3,4-Dichloroisothiazole-5-Carboxylic Acid

3,4-Dichloroisothiazole-5-Carboxylic Acid


    • Product Name 3,4-Dichloroisothiazole-5-Carboxylic Acid
    • Alias 3,4-Dichloro-5-isothiazolecarboxylic acid
    • Einecs 681-481-8
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    637970

    Chemical Formula C4HCl2NO2S
    Molecular Weight 198.027 g/mol
    Appearance Typically a solid (physical state can depend on conditions)
    Solubility Solubility characteristics would depend on the solvent, may have limited solubility in water
    Melting Point Specific melting point data would require literature search
    Boiling Point Boiling point data would need to be sourced from relevant literature
    Pka Value Relevant for understanding its acidic properties, exact value from literature
    Density Density information would be obtained from experimental data or literature
    Stability Stability can vary based on environmental factors like temperature, light, and presence of reactive substances
    Reactivity Can react with various nucleophiles, electrophiles, etc. depending on reaction conditions

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

    Packing & Storage
    Packing 100 - gram bottles of 3,4 - Dichloroisothiazole - 5 - Carboxylic Acid, well - sealed.
    Shipping 3,4 - Dichloroisothiazole - 5 - Carboxylic Acid is shipped in well - sealed, corrosion - resistant containers. It adheres to strict chemical shipping regulations, ensuring safe transportation to prevent leakage and environmental hazards.
    Storage Store 3,4 - Dichloroisothiazole - 5 - Carboxylic Acid in a cool, dry, well - ventilated area. Keep it away from heat sources, ignition sources, and incompatible substances such as strong oxidizing agents and bases. Store in a tightly closed container to prevent moisture absorption and potential degradation. Ensure proper labeling for easy identification.
    Application of 3,4-Dichloroisothiazole-5-Carboxylic Acid
    Conversion is achieved via the cyclization of dinitrile disulfide precursors with 3,4-Dichloroisothiazole-5-Carboxylic Acid serving as the acid chloride feedstock after treatment with thionyl chloride; the resulting intermediate, 4,5-dichloro-2-methylisothiazol-3-one (DCMIT), is the active biocide component in multiple ISO 11930:2019 challenge-tested preservative systems for metalworking fluids and polymer emulsions. In-can preservation formulations typically require a 3:1 ratio of 5-chloro-2-methyl-4-isothiazolin-3-one (CMIT) to DCMIT, with the latter deriving directly from this dichlorinated acid building block. Addition rates for the finished isothiazolinone blend in water-based adhesives range from 7 ppm to 15 ppm active, while heavy-duty metalworking fluid concentrates may require 50 ppm to 150 ppm depending on tramp oil load and bacterial challenge measured via dip-slide counts exceeding 10⁶ CFU/mL. Compliance boundaries are stringently defined: EU Regulation (EC) No 1272/2008 Annex VI mandates specific skin sensitization warning labeling for mixtures containing ≥ 15 ppm combined CMIT/MIT, and the German TRGS 611 technical rule restricts water-miscible coolant preservative dosing when operator dermal contact is unavoidable. Published data for this specific configuration is limited regarding aerosolized mist exposure thresholds during high-pressure machining operations using minimum quantity lubrication with dosed biocides.

    Pulp and paper mill process water infected with Bacillus species forming endospores requires oxidative pretreatment with chlorine dioxide prior to slimicide dosing; the isothiazolinone derivative synthesized from this carboxylic acid precursor is then metered at 2.5 kg to 5.0 kg active per ton of bone-dry fiber in the broke storage chest, with continuous feed rather than slug dosing to maintain 0.5 ppm to 1.0 ppm residual in the white-water circuit. TAPPI T 299 alkaline extraction liquor monitoring is implemented alongside biocide injection to confirm that pH in the short circulation loop does not exceed 8.2, beyond which hydrolytic ring-opening of the isothiazolinone heterocycle accelerates, halving the half-life from 22 hours at pH 7.0 and 35°C to approximately 2.5 hours at pH 8.5. Microbiological failure is detectable within 48 to 72 hours when slime deposits increase headbox pressure differential by more than 15 kPa, a value directly observable on Siemens SITRANS P DS III differential pressure transmitters installed across the slice opening. Equipment corrosion from the chloride liberated during biocide degradation is mitigated when the carboxylic acid precursor purity exceeds 99.0%, minimizing unreacted chlorinated byproducts that accelerate pitting on 316L stainless steel breast roll surfaces operating at 1,200 m/min wire speed.

    What mechanisms govern leaching rates of DCMIT-derived antifoulants from rosin-based self-polishing copolymer matrices in tropical harbors?

    Marine antifouling coating systems incorporating DCMIT synthesized from 3,4-Dichloroisothiazole-5-Carboxylic Acid as the precursor active are formulated within rosin-modified self-polishing copolymers (SPCs) at a cuprous oxide co-biocide loading of 35 wt% to 45 wt% and an isothiazolinone booster biocide content of 4 wt% to 8 wt% on total wet paint. The addition rate of the booster biocide must remain below 10 wt% to avoid plasticization of the rosin matrix, which manifests on production-scale Buhler PML-2 bead mills as a measurable drop in mill base viscosity from 120 KU to 85 KU at 23°C and corresponding fineness-of-grind deterioration exceeding 60 μm. ISO 15181-1:2007 specifies the rotating cylinder method for quantifying biocide release rates, with an acceptable leaching window of 1.5 μg to 3.5 μg active per cm² per day during the initial 45-day immersion period. Below 1.0 μg/cm²/day, settlement of Amphibalanus amphitrite cyprids becomes statistically significant at a 95% confidence level within 30 days static immersion at 25°C in filtered seawater of 34 PSU salinity. The IMO Antifouling System Convention (AFS 2001) risk assessment framework requires any booster biocide exceeding 1,000 ng/L predicted environmental concentration in confined harbor waters to undergo additional chronic ecotoxicity testing on three trophic levels, as prescribed in OECD Test No. 201, 202, and 211, with the NOEC for Crassostrea gigas larval development serving as the most sensitive endpoint in temperate water risk characterization.

    Production-scale SPC manufacturing using Ikegai PCM-87 twin-screw extruders at L/D 48 requires the DCMIT powder to be pre-dispersed in diisobutyl ketone solvent at 20°C prior to addition into the barrel at Zone 5 (of 12 barrel zones), after the rosin zinc carboxylate formation is complete at Zone 3. Injection at this point avoids thermal decomposition of the isothiazolinone moiety when melt temperatures are maintained below 165°C, measured by a flush-mounted Dynisco SPX melt transducer at the Zone 6 barrel port; excursions above 180°C for more than 90 seconds result in chloride release that attacks the Xaloy X-800 bimetallic barrel lining, inducing surface roughness exceeding Ra 1.6 μm within 500 operating hours. Vessel trials conducted on 40,000 DWT bulk carriers dry-docked after 60 months reveal that static raft data significantly overpredicts polishing rate by a factor of 1.4 to 2.0 when the service speed exceeds 14 knots, a hydrodynamic effect requiring reformulation adjustment to increase rosin-to-carboxylate ratio. Copper-based formulations containing DCMIT must maintain a cuprous oxide to booster ratio of at least 6:1 to prevent synergistic leaching that depletes the booster faster than the controlled depletion polymer (CDP) mechanism can sustain, leading to premature barnacle fouling on vessel bottoms in biofouling hotspots including the Malacca Strait and the Gulf of Guinea.

    Chemical Release Rate and Biocide Composition for Rosin SPC Paints Containing DCMIT
    ParameterRange (Initial 45 Days)Range (Steady-State After Day 90)Measurement Method
    DCMIT release rate1.5–3.5 μg/cm²/day0.8–1.5 μg/cm²/dayISO 15181-1:2007
    Cu release rate25–40 μg/cm²/day15–22 μg/cm²/dayISO 15181-2:2007
    Total paint thickness reduction40–60 μm/year25–35 μm/yearASTM D6132-13
    Carboxylate backbone hydrolysis pH minimum at surface8.1–8.47.8–8.0Micro-pH electrode (flat-tip)

    Organotin-free deep-sea antifouling systems deployed on subsea wellhead equipment at depths exceeding 1,200 meters present a distinct challenge: isothiazolinone biocides formulated into epoxy-glass flake barrier coatings at 2.0 wt% exhibit virtually zero polishing rate, with release governed purely by Fickian diffusion through the 100–150 μm dry film, yielding a service life exceeding 15 years when the initial surface concentration is established at 12% to 15% of the binder matrix mass. The carboxylic acid precursor must be vacuum-dried to <0.05% moisture before chlorination to prevent hydrolysis of the acid chloride during subsequent DCMIT synthesis, a step monitored by Karl Fischer titration (ASTM D1533-20) on each 500 kg batch. Published data for this specific application on ultra-deepwater Christmas tree assemblies is limited, but subsea observation via ROV-mounted cameras at 1,300 meters in the Gulf of Mexico confirmed no macrofouling coverage exceeding 5% area after 96 months for a compliant formulation.

    In the compounding of ethylene-propylene-diene monomer (EPDM) roofing membranes calendered to 0.045-inch thickness on Troester four-roll inverted-L calenders, the isothiazolinone biocide obtained from this dichlorinated acid precursor is metered into the Banbury F270 internal mixer at 0.5 phr to 1.2 phr alongside carbon black N550 at 80 phr and paraffinic process oil at 60 phr. Addition above 1.5 phr initiates a scorch reaction observable as a ≥5 Mooney unit rise within 3 minutes at 121°C as measured on a Monsanto MV 2000 viscometer, due to the chlorine atoms on the isothiazole ring acting as halogen donors in the presence of zinc oxide activators in the cure package. The critical processing constraint is the dump temperature from the drop door: if the compound exceeds 155°C before the biocide is adequately dispersed to a Phillips Dispersion Rating of 4 or better, surface bloom of the biocide will manifest on the finished sheet within 14 days of warehouse storage at 40°C, detected as a hazy residue using ATR-FTIR spectroscopy with the characteristic carbonyl stretch at 1685 cm⁻¹. ASTM D4637-14 tensile testing of die-cut dumbbells at 500 mm/min confirms that biocide levels below 0.8 phr do not alter the 9.0 MPa minimum tensile strength requirement for Type III EPDM sheet per ASTM D4637 classification, whereas incorporation at 1.5 phr reduces ultimate elongation from 300% to 240% due to localized crosslink density disruption at crystal boundaries in the zinc-stearate-cured matrix.

    Single-Pot Synthetic Routes to Agrochemical Thiocarboxamide Derivatives Using 3,4-Dichloroisothiazole-5-Carboxylic Acid

    Agrochemical discovery programs targeting soilborne oomycete pathogens (Phytophthora infestans, Pythium ultimum) exploit the activated acid chloride derived from this isothiazole carboxylic acid to synthesize a library of substituted anilides via Schotten-Baumann condensation in a biphasic toluene-water system at 0°C to 5°C maintained by jacket-controlled Buchi ChemReact CR-60 pilot-scale reactors. The reaction sequence involves dissolving 1.0 molar equivalent of the acid in toluene containing 0.1 wt% DMF as catalyst, adding 1.05 equivalents of thionyl chloride dropwise at 0°C, and aging for 2.5 hours before charging the substituted aniline (1.0 eq) pre-dissolved in 10% aqueous NaOH to maintain pH 9.5–10.5 during amide bond formation. The target compound, typically a 3,4-dichloroisothiazole-5-carboxanilide, precipitates from the organic layer upon cooling to -5°C and is isolated via Nutsche filter washed with cold toluene, yielding 72% to 88% after vacuum drying at 50°C/10 mbar on a Buchi R-250 rotary evaporator. Purity exceeding 98% by HPLC (area%, C18 column, 70:30 acetonitrile:water mobile phase, 1.0 mL/min) is essential for subsequent greenhouse pot trials where the active ingredient is formulated as a 20% EC (emulsifiable concentrate) using Solvesso 200 ND and anionic/nonionic emulsifier blends at 8 wt%. Registration under EU Regulation (EC) No 1107/2009 for plant protection products requires OECD 307 aerobic soil degradation half-life data (DT₅₀) assessed in at least four representative EU soils at 20°C and 60% water-holding capacity, with the dichlorinated isothiazole ring demonstrating a DT₅₀ typically ranging from 22 to 85 days depending on soil organic carbon content and clay fraction.

    Field-scale synthesis campaigns at 2,000-gallon glass-lined steel reactors (e.g., Pfaudler GL series) require careful control of the acid chloride generation exotherm; the ΔTadiabatic of thionyl chloride addition is +115°C for the neat reaction mass, mandating staged addition over 90 minutes with brine cooling capacity of -15°C at 45 kW/m² heat transfer area. Process safety interlocks on the Siemens SIMATIC PCS 7 distributed control system are calibrated to trigger emergency quench via dump into a 5,000-liter kill tank containing 10% sodium bicarbonate when the jacket outlet temperature exceeds +8°C for more than 30 seconds, a threshold based on accelerating decomposition of the acid chloride intermediate that releases sulfur dioxide and hydrogen chloride gases. The anilide product's melting point, typically 142°C to 168°C for the 4-fluoro-3-chloroanilide derivative, dictates the dryer tray temperature limit during final polishing under 10 mbar vacuum, where exceeding the Tm minus 30°C threshold causes caking that reduces sieve passage through 50-mesh ( 297 μm aperture) screens to below 85%.

    An alternative reaction pathway bypasses acid chloride isolation entirely: the potassium salt of 3,4-Dichloroisothiazole-5-Carboxylic Acid is suspended in acetone at 0°C and treated with ethyl chloroformate (1.1 eq) and triethylamine (1.2 eq) to generate the mixed anhydride in situ, followed by addition of substituted hydroxylamine hydrochloride to yield the corresponding hydroxamic acid derivative, a structural motif showing EC₅₀ < 5 mg/L against Botrytis cinerea mycelial growth inhibition in 96-well microtiter assays. This avoids the HCl plume scrubber load associated with thionyl chloride use on multi-ton campaigns, reducing the demand on the Körting water-jet vacuum system scrubbing loop to process the SO₂ off-gas stream through a 5 wt% NaOH packed column at 2.0 Nm³/h flow. Published data for the mixed anhydride route with this specific isothiazole carboxylic acid is limited, but analogous heterocyclic mixed anhydride preparations achieve overhead yields in the 80–93% range when acetone is rigorously dried over 4Å molecular sieves to <50 ppm water as determined by Mettler Toledo C30 coulometric KF titrator.

    When the Isocyanate Blocking Component in Moisture-Cure Urethane Adhesives Fails Prematurely at Elevated Humidity

    The potassium salt or zinc complex of 3,4-Dichloroisothiazole-5-Carboxylic Acid functions as a latent isocyanate blocking agent capable of deblocking at 120°C to 135°C, a thermal window that aligns with the cure cycle of one-component moisture-cure hot-melt polyurethane adhesives processed through Nordson ProBlue melter applicators at 130°C slot-die coating temperature onto oriented strand board (OSB) substrates. When formulated at 2.0 to 4.0 parts per hundred polyol (php) into a prepolymer based on 4,4'-MDI and a 2,000 MW polypropylene glycol diol (OH value 56), the blocking reaction sequesters approximately 15% to 25% of the available NCO groups as thermally labile carboxamide adducts, confirmed by the disappearance of the 2270 cm⁻¹ isocyanate peak in ATR-FTIR and corresponding reduction in DIN EN 1242:2013 free isocyanate titration values from 12.8% NCO to 9.6% NCO. Lamination onto 18 mm plywood on a Barberán PUR laminating line at 45 m/min line speed requires a bond strength development of ≥0.3 N/mm² within 45 minutes as per ASTM D7247-17 cantilever beam testing on 50 mm × 200 mm cut specimens, a rate that is compromised when storage of the packaged adhesive at >30°C and >70% RH for more than 14 days prematurely triggers deblocking and crosslinking in the unopened pail, causing a viscosity increase from 15,000 mPa·s to over 110,000 mPa·s at 120°C (Brookfield DV-III Ultra with Thermosel, spindle SC4-27 at 5 RPM) that exceeds the pumping capacity of the gear pump on the melter unit.

    The critical limiting factor in this application is moisture ingress through the blown polyethylene liner of the 20-liter pail, quantified by ASTM F1249-20 water vapor transmission rate testing: liners exceeding 2.0 g/m²/day at 38°C/90% RH are unacceptable for blocking-agent-stabilized adhesives because hydrolytic cleavage of the isothiazole-blocked NCO adduct regenerates free amine species that catalyze further polycondensation at an autoaccelerating rate, producing carbon dioxide bubbles that manifest in the laminated panel as delamination blisters exceeding 5 mm diameter under EN 314-1:2004 Class 3 wet test conditions ( 72 hours boiling water immersion). A desiccant breather cap containing molecular sieve 13X installed on the pail bung reduces headspace dew point to -30°C, extending shelf-life to 8 weeks at 25°C ambience. Published data for the zinc salt variant of this particular carboxylic acid functioning as a blocking species is limited, but tin-free catalyst compatibility is advantageous in meeting EU Regulation (EU) 10/2011 overall migration limits for food contact adhesives used in flexible packaging lamination.

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    Certification & Compliance
    More Introduction
    In the synthesis of fungicidal active ingredients targeting the succinate dehydrogenase (SDH) complex, the heterocyclic scaffold of 3,4-dichloroisothiazole-5-carboxylic acid (CAS 1407-24-6, molecular formula C₄HCl₂NO₂S, molecular weight 198.03 g·mol⁻¹) provides a critical vector for introducing two chlorine substituents at positions that modulate electron density and metabolic stability. The compound is typically supplied as a crystalline solid with a purity specification of ≥98.5% (HPLC, area normalization) and an assay of ≥97.0% (argentometric titration following Schöninger flask combustion). Single-batch lots produced via a tetrachlorothiophene-to-isothiazole rearrangement route yield a light-yellow to off-white powder with a melting range of 162–165 °C (DSC, 10 K·min⁻¹). The methyl ester derivative, commonly prepared in situ for further elaboration, exhibits a slightly broader melting range due to residual esterification catalyst carryover unless subjected to short-path distillation under reduced pressure (≤0.5 mbar).

    What Limits the Direct Amidation of 3,4-Dichloroisothiazole-5-Carboxylic Acid Under Microwave Irradiation?

    Attempts to accelerate amide bond formation using microwave-assisted protocols encounter a competing decarboxylation pathway that becomes kinetically significant when the internal reaction temperature exceeds 148 °C. Differential scanning calorimetry traces correlate the onset of exothermic mass loss at 151 ± 3 °C with the liberation of CO₂ and formation of 3,4-dichloroisothiazole as the primary degradation product, detectable by GC-MS at m/z 149/151/153 (isotopic cluster for two chlorine atoms). Production-scale amidation on a 50 L glass-lined reactor therefore employs pre-cooled DMF as solvent and a controlled addition rate of thionyl chloride to generate the acid chloride, holding the jacket temperature at −5 to 0 °C to maintain a solution temperature below 10 °C during the exothermic activation step. Comparative reactivity studies using the acid chloride route vs. carbodiimide-mediated coupling (EDC·HCl/HOBt in acetonitrile) have documented 12–18% lower isolated yields for the latter when the carboxylic acid batch contained residual moisture above 0.3 wt% (Karl Fischer), attributed to hydrolysis of the activated ester intermediate. A typical downstream processing sequence for a 5 kg reaction scale involves quenching the acid chloride solution into an aqueous potassium carbonate slurry maintained at 0–5 °C. Filtration through a 0.5 μm polypropylene cloth followed by reslurrying in chilled deionized water yields a technical-grade intermediate with a chloride content, measured as residual NaCl, of <0.1%. Vacuum drying at 40 °C for 16 hours reduces the loss on drying to <0.5% (Mettler Toledo halogen moisture analyzer, 105 °C endpoint). Users of rotary drum vacuum dryers with 316L stainless steel construction have reported localized darkening of the product at the steam jacket interface if the wall temperature overshoots 45 °C during the initial heat-up phase, a phenomenon reversible only by recrystallization from toluene/heptane (3:1 v/v).

    Difference in Reactivity Profile Compared to 4,5-Dichloroisothiazole-3-Carboxylic Acid

    The regioisomeric counterpart, 4,5-dichloroisothiazole-3-carboxylic acid, exhibits a markedly attenuated propensity toward nucleophilic acyl substitution owing to the electronic character imparted by the adjacent ring nitrogen. In the 5-carboxylic acid regioisomer, the carboxyl group is situated at a position where the electron-withdrawing effect of the endocyclic sulfur and the imine-type nitrogen creates a stronger inductive pull, raising the carbonyl carbon electrophilicity as assessed by the computed C=O stretching frequency at ~1724 cm⁻¹ (FTIR, KBr pellet) compared to ~1698 cm⁻¹ for the 3-carboxylic acid isomer. This difference manifests practically in a 15–20% shorter reaction time for esterification with methanol under Fischer-Speier conditions (H₂SO₄ cat., reflux, 65 °C). Furthermore, the 5-carboxylic acid is less susceptible to ring-opening degradation under strongly basic conditions; treatment with 2M NaOH at 25 °C for 24 hours leaves 94% of the isothiazole ring intact, whereas the 3-carboxylic acid analogue undergoes 35–40% degradation to acyclic thiol intermediates under identical conditions, as monitored by 1H NMR disappearance of the aromatic proton singlet. For solid-phase peptide synthesis applications requiring temporary protection of a cysteine residue, the activated pentafluorophenyl (Pfp) ester of 3,4-dichloroisothiazole-5-carboxylic acid has been utilized as a capping agent, leveraging the irreversible formation of a thioether linkage that is refractory to HF cleavage. In contrast, the corresponding Pfp ester of the 3-carboxylic acid isomer yields a thioester that undergoes partial hydrolysis (8–12%) during the standard TFA cleavage cocktail (95% TFA, 2.5% water, 2.5% TIS). These regiochemistry-driven stability differences inform the choice of the 5-carboxylic acid derivative in impurity profiling reference standard syntheses, where persistent mass-balance discrepancies as low as 0.15% can trigger out-of-specification investigations under ICH Q7. When tetramethylammonium fluoride (TMAF) is employed as a silyl-deprotection agent during the synthesis of a 3,4-dichloroisothiazole-5-carboxamide prodrug, the fluoride ion interacts competitively with the chlorine atoms at positions 3 and 4. C-4, being para to the sulfur atom and meta to the imine nitrogen, exhibits a 3.7-fold higher relative rate of halogen substitution in the presence of 5 equivalents of TMAF in DMSO at 60 °C than does C-3, based on 19F NMR integration of the resulting fluoro-dechlorinated byproducts. This differential lability necessitates the inclusion of a radical scavenger (BHT at 0.1 wt%) and rigorous control of the fluoride-to-substrate ratio at ≤3.0 to preserve the desired dichloro substitution pattern. Pilot plant campaigns on a 100 L Hastelloy C-22 reactor have validated that a stepwise addition of TMAF over 90 minutes limits the total fluorinated impurity content to <0.8% (HPLC, 254 nm), which is below the toxicological qualification threshold of 1.0 mg/day defined in ICH M7 for a compound with a maximum daily dose of 250 mg. The compound’s solubility profile in common process solvents is a critical parameter during route scouting. At 20 °C, 3,4-dichloroisothiazole-5-carboxylic acid exhibits a saturation concentration of <5 g·L⁻¹ in toluene and <2 g·L⁻¹ in heptane, whereas solubility in tetrahydrofuran exceeds 180 g·L⁻¹. This pronounced disparity is exploited during purification: a crude reaction mixture is concentrated, taken up in THF, and precipitated by controlled addition to a ten-fold volume of n-heptane at −10 °C, resulting in a 92–95% recovery with a 99.2% LC purity. Attempts to substitute methyl tert-butyl ether (MTBE) for THF have resulted in paste-like slurries with poor filtration rates (~12 L·m⁻²·h⁻¹ through a 10 μm stainless steel mesh) owing to the formation of a needle-shaped crystal habit that compacts into a nearly impermeable filter cake. The addition of 0.5% seed crystals of the desired thick prismatic polymorph (obtained via slow cooling of a saturated toluene solution from 70 °C to 5 °C at 0.1 °C·min⁻¹) effectively suppresses needle formation and improves filtration throughput to ~85 L·m⁻²·h⁻¹.

    Analytical Specification and Certificate of Analysis Parameters

    Typical release specification against USP/EP acceptance criteria for advanced pharmaceutical intermediates
    ParameterMethodSpecification Limit
    AppearanceVisual (against white background, D65)Off-white to pale yellow crystalline powder
    Assay (anhydrous basis)Potentiometric titration with tetrabutylammonium hydroxide97.0–102.0%
    Purity (HPLC)Inertsil ODS-3, 5 μm, 250×4.6 mm; mobile phase: 0.1% H₃PO₄/MeCN gradient; detection 230 nm≥98.5% main peak
    Related substancesHPLC as above, relative response factors verifiedSingle impurity ≤0.5%, total ≤1.5%
    Water (Karl Fischer)Coulometric titration, Hydranal Composite 5≤0.5%
    Residual solventsHeadspace GC-FID, BP-624 columnToluene ≤890 ppm, heptane ≤500 ppm, THF ≤720 ppm (class 2)
    Sulfated ashIgnition at 600 °C≤0.1%
    Chloride (ionic)Ion chromatography with suppressed conductivity≤200 ppm
    A comparison of these metrics with published certificates for the isomeric 4,5-dichloroisothiazole-3-carboxylic acid reveals a systematically higher (2.4–3.8-fold) chloride content in the latter, stemming from the formation of a water-soluble acid salt during the chlorination step that requires an additional ethanol/water reslurry cycle for removal. Consequently, facility changeover from the 3-carboxylic acid to the 5-carboxylic acid necessitates a validated cleaning procedure involving a first pass with 5% sodium bicarbonate solution at 50 °C to neutralize residual acidic species, followed by a 70 °C water rinse, and dried until the condensate resistivity exceeds 18 MΩ·cm. Swab sampling limits for cross-contamination have been set at 50 μg/L for the 5-carboxylic acid in the subsequent production campaign.

    Intermediates for Downstream Derivatization and Handling Constraints

    Pilot-scale preparation of the acid chloride, 5-(chlorocarbonyl)-3,4-dichloroisothiazole, is routinely monitored by in-line ReactIR to track the disappearance of the carboxylic acid carbonyl band at 1718 cm⁻¹ and the emergence of the acyl chloride band at 1785 cm⁻¹. A processing window of ≤5 °C must be maintained during the solvent switch from DMF to dichloromethane for subsequent Friedel-Crafts acylation sequences, as the acid chloride undergoes rapid solvolysis on contact with ambient moisture; the half-life in unstabilized dichloromethane containing 150 ppm water is 9 minutes at 22 °C, dropping to 2.3 minutes at 30 °C. Production-scale distillation of the acid chloride under reduced pressure (0.1 mbar, boiling range 92–95 °C) using a wiped-film evaporator with an internal condenser temperature of −10 °C is feasible, but exposure of the distillate to stainless steel surfaces must be minimized to prevent trace metal-catalyzed dechlorination. Glass-lined or PTFE-lined receivers are mandatory; even 10 ppm of dissolved iron can double the rate of C-4 chlorine substitution within 6 hours of holding time. When a coupling partner bears a free primary amine, the order of addition is critical to avoid symmetrical urea formation via phosgene-like side reactivity of the acid chloride with adventitious water. Introduction of the amine solution to a pre-formed mixed anhydride prepared from the carboxylic acid and isobutyl chloroformate in the presence of N-methylmorpholine at −15 °C reduces the total dimeric urea impurity level to <0.2%, as determined by LC-MS extracted ion chromatogram (EIC) at m/z corresponding to the urea adduct. This mixed anhydride route has been adopted for the multikilogram manufacture of a Phase II clinical candidate targeting a parasitic nematode ion channel, achieving a cumulative yield over three telescoped steps (activation, coupling, and deprotection) of 71% compared to 54% for the acid chloride-based process. Storage stability of bulk 3,4-dichloroisothiazole-5-carboxylic acid under tropical climate conditions (30 °C/75% RH) was evaluated per ICH Q1A(R2) guidelines. After 6 months in double LDPE bags inside a sealed HDPE drum with a desiccant pouch, the assay declined by 0.3% with no new impurity peaks above the 0.05% reporting threshold. However, when the desiccant was omitted, moisture ingress raised the water content to 1.8% and triggered a slow hydrolysis that yielded 3,4-dichloroisothiazole-5-carboxylic acid hydrate, detectable as a shoulder on the DSC melting endotherm at 147 °C. The hydrate can be completely reverted to the anhydrous form by drying at 50 °C under vacuum for 24 hours. Facilities operating in Southeast Asia have implemented nitrogen-flushed packaging with integrated humidity indicator cards (≤10% RH target) to eliminate this aging phenomenon. A further distinction from the broader family of dichloroisothiazole regioisomers lies in the 13C NMR chemical shift of the C-5 carbon bearing the carboxyl group. In 3,4-dichloroisothiazole-5-carboxylic acid, the C-5 resonance appears at ~161.4 ppm (DMSO-d6, 125 MHz), deshielded by the combined influence of the chlorine at C-4 and the ring heteroatoms. This chemical shift is diagnostic for batch-to-batch structural identity and serves to differentiate the product from the 3-carboxylic acid isomer, whose carboxyl-bearing carbon resonates at ~158.2 ppm under identical conditions. NMR spectroscopy in production QC laboratories typically employs a 400 MHz instrument with a 5 mm broadband probe, using 20 mg of sample dissolved in 0.6 mL DMSO-d6; the absence of signals in the 150–155 ppm region is a release criterion for isomer content.
    Comparative stability in selected organic solvents under accelerated conditions (40 °C, 7 days)
    SolventRecovery (%)Degradation Product (>1%)
    Acetonitrile99.8None detected
    N,N-Dimethylformamide98.23,4-Dichloroisothiazole (1.3%)
    Ethyl acetate99.5None detected
    Methanol95.4Methyl ester (4.1%), unknown (0.5%)
    Acetone97.6Self-condensation product (2.0%)
    The data in the table above illustrate the solvent-dependent degradation pathways; methanol promotes direct esterification even in the absence of an acid catalyst, while acetone undergoes aldol-type condensation at the carbonyl carbon following nucleophilic attack by the enolate form. As a consequence, acetone is excluded from final purification steps, and solvent exchange to acetonitrile is specified in the master batch record for the final API step when 3,4-dichloroisothiazole-5-carboxylic acid is the starting material of a regulatory filing under a Type II Drug Master File. The compound’s utility as a coupling partner in palladium-catalyzed C–H activation has been limited by the tendency of the chlorine atoms to participate in oxidative addition with electron-rich palladium(0) species. When employing Pd(PPh₃)₄ as catalyst in a deprotonative cross-coupling with a thiazole C-2 position, product profiles reveal up to 8% of a homocoupling dimer linked through the C-3 position of the isothiazole ring. Switching to the air-stable PdCl₂(dtbpf) precatalyst (2 mol%) and using potassium pivalate as base in dioxane at 90 °C suppresses homocoupling to <0.5%, as determined by a dedicated HPLC method with a 60-minute gradient. This finding is consistent with a mechanism where pivalate accelerates the concerted metalation-deprotonation step without generating a solvent-stabilized Pd(0) intermediate that would be susceptible to oxidative addition into the C–Cl bonds.