4-Choroo-2-Hydroxybenzothiazole

4-Choroo-2-Hydroxybenzothiazole


    • Product Name 4-Choroo-2-Hydroxybenzothiazole
    • Alias 4-CBT
    • Einecs 402-110-7
    • 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
    VTB
    Specifications

    HS Code

    714398

    Chemical Formula C9H6NOS
    Molecular Weight 176.22 g/mol
    Appearance Solid
    Color Typically off - white to light yellow
    Odor Characteristic odor
    Melting Point 168 - 172 °C
    Solubility In Water Poorly soluble
    Solubility In Organic Solvents Soluble in some organic solvents like ethanol, acetone
    Density Data may vary but around 1.3 - 1.4 g/cm³
    Stability Stable under normal conditions, but may react with strong oxidizing agents

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

    Packing & Storage
    Packing 500g of 4 - Chloro - 2 - Hydroxybenzothiazole packaged in air - tight plastic bags.
    Shipping 4 - Chloro - 2 - Hydroxybenzothiazole is shipped in well - sealed, corrosion - resistant containers. Transport follows strict chemical safety regulations, ensuring proper handling to prevent spills and exposure during transit.
    Storage 4 - Chloro - 2 - Hydroxybenzothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, open flames, and oxidizing agents. Store in a tightly closed container to prevent moisture absorption and potential contamination. Avoid storing near incompatible substances to ensure its stability and safety.
    Application of 4-Choroo-2-Hydroxybenzothiazole
    In open recirculating cooling water systems, microbial-induced corrosion (MIC) and biofilm-derived fouling on heat exchanger surfaces create an operational penalty quantified as a 0.5–1.2% increase in specific fuel consumption per 100 µm of scale thickness. 4-Chloro-2-hydroxybenzothiazole functions as a non-oxidizing biocide with a dual mechanism: thiazole-ring-mediated disruption of the microbial electron transport chain and concurrent formation of a protective chemisorbed film on copper-nickel (CuNi 90/10) tube bundles, as verified by linear polarization resistance (LPR) probes in side-stream test rigs. Its hydrolytic stability in the pH 7.8–9.2 operating window—common to carbonate-based scale inhibition programs—substantially exceeds that of isothiazolinone analogs, which undergo rapid base-catalyzed ring opening above pH 8.1. Field dosing data from induced-draft counterflow towers with 3,000–5,000 m³/h circulation rates indicate a maintenance dose of 12–18 ppm active substance. Shock dosing at 35–50 ppm is applied when sessile bacterial counts measured via Robbins device coupons exceed 10⁴ CFU/cm². Incompatibility arises with ammonia-based pH adjusters: residual free ammonia forms a transient adduct that temporarily masks the active thione tautomer, reducing instantaneous kill rate by an estimated 30–40%. Compliance is governed by ASTM E645-18 (Procedure B for sessile kill) and the EU Biocidal Products Regulation (BPR) active substance dossiers, while discharge limits must align with the site’s NPDES permit for total residual oxidant demand. The compound is introduced via positive-displacement diaphragm metering pumps with PTFE elastomer heads, injected directly into the cooling water return header upstream of the distribution deck to ensure 98% tracer-confirmed distribution within 12 minutes of full-loop turnover. The finished application is stabilized liquid biocide concentrate, typically packaged at 15% active content in propylene glycol as a freeze-point depressant down to −18°C.

    Metalworking Fluid Central System Contamination Suppression and Yellow Metal Passivation

    In water-dilutable soluble oils and semi-synthetic metalworking fluids operating in 30,000–80,000-liter central sumps, the dominant microbial contaminant spectrum shifts from Pseudomonas aeruginosa to sulfate-reducing Desulfovibrio populations when tramp oil exceeds 3.5% and anaerobic micro-zones form under swarf sediment. Here 4-chloro-2-hydroxybenzothiazole is dosed at 0.08–0.15% (w/w based on fluid charge) in a pre-blended package with a triazine-based formaldehyde-release extender to overcome the lag-phase regrowth observed with single-mode actives. A distinguishing technical advantage over benzisothiazolinone (BIT) is the thiazole compound’s passivation behavior toward copper, brass, and copper-aluminum heat exchanger alloys; scanning electron micrographs from sump-side extracted copper strips immersed for 28 days at 60°C reveal a 45–55% reduction in dezincification pit density compared to untreated control fluid, aligning with a mixed-type corrosion inhibition mechanism confirmed by Tafel extrapolation. This is critical in Swiss-type CNC lathes where guide bush clearances of 5–8 µm are intolerant of any surface roughening. The formulation boundary is demarcated by amine-based corrosion inhibitors: diethanolamine and monoethanolamine concentrations exceeding 1.2% in the concentrate cause progressive inactivation through the formation of an ethanolamine-thiazolium adduct that exhibits an octanol/water partition coefficient (log P) reduced by 0.8 units, effectively leaching the biocide into tramp oil rather than retaining it in the aqueous phase. Batch-mixing protocols demand that the thiazole additive be introduced post emulsification and after the fluid temperature has dropped below 40°C to avoid volatilization of the heterocyclic core. The final treated fluid is monitored per ASTM E2275-19 for biocide persistence using the Kathon titration equivalent and per DIN 51360-2 for copper strip corrosion classification, with an acceptable outcome of 1a or 1b. Fluid service life extension from 6 to 11 weeks on a single charge is documented in manufacturing cells machining EN AW-7075 aluminum structural components.

    What Ensures Long-Term In-Can Stability in High-pH Latex Paints and Adhesives?

    In styrene-acrylic and vinyl acetate-ethylene (VAE) copolymer latex paints formulated in the pH 8.0–9.0 range, the spoilage cascade initiated by Enterobacter and Proteus species manifests first as a 10–15 KU drop in Stormer viscosity within 72 hours due to enzymatic cleavage of hydroxyethyl cellulose thickener side chains. 4-Chloro-2-hydroxybenzothiazole is incorporated at 0.25–0.35% (w/w of wet paint) during the letdown stage, downstream of the high-speed disperser but before the final rheology modifier adjustment. Unlike tetramethylolacetylenediurea-based preservatives, this thiazole does not liberate formaldehyde, thus eliminating the potential for a positive result under the Japanese JIS A 1901:2015 small chamber formaldehyde emission test, a critical compliance requirement for indoor air quality certification in prefabricated housing modules. Its efficacy is quantified through a six-cycle challenge test following ASTM D5589-19, where a log 4 reduction in bacterial count within 24 hours and zero recovery at day 28 are the minimum acceptance criteria; data from commercial flat wall paint batches demonstrate compliance at the 0.28% addition level even under simulated tropical shipment conditions (45°C, 85% RH, 14-day container simulation). A further constraint particular to this colloidal matrix is the competitive adsorption of the biocide onto titanium dioxide pigment surfaces when wetting and dispersing agents are sub-optimized; to avoid sequestration, the alkylphenol ethoxylate (APEO)-free polyacrylate dispersant loading must be maintained above 1.2% on pigment weight. In the finished goods specification, the in-can preservative must demonstrate compatibility with metallic-effect pastes—aluminum bronze pigments, specifically, must not exhibit gassing (hydrogen evolution) when stored in partially filled containers, a failure mode traced to the thione-thiol tautomerism inducing surface pitting at a redox potential of +0.35 V vs. SHE. The terminal products are interior matt emulsion paints, joint compounds, and PVA-based wallpaper adhesives supplied to the professional contractor channel in 18-liter and 200-liter HDPE pails.Leather wet-blue preservation programs historically relied on pentachlorophenol, the obsolete application of which left a recalcitrant toxic residue in downstream splitting and shaving dust. 4-Chloro-2-hydroxybenzothiazole has been adopted in chrome-tanning and chrome-free wet-white processes as an in-drum fungicide added at 0.03–0.06% on fleshed hide weight directly into the pickle float at the final 15 minutes of the acidification step when the float pH is 2.8–3.2. This timing exploits the compound’s optimal absorption plateau at the hide’s isoelectric point, achieving a 94% uptake efficiency verified by UV-Vis spectrophotometric depletion measurement of the spent float. The critical microbiological target is the saprophytic fungi Trichoderma harzianum and Penicillium glabrum, which are responsible for the characteristic “mossy” spotting that renders a whole pallet of hide ungradeable; full protection through a 90-day warehouse storage period at relative humidity up to 85% without re-fungicide application is achieved when the residual active content in the wet-blue crust exceeds 0.012% by weight. Process safety boundaries must be enforced: float temperatures above 38°C during basification (pickle to chrome tannage transition) degrade the active molecule through dechlorination, reducing the effective half-life to less than 6 hours. Furthermore, sulfate-burnt chrome powders with basicity above 42% generate a transient pH spike that can precipitate the thiazole as an insoluble chromium (III) complex, diminishing both tanning effect and mildew resistance. The treated leather intermediates conform to the ZDHC Manufacturing Restricted Substances List (MRSL) Version 3.1 and meet the IULTCS IUF 354 test method for fungal resistance. Final article classes include automotive seat upholstery leather, footwear leather for cement-lasted construction, and furniture upholstery.

    Diazotization-Based Route to Benzothiazole Heterocyclic Disperse Dyes

    In the downstream synthesis of monoazo disperse dyes for polyester coloration, 4-chloro-2-hydroxybenzothiazole serves as a diazo component precursor following a sequence of nucleophilic substitution to replace the 2-hydroxy group with a primary amine, generating 2-amino-4-chlorobenzothiazole. This intermediate is diazotized in concentrated sulfuric acid (96–98% H₂SO₄) at −5 to 0°C using nitrosylsulfuric acid, a method dictated by the extremely low basicity of the thiazole amine (pKa ~ 2.3) which precludes conventional aqueous HCl/NaNO₂ diazotization. The resulting diazonium salt is subsequently coupled to N,N-disubstituted aniline coupling components bearing hydroxyl or alkoxyethyl groups, yielding vibrant red to violet-blue shades with molar extinction coefficients exceeding 45,000 L·mol⁻¹·cm⁻¹, a bathochromic shift attributable to the electron-withdrawing chlorine at the 4-position extending the π-conjugation of the benzothiazole ring system. Industrial-scale production proceeds in 5,000-liter glass-lined reactors equipped with jacket cooling and a raster-type agitator running at 65 rpm, where improper control of the exothermic coupling—temperature deviations beyond ±1.5°C—results in a bimodal particle size distribution that compromises dispersion stability in dyebath application. The washed filter cake is standardized with a naphthalene sulfonate formaldehyde condensate dispersant to a controlled dye content of 42–45%, subsequently spray-dried at an inlet temperature of 190°C. The final fine powder disperses to a residual particle size below 5 µm as tested per AATCC Test Method 146-2018 using a filtration test through a 5 µm polypropylene felt. Dyehouse processing follows high-temperature exhaust dyeing at 130°C for 45 minutes in jet dyeing machines for woven and knitted 100% PET fabrics; the chlorine substituent contributes a sublimination fastness rating of 4–4.5 (ISO 105-P01), making these colorants suitable for automotive interior textiles exposed to cabin temperatures up to 110°C. Compliance with the Oeko-Tex Standard 100 Annex 4 requires confirmation that the free 4-chloro-2-hydroxybenzothiazole precursor content in the final dye is below 250 mg/kg via HPLC-MS determination.Formulation of tin-free self-polishing copolymer (SPC) antifouling coatings for oceangoing vessels operating in the 5–20-knot speed regime must satisfy the dual requirement of static antifouling efficacy during 21-day anchorage periods and dynamic paint polishing rates of 8–12 µm per 10,000 nautical miles. 4-Chloro-2-hydroxybenzothiazole is incorporated as a booster biocide co-formulated with zinc pyrithione at a combined loading of 3–5% (w/w of dry film) in a copper-free, silyl acrylate-based binder system. Its mode of action against macrofouling organisms—particularly Balanus amphitrite cyprid settlement—is believed to involve interference with adenylate cyclase signaling, based on in situ settlement panel assay data collected at tropical test sites (Kerala, India: 22°C–31°C seawater temperature range) that indicate a suppression of barnacle settlement density to below 15 individuals/dm² after 18 months of immersion, compared to over 120 individuals/dm² for the non-biocide blank. A critical processing limitation manifests during high-shear orbital mixing for pigment dispersion: localizing the thiazole in the presence of copper oxide-based co-biocides, even at concentrations as low as 0.5% Cu, triggers a ligand-exchange reaction producing a poorly soluble Cu(II)-thiazole complex that forms a pseudoplastic rheology hump exceeding 120 KU at 25°C, effectively stalling the dissolver. Hence, the manufacturing procedure must be sequenced so that the thiazole is introduced only into the letdown mixture after all metal oxide pigments have been fully deagglomerated. The applied coating is assessed according to ISO 15181-1:2007 for biocide leaching rate determination, and must comply with the IMO Anti-Fouling System Convention (AFS/CONF/26) devoid of organotin residues. The end products are two-component high-solids antifouling topcoats applied via airless spray at 300 bar to self-polishing tie-coats on dry-docked VLCC and container vessel hulls.
    Compliance Standards Matrix by Application Context
    Application ScenarioPrimary Evaluation StandardSecondary / Corrosion StandardRegulatory Framework
    Cooling Water SystemsASTM E645-18 (Sessile Kill Rate)ASTM D1384-18 (Corrosion in Glassware)EU BPR, US EPA FIFRA
    Metalworking FluidsASTM E2275-19 (Biocide Durability)DIN 51360-2 (Copper Strip Test)EU CLP Regulation (EC) No 1272/2008
    In-Can Paint PreservationASTM D5589-19 (Challenge Test)JIS A 1901:2015 (Formaldehyde Emission)EU Ecolabel for Indoor Paints
    Wet-Blue LeatherIULTCS IUF 354 (Fungal Resistance)ISO 17226:2008 (Formaldehyde Content)ZDHC MRSL V3.1
    Disperse Dye SynthesisAATCC 146-2018 (Dispersion Fineness)ISO 105-P01:1993 (Sublimation Fastness)Oeko-Tex Standard 100 Annex 4
    Marine Antifouling CoatingsISO 15181-1:2007 (Leaching Rate)ASTM D6990-05 (Dynamic Polishing)IMO AFS/CONF/26
    Formulation Guidance and Operational Boundary Conditions
    ApplicationRecommended Dose (% w/w or ppm)Operational pH WindowCritical IncompatibilityProcessing Temperature Limit
    Open Cooling Water12–18 ppm maintenance / 35–50 ppm shock7.8–9.2Free ammonia, amine pH adjustersInjection at <40°C
    Metalworking Fluid Sumps0.08–0.15% on charged fluid8.8–9.5DEA/MEA > 1.2% in concentratePost-emulsion <40°C
    Latex Paint / Adhesives0.25–0.35% wet weight7.5–9.0Alkylphenol ethoxylate-free systems with sub-optimized polyacrylateLetdown stage at <50°C
    Wet-blue Hide Processing0.03–0.06% on fleshed weight2.8–3.2 (pickle float)High-basicity chrome powder (> 42%) during basificationFloat must remain <38°C
    Azo Disperse Dye CouplingStoichiometric (precursor)N/A (conc. H₂SO₄)Moisture in diazotization mediumDiazotization at −5 to 0°C; coupling at 0–5°C
    SPC Antifouling Paint3–5% dry film weightN/A (non-aqueous)Copper oxide pigment (forms complex)Letdown addition at <30°C
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    Certification & Compliance
    More Introduction

    Introduced under trade codes such as HOBT-Cl-4 and similar alphanumeric designators reflecting the substitution pattern, 4-chloro-2-hydroxybenzothiazole (CAS 39207-91-3, molecular formula C₇H₄ClNOS, relative molecular mass 185.63 g·mol⁻¹) exists as a pale-yellow to off-white crystalline solid at ambient conditions. The product is routinely supplied in technical grade (98.0% minimum purity by HPLC, area normalization) and high-purity grade (99.5% minimum) for pharmaceutical intermediate synthesis. The heterocyclic backbone combines a benzothiazole nucleus with a hydroxyl substituent at the 2-position and an aromatic chlorine atom at the 4-position, yielding a hydrogen-bond donor-acceptor profile that governs its solubility in polar aprotic solvents (DMF, NMP, DMSO) and limited solubility in water (<0.5 g·L⁻¹ at 25°C, unbuffered). Manufacturing routes typically proceed via cyclocondensation of 2-amino-4-chlorophenol with carbon disulfide under alkaline conditions, followed by acidification and recrystallization from toluene-methanol mixtures. The resulting crystal habit—platelets of 10–50 μm median particle size when milled under a pin-disc system—affects dissolution kinetics in downstream amidification and etherification steps. Producers ship the anhydrous material in 25 kg net fibre drums with PE inner liners; storage stability exceeds 24 months at ≤25°C and ≤60% relative humidity, provided the package remains sealed.

    What Differentiates 4-Chloro-2-Hydroxybenzothiazole from Mercapto- and Amino-Benzothiazoles in Crosslinking Chemistry?

    The displacement of the 2-mercapto group found in 2-mercaptobenzothiazole (MBT) with a hydroxyl moiety markedly alters the compound’s role in accelerated sulfur vulcanization. While MBT and its sulfenamide derivatives (CBS, TBBS) act as direct accelerators by generating zinc-thiolate complexes that activate elemental sulfur, 4-chloro-2-hydroxybenzothiazole is not employed as a standalone accelerator. Instead, it serves as a versatile precursor to a class of delayed-action accelerators where the hydroxyl group is converted to a sulfenamide or thiocarbamate function. Conversion with primary amines in the presence of sulfur monochloride yields N-substituted 4-chloro-2-benzothiazole sulfenamides, which exhibit scorch times (ts₂ at 135°C) exceeding 8–12 min when tested per ASTM D5289-19a (MDR 2000 rheometer, 0.5° arc). By contrast, standard MBT-accelerated natural rubber compounds typically record scorch times of 2–4 min under identical conditions. The electron‑withdrawing chlorine at the 4‑position further moderates cure rate by reducing electron density on the thiazole ring, raising the activation energy for accelerator decomposition. Vulcanization kinetic parameters derived from oscillating disc rheometer data show a cure rate index (CRI) reduction of 30–45% relative to unsubstituted 2-mercaptobenzothiazole, making the chloro‑hydroxy precursor attractive for thick‑section industrial rubber goods where premature crosslinking during processing is a recurrent failure mode on L/D=16 cold‑feed extruders. Published data for this specific derivative in direct vulcanization systems are limited; most industrial applications proceed through the in‑situ generation of the active sulfenamide species.

    Physical Specifications and Batch‑to‑Batch Consistency Metrics

    The following table collates standard release criteria anchored to recognized test methods, enabling verification across procurement lots destined for cGMP intermediate synthesis and technical rubber chemical manufacturing.

    ParameterMethodTypical Value
    AppearanceVisual / USP 〈761〉Pale yellow crystalline powder
    Identification (FTIR)USP 〈197M〉 / EP 2.2.24Absorbance at 1615 cm⁻¹, 1560 cm⁻¹, 745 cm⁻¹
    Purity (HPLC, 254 nm)ASTM E682 / in‑house gradient98.5% area
    Melting rangeUSP 〈741〉, Class I apparatus214–218°C (decomposition observed)
    Water content (KF coulometry)ASTM E2030.3% w/w
    Residue on ignitionUSP 〈281〉0.10%
    Chloride content (ion chromatography)ASTM D43270.05%
    Heavy metals (as Pb)USP 〈231〉 / Method II10 ppm

    Process‑induced variability in crystal morphology can alter bulk density (0.45–0.55 g·cm⁻³ tapped) and flow properties. Air‑micronized material with a d₉₀ of 15 μm is specified for suspension concentrate formulations requiring long‑term physical stability without sediment compaction. Pre‑drying in a vacuum tray dryer at 60°C and ≤10 mbar for 4 h is mandatory when the moisture content exceeds 0.5% upon receipt; failure to do so leads to hydrolysis of downstream sulfenamide products and a 15–20°C depression in the melting point of the isolated intermediate. The compound is incompatible with strong bases—aqueous sodium hydroxide above 1 M induces ring‑opening and generation of 2‑amino‑4‑chlorothiophenol, detectable by a distinct mercaptan odor. Thermal gravimetric analysis (TGA) at 10°C·min⁻¹ under nitrogen flow reveals the onset of mass loss at approximately 180°C, accelerating above 220°C with HCl evolution; thus, reactors for derivatisation should be designed with Hastelloy C‑22 condensers and alkali scrubber capacity.

    A second table integrates European regulatory compliance positions, which frequently govern formulation and transboundary shipment decisions for specialty chemical intermediates derived from this benzothiazole.

    RegulationScopeStatus / Remarks
    EU REACH (EC 1907/2006)Substance manufactured > 1 t·a⁻¹Pre‑registered; full registration dossier inclusive of CSR
    RoHS Directive 2011/65/EUElectrical & electronic equipmentNot listed as restricted; no cadmium, lead, mercury, CrVI intents
    FDA 21 CFRIndirect food contact (adhesives, coatings)No food‑contact clearances in force; consult suitability for repeat‑use rubber articles per 21 CFR 177.2600
    Japan CSCLExisting chemical substanceMITI No. (5)-2927; non‑Class I specified
    Australia NICNASIndustrial useExempt from notification when used as <1% constituent in formulated products

    When the 4-Chloro Substituent Enables Nucleophilic Aromatic Substitution Routes to Pharmaceutical Building Blocks

    Synthetic sequences targeting 4‑substituted benzothiazole pharmacophores exploit the lability of the aromatic chlorine atom under nucleophilic attack. In polar, high‑boiling solvents such as N‑methyl‑2‑pyrrolidone (NMP) at 120–140°C, the 4‑chloro position undergoes ipso‑substitution with primary and secondary aliphatic amines—piperidine, morpholine, and N‑Boc‑piperazine—to generate derivatives used as kinase inhibitor intermediates. Reaction progress is monitored by quenching aliquots into dilute HCl and extracting with ethyl acetate; TLC (silica gel 60 F254, hexane:EtOAc 3:1) tracks the disappearance of the starting material at Rf 0.55. Extended heating beyond 48 h yields a bis‑adduct impurity where the 2‑hydroxyl group engages in Ullmann‑type coupling, a side‑reaction suppressed by switching to a tertiary amine base with no N–H bonds, such as DIPEA at 2.0 eq. The electron‑withdrawing effect of the thiazole ring renders the 4‑position roughly 10³ times more reactive toward amines than the 2‑chloro analog, 2,4‑dichlorobenzothiazole, a derivative that introduces cross‑reactivity with the 2‑position unless carefully temperature‑controlled.

    In fine chemical production environments, an agitated glass‑lined reactor of 2000 L capacity, equipped with a split‑tube glass condenser and a temperature‑controlled heating jacket circulating pressurised water, is charged with 150 kg of 4‑chloro‑2‑hydroxybenzothiazole, 320 L anhydrous NMP, and the amine nucleophile in slight excess (1.05 eq). The headspace is blanketed with nitrogen at 0.2 bar positive pressure throughout the reaction period. At completion, the batch is quenched into 1500 L deionised water at 5–10°C, precipitating the product, which is isolated via a pressure nutsche filter and washed with cold isopropanol. The damp cake undergoes recrystallization from a 3:1 toluene‑isopropanol mixture, yielding a target purity exceeding 99.0% by HPLC. Differential scanning calorimetry (DSC) of the dried intermediate typically exhibits a sharp endothermic melt at 178–182°C (ΔH ∼95 J·g⁻¹), with no decomposition exotherm below 250°C. The use of a Hastelloy‑lined dryer is recommended when the recrystallization solvent retains even traces of hydrogen chloride, as stainless steel 316L surfaces are prone to pitting corrosion under these conditions.

    The application of 4-chloro-2-hydroxybenzothiazole as a building block extends to thioether formation when treated with sodium hydrosulfide in DMF at 80°C, generating a mercapto intermediate that is alkylated in situ to produce 4‑alkylthio derivatives with logP values shifted upward by approximately 1.2–1.8 units compared to the 4‑chloro precursor, as estimated by shake‑flask OECD TG 107 methodology. These sulfur‑bridged analogues display potent activity in high‑throughput screening campaigns targeting bacterial DNA gyrase; published IC₅₀ values against Staphylococcus aureus gyrase fall in the 200–500 nM range for select analogs, though the parent compound itself shows no significant enzyme inhibition. Critically, the 4‑chloro handle is orthogonal to the 2‑hydroxy group, permitting sequential functionalization without protective group strategies, a molecular feature that separates it from 2‑amino‑4‑chlorobenzothiazole, where both positions require differentiation through acyl protection.

    Microbicide Performance and Compatibility Boundaries in Recirculating Aqueous Systems

    The compound’s role in industrial water treatment is distinct from the fast‑kill profile associated with 5‑chloro‑2‑methyl‑4‑isothiazolin‑3‑one (CMIT) and its blends with MIT. Where isothiazolinones achieve a log‑4 reduction in viable cell counts within 30 min at 5–15 ppm active concentration, benzothiazole‑based microbicides like 4‑chloro‑2‑hydroxybenzothiazole—frequently formulated as its water‑soluble sodium salt hydrate—exhibit a slower kill kinetic that translates to extended preservation of metalworking fluid sumps. Efficacy testing per ASTM E2315 (time‑kill suspension test) against Pseudomonas aeruginosa ATCC 15442 yields a >3‑log reduction at 500 ppm active after 24 h contact time, but only 1.5‑log at 100 ppm over the same interval. This moderate activity is deliberately leveraged in formulations where maintenance of a persistent low‑level biostatic concentration (50–200 ppm) suffices to suppress biofilm development on heat exchanger surfaces, without the rapid consumption observed for more electrophilic biocides that react with tramp lubricating oils.

    Compatibility with common coolant additives is a governing factor in formulation design. The sodium salt of 4‑chloro‑2‑hydroxybenzothiazole remains soluble in hard water containing 500 ppm CaCO₃ without precipitation, and it is stable for 28 days at pH 8.5–9.5 and 40°C, based on accelerated stability testing per OECD GD 111. However, the presence of quaternary ammonium‑based cationic corrosion inhibitors at concentrations exceeding 100 ppm triggers flocculation through charge neutralization; this incompatibility does not arise with 2‑mercaptobenzothiazole‑based corrosion inhibitors, which remain monomeric under identical conditions. Field experience from automotive engine plant central systems (twin‑belt filtration, sump volume 40 m³) demonstrates that maintaining 150–200 ppm of the benzothiazole actives in the aqueous phase, confirmed by UV absorbance at 315 nm, suppresses fungal growth on acrylic sight glasses and reduces the frequency of dump‑and‑clean cycles from 8 weeks to beyond 16 weeks. Despite these performance data, the compound is not classified as a biocide active substance under EU BPR (528/2012) in most jurisdictions, and formulators must independently validate regulatory compliance for end‑use claims.