|
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 | 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. |
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 68–72 °C under nitrogen blanketing for 4–6 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 2.0–2.5 with 6N hydrochloric acid at 5–10 °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 20–25 °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 8–12 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 8–10 hours achieves a conversion of 82–94% 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 ScaffoldsA 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 0–5 °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 −5–0 °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 0–3 °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 4.8–5.2 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 CoatsThe 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.
*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 155–165 °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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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.
| Parameter | Specification | Test Method |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual 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 point | 84 °C – 88 °C | Ph. 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 content | ≤ 0.5% (w/w) | Ph. Eur. 2.5.12, Karl Fischer coulometric titration |
| Residue on ignition | ≤ 0.1% | Ph. Eur. 2.4.14 |
| Heavy metals (as Pb) | ≤ 10 ppm | Ph. Eur. 2.4.8, Method C |
| Residual solvents: ethanol | ≤ 0.5% | Headspace GC-FID per USP <467> Class 3 |
| Residual solvents: acetonitrile | ≤ 410 ppm | Headspace GC-FID, ICH Q3C limit |
| 4-Chloro-2-oxobenzothiazole (des‑ester impurity) | ≤ 0.15% | HPLC, same conditions as purity; RRT 0.82 |
| Compound | Molecular Weight (g mol⁻¹) | Melting Point (°C) | Key Reactivity Feature | Process Limitation |
|---|---|---|---|---|
| Ethyl (4-chloro-2-oxo-1,3-benzothiazol-3(2H)-yl)acetate | 271.72 | 84–88 | Simultaneous ester & chlorine handles; chlorine activates ring for SNAr | Saponification competitive above pH 9 at > 40 °C |
| 4‑Chloro-2-oxobenzothiazole (NH analog) | 185.63 | 202–206 | Solely N‑functionalization via alkylation; stronger H‑bond donor | Low solubility in aprotic solvents; requires polar media |
| Ethyl (2-oxo-1,3-benzothiazol-3(2H)-yl)acetate (des‑Cl) | 237.26 | 78–81 | Ester handle enables hydrazide formation; no chlorine blocking regioselectivity | Nitration yields 3:1 mixture of 6‑ and 4‑nitro isomers |