2,4-Dichlorothiazole

2,4-Dichlorothiazole


    • Product Name 2,4-Dichlorothiazole
    • Alias 2,4-Dichloro-1,3-thiazole
    • Einecs 211-412-8
    • 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

    505883

    Chemical Formula C3HCl2NS
    Molecular Weight 168.02 g/mol
    Appearance Solid (usually colorless to pale yellow)
    Boiling Point Approx. 218 - 220 °C
    Melting Point Approx. 45 - 47 °C
    Solubility In Water Low solubility in water
    Solubility In Organic Solvents Soluble in many organic solvents like ethanol, acetone
    Odor Characteristic pungent odor
    Density Approx. 1.64 g/cm³
    Flash Point Approx. 86 °C
    Stability Stable under normal conditions but may react with strong oxidizing agents

    As an accredited 2,4-Dichlorothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of 2,4 - Dichlorothiazole packaged in a sealed, corrosion - resistant plastic bottle.
    Shipping 2,4 - Dichlorothiazole is a chemical. Shipping should follow strict regulations. It must be properly packaged in corrosion - resistant containers, labeled clearly, and transported by carriers licensed for hazardous chemicals to ensure safety during transit.
    Storage 2,4 - Dichlorothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, open flames, and incompatible substances such as strong oxidizers. Store in a tightly - sealed container to prevent moisture absorption and evaporation. It is crucial to label the storage container clearly to avoid misidentification.
    Application of 2,4-Dichlorothiazole

    In industrial heterocyclic chemistry, 2,4-Dichlorothiazole occupies a narrow but commercially critical niche as a bis-electrophilic scaffold. The chlorine atoms at the 2- and 4-positions exhibit differential reactivity toward nucleophilic displacement: the 4-position chlorine is generally more labile under basic conditions, while the 2-position halogen requires elevated temperatures or copper(I)-mediated catalysis for efficient substitution. This orthogonal activation profile enables sequential functionalization strategies that are exploited across multiple downstream manufacturing verticals. The compound is handled as a low-melting solid (mp 42–44 °C) that darkens upon prolonged exposure to ambient moisture, necessitating storage under inert gas with desiccant packs in HDPE drums lined with antistatic film. Commercial shipments from Asian manufacturing hubs routinely specify purity by GC area% at ≥98.5%, with the predominant impurity being the monochloro isomer 2-chlorothiazole, which arises from incomplete chlorination and is quantified using a DB-5 capillary column (30 m × 0.25 mm ID, 0.25 µm film) with FID detection at 280 °C.

    Fungicidal Sulfonamide Conjugates in Agrochemical Pipeline Development

    Several patent families assigned to multinational crop science entities disclose 2,4-dichlorothiazole as the core heterocycle in experimental succinate dehydrogenase inhibitor (SDHI) candidates. The synthetic sequence begins with selective displacement of the 4-chloro substituent by 2-aminomethylpyridine or a substituted aniline nucleophile in refluxing acetonitrile with powdered K₂CO₃ as the acid scavenger. Reaction progress is monitored by TLC on silica gel 60 F₂₅₄ plates developed in ethyl acetate/hexane (3:7 v/v), targeting disappearance of the starting material at Rf 0.68. The intermediate 4-amino-2-chlorothiazole is isolated by drowning the reaction mass into ice water, filtering the precipitate through a Nutsche filter, and drying under vacuum at 45 °C to a moisture content below 0.3 wt% by Karl Fischer titration. Subsequent sulfonylation at the 4-amino position with 3-(difluoromethyl)-1-methyl-1H-pyrazole-4-sulfonyl chloride in dichloromethane containing 1.05 equivalents of triethylamine at 0–5 °C yields the penultimate intermediate. The residual 2-chloro handle remains available for late-stage diversification, typically a Suzuki-Miyaura coupling with a boronic acid partner bearing a substituted phenyl or pyridyl ring. The coupling employs Pd(PPh₃)₄ at 2 mol% loading and aqueous Na₂CO₃ in a degassed dioxane/water biphasic system at 90 °C for 12–16 hours. Final products are purified by flash chromatography on silica gel (particle size 40–63 µm) and recrystallized from ethanol/water to achieve ≥99.0% purity by HPLC at 254 nm. Published greenhouse efficacy data against Botrytis cinerea on cucumber and Puccinia recondita on wheat indicates EC₅₀ values in the single-digit parts-per-million range for the most active analogues, though field trial results remain proprietary and the specific formulations incorporating these compounds have not yet received registration in major agricultural markets.

    Process engineering for kilo-lab scale-up of the 4-amination step has identified a significant thermal hazard associated with the exotherm upon K₂CO₃ addition. Reaction calorimetry in a Mettler Toledo RC1e reactor recorded an adiabatic temperature rise of ΔTad = 64 K and a maximum temperature of the synthesis reaction (MTSR) of 112 °C when the base is charged in a single portion at 25 °C. The recommended safer protocol involves controlled dosing of the carbonate as a slurry in acetonitrile over 45 minutes while maintaining jacket temperature at 15 °C, with a maximum allowable reaction temperature of 80 °C before emergency quenching with aqueous ammonium chloride. The 4-chloro displacement with poorly nucleophilic anilines requires the addition of catalytic tetrabutylammonium iodide (4 mol%) to achieve complete conversion within 8 hours at reflux; without the phase-transfer catalyst, residual starting material persists at 12–18% by GC even after 24 hours. Corrosion of 316L stainless steel reactors has been observed in prolonged campaigns, attributed to chloride ion accumulation from the displacement reaction, and glass-lined equipment is specified for production batches exceeding 100 kg.

    When an Antiviral Pharmacophore Requires Regioselective Heteroaryl Installation

    Medicinal chemistry programs targeting non-nucleoside inhibition of viral RNA-dependent RNA polymerase have employed 2,4-dichlorothiazole as a central building block. The strategy exploits sequential C–N bond formation at the 2-position followed by C–C bond formation at the 4-position, or the reverse order depending on the substituent electronic demands. In one disclosed route toward a clinical candidate, the 2-chloro group is displaced by 4-fluoro-2-methoxyaniline in N-methyl-2-pyrrolidone (NMP) at 130 °C using 1.2 equivalents of N,N-diisopropylethylamine (DIPEA). The solvent selection is critical: dipolar aprotic solvents with high boiling points accelerate the otherwise sluggish 2-position substitution, with DMSO, DMF, and NMP affording relative rate ratios of approximately 1.0 : 1.8 : 3.2 as measured by in-situ ReactIR monitoring of the C–N stretch at 1340 cm⁻¹. After aqueous workup and crystallization from isopropanol, the 4-chloro-2-arylamino thiazole intermediate is subjected to a Negishi coupling with cyclopropylzinc bromide prepared in situ from cyclopropyl bromide and zinc dust activated with 1,2-dibromoethane and TMSCl. The coupling proceeds in THF at 60 °C with Pd₂(dba)₃ (1 mol%) and SPhos (2 mol%) as the catalytic system, reaching full conversion in 3 hours. The final compound is isolated as its hydrochloride salt by treatment with HCl in dioxane (4 M) and recrystallized from acetonitrile/MTBE to deliver the active pharmaceutical ingredient in polymorphically pure Form A, confirmed by XRPD with characteristic peaks at 2θ = 8.7°, 16.2°, and 22.9° (Cu Kα radiation). Residual palladium content is controlled below 10 ppm by treatment with a trimercaptotriazine-functionalized silica scavenger (Si-TMT) at 50 °C for 2 hours, with quantification by ICP-MS following microwave digestion in concentrated HNO₃/H₂O₂.

    The generation and consumption of the organozinc reagent present a robustness challenge in larger-scale preparations. Activation of zinc dust requires rigorous control of particle size distribution (D₅₀ ≤10 µm) and the exotherm during 1,2-dibromoethane addition must be managed by portionwise addition while maintaining an internal temperature below 40 °C to avoid runaway polymerization of the solvent. Titration of the resulting cyclopropylzinc bromide solution against iodine in THF at 0 °C typically reveals concentrations of 0.45–0.55 M, and batch-to-batch variability in this concentration is a primary source of yield fluctuation in the coupling step. When the organozinc titer drops below 0.40 M, the stoichiometry must be adjusted to 2.5 equivalents relative to the 4-chloro substrate to ensure complete conversion, driving the isolated yield of the crude product after silica plug filtration to 74–81% (compared to 88–92% with freshly titrated reagent at 2.0 equivalents). In-process control by HPLC at 210 nm uses a C18 column (150 × 4.6 mm, 3 µm) with a gradient of 10–95% acetonitrile in water containing 0.05% trifluoroacetic acid over 15 minutes. The Product monograph filed with regulatory authorities includes a specification for the 2,5-dichlorothiazole positional isomer at NMT 0.10%, as this impurity can be carried through the synthetic sequence and form a regioisomeric analogue with distinct pharmacological activity.

    Photo-stabilization of Engineering Thermoplastics in Outdoor Glazing Applications

    A structurally distinct class of benzotriazole ultraviolet absorbers (UVA) derived from 2,4-dichlorothiazole has been developed for polycarbonate sheet used in architectural and transportation glazing where long-term retention of visible light transmission and impact resistance is mandatory. The synthesis initiates with the selective reduction of the 4-nitro group in a 2-chloro-4-nitrothiazole precursor, which is itself prepared by nitration of 2-chlorothiazole with mixed acid (HNO₃/H₂SO₄) at 0–5 °C. Catalytic hydrogenation over Raney nickel (5 wt% loading, wet basis) in methanol at 30 psi H₂ pressure and 25 °C provides the corresponding 4-amino compound. Diazotization with NaNO₂ in aqueous HCl at −5 °C followed by coupling with 2-tert-butyl-6-methylphenol in alkaline methanol generates the azo intermediate, which is then oxidatively cyclized using copper(II) sulfate and aqueous ammonia in refluxing methanol to form the benzotriazole ring. The residual 2-chloro group on the thiazole ring is subsequently displaced by 2-ethylhexylamine in xylene at reflux with K₂CO₃, providing a tertiary amine-substituted UVA with enhanced solubility in polycarbonate resin. Incorporation into the polymer matrix is achieved by compounding a 15 wt% masterbatch of the UVA in polycarbonate powder (Makrolon 3108 grade, MVR 6 cm³/10 min at 300 °C/1.2 kg per ISO 1133-1:2022) on a co-rotating twin-screw extruder with L/D ratio of 40:1 and screw diameter 26 mm, operated at a barrel temperature profile of 260–290 °C and screw speed 350 rpm. The masterbatch is let down to a final UVA concentration of 0.25–0.40 wt% in the finished sheet, which is produced by a single-screw extruder (L/D 33:1, compression ratio 2.5:1) feeding a flat die with a polished chill roll stack maintained at 130 °C.

    Accelerated weathering performance is evaluated according to ISO 4892-2:2013 (xenon-arc lamp, daylight filter, black panel temperature 65 °C, relative humidity 50%, irradiance 0.51 W/m² at 340 nm). Polycarbonate sheets containing the thiazole-derived UVA at 0.30 wt% retained 87% of initial notched Izod impact strength (ISO 180/A:2023) and exhibited a Yellowing Index (YI) shift of less than 4 units (ASTM E313-20) after 5000 hours of exposure, compared to YI shifts exceeding 12 units for unprotected control specimens. Migration and blooming behavior was assessed by storing the sheet at 90 °C and 95% RH for 1000 hours followed by FTIR-ATR surface analysis; no absorption bands characteristic of the UVA were detected at the sheet surface within the instrument detection limit of ~0.05 wt%. The compatibility of the thiazole-benzotriazole UVA with tin-based heat stabilizers used in rigid PVC profiles was found to be poor, as the organotin mercaptide (typically dioctyltin bis(2-ethylhexyl thioglycolate)) promotes dechlorination of the thiazole ring at processing temperatures above 190 °C, liberating HCl that corrodes tool steel dies and catalyzes PVC dehydrochlorination. For coextruded PVC/polycarbonate capstock systems, a tie layer of tin-free acrylic copolymer is mandatory to prevent direct contact between the UVA-modified polycarbonate cap and the tin-stabilized PVC substrate.

    Injection molding of polycarbonate automotive glazing components (side windows, panoramic roof panels) containing the thiazole-based UVA requires specific attention to mold surface temperature uniformity. Localized cold spots below 115 °C during the filling phase can induce differential orientation of the UVA molecules in the frozen skin layer, manifesting as visible haze bands in transmitted light. Mold temperature control units maintaining 125 ± 3 °C across all zones, combined with sequential valve gating to manage the melt front velocity below 200 mm/s, are standard countermeasures documented in processing guidelines from a major German automotive OEM. The finished molded parts are subjected to a condensation test (ISO 6270-2:2017) for 240 hours followed by cross-cut adhesion testing (ISO 2409:2020) of any applied hardcoat; adhesion loss exceeding Grade 2 triggers rejection of the production batch and investigation into residual volatiles in the polycarbonate substrate, which are quantified by headspace GC-MS at 120 °C for 30 minutes and specified at total VOC less than 50 µg/g.

    The synthesis of 2,4-dichlorothiazole-derived organosulfur compounds with vulcanization acceleration activity has been investigated, though published data for this specific configuration is limited. Patent literature describes the reaction of 2,4-dichlorothiazole with two equivalents of sodium 2-mercaptobenzothiazole in refluxing ethanol, yielding a bis-thioether that was evaluated as a secondary accelerator in a natural rubber / styrene-butadiene rubber (NR/SBR) truck tire tread compound. The accelerator was incorporated at 0.3 phr alongside CBS (N-cyclohexyl-2-benzothiazolesulfenamide) at 1.2 phr and sulfur at 1.8 phr. Moving-die rheometer (MDR) data at 160 °C per ASTM D5289-19a showed a reduction in scorch time (ts2) from 4.2 minutes to 3.1 minutes relative to the control without the thiazole accelerator, while the cure rate index increased by 18%. Tensile properties measured on dumbbell specimens (ISO 37:2017, Type 2) after cure to t90 at 160 °C showed a 9% increase in modulus at 300% elongation, from 12.4 MPa to 13.5 MPa, with no significant change in elongation at break which remained at 480–510%. The reversion resistance at 180 °C (a critical parameter for truck tire service where running temperatures approach 100 °C in the shoulder region) was assessed by monitoring the torque decay over 60 minutes on the MDR; the compound containing the thiazole accelerator retained 82% of its maximum torque compared to 74% for the control. However, the commercial viability of this accelerator system has not been established, and concerns about nitrosamine generation during vulcanization (relevant to workplace exposure limits under German TRGS 552) have not been addressed in the available literature.

    Where Does This Heterocycle Find Application in Marine Antifouling Systems?

    Self-polishing copolymer (SPC) antifouling paints formulated with thiazole-functionalized zinc acrylate binders represent a niche but documented use of 2,4-dichlorothiazole derivatives. The monomeric precursor is prepared by esterification of acrylic acid with 2,4-dichloro-5-hydroxymethylthiazole, which is itself obtained by selective reduction of the corresponding aldehyde with sodium borohydride in methanol at 0–10 °C. The aldehyde, in turn, is generated by Vilsmeier-Haack formylation (POCl₃/DMF) of 2,4-dichlorothiazole at the 5-position, a reaction that proceeds with 76% isolated yield when the reagent ratio is controlled at 1.15 equivalents of the Vilsmeier complex and the quench is performed by pouring onto crushed ice with vigorous agitation. The acrylic ester monomer is copolymerized with butyl acrylate, methyl methacrylate, and acrylic acid at a weight ratio designed to achieve a glass transition temperature (Tg) of 8–12 °C as calculated by the Fox equation, using 2,2′-azobis(2-methylbutyronitrile) (AMBN) as initiator at 1.0 wt% on total monomers in a mixture of xylene and n-butanol (4:1 w/w) at 90 °C under nitrogen. The resulting copolymer, containing 12–18 wt% of the thiazole ester units, is formulated into a paint at 40% pigment volume concentration (PVC) with cuprous oxide as the primary biocide and zinc oxide as the pigment extender and polishing rate regulator.

    Seawater hydrolysis of the thiazole ester pendant groups generates a hydrophilic carboxylate surface layer on the copolymer that is slowly eroded by moving seawater, continuously exposing fresh biocide at the coating surface. Polishing rate measurements on rotating cylinder test rigs operating at a peripheral speed of 17 knots (equivalent to 8.7 m/s) in natural seawater at 23–25 °C indicate a linear erosion rate of 4.2–5.1 µm/month for paints containing the thiazole-acrylate copolymer, compared to 3.0–3.8 µm/month for conventional copper acrylate binders. The slight acceleration in polishing rate has been attributed to the electron-withdrawing effect of the thiazole ring enhancing the hydrolytic lability of the ester linkage. The critical pigment volume concentration (CPVC) of the formulation must be carefully balanced: exceeding 45% PVC leads to a porous dry film that polishes too rapidly (rate > 8 µm/month), resulting in premature coating depletion within 24 months of service, while PVC below 35% yields a film that polishes slower than 2 µm/month and accumulates a leached layer of insoluble copper salts that inhibits further biocide release. The optimal formulation window is established by laboratory polishing tests using a reciprocating abrasion tester (Taber 5750 Linear Abraser with a CR-2000 Calibrase wheel loaded to 500 g) on films immersed in artificial seawater (ASTM D1141-98e1) at 30 °C, correlating weight loss per cycle to field polishing rates via an empirical calibration curve established for a reference tributyltin self-polishing copolymer paint of known performance history. Environmental regulatory assessment under the EU Biocidal Products Regulation (BPR, Regulation (EU) 528/2012) and IMO Anti-Fouling Systems Convention requirements would be needed for any commercial product; the thiazole moiety is not listed in Annex I of the AFS Convention, but the hydrolysis product (2,4-dichloro-5-hydroxymethylthiazole) has not undergone a comprehensive marine ecotoxicological evaluation, and its octanol-water partition coefficient (log Pow, estimated at 1.8–2.2 by computational models) suggests moderate bioaccumulation potential that would likely trigger a higher-tier risk assessment under the BPR.

    Comparative Substitution Reactivity of 2,4-Dichlorothiazole Under Nucleophilic Conditions
    NucleophileSolventTemperature (°C)Time to >95% Conversion (h)Predominant SiteProduct Ratio (4- : 2-)
    Morpholine (1.1 eq)THF256.0C4-Cl>50:1
    Sodium thiophenolate (1.0 eq)EtOH251.5C4-Cl>50:1
    Benzylamine (1.3 eq)MeCN804.0C4-Cl16:1
    Methanol (10 eq) + K₂CO₃MeOH6518.0C4-Cl6:1
    Imidazole (2.0 eq, neat melt)None1203.0C4-Cl22:1
    Copper(I) cyanide (1.5 eq)NMP15024.0C2-Cl~1:4

    An aqueous-based adhesive system for bonding vulcanized EPDM rubber to a primed metal substrate during automotive weatherseal manufacturing utilizes an intermediate tie coat containing a 2,4-dichlorothiazole-modified polybutadiene resin. The base resin is a maleinized polybutadiene (molecular weight Mw 5,000–8,000 g/mol by GPC against polystyrene standards, acid number 45–55 mg KOH/g) dissolved in toluene at 22% solids. 2,4-Dichlorothiazole is pre-dissolved in xylene at 30% concentration and metered into the resin solution at a ratio of 1 part thiazole per 100 parts resin solids. The mixture is stirred at 40 °C for 2 hours to allow partial reaction between the maleic anhydride groups and the thiazole ring (a reaction believed to involve nucleophilic attack at the 2-position, though the exact structure of the adduct has not been fully characterized in open literature). The activated resin is formulated with carbon black (N330 grade, 20 phr), zinc oxide (3 phr), and a phenolic tackifier resin (SP-1068 type, 5 phr) on a high-speed disperser at 3000 rpm for 20 minutes to achieve a Hegman grind of 6.5+. This composition is applied by brush or robotic spray to the phosphate-treated steel carrier at a dry film thickness of 12–18 µm measured by an eddy current gauge, allowed to flash off for 10 minutes, and then overcoated with a proprietary EPDM-based cover cement containing sulfur, accelerators (MBTS and ZDBC at 0.8 phr each), and a heat-activated crosslinking agent. The assembled weatherseal is cured in a continuous hot air oven at 190 °C for 4 minutes. Peel adhesion testing according to ASTM D429-14 (Method B, 90° peel at 50 mm/min crosshead speed) on specimens conditioned at 23 °C and 50% RH for 24 hours routinely yields values of 8–12 kN/m with cohesive failure within the rubber layer. Omission of the thiazole component typically results in interfacial adhesive failure at 2–4 kN/m. The operative mechanism is hypothesized to involve covalent bonding between the thiazole-modified resin and both the metal oxide surface and sulfur crosslinks in the EPDM matrix, though direct spectroscopic evidence of the postulated interfacial bonds has proven elusive due to the difficulty of isolating nanogram quantities of interphase material for XPS analysis.

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    Certification & Compliance
    More Introduction

    2,4-Dichlorothiazole (CAS 4175-78-4) is a heterocyclic building block supplied as a white to pale yellow crystalline solid with a melting point of 39–41°C and a boiling point of 204–206°C at atmospheric pressure. Commercial product typically carries a purity specification of ≥98.0% by GC, with a single major impurity being the regioisomer 2,5-dichlorothiazole capped at ≤0.5%. Moisture content is controlled below 0.1% (Karl Fischer titration) to prevent ring-opening hydrolysis during storage, and the material is packaged under nitrogen in 25 kg or 50 kg UN-approved fibre drums with aluminium laminate liners. Unlike 2-chlorothiazole, the second chlorine substituent at the 4-position deactivates the ring toward electrophilic attack while preserving reactivity at the 2-position for nucleophilic displacement, making the compound a selective intermediate in the synthesis of thiazole carboxamide fungicides and kinase inhibitor scaffolds.

    Purity-graded product specifications and QC release criteria

    Two standard commercial grades are available: technical grade (minimum 97.0%) and synthesis grade (minimum 98.5%). The technical grade is appropriate for early-stage amination or Suzuki coupling steps where downstream purification removes unreacted starting material, while synthesis grade is specified for final-stage active pharmaceutical ingredient (API) intermediate construction where residual mono-chloro impurities must remain below 0.3% to avoid carry-through genotoxic impurity concerns under ICH M7 guidelines. A representative certificate of analysis for synthesis-grade material includes the following parameters determined by validated in-house methods calibrated against certified reference standards:

    Typical release specification — 2,4-dichlorothiazole, synthesis grade
    ParameterTest methodAcceptance criterion
    Assay (GC, area%)In-house method derived from ASTM D3465-21≥98.5%
    2,5-Dichlorothiazole isomerGC-FID, DB-1 column 30 m × 0.25 mm × 0.25 µm≤0.5%
    Unidentified individual impuritySame as above≤0.10%
    Water contentKarl Fischer coulometry, ISO 760:1978≤0.1%
    AppearanceVisual inspection against white standard tileWhite to off-white crystalline mass
    Melting rangeDifferential scanning calorimetry, onset, 10°C/min38.0–42.0°C

    Lot-to-lot consistency in large-scale amination reactions is strongly correlated with the 2,5-dichlorothiazole content; when this isomer exceeds 0.8%, competitive displacement generates a regioisomeric impurity that co-elutes with the desired 2-amino-4-chlorothiazole intermediate on standard silica TLC (ethyl acetate/hexane 1:4), complicating column chromatography on pilot scale.

    What drives the differential reactivity between 2,4- and 2,5-dichlorothiazole?

    The distinction between 2,4-dichlorothiazole and its 2,5-isomer (CAS 2949-62-4) is of practical consequence in medicinal chemistry and process development. In the 2,4-isomer, the 4-chloro substituent occupies a position conjugated with the ring nitrogen through the C=N–C=C pathway, withdrawing electron density via both inductive and mesomeric effects. This lowers the LUMO energy at C-2 relative to the 2,5-isomer, where the 5-chloro substituent is conjugated only through the sulphur atom and exerts a weaker net activation effect on the 2-position. Experimentally, this manifests as a faster rate of nucleophilic aromatic substitution with primary amines in refluxing ethanol: k2,4/k2,5 ≈ 3.2 for the reaction with n-butylamine at 78°C as determined by competition experiments monitored by 19F NMR after derivatization with 4-fluoroaniline. This kinetic advantage translates directly into lower amine equivalents (1.05 eq vs. 1.30 eq) and shorter cycle times in production of substituted 2-aminothiazoles, which are key intermediates for TRPV1 antagonists and COX-2 selective inhibitors.

    Conversely, the 4-chloro substituent of 2,4-dichlorothiazole is itself susceptible to displacement under forcing conditions (alkoxide in DMF, 120°C), but this reaction requires careful exclusion of moisture to avoid competitive hydrolysis to the corresponding 4-hydroxythiazole, which tautomerizes to an inactive thiazolone. In batch reactors with glass-lined vessels of 2000 L capacity, pH monitoring at the condenser outlet is used as a proxy for hydrolysis onset; a pH drop below 4.0 in the distillate signals HCl evolution from ring degradation, at which point the jacket temperature is immediately ramped down from 120°C to 80°C to salvage the batch.

    Storage stability and handling boundaries in multi-purpose plants

    2,4-Dichlorothiazole is classified as a combustible solid (UN 3077, Class 9 environmentally hazardous substance) and must be stored away from strong oxidizing agents, strong bases, and primary amines. Thermal stability assessed by accelerating rate calorimetry shows an onset temperature for exothermic decomposition at 290°C, but the practical safe storage ceiling is set at 40°C to prevent sublimation-driven headspace accumulation of corrosive chlorinated vapours in closed containers. For operations conducted in multi-purpose plants handling amine hydrochlorides in adjacent bays, dedicated air-handling with HEPA inlet and activated carbon exhaust is mandated because even trace amine vapours diffuse into opened 2,4-dichlorothiazole kegs and initiate surface amination, forming a gummy red-brown layer that fouls charging funnels on automated weigh-hoppers (Schenck Process, type Intecont Plus) during subsequent dispensing.

    The product exhibits a negative solubility coefficient in hydrocarbon solvents: solubility in n-heptane decreases from 12 g/100 mL at 50°C to 2.1 g/100 mL at 0°C, allowing simple recrystallization for recovery from process mother liquors. On one production campaign at pilot scale (50 kg input), solvent recovery by vacuum distillation in a wiped-film evaporator (bühler, 0.1 m² surface) returned material of 96% purity, which was then upgraded by recrystallization from n-heptane/toluene (9:1, v/v) to the synthesis grade target with 88% mass recovery—a workflow now embedded in the plant’s standard waste-minimization protocol.

    If residual palladium is a concern in downstream Suzuki couplings

    When 2,4-dichlorothiazole is employed directly in palladium-catalyzed cross-coupling without prior purification beyond the commercial specification, batch records from an API intermediate scale-up campaign at 30 kg scale documented that the residual iron content (typically < 3 ppm) and palladium scavenger pre-treatment were critical: the 2-position chlorine undergoes oxidative addition with Pd(PPh₃)₄ at 60°C in THF, but if dissolved oxygen exceeds 1 ppm, the catalyst oxidatively degrades to inactive Pd(II) species, resulting in stalling at 60–65% conversion. Switching from magnetic agitation to overhead mechanical stirring (Heidolph Hei-TORQUE Value 200, 250 rpm) and sparging with argon for 45 min prior to catalyst charge restored full conversion, as measured by IPC HPLC (C18 column, acetonitrile/water gradient, 254 nm). This sensitivity to dissolved gases is not observed with 2,5-dichlorothiazole under identical conditions; the 5-chloro orientation shifts oxidative addition kinetics, requiring higher temperature (80°C) but tolerating 5 ppm dissolved oxygen, a difference attributed to the ring’s altered electron density distribution mapped by DFT calculations at the B3LYP/6-31G(d) level available in the peer-reviewed literature.

    2,4-Dichlorothiazole also participates in thiazole-directed ortho-metallation using lithium tetramethylpiperidide (LiTMP) in THF at −78°C, providing a route to 5-substituted derivatives inaccessible via electrophilic halogenation. The metallation is highly regioselective and has been validated in a kilo-lab campaign using syringe-pump-controlled addition of LiTMP over 90 min to maintain internal temperature within ±3°C of the setpoint; excursions above −70°C trigger irreversible ring fragmentation to an intractable tar mixture that requires mechanical cleaning of the Hastelloy C-22 reactor vessel.

    Regulatory context and cross-referenced substance inventories

    The compound is listed on the TSCA inventory, EINECS (224-039-3), and is pre-registered under REACH with a planned registration dossier by the lead registrant for the 100–1000 t/a band. It does not appear in Annex VI of the CLP regulation as a harmonized classification, but self-classification based on acute oral toxicity data (LD₅₀ rat 200–500 mg/kg) yields Acute Tox. 3, H301. Shipping classification follows IMDG Code, special provision 274 for marine pollutants. For pharmaceutical applications, a Type II drug master file (DMF) is maintained with the US FDA by major producers, enabling cross-referencing in ANDA submissions for generic drug products whose synthesis relies on 2,4-dichlorothiazole as a starting material. An audit trail of the supply chain for one such DMF demonstrated that variation in the 2,5-isomer level below the 0.5% specification had no detectable effect on the final API impurity profile determined by UPLC-MS down to 0.015% LOQ, supporting the currently marketed quality target product profile (QTPP).

    From an environmental release perspective, the octanol-water partition coefficient (log Kow) measured by HPLC method OECD 117 is 2.34, indicating moderate bioaccumulation potential. Wastewater from process quenches must be treated with activated carbon (Norit GAC 830, contact time 30 min) to achieve effluent concentration below 0.1 mg/L prior to discharge to municipal biological treatment, based on toxicity threshold data for activated sludge respiration inhibition (OECD 209).

    In the broader landscape of polychlorinated thiazole intermediates, 2,4-dichlorothiazole occupies a specific reactivity niche that cannot be universally substituted by either 2-chlorothiazole or 2,5-dichlorothiazole without altering the synthetic sequence length and overall yield in at least three distinct scaffold families: o-aminothiazole carboxamides, 2,4,5-trisubstituted thiazole analogues of natural products, and thiazole-fused heterocycles for OLED host materials. In the latter case, published data for the configuration employing 2,4-dichlorothiazole as the halogenated monomer in a Suzuki polycondensation with a diboronic ester are limited, but preliminary GPC traces (THF eluent, RI detection) indicate Mn values in the range 8,000–12,000 Da with PDI 1.9–2.2, comparable to analogous polymers prepared from 2,7-dibromo-9,9-dioctylfluorene, suggesting chain-growth control is achievable with appropriate phase-transfer catalyst selection.