic libraries targeting kinase hinge-binding motifs, the compound serves as a conformationally restrained pharmacophore that positions the 4‑chlorine and the ester chain in a defined spatial arrangement. In a directed library of 96 analogs synthesized via parallel amide condensation using a Chemspeed SWING platform, compound identity was confirmed by UPLC‑MS with a mass accuracy of < 3 ppm. The cassette was screened against a panel of 50 kinases at 1 µM concentration; the hit rate for sub‑micromolar inhibition exceeded 8%, attributable to the hydrogen‑bond acceptor properties of the benzothiazolone oxygen and the vector alignment afforded by the ethyl acetate tail. Differences between the target compound and its des‑chloro or des‑ester counterparts become pronounced when considering regioselective late‑stage functionalization attempts.
    Comparative Profile of Structurally Related Benzothiazolone Synthons
    CompoundMolecular Weight (g mol⁻¹)Melting Point (°C)Key Reactivity FeatureProcess Limitation
    Ethyl (4-chloro-2-oxo-1,3-benzothiazol-3(2H)-yl)acetate271.7284–88Simultaneous ester & chlorine handles; chlorine activates ring for SNArSaponification competitive above pH 9 at > 40 °C
    4‑Chloro-2-oxobenzothiazole (NH analog)185.63202–206Solely N‑functionalization via alkylation; stronger H‑bond donorLow solubility in aprotic solvents; requires polar media
    Ethyl (2-oxo-1,3-benzothiazol-3(2H)-yl)acetate (des‑Cl)237.2678–81Ester handle enables hydrazide formation; no chlorine blocking regioselectivityNitration yields 3:1 mixture of 6‑ and 4‑nitro isomers
    When the des‑chloro analog is subjected to nitration with HNO₃/H₂SO₄ at -5 °C, HPLC analysis reveals a 74:26 ratio of 6‑nitro to 4‑nitro derivatives, necessitating fractional crystallization from 2‑propanol to obtain isomerically pure material. In contrast, the 4‑chloro‑substituted ester is effectively deactivated at the 4‑position, driving nitration selectively to the 6‑position with an isomer purity exceeding 98.5% after a single recrystallization. These regioisomeric distinctions directly impact bioisosteric replacement strategies in medicinal chemistry programs where the spatial trajectory of the ester side chain relative to the chlorine atom modulates metabolic stability and CYP inhibition profiles. Published data for the comprehensive CYP panel of the 4‑chloro vs. 6‑chloro ethyl ester derivatives remain limited, though in silico docking simulations using the CYP3A4 crystal structure (PDB 1TQN) suggest that the 4‑chloro configuration positions the lipophilic ester deeper into the heme pocket, predicting a modest increase in metabolic liability (estimated intrinsic clearance of 22 µL min⁻¹ mg⁻¹ microsomal protein versus 14 µL min⁻¹ mg⁻¹ for the 6‑chloro regioisomer). Such predictions underscore the need for confirmatory in vitro ADME data before committing to kilogram-scale campaigns. Handling at ambient humidity above 60% RH demands pre-drying of the powder in a vacuum oven at 35 °C for at least 4 h to prevent weight errors during weighing. The compound is incompatible with strong bases (e.g., sodium hydride, potassium tert‑butoxide) at temperatures above 25 °C because deprotonation at the nitrogen α‑position triggers ring‑opening to yield a thiocarbamate intermediate. Disposal routes must comply with local regulations for halogenated organic waste; incineration in a facility capable of handling chlorinated organics at 1,100 °C with a residence time of > 2 s is recommended.