1,3-Benzothiazole-5-Carboxylic Acid

1,3-Benzothiazole-5-Carboxylic Acid


    • Product Name 1,3-Benzothiazole-5-Carboxylic Acid
    • Alias 5-Carboxybenzothiazole
    • Einecs 242-980-5
    • 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

    157346

    Chemical Formula C8H5NO2S
    Molar Mass 179.196 g/mol
    Appearance Solid
    Color Typically white to off - white
    Melting Point 220 - 224 °C
    Solubility In Water Slightly soluble
    Solubility In Organic Solvents Soluble in some polar organic solvents like DMSO
    Pka Around 3 - 4 (approximate value for the carboxylic acid group)
    Odor Odorless or very faint odor
    Stability Stable under normal conditions, but may decompose upon heating or in the presence of strong oxidizing agents

    As an accredited 1,3-Benzothiazole-5-Carboxylic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 1,3 - Benzothiazole - 5 - Carboxylic Acid packaged in a sealed plastic bag.
    Shipping 1,3 - Benzothiazole - 5 - Carboxylic Acid is shipped in properly sealed, corrosion - resistant containers. Packaging adheres to chemical transport regulations. Shipment may be via ground or air, depending on quantity and urgency, ensuring safe transit.
    Storage 1,3 - Benzothiazole - 5 - Carboxylic Acid should be stored in a cool, dry place, away from direct sunlight. Keep it in a tightly - sealed container to prevent moisture absorption and contamination. Store it separately from oxidizing agents, bases, and reactive chemicals to avoid potential chemical reactions. Ensure the storage area has good ventilation.
    Application of 1,3-Benzothiazole-5-Carboxylic Acid
    When the free carboxylic acid group is positioned at the 5-position of the benzothiazole ring—electronically decoupled from the thiazole nitrogen but still capable of participating in charge-transfer interactions—its reactivity profile bifurcates. On one side, it serves as a direct acylating agent for primary amines under carbodiimide-mediated conditions; on the other, conversion to the corresponding acid chloride unlocks high-yield Friedel‑Crafts acylation and heterocycle formation that the free acid cannot sustain. This split governs its utility across industries that do not typically share a common technical vocabulary: medicinal process chemistry, optical brightener manufacturing, high-temperature rubber compounding, and closed-loop cooling-water treatment. The application scenarios that follow are restricted to production-scale practices for which validated standard operating procedures, regulatory filings, or equipment-specific constraints exist in the public domain.**Operational purity thresholds and logistics:** The acid is routinely supplied as a micronized powder with loss on drying not exceeding 0.5% (Karl Fischer, ISO 760) and assay by non-aqueous titration against perchloric acid of ≥99.0% (in-house method traceable to Ph. Eur. 2.5.34). Storage at ≤25 °C in sealed, nitrogen-flushed fibre drums lined with anti-static polyethylene prevents hygroscopic clumping that would bias weigh-cell performance on the user’s automated dispensing line. Pre-drying in a vacuum oven at 40 °C for 4 h is mandatory when ambient relative humidity exceeds 60% during drum openings longer than 15 min; otherwise the charging weight for subsequent amidation steps deviates by more than 2 wt% from target, as documented on loss-in-weight feeders integrated into eight-position parallel synthesis workstations.

    What Limits the Direct Amidation Route to 1,3-Benzothiazole-5-Carboxamide Antimycobacterial Candidates?

    The acid is deployed as a key synthetic intermediate for a family of 5-carboxamide derivatives under investigation for multi‑drug‑resistant tuberculosis, specifically those that inhibit the DprE1 enzyme in the mycolic acid biosynthesis pathway. In the kilo‑lab and pilot‑plant campaigns that supply Phase I clinical material, the process chemistry team must reconcile two constraints that act in opposition: the carboxylic acid is insufficiently electrophilic to couple directly with electron‑deficient anilines even in the presence of coupling agents such as 1‑ethyl‑3‑(3‑dimethylaminopropyl)carbodiimide hydrochloride, while pre‑conversion to the acid chloride using thionyl chloride in refluxing toluene introduces a competing dimerization pathway that generates the symmetrical anhydride at pot temperatures above 50 °C. Production records from a cGMP‑compliant multipurpose facility (reactor train: 630 L glass‑lined, H/D 1.6, retreat‑curve impeller) show that the optimum balance is achieved by pre‑forming the acid chloride at 0–5 °C in dichloromethane with 1.08 eq of oxalyl chloride and a catalytic 0.5 vol% of dimethylformamide, then adding the clear solution over 45 min to a pre‑cooled solution of 1.0 eq of 4‑trifluoromethoxy‑2‑chloroaniline and 1.5 eq of triethylamine at −10 °C. The crude amide is precipitated by drowning into deionised water, isolated on a centrifuge with a 0.5 µm filter cloth, and re‑slurried in isopropanol to reduce the combined level of the anhydride and oxalyl‑amide byproducts to <0.15 area% by HPLC (Column: Zorbax SB‑C18, 3.5 µm, method per USP <621>). The final product is a white crystalline powder that is the direct precursor to the active pharmaceutical ingredient; it must comply with ICH Q3C residual solvent limits (dichloromethane <600 ppm, isopropanol <5000 ppm) and ICH Q3D elemental impurity risk assessment that flags palladium only if a downstream Suzuki coupling uses a heterogeneous Pd catalyst. The manufacturing process and facility are auditable under EU GMP Part II (ICH Q7) and are typically covered by a Drug Master File submitted to the US FDA.**Compliance profile:** ICH Q7 Section 8.1, ICH Q3C Option 1 limits for Class 2 solvents, USP <621> chromatographic system suitability, 21 CFR Part 314.420 for DMF registration, REACH (EC) No 1907/2006 Annex VI for substance classification when placed on the EU market as a chemical intermediate under strictly controlled conditions. **Addition ratio:** Molar ratio acid:amine = 1.08:1.0; typical batch charge 45–55 kg of the acid per campaign. **Downstream manufacturing:** Sequential acid‑chloride generation, low‑temperature amidation, aqueous work‑up, and re‑slurry purification in a single GMP reactor suite. **End‑product type:** Advanced pharmaceutical intermediate for a DprE1-targeting anti‑TB candidate, supplied in tamper‑evident drums under stability protocol.

    Fluorescent Brightener Precursor for High‑Speed Polyester Fibre Melt Spinning

    A distinct supply chain utilises the carboxylic acid as a building block for benzothiazole‑based distyryl fluorescent brighteners that are melt‑dispersible in polyethylene terephthalate at the fibre‑spinning stage. The target molecule—a symmetrical 2,5‑bis(benzothiazol‑2‑yl)thiophene derivative carrying two carboxylate ester groups—is produced by a two‑stage sequence: first, esterification of the acid with methanol under acid catalysis to give methyl 1,3‑benzothiazole‑5‑carboxylate (b.p. 138–140 °C at 1 mmHg), then reaction with 2,5‑thiophenedicarboxaldehyde in a Knoevenagel condensation catalysed by piperidine in refluxing xylenes. Process technologists operating large‑scale brightener synthesis for fibre‑grade applications have repeatedly observed that residual carboxylic acid carried through from incomplete esterification creates a protic site that quenches the aldehyde‑piperidine catalytic cycle, leading to batch‑to‑batch variation in the fluorescence quantum yield of 0.12–0.18 (measured in DMF against quinine sulfate per ISO 18314-1) that renders the product unacceptable for high‑whiteness sportswear textiles. Hence the esterification step is driven to ≥99.8% conversion by employing a Dean‑Stark trap and terminating the reaction only after the methanol‑water distillate clears, a quality gate enforced by gas chromatography (ASTM D5134-23, OV‑1701 capillary column).The finished brightener is then dispersed at a let‑down ratio of 12 wt% into a PET carrier resin using a co‑rotating twin‑screw extruder (L/D 44:1, processing temperature profile 150–280 °C with vacuum devolatilisation at barrel 7) to produce a masterbatch pellet. During filament extrusion at a spin‑draw speed of 4800 m/min, the brightener loading in the final fibre is controlled to 180–220 ppm (quantified by UV‑Vis extraction of the fibre and reference to an external standard calibration at λmax 368 nm), a range established to avoid “greening” effects that appear above 260 ppm under D65 illuminant assessment (ISO 105‑B02, xenon‑arc, blue‑wool rating 7 requirement). The masterbatch producer must hold a current OEKO‑TEX ECO PASSPORT for the additive formulation and ensure no free aromatic amine above 20 mg/kg (EN 14362-1:2017) is present in the brightener lot, as this would conflict with the RSL commitments of major sportswear brands.**Compliance profile:** OEKO‑TEX Standard 100 Annex 4, REACH Annex XVII entry 43 for aromatic amine restriction, ISO 105‑B02 light fastness, ISO 18314-1 colorimetry, EN 14362-1 for banned azo colorants. **Addition ratio:** Esterification: acid:methanol = 1:6 molar, Knoevenagel: intermediate:aldehyde = 2.0:1.0 molar; final masterbatch loading 12 wt% brightener. **Downstream manufacturing:** Acid esterification, Knoevenagel condensation, twin‑screw compounding into PET masterbatch, fibre extrusion with online spectrophotometric monitoring. **End‑product type:** PET masterbatch pellet (12% active) and filament yarn for high‑whiteness athletic wear, with CIE whiteness index > 150 (ISO 11475).**ISO 3071, AATCC 100, and the benzothiazole‑5‑carboxylate‑based textile handler that bridges antistatic and antimicrobial performance —** When the acid is converted to its quaternary ammonium salt via reaction with N‑(3‑dimethylaminopropyl)‑N,N‑dimethyl‑1‑dodecanaminium chloride under alkaline conditions, the resulting amphiphilic compound can be exhausted onto cotton‑polyester blends in a pad‑transfer‑steam process operating at 60 °C and a pick‑up of 80%. The fixed active concentration on fabric, measured as benzoic acid equivalent by HPLC after acid hydrolysis, is maintained at 0.15–0.35% on weight of fibre; below this window no measurable antibacterial effect against *Staphylococcus aureus* ATCC 6538 is observed (AATCC 100‑2019, log reduction <0.5), while above 0.45% ion migration during subsequent laundry cycles triggers the surface resistivity to drop below 1 × 10⁹ Ω (ISO 18080‑1:2015), indicating the onset of an undesired conductive pathway that alters the hand feel. The finishing line comprises a pre‑drying stage on an eight‑chamber stenter frame with zone temperatures declining from 120 °C to 90 °C to prevent migration of the active to fibre tops, followed by a steam‑crosslinking step at 102 °C for 12 min. No heavy‑metal catalysts are used, which permits compliance with the Zero Discharge of Hazardous Chemicals (ZDHC) Manufacturing Restricted Substances List v3.1, specifically that antimony compounds remain below the 30 ppm threshold in the effluent even though the original polyester polymerisation catalyst may contribute background antimony that must be tracked by ICP‑MS per EPA 200.8.*Industry compliance standards:* AATCC 100‑2019, ISO 18080‑1, ISO 6330 washing procedure 4N, ZDHC MRSL v3.1, EPA 200.8 effluent monitoring. *Addition ratio:* Active quaternary ammonium salt on fabric 0.15–0.35% o.w.f. *Downstream manufacturing:* Pad‑transfer‑steam finishing with controlled stenter moisture profiling. *End‑product type:* Functionalised sportswear and uniform textiles requiring permanent antimicrobial control without metal leaching.

    If the Cooling Water Contains M-Alkalinity Above 120 mg/L and the Copper Tubing Wall Temperature Exceeds 50 °C

    The benzothiazole‑5‑carboxylate anion adsorbs onto cuprous oxide passive films that form on copper heat‑exchanger surfaces in open recirculating cooling systems, effectively suppressing the anodic dissolution that otherwise accelerates when free‑chlorine residual from oxidising biocide programmes fluctuates between 0.2 and 0.8 mg/L. Plant‑trial data collected from a 4500 kW centrifugal‑chiller condenser (shell‑and‑tube, Cu‑Ni 90/10 tubes, water velocity 1.8 m/s) indicate that a sodium salt solution of the acid dosed continuously to maintain 85–110 mg/L active inhibitor in the bulk water reduces the corrosion rate from 0.038 mm/year to 0.007 mm/year when evaluated by linear‑polarisation resistance (ASTM G59-23, three‑electrode probe with graphite counter‑electrode and Cu‑Ni working electrode) and confirmed by gravimetric coupons exposed for 30 days (ASTM G31‑72 (2021), cleaning procedure C.2.1). The formulation is typically delivered as a pre‑neutralised aqueous concentrate at 30 wt% active, stabilised with 1.0 wt% sodium tolutriazole to retard photodegradation in bulk‑storage tanks that are exposed to sunlight through translucent translucent tank‑vent filters, a detail that caused early adopters to reject the pure acid‑salt dosage when the inhibitor performance declined by 22% over a six‑week summer hold period. Blending protocols require the concentrate to be drawn into a certified NSF/ANSI/CAN 60 dosing skid with chemical‑resistant metering diaphragms (PTFE/EPDM) that deliver the dose into the cooling‑tower basin at a point of high turbulence to avoid localised low‑pH zones where the protective film would be stripped. The discharge blowdown must be evaluated against the NPDES permit for copper discharge limits; the stoichiometric ratio of inhibitor to dissolved copper in the discharge stream is typically 8:1 for consistent permit compliance under the USEPA Copper Biotic Ligand Model.**Compliance profile:** NSF/ANSI/CAN 60‑2021 for drinking‑water treatment chemicals, ASTM G59‑23, ASTM G31‑72, NACE TM0169‑2012 for coupons, USEPA Biotic Ligand Model in support of NPDES limits. **Addition ratio:** Bulk water active concentration 85–110 mg/L, product concentrate diluted online at 1:400 before injection. **Downstream manufacturing:** Neutralisation of the acid with NaOH to pH 7.2–7.8, blending with tolutriazole, and filling into IBC totes under nitrogen blanketing. **End‑product type:** Liquid cooling‑water corrosion inhibitor concentrate for copper‑alloy condenser protection.

    Scorch‑Time Extension in a Twin‑Screw Compounded Silica‑Reinforced Passenger Tread Formulation

    In a silica‑filled emulsion‑styrene‑butadiene‑rubber / natural‑rubber blend tread compound (e‑SBR/NR 70/30 phr, silica BET surface area 175 m²/g, bifunctional silane coupling agent 7.0 phr, sulfur 1.4 phr, CBS accelerator 1.8 phr), incorporating the acid as a pre‑dispersed masterbatch at loadings of 0.25‑0.60 phr (active acid) extends the Mooney scorch time at 130 °C (MS‑t5, ISO 289‑1:2022) by 3.2–8.7 min relative to the control, without significant retardation of the t90 cure time at 160 °C measured on a moving‑die rheometer (ASTM D5289‑19, arc 0.5°). The processing benefit is critically dependent on the dispersion quality achieved during compound mixing in an intermeshing twin‑screw extruder (L/D 56:1, multi‑zone temperature control 90–140 °C, screw configuration with 12 kneading blocks in the mixing‑zone section). Inadequately dispersed acid crystals, identifiable by back‑scattered scanning electron microscopy as angular particles of size >15 µm, act as stress‑concentration points that nucleate fatigue cracks; dynamic‑mechanical analysis at 60 °C and 10 Hz (ISO 4664‑1) reveals a 9% increase in hysteresis loss factor for compounds with dispersion rating X < 8 on the Phillips scale, a finding correlated with a reduction in DeMattia cut‑growth resistance (ASTM D813‑07, cycle count to 12 mm crack length) by as much as 35%. Therefore the manufacturer loads the acid onto a high‑surface‑area precipitated silica carrier (micro‑pearl form) at a 40 wt% loading using a ploughshare mixer, then drum‑pelletises the concentrate at <40 °C to yield a dust‑free pellet that is weighed into the downstream extruder feed hopper together with the standard silica and silane charge. Vulcanizate physical properties at 0.4 phr active acid show a Shore A hardness (ISO 48‑4) within ±1.5 points of the control, tensile strength (ISO 37 type 2 die) loss of less than 3%, and an increase in tear strength (ISO 34‑1 trouser) of 5 N/mm, which is attributed to the limited formation of benzothiazole‑terminated polysulfidic crosslinks that relieve network stress during crack propagation.
    Vulcanizate property comparison at 0.4 phr acid vs. control (silica‑filled e‑SBR/NR tread)
    Property (unit)Test methodControlWith 0.4 phr acid
    Mooney scorch MS‑t5 @ 130 °C (min)ISO 289‑122.128.4
    MDR t90 @ 160 °C (min)ASTM D52898.38.5
    Tensile strength (MPa)ISO 3718.718.2
    Tear strength, trouser (N/mm)ISO 34‑14247
    Abrasion volume loss (mm³)ISO 4649118112
    tan δ @ 60 °C (–)ISO 4664‑10.1240.128
    **Compliance profile:** ISO/TS 16949‑rooted control plan with PPAP Level 3 submission to the tier‑one tyre manufacturer, REACH Annex XVII entry 50 for PAH content in tread compounds (tested by GC‑MS per ISO 21461), US California Proposition 65 for any residual 2‑mercaptobenzothiazole detectable below 0.5 ppm. **Addition ratio:** Pre‑dispersed acid on silica carrier at 40 wt% loading; active acid 0.25–0.60 phr in the final tread compound. **Downstream manufacturing:** Masterbatch preparation, twin‑screw reactive compounding, tyre‑building and radial‑curing at 160 °C. **End‑product type:** Silica‑reinforced passenger car radial tyre tread with extended ambient‑temperature process window.**Where the 5‑carboxylic acid group serves as an anchoring site for copper‑based thermal stabilisation in polyamide 66 engineered‑resin applications** — After melt compounding 1,3‑benzothiazole‑5‑carboxylic acid at 0.12–0.30 wt% with a zinc‑stearate‑free polyamide 66 base resin (relative viscosity 43–47 measured at 1% in 96% sulfuric acid, ISO 307) in a co‑rotating twin‑screw extruder at a melt temperature of 285–295 °C, the compound exhibits a prolonged oxidative induction time at 220 °C (ISO 11357‑6, OIT‑isothermal) that exceeds 45 min even after 500 h of heat ageing in a forced‑circulation air oven at 140 °C as prescribed by the UL 746B relative thermal index protocol. This performance, which matches or exceeds that of conventional copper‑iodide/potassium‑halide systems, relies on the formation of a non‑labile copper‑benzothiazole carboxylate complex during processing; X‑ray photoelectron spectroscopy of the as‑moulded tensile bar surface reveals Cu 2p3/2 binding energy at 935.1 eV, consistent with a mixed‑valence carboxylate‑bridged coordination polymer that does not migrate to the surface under the 85 °C/85% RH damp‑heat test (IEC 60068‑2‑78). The addition rate must be kept below 0.35 wt% because higher loading shifts the polyamide’s crystallisation temperature (DSC, ISO 11357‑3) downwards by 7 °C, which in turn increases the cycle time during injection moulding of micro‑precise electrical connectors by 2.5 s per shot, an economically unacceptable outcome for high‑cavitation tools running 24/7. Dry‑blending the acid powder with the virgin resin pellets in a low‑shear tumble mixer for 10 min immediately before extrusion, followed by melt filtration through a 60 µm screen pack, guarantees the dispersion quality needed to pass the 1000‑cycle thermal shock test on overmoulded bus‑bar insulators per UL 746C.*Industry compliance standards:* UL 746B RTI‑mechanical, UL 746C, ISO 11357‑6, ISO 11357‑3, IEC 60068‑2‑78, EN 45545‑2 for railway interior materials when applicable. *Addition ratio:* 0.12–0.30 wt% based on resin charge. *Downstream manufacturing:* Tumble‑mixing, compounding in a 75‑mm twin‑screw extruder, injection moulding into test plaques and connector housings. *End‑product type:* Heat‑stabilised PA66 moulding granules for under‑hood automotive electrical components and railway interior connectors, rated for continuous use at 140 °C (RTI‑mechanical).
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    Certification & Compliance
    More Introduction

    1,3-Benzothiazole-5-carboxylic acid (CAS 68867-14-1) presents as a crystalline off-white powder with an assay typically exceeding 98.5% by HPLC (peak area, 254 nm). Its molecular formula is C8H5NO2S, yielding a formula weight of 179.20 g·mol⁻¹. The compound melts within the range 262–267 °C, accompanied by decomposition, a thermal behavior that precludes melt-phase processing and mandates solution-phase derivatization. Storage in sealed containers under dry nitrogen at 2–8 °C is prescribed; exposure to ambient humidity above 60% RH induces hydration to a monohydrate form, which shifts the melting point downward by approximately 15 °C and complicates gravimetric dispensing during parallel synthesis campaigns. The material is classified under Harmonized System code 2934.99 and is registered under EU REACH with a minimum purity threshold of 97.0% for tonnage band I–10.

    What structural feature distinguishes 5-carboxylic substitution from the more common 2-carboxy isomer?

    The benzothiazole nucleus presents three non-equivalent aromatic C–H positions susceptible to electrophilic functionalization: C-4, C-5, and C-6, with C-5 lying meta to the endocyclic nitrogen and para to the sulfur atom. In 1,3-benzothiazole-5-carboxylic acid, the electron density distribution diverges markedly from that of 1,3-benzothiazole-2-carboxylic acid (CAS 3622-35-3). The 5-carboxy group deactivates the fused benzene ring more uniformly than the 2-carboxy substituent, which exerts a strong electron-withdrawing influence directly on the thiazole ring. This differential activation is reflected in Hammett σmeta values of approximately +0.37 for the 5-position versus +0.51 for the 2-position substituent when the carboxylic acid is converted to its methyl ester. Consequently, nucleophilic aromatic substitution at the 6-position becomes kinetically accessible under milder conditions for the 5-carboxy derivative — a reactivity window exploited in the synthesis of 6-amino-1,3-benzothiazole-5-carboxylic acid intermediates used in kinase inhibitor scaffolds.

    Metal-catalyzed cross-coupling under basic conditions: a processing conflict

    Bulk amidation of 1,3-benzothiazole-5-carboxylic acid via the acid chloride route imposes severe equipment constraints. Conversion to the acid chloride using thionyl chloride in refluxing dichloromethane (40 °C jacket temperature, glass-lined reactor) generates HCl and SO2, necessitating a caustic scrubber loop rated for 50 kg/h off-gas flow. The acid chloride itself hydrolyzes exothermically with a half-life of less than 90 seconds in unbuffered water at 25 °C. When the subsequent coupling with primary amines is performed in DMF at 0–5 °C, the free carboxylic acid is often regenerated by residual moisture, lowering isolated yields to 45–60% at scales above 100 g. An alternative activation pathway — employing EDC·HCl and HOBt in anhydrous NMP — boosts conversion to 88–93% on a 5 kg batch size, provided the NMP is dried over 4 Å molecular sieves to a water content ≤50 ppm as confirmed by Karl Fischer titration per ASTM E203-16. Process records from pilot-plant campaigns at 20 L volume reveal that omission of the pre-drying step results in a 12–18% absolute yield loss, attributed to competitive hydrolysis of the active ester.

    The compound has been deployed in the preparation of bis(benzothiazole) diamide ligands for copper(I)-catalyzed azide-alkyne cycloaddition. In one documented protocol, coupling of 1,3-benzothiazole-5-carboxylic acid with 1,2-diaminocyclohexane in the presence of HATU and DIPEA in DMF yielded a C2-symmetric ligand that accelerated the click reaction with a rate constant of 0.82 M⁻¹·s⁻¹ in water/tert-butanol (1:1), a factor of 2.4 over the analogous 6-carboxy-derived ligand. The enhancement is ascribed to a pre-organized binding pocket formed by the 5-substituted benzothiazole rings, placing the copper center within 3.2 Å of the alkyne substrate as inferred from DFT-optimized geometries.

    Regioisomeric benzothiazole carboxylic acids: comparative physical and reactivity data
    Parameter5-COOH Isomer (CAS 68867-14-1)2-COOH Isomer (CAS 3622-35-3)6-COOH Isomer (CAS 3622-36-4)
    Melting point (°C)262–267 (dec.)108–110245–250 (dec.)
    pKa (COOH, 50% aq. dioxane)3.94 ± 0.102.78 ± 0.054.02 ± 0.08
    Relative rate of EDC/HOBt amidation (krel)1.02.30.9
    Solubility in DMF at 25 °C (mg/mL)12034095
    Preferred protecting group for NH-azoleNot requiredBoc or SEMNot required

    When the target scaffold demands a benzothiazole C-5 vector: agrochemical MBI candidates

    The 5-carboxy motif maps onto the pharmacophore of several mitochondrial complex II inhibitors under development with inhibition constants (IC50) in the nanomolar range against Zymoseptoria tritici. In these structures, the carboxylic acid is converted to an N-methylamide to mimic the natural ubiquinone head group, positioning the benzothiazole sulfur within hydrogen-bonding distance of Ser83 of the succinate dehydrogenase iron-sulfur subunit. Field trial data abstracted from regulatory submissions indicate that the 5-substituted benzothiazole amide achieved 85% control of septoria leaf blotch at application rates of 75 g a.i./ha, whereas the corresponding 6-substituted analogue required 125 g a.i./ha for equivalent efficacy. The difference is attributed to slower metabolic oxidation of the 5-substituted benzothiazole ring in planta, as measured by radiolabeled residue studies where the 5-isomer showed a DT50 of 4.2 days versus 2.8 days for the 6-isomer in wheat foliage.

    Compatibility with common formulants is a critical differentiator. The free acid exhibits a sharp drop in suspension stability when tank-mixed with polyethoxylated tallow amine (POEA) surfactants below pH 5.0, leading to flocculation visible as sediment in spray-tank filters after 30 minutes of recirculation. This limitation is circumvented by pre-salification with triethanolamine (TEA) to form the water-soluble TEA salt, which maintains 98% solubility after 6 hours at pH 4.8 in a simulated spray solution per CIPAC MT 46.3. The TEA salt, however, introduces a 9% weight dilution of active content and must be handled in stainless steel vessels (AISI 316L) to avoid copper-ion-catalyzed degradation.

    Another distinguishing characteristic of the 5-carboxy isomer versus the 2-and 6-isomers is its behavior toward decarboxylative cross-coupling. When subjected to Pd(PPh3)4 (5 mol%) and Cs2CO3 in N-methyl-2-pyrrolidone at 160 °C, 1,3-benzothiazole-5-carboxylic acid undergoes decarboxylative arylation with 4-iodotoluene in 72% isolated yield, affording 5-(p-tolyl)benzothiazole. The 6-carboxy isomer delivers only 38% yield under identical conditions, a consequence of the lower electron density at the position para to the carboxylate in the 6-substituted intermediate. This reactivity differential has been leveraged in the divergent synthesis of arylated benzothiazole libraries for high-throughput screening.

    Specifications, residual impurities, and batch-to-batch variability in commercial supplies

    Technical dossiers from ISO 9001:2015-certified manufacturers list the following typical lot-release criteria: appearance (off-white powder, consistent with reference standard lot), identification (FTIR matching library spectrum with peak correlation ≥0.98), assay by HPLC (≥98.0%, area normalization), water content (≤0.5% by KF), and residue on ignition (≤0.1%). Trace levels of the 5-bromo precursor, 1,3-benzothiazole-5-bromide, are controlled below 0.2% by GC-MS, as this impurity can act as a chain-termination agent in Suzuki polycondensations when the carboxylic acid is used as a monomer end-cap. One production campaign recorded a batch failure at 15 kg scale when the bromo impurity spiked to 1.8% due to incomplete lithiation/carboxylation; the material was reworked by reslurrying in 2 M aqueous NaOH and toluene, reducing the bromide content to 0.08%, though overall recovery dropped to 62%.

    Analytical specification sheet and test methods (typical)
    PropertySpecification LimitMethod
    Assay (HPLC, anhydrous basis)98.0%In-house SOP based on Ph. Eur. 2.2.29
    Water (Karl Fischer)0.5%ASTM E203-16
    Residual solvents (GC)THF ≤500 ppm, heptane ≤200 ppmUSP <467> Class 2/3
    Heavy metals (ICP-MS)Pb ≤2 ppm, Cd ≤1 ppm, As ≤1 ppmUSP <233>
    Melting point262–267 °C (dec.)Capillary, 2 °C/min ramp
    Sulfated ash0.1%Ph. Eur. 2.4.14
    Chloride (ion chromatography)100 ppmUSP <221>

    Users in parallel medicinal chemistry routinely aliquot the compound into tared vials under dry argon using an automated powder dispenser (e.g., Chemspeed SWAVE). Static charge accumulation on the crystalline powder can lead to mass deviations exceeding ±5% at target masses below 20 mg; mitigation involves ionizing bars or humidification of the glovebox to 45% RH, though the latter must be balanced against the hydration threshold. Published data for the optimal dispense-unit humidity setpoint balancing static dissipation and water uptake are limited, but in-house data from a major pharma partner indicate that a 35–40% RH window minimized both variance and monohydrate formation over a 24-hour period.

    What distinguishes this intermediate from benzoxazole and benzimidazole analogues?

    Replacement of the benzothiazole sulfur with oxygen (benzoxazole-5-carboxylic acid, CAS 148836-29-3) or nitrogen (1H-benzo[d]imidazole-5-carboxylic acid, CAS 15788-16-6) alters both the hydrogen-bonding capacity and the lipophilicity of the derived amides. The sulfur atom in 1,3-benzothiazole-5-carboxylic acid provides a +0.8 logP unit increment over the benzoxazole congener, as calculated by the Crippen fragmentation method, while retaining fewer hydrogen-bonded water molecules in the first solvation shell compared to benzimidazole. In a congeneric series of thrombin inhibitors, the 5-carboxybenzothiazole-derived P3 fragment yielded a Ki of 8.2 nM, whereas the benzoxazole analog lost a factor of 12 in potency, largely attributable to the loss of a sulfur-π interaction with Trp215 confirmed by X-ray crystallography (PDB entry 3F68). Yet this same sulfur introduces a metabolic liability: CYP3A4-mediated S-oxidation generates a sulfoxide metabolite with an unbound clearance (CLint,u) of 18 μL/min/pmol in human liver microsomes, 4.5-fold higher than the corresponding sulfone. The benzoxazole and benzimidazole cores lack this oxidative soft spot, making them structurally superior when hepatic extraction ratios exceeding 0.7 must be avoided. The 5-carboxy substitution does not modulate the S-oxidation rate compared to the 6-carboxy analogue, but conjugating the carboxylic acid to a polar polyethylene glycol chain reduces microsomal turnover by 62%.

    At pilot scale, the thiazole ring sulfur also poses a catalyst-poisoning risk. In hydrogenation steps performed downstream (e.g., nitro reductions on the benzothiazole scaffold), palladium-on-carbon (5% Pd/C) activity diminished by 20–30% after three recycles when the substrate contained the 5-carboxybenzothiazole moiety, compared to 5–8% activity loss with the benzoxazole equivalent. This is attributed to strong Pd–S binding verified by XPS showing a shift in Pd 3d5/2 binding energy from 335.0 eV to 336.2 eV in poisoned catalysts. A sulfur-resistant catalyst system, such as a Raney nickel slurry in ethanol at 45 psig H2, alleviates this poisoning but requires post-filtration chelating resin treatment (Lewatit TP 207) to remove leached nickel below 2 ppm.

    Differences from other heterocyclic carboxylic acids also impinge on safety protocols during scale-up. Differential scanning calorimetry (DSC) at 10 K/min reveals an exotherm onset at 291 °C with an energy release of −820 J/g, placing 1,3-benzothiazole-5-carboxylic acid in the Class 3 decomposition category per the Yoshida correlation. While this is manageable in batch processes, continuous-flow reactors with channel diameters below 1 mm are recommended for N-acylation reactions run above 180 °C to maintain the thermal diffusion time constant below the adiabatic induction time. The benzoxazole analogue decomposes with a substantially lower enthalpy (−490 J/g), offering a wider safe processing window but at the cost of the aforementioned potency decrement.