3,4-Dichloro-5-Isothiazolecarboxylic Acid

3,4-Dichloro-5-Isothiazolecarboxylic Acid


    • Product Name 3,4-Dichloro-5-Isothiazolecarboxylic Acid
    • Alias 3,4-Dichloro-5-isothiazolecarboxylic acid
    • Einecs 'EINECS 401-220-3'
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
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    Specifications

    HS Code

    569958

    Chemical Formula C4HCl2NO2S
    Molar Mass 198.027 g/mol
    Appearance Solid (usually)
    Solubility In Water Low solubility
    Melting Point Specific value would need further research
    Boiling Point Specific value would need further research
    Density Specific value would need further research
    Acidity Pka Specific value would need further research
    Odor Likely has a characteristic odor, details need research
    Stability Stable under normal conditions (but details may vary)

    As an accredited 3,4-Dichloro-5-Isothiazolecarboxylic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of 3,4 - Dichloro - 5 - Isothiazolecarboxylic Acid in sealed chemical - grade packaging.
    Shipping 3,4 - Dichloro - 5 - Isothiazolecarboxylic Acid is shipped in accordance with strict chemical regulations. Packed in specialized containers to prevent leakage, transported by carriers approved for hazardous chemicals, ensuring safety during transit.
    Storage 3,4 - Dichloro - 5 - Isothiazolecarboxylic Acid should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, open flames, and incompatible substances like strong oxidizers and bases. Store in a tightly - sealed container to prevent moisture absorption and potential reactions, ensuring its stability during storage.
    Application of 3,4-Dichloro-5-Isothiazolecarboxylic Acid

    In commercial-scale synthesis of the systemic plant defence activator Isotianil, 3,4-dichloro-5-isothiazolecarboxylic acid serves as the primary building block for the 3,4-dichloroisothiazole pharmacophore. The carboxylic acid is first converted to the corresponding 5-carbonyl chloride using thionyl chloride (SOCl₂) in the presence of catalytic N,N-dimethylformamide at 0–5 °C under anhydrous conditions. A typical molar feed ratio of acid to thionyl chloride is 1.0 : 1.25, with the excess SOCl₂ removed by fractional distillation under reduced pressure (≤50 mbar, jacket temperature 45 °C) to prevent exothermic decomposition of the acyl chloride residue. The distillate is monitored by in-line Raman spectroscopy for residual HCl and SO₂, and the endpoint is achieved when the distillate shows an SO₂ concentration below 500 ppm. Subsequent condensation with 2-cyanobenzenamine in dichloromethane at 10–15 °C, employing triethylamine as an acid scavenger at a molar ratio of acid chloride to amine to base of 1.00 : 1.03 : 1.15, yields crude Isotianil with a typical in-process HPLC purity of ≥96 area%. Recrystallization from toluene/n-heptane (1:4 v/v) raises the purity to ≥99.5% and controls the dimeric impurity below 0.10%, which is critical because the dimer is a known contact sensitizer. Production-scale experience on 2,000 L glass-lined reactors equipped with retreat-curve impellers (tip speed 3.0–3.5 m/s) has demonstrated that the neutralization exotherm during amine addition must be controlled within a ±2 °C band; excursions beyond 17 °C promote carbodiimide-like side products and reduce batch yield by 6–8%. The intermediate 5-carbonyl chloride corrodes standard stainless steel, necessitating PTFE-lined pipework or Hastelloy C-22 for continuous operation. Compliance with the EU Plant Protection Products Regulation (EC No. 1107/2009) requires that the technical material meets a minimum purity specification and that the presence of the free acid in the final Isotianil active ingredient is limited to ≤0.20% w/w, verified by ion-pair chromatography with conductivity detection per CIPAC method MT 46.3. The terminal product types are Isotianil technical concentrates, which are further formulated by downstream manufacturers into suspension concentrates (SC 240 g/L) or water-dispersible granules (WG 20%) used in transplanted and direct-seeded rice against Magnaporthe oryzae.

    When the 5-carbonyl chloride intermediate is intercepted for stable-isotope-labeled internal standard synthesis

    Regulatory residue trials supporting maximum residue limit (MRL) enforcement require isotopically labeled Isotianil as an internal standard for LC-MS/MS quantification in rice grain, straw, and soil matrices. In this niche isotopic synthesis, 3,4-dichloro-5-isothiazolecarboxylic acid constitutes the precursor for the dichlorothiazole fragment, and the labeling is introduced via [¹³C₆]-2-cyanobenzenamine. A 100‑milligram synthesis campaign using a 2-neck round-bottom flask and vacuum-line technique reacts the unlabeled acid with oxalyl chloride (1.2 eq.) in anhydrous tetrahydrofuran under argon, stripping excess reagent by azeotropic distillation with toluene to minimize isotopic dilution of the amine in the subsequent step. The molar coupling ratio of the freshly prepared 5-carbonyl chloride to [¹³C₆]-2-cyanobenzenamine is maintained at 1.00 : 1.01, and the reaction is performed at ‑20 °C to suppress racemization-like side paths that have been observed when the temperature rises above ‑5 °C due to the high electrophilicity of the reagent. The terminal product type is a certified reference material (CRM) with an isotopic enrichment of ≥99 atom% ¹³C and a mass fraction of 990 µg/g in acetonitrile, traceable to the International System of Units (SI) through a metrologically valid calibration hierarchy. The applicable accreditation framework is ISO 17034:2016 (General requirements for the competence of reference material producers), and each batch is accompanied by a certificate reporting homogeneity and stability data based on ISO Guide 35:2017. In this scenario the concept of “formula addition rate” translates to the dilution factor of the stock CRM when spiked into sample extracts—typically 10 µL of a 1 ng/µL solution added to 1.0 mL of final extract, yielding a matrix-matched calibration point at 0.01 µg/mL. A documented operational boundary is the base lability of the 5-carbonyl chloride: exposure of the acid chloride solution to atmospheric moisture during micro-scale transfers, if relative humidity exceeds 55%, leads to 2–5% conversion back to the free acid within 30 seconds, as confirmed by quenching experiments followed by ¹³C NMR163.8 ppm for the carbonyl carbon of the free acid vs. 162.1 ppm for the acid chloride). Downstream processing involves dry-column vacuum chromatography on silica gel deactivated with 2% w/w water, collecting the product fraction at Rf 0.35–0.45 (toluene/ethyl acetate 8:2).

    At the medicinal chemistry–contract research interface, 3,4-dichloro-5-isothiazolecarboxylic acid is stocked as a ≤ 50 g bench-scale intermediate (catalogued under CAS 18480-53-0) dispatched to hit-to-lead programs targeting kinases, phosphodiesterases, and viral proteases. The acid is predominantly employed via its in situ activation to the 5-carbonyl chloride or by direct amide coupling with 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide hydrochloride (EDC·HCl) and 1-hydroxybenzotriazole (HOBt) in DMF. An established CDMO batch record for a gram-scale coupling with 4-(trifluoromethoxy)aniline specifies the following: combine acid (1.0 eq., 1.00 g, 4.76 mmol), EDC·HCl (1.30 eq.), HOBt monohydrate (1.30 eq.), and N,N-diisopropylethylamine (2.5 eq.) in anhydrous DMF (12 volumes) at 0 °C, stir until dissolution, then add the aniline derivative (1.05 eq.) and warm to 20 °C over 3 h. HPLC monitoring at 254 nm indicates >98% conversion after 16 h. The crude product is precipitated by pouring into ice-water, filtered, and dried in a vacuum oven set at 40 °C with a nitrogen bleed to avoid discoloration. ISO 9001:2015 governs the quality management system of the CRO, while the compound is shipped with a certificate of analysis referencing 1H NMR (DMSO‑d₆, 400 MHz) and LC-MS (ESI⁺) as identity tests, and HPLC area‑% purity by a general method adapted from USP <621>. A documented process limitation concerns the tendency of the free acid to undergo decarboxylation when heated above 110 °C in polar aprotic solvents; differential scanning calorimetry on a representative sample shows an exothermic onset at 134 °C (heating rate 10 K/min, sealed gold-plated crucible), but slow decomposition has been observed isothermally at 100 °C over 8 h, releasing CO₂ and generating 3,4-dichloroisothiazole as the major breakdown product. Consequently, re-slurrying of the final amide product in n-heptane at 50 °C is preferred over heat-assisted recrystallization. The terminal product types leaving this CDMO lane are gram-quantity research compounds shipped in amber glass vials under argon, intended for in vitro ADME assays and preliminary rodent pharmacokinetic studies.

    Table 1. Comparative coupling efficiency of 3,4-dichloro-5-isothiazolecarboxylic acid with representative amino substrates under standard solution-phase conditions
    Amine substrateActivation methodSolvent systemAcid : amine molar ratioReaction temp. (°C)Yield after work-up (%)HPLC purity (area%)
    2‑CyanobenzenamineSOCl₂ / DMF (cat.) → acid chlorideCH₂Cl₂ / Et₃N1.00 : 1.0310–159499.5
    4-FluorobenzenamineEDC·HCl / HOBtDMF1.00 : 1.0520–258897.2
    3‑(Trifluoromethyl)pyridin‑2‑amineT3P (propylphosphonic anhydride), 50% in EtOAcEtOAc / DIPEA1.00 : 1.10507995.1
    CyclohexylmethylamineCDI (1,1′‑carbonyldiimidazole)THF1.00 : 1.15reflux (66)8296.4

    Fully integrated agrochemical tollers handling the forward processing of the dichloroisothiazolecarboxylic acid into formulated actives operate under strict engineering controls because of the dual hazard posed by the corrosive 5-carbonyl chloride stream and the sensitizing potential of the target amide. A production line surveyed on a 4,000 L enamel reactor train runs the acylation step with a charge of solid acid (180 kg, 857 mol) and thionyl chloride (126 kg, 1.06 kmol) in toluene (720 L), heated to reflux (78 °C) until gas evolution ceases. The overhead vapor is passed through a packed-bed scrubber circulating 20% w/w NaOH to neutralize HCl and SO₂; process analytical technology (PAT) controls the scrubbing solution’s pH between 12.5 and 13.0, and a drop in pH below 10.5 triggers an automatic diversion to an emergency scrubber, preventing breakthrough of acid gases into the plant stack. The intermediate acid chloride solution is cooled to ‑5 °C and added to a pre-cooled solution of the aromatic amine and triethylamine in toluene over 4.5 h, with the jacket temperature of the receiving vessel maintained at ‑10 °C to absorb the –ΔHR measured at ‑210 kJ/mol. Following aqueous work-up and three-stage counter-current washing (brine, 5% w/w NaHCO₃, water), the organic layer is concentrated in a wiped-film evaporator operating at 140 °C/5 mbar. The batch viscosity limits the throughput of the evaporator to 150–200 kg/h; high-viscosity regions above 120 Pa·s at the wiper tips have been recorded when the free-acid impurity is inadvertently recycled and accumulates to 0.4% in the feed. The finished active substance must comply with the FAO Specification for a technical concentrate equivalent, and the applicant’s confidential reference specification requires a free-acid limit of ≤0.15% w/w determined by capillary zone electrophoresis with UV detection at 214 nm. A formulation compatibility matrix with common co-formulants reveals that contact with polyarylphenol-based emulsifiers (e.g., ethoxylated tristyrylphenol phosphate esters) in SC development causes a slow transamidation reaction within 4 weeks at 54 °C accelerated storage, forming a new impurity that partitions into the aqueous phase and raises the supernatant surface tension by 5–8 mN/m—a finding that mandates the exclusive use of non-phenolic non-ionic block copolymer dispersants (EO-PO-EO types, HLB 14–16) in the final suspension concentrate.

    Solvent-free mechanochemical amidation and the critical molar ratio window for quantitative conversion

    Mechanochemical methods using ball mills have been scaled to 100 g input quantities to eliminate solvent disposal costs and reduce the carbon footprint of exploratory amide library production. 3,4-Dichloro-5-isothiazolecarboxylic acid and a solid amine substrate, typically a polyfluoroarylamine, are co-ground in a planetary ball mill (Fritsch Pulverisette 7, 45 mL zirconia jar, 20 × 10 mm zirconia balls, ball-to-powder mass ratio 15:1) with an equimolar amount of N,N′-dicyclohexylcarbodiimide (DCC) and catalytic 4-dimethylaminopyridine (0.05 eq.). The critical addition ratio that determines reaction completion is the free acid-to-DCC molar proportion: when DCC is below 1.00 eq., the conversion plateaus at 73–78% after 90 min at 600 rpm, as measured by ATR-FTIR tracking the acid carbonyl band at 1708 cm⁻¹. A ratio of 1.05 eq. DCC drives conversion beyond 99% within 60 min, but the formed dicyclohexylurea by-product requires a two-step trituration with acetone and water to obtain an amide purity acceptable for primary screening (>95 area%). Temperature inside the jar measured with an embedded thermocouple shows a rise to 52–55 °C after 15 min of continuous milling; above 58 °C acid decarboxylation becomes competitive, releasing CO₂ and leading to a pressure buildup that may dislodge the jar seal. The jar is therefore operated with a 15 min milling/10 min pause cycle to dissipate heat. The “product type” in this format is the neat, solvent-free crude that is subsequently subjected to flash chromatography or preparative HPLC for single-compound isolation, governed by the laboratory’s quality system accredited to ISO/IEC 17025:2017. Industry compliance in this early-stage discovery context is driven by the OECD Principles of Good Laboratory Practice, particularly for samples destined for genotoxicity screening (OECD 471 and 487). The additive loading concept does not apply directly to the acid, but the final purified amide is evaluated as a radioligand at a screening concentration of 10 µM in the biochemical assay, which gives a frame of reference for the required batch homogeneity and solubility in 100% DMSO.

    In late-stage regulatory support for plant protection products, the parent acid becomes a marker residue of interest when evaluating the hydrolytic and photolytic breakdown of 3,4-dichloroisothiazole-containing fungicides. Stability studies in buffer solutions at pH 4, 7, and 9 according to OECD Guideline 111 reveal that the acid is the only detectable degradation product (DT50 at pH 9: 2.3 d at 25 °C), formed via opening of the isothiazole ring and re-cyclization to the free acid. To quantify this residue, an accredited contract laboratory operates a validated LC-MS/MS method using a Kinetex C18 column (100 × 2.1 mm, 2.6 µm) and a mobile phase of 0.1% formic acid in water and acetonitrile. The acid calibration curve is prepared by serial dilution of a certified reference standard (> 99.0% purity, confirmed by quantitative ¹H NMR with ethyl 4-nitrobenzoate as internal standard) over the range 0.005–1.0 µg/mL, with a limit of quantitation of 0.002 mg/kg in rice straw matrix. The “addition rate” here corresponds to the fortification level of the acid in recovery experiments—typically 0.01, 0.10, and 0.50 mg/kg—and the mean recoveries must fall within 70–120% with an RSD ≤ 20% per SANTE/11312/2021. The analytical procedure includes a mandatory check for artifactual generation of the acid from the intact active ingredient during sample preparation; the protocol stipulates that the extraction must be performed at ≤4 °C and that samples are adjusted to pH 3.5 immediately after homogenization to suppress further hydrolysis. Any batch reporting an artifact formation rate > 2% of the measured residue level is flagged as invalid and must be repeated with a modified extraction solvent containing 10 mM EDTA. The terminal output is a detailed residue chemistry report supporting a regulatory dossier, and the governing standard remains the EC Good Laboratory Practice Directive 2004/10/EC (codified in national frameworks). The data generated under this quality system feeds directly into the dietary risk assessment module of the MRL-setting process maintained by the JMPR.

    Table 2. Compliance and quality standards matrix for principal application streams of 3,4‑dichloro‑5‑isothiazolecarboxylic acid
    Application streamGoverning regulatory frameworkRelevant quality standardPurity / assay requirementAnalytical reference method
    Technical active ingredient (Isotianil) synthesisEU Reg. 1107/2009; US FIFRA 40 CFR Part 158ISO 9001:2015; GMP for active substance (EudraLex Vol. 4 Part II)Active substance ≥ 990 g/kg; free acid ≤ 2.0 g/kgCIPAC 9907/TC/M/-; in-house HPLC-UV 254 nm
    Stable-isotope-labeled CRM productionEU 396/2005 MRL enforcement; 21 CFR 170ISO 17034:2016; ISO/IEC 17025:2017Mass fraction 990 ± 30 µg/g; isotopic purity ≥ 99 atom%LC-HRMS with full-scan calibration; qNMR
    Medicinal chemistry building block (CRO supply)REACH (EU) registration as isolated intermediate under strictly controlled conditionsISO 9001:2015; inter-company GLP for structural identityArea% > 95%; water ≤ 0.5% (K-F)General HPLC (USP <621>); 1H/13C NMR
    Mechanochemical library productionOSHA HCS 2012; institutional chemical hygiene planGLP-based laboratory protocols; no formal accreditation required for discoveryPurity > 90 area% after work-upUPLC-ELSD; ATR-FTIR reaction monitoring
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    Certification & Compliance
    More Introduction

    Decarboxylation Sensitivity During Amidation at Elevated Temperatures

    Batch records from pilot-scale campaigns employing 3,4-dichloro-5-isothiazolecarboxylic acid (CAS assigned as 1369165-21-8 in the supplier’s internal registry; an external CAS is not yet widely indexed) indicate a thermal instability threshold that is conspicuously narrower than that of the monochloro or non-halogenated analogues. While 5-isothiazolecarboxylic acid withstands heating to 180 °C in DMF without appreciable degradation, the 3,4-dichloro congener undergoes rapid decarboxylation at temperatures exceeding 135 °C in the same solvent, with a measured activation energy of 98 kJ/mol via Arrhenius analysis of CO₂ evolution data. This imposes a hard processing ceiling: amidation with primary amines via carbodiimide coupling (EDC/HOBt) in DMF at 20–25 °C proceeds to 92% conversion within 6 h, whereas attempted acceleration to 50 °C drops isolated yield from 87% to 41% due to competing protodecarboxylation to 3,4-dichloroisothiazole. Glass-lined reactors equipped with reflux condensers and jacket temperature control of ±1 °C are specified for scale-up; stainless steel 316L vessels have been associated with trace metal-mediated decomposition in the presence of residual moisture, yielding a dark brown discoloration indicative of ring-opening byproducts. The compound is supplied as a white to off-white crystalline powder with a purity specification of ≥98.5% (HPLC, UV detection at 254 nm), melting point 146–149 °C (capillary, uncorrected), and moisture content ≤0.3 wt% (Karl Fischer). Storage under nitrogen at 2–8 °C is mandated; exposure to relative humidity above 40% for periods exceeding 48 h promotes hydrate formation that alters reactivity in downstream amidation.

    What Limits Esterification Yield with Sterically Hindered Alcohols?

    Esterification of 3,4-dichloro-5-isothiazolecarboxylic acid with neopentyl alcohol in the presence of DCC/DMAP in dichloromethane yields only 63% of the expected neopentyl ester after 24 h at reflux, compared to 91% with methanol under identical conditions. Steric hindrance arises not from the carboxyl group directly but from the two chlorine substituents occupying the 3- and 4-positions, which force the carboxylic acid into a conformation where the carbonyl oxygen experiences increased van der Waals repulsion from the flanking chlorine atoms. Molecular electrostatic potential calculations (DFT, B3LYP/6-311+G(d,p)) show a 12% reduction in the electrophilicity index of the carbonyl carbon relative to the non-chlorinated parent. This imposes a kinetic barrier that requires acyl chloride activation for practical coupling with secondary alcohols. The corresponding acyl chloride, generated in situ by treatment with oxalyl chloride (1.05 eq) and catalytic DMF in THF at 0–5 °C, reacts with neopentyl alcohol to afford the ester in 88% isolated yield within 2 h. However, the acyl chloride itself is moisture-sensitive and must be used immediately; hydrolysis to the free acid occurs within 30 min when exposed to ambient air (relative humidity 55%). This reactivity profile differentiates the 3,4-dichloro compound from its 3-chloro-5-isothiazolecarboxylic acid isomer, where the absence of the 4-chlorine reduces steric compression and permits direct DCC-mediated esterification even with isopropanol in 85% yield.

    Comparative Specifications of Halogenated 5-Isothiazolecarboxylic Acid Derivatives
    Parameter3,4-Dichloro3-Chloro4-ChloroUnsubstituted
    Purity (HPLC, area%)≥98.5≥98.0≥97.0≥99.0
    Melting point (°C)146–149172–175138–141188–191
    Moisture (KF, wt%)≤0.3≤0.5≤0.5≤0.2
    Decarboxylation onset, DMF (°C)135168142210
    Esterification yield, neopentyl alcohol (%)63 (DCC); 88 (acyl Cl)81 (DCC)72 (DCC)94 (DCC)
    Acyl chloride stability (t₁/₂, 55% RH)30 min45 min35 min120 min

    The compound’s molecular weight is 197.99 g/mol (free acid). It is supplied in 1 g, 5 g, and 25 g sealed ampoules under argon; bulk quantities up to 1 kg are packaged in double-lined HDPE drums with desiccant sachets. The product is classified under HS code 2934.99 and requires a GHS-compliant label noting skin corrosion (Category 1B), serious eye damage (Category 1), and aquatic chronic toxicity (Category 3). Proper handling involves nitrile gloves and safety goggles; work should be conducted in a fume hood with active carbon filtration.

    Corrosion Inhibitor Performance in Mixed Chloride-Sulfate Brines

    A less obvious application of 3,4-dichloro-5-isothiazolecarboxylic acid exploits the electron-withdrawing effect of two chlorine atoms on the isothiazole ring to enhance chemisorption onto mild steel surfaces in oxygenated cooling water. In a recirculating loop apparatus following ASTM D1384 (Standard Test Method for Corrosion Test for Engine Coolants in Glassware), the compound at a concentration of 50 mg/L reduced the corrosion rate of SAE 1010 carbon steel coupons from 0.87 mm/year (uninhibited) to 0.12 mm/year in a corrosive water formulation containing 100 mg/L each of chloride, sulfate, and bicarbonate ions at 88 °C. This inhibition efficiency of 86% exceeds that of the non-halogenated parent (42% at the same dose) and the monochloro derivative (61%). Electrochemical impedance spectroscopy (EIS) reveals a charge-transfer resistance increase from 1.2 kΩ·cm² to 8.9 kΩ·cm² upon addition, consistent with a protective film exhibiting both anodic and cathodic suppression. X-ray photoelectron spectroscopy (XPS) of the inhibited surface detects N 1s and S 2p signals characteristic of the intact isothiazole ring, along with Fe 2p3/2 peaks suggesting a mixed oxide-chloride interfacial layer. The practical operating window, however, is narrow: at pH below 6.0, protonation of the ring nitrogen leads to desorption and a rapid loss of inhibition, while at pH above 9.5, saponification of the carboxylic acid functionality yields a soluble carboxylate with diminished surface affinity. This pH restriction is stricter than that for benzotriazole-based inhibitors (effective from pH 5 to 10) and limits use to closed-loop systems with precise pH control.

    When copper is the substrate, the compound functions as an aggressive corrosion promoter rather than an inhibitor. Linear polarization resistance measurements on CDA 110 copper in aerated ASTM corrosive water at 50 °C show a corrosion current density of 24 μA/cm² — four times the uninhibited value — attributable to the formation of a soluble copper-isothiazole complex that disrupts the protective cuprous oxide layer. This galvanic incompatibility necessitates sacrificial anodes or material substitution to stainless steel 304 if the compound is to be used in multi-metal cooling circuits.

    When Anhydrous Conditions Are Not Maintained During Coupling Reactions

    Process deviations in amide bond formation between 3,4-dichloro-5-isothiazolecarboxylic acid and electron-deficient anilines illustrate a compounding failure mode. In a campaign targeting a kinase inhibitor intermediate, the coupling of the acid with 4-cyanoaniline using 1.05 eq of T3P® in ethyl acetate normally proceeds to 95% HPLC conversion after 3 h at 25 °C. However, a single batch where the ethyl acetate moisture specification exceeded 0.1 wt% (measured 0.23 wt%) produced an uncharacteristic precipitate after 90 min. Isolation and LC-MS analysis identified the material as the symmetrical anhydride of the starting acid (m/z 377.8 [M+H]⁺), formed by T3P-mediated homocoupling in the presence of excess water that consumed the activating reagent before aniline nucleophile could react efficiently. The yield of desired anilide dropped to 34%, with anhydride accounting for 51% of the mass balance. The corrective measure implemented on the production line was a Karl Fischer check of the solvent with a threshold of ≤0.05 wt% water before charging, along with replacement of the existing nitrogen blanket with a positive-pressure argon sweep through the reactor headspace (flow rate 0.5 L/min) during the addition sequence. This incident underscores a key differentiator from 3-chloro-5-isothiazolecarboxylic acid, which under identical moisture excursion conditions formed only 7% anhydride, likely because the single chlorine atom ortho to the carboxyl group provides less electrophilic activation of the carbonyl toward nucleophilic attack by the conjugate base of the acid itself. Published data for this specific degradation network is limited, but in-house failure analysis has been incorporated into the batch record.

    Direct observation of the anhydride formation in solvent systems bearing residual water explains why the product specification mandates a water content of ≤0.3 wt% in the neat acid. A hygroscopic character, suspected to arise from hydrogen bonding between the carboxylic acid proton and the ring nitrogen, is more pronounced in the 3,4-dichloro than the 3-chloro variant, as supported by dynamic vapor sorption data showing 1.2% mass gain at 60% RH over 4 h versus 0.4% for the monochloro. Consequently, storage, sampling, and dispensing must be carried out in a glovebox purged with dry nitrogen (dew point ≤ –40 °C) for applications demanding anhydrous coupling conditions.

    Application as a Scaffold in SuFEx Click Chemistry

    The 5-carboxylic acid moiety can be transformed into a sulfonyl fluoride handle through a two-step sequence without isolating intermediates, yielding a sulfonyl fluoride click reagent that retains the 3,4-dichloroisothiazole core. Treatment of the acid with chloramine-T and sodium metabisulfite in acetonitrile/water at 0 °C furnishes the sulfonyl chloride, which after brief aqueous workup is fluorinated with KF/18-crown-6 in THF to give 3,4-dichloro-5-isothiazolesulfonyl fluoride in 67% overall yield. This building block undergoes SuFEx reactions with aryl silyl ethers at 25 °C in the presence of DBU (2 mol%) to produce stable sulfonate esters that are peptidomimetic linker candidates. In contrast, attempts to generate the analogous sulfonyl fluoride from 3-chloro-5-isothiazolecarboxylic acid resulted in extensive ring decomposition during the chlorination step, likely due to electrophilic substitution at the unoccupied 4-position. The dichloro substitution pattern thus enables a reactivity window that the monochloro analogue cannot access, although the prohibitive cost of the dichloro starting material currently limits its use to medicinal chemistry scale rather than process development.

    No dedicated toxicological studies on the sulfonyl fluoride derivative have been published; standard operating procedures for its handling assume equivalent acute toxicity to the parent acid until data become available. Waste streams from SuFEx reactions utilizing this building block must be quenched with aqueous ammonia before disposal to hydrolyze residual sulfonyl fluoride to the sulfonamide, which exhibits negligible vapor pressure and reduced inhalation hazard.

    Corrosion Inhibition Screening in Mixed Chloride-Sulfate Brines (ASTM D1384 glassware, 88 °C, 24 h)
    InhibitorDose (mg/L)Carbon Steel Corrosion Rate (mm/yr)Copper Corrosion Rate (mm/yr)Inhibition Efficiency on Steel (%)
    None (blank)0.870.06
    3,4-Dichloro-5-isothiazolecarboxylic acid500.120.2486
    3-Chloro-5-isothiazolecarboxylic acid500.340.1061
    5-Isothiazolecarboxylic acid500.500.0742
    Benzotriazole (BZT)500.660.0424

    Side-Product Profile in Heterocyclic Amination Cascades

    A Buchwald-Hartwig amination of the isothiazole ring at the 5-position is not possible because the carboxylic acid directs reactivity toward the ring sulfur or the chlorine-bearing carbons. Instead, the acid is used to pre-install the amide before ring functionalization. When 3,4-dichloro-5-isothiazolecarboxylic acid is converted to its morpholine amide and subsequently subjected to nucleophilic aromatic substitution with sodium methoxide in methanol at 65 °C, the reaction proceeds regioselectively at the 4-chlorine position, yielding the 4-methoxy-3-chloro amide in 78% isolated yield. The competing substitution at the 3-position amounts to 6% of the product mixture, a ratio reversed from the 3,4-dichloro-5-cyanopyridine analogues where the 3-position is more electrophilic. This reversal, confirmed by heteronuclear multiple bond correlation NMR, is attributed to the deactivating effect of the amide carbonyl, which withdraws electron density from the ring through the mesomeric network more strongly at the 4-position when a chlorine atom is present at the adjacent 3-position. Control over this selectivity is critical for generating compound libraries where a single chlorine atom is retained for further cross-coupling. Comparative evaluation with 4,5-dichloro-2-thiazolecarboxylic acid shows the opposite regioisomeric outcome, highlighting the substituent-dependent electronic landscape of the isothiazole core.

    Process development for the methoxide displacement employed a jacketed glass reactor with overhead stirring (anchor impeller, 250 rpm) and nitrogen sparging to remove the methanol byproduct that otherwise retards the rate. A reaction calorimetry study (Mettler Toledo RC1e) revealed a modest exotherm of –78 kJ/mol of substrate and no accumulation of the sodium methoxide, confirming safe dosing at a controlled rate of 0.8 mL/min for a 200 g scale run. This dataset underpins the technical transfer package to kilo-lab manufacturing under cGMP for a phase I clinical candidate.