|
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 | 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. |
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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.
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 AcidAgrochemical 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 HumidityThe 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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| Parameter | Method | Specification Limit |
|---|---|---|
| Appearance | Visual (against white background, D65) | Off-white to pale yellow crystalline powder |
| Assay (anhydrous basis) | Potentiometric titration with tetrabutylammonium hydroxide | 97.0–102.0% |
| 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 substances | HPLC as above, relative response factors verified | Single impurity ≤0.5%, total ≤1.5% |
| Water (Karl Fischer) | Coulometric titration, Hydranal Composite 5 | ≤0.5% |
| Residual solvents | Headspace GC-FID, BP-624 column | Toluene ≤890 ppm, heptane ≤500 ppm, THF ≤720 ppm (class 2) |
| Sulfated ash | Ignition at 600 °C | ≤0.1% |
| Chloride (ionic) | Ion chromatography with suppressed conductivity | ≤200 ppm |
| Solvent | Recovery (%) | Degradation Product (>1%) |
|---|---|---|
| Acetonitrile | 99.8 | None detected |
| N,N-Dimethylformamide | 98.2 | 3,4-Dichloroisothiazole (1.3%) |
| Ethyl acetate | 99.5 | None detected |
| Methanol | 95.4 | Methyl ester (4.1%), unknown (0.5%) |
| Acetone | 97.6 | Self-condensation product (2.0%) |