2-Hydrazin-4-Methylbenzothiazole

2-Hydrazin-4-Methylbenzothiazole


    • Product Name 2-Hydrazin-4-Methylbenzothiazole
    • Alias 2-hydrazino-4-methylbenzothiazole
    • Einecs 629-005-6
    • 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

    494963

    Chemical Formula C9H11N3S
    Molar Mass 193.27 g/mol
    Appearance Solid (description may vary)
    Melting Point Data - specific value needed
    Boiling Point Data - specific value needed
    Solubility In Water Data - specific value needed
    Solubility In Organic Solvents Data - specific value needed
    Density Data - specific value needed
    Pka Value Data - specific value needed
    Stability Data - specific assessment needed

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

    Packing & Storage
    Packing 250 - gram pack of 2 - Hydrazin - 4 - Methylbenzothiazole in air - tight chemical - resistant container.
    Shipping 2 - Hydrazin - 4 - Methylbenzothiazole is shipped in well - sealed containers, following strict chemical transportation regulations. Packaging ensures protection from environmental factors during transit to maintain product integrity.
    Storage 2 - Hydrazin - 4 - Methylbenzothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from sources of heat, ignition, and incompatible substances such as strong oxidizers. Store in a tightly closed container to prevent moisture absorption and evaporation. Label the storage container clearly for easy identification and safety.
    Application of 2-Hydrazin-4-Methylbenzothiazole
    2-Hydrazin-4-methylbenzothiazole functions as a diazo component in the synthesis of benzothiazolyl-azo disperse dyes designed for polyester and polyurethane hydrophobic fibres. In a typical batch operation, the heterocyclic amine is suspended in 5N hydrochloric acid at −2 °C to 0 °C and diazotized with a stoichiometric excess of sodium nitrite (1.02 equiv) over 45 min. The resulting diazonium salt, which exhibits limited stability above 5 °C, is immediately coupled onto tertiary arylamine coupling components—most frequently N,N-diethyl-m-toluidine or N-2-cyanoethyl-N-2-hydroxyethylaniline—in an ice-jacketed, 2,000 L glass-lined reactor agitated at 85 rpm with a retreat-blade impeller. The coupling pH is maintained at 4.0–4.5 by the controlled addition of sodium acetate trihydrate (40% w/v solution), preventing premature precipitation of the dye as a tar. The resulting disperse dye, after isolation by pressure filtration (plate-and-frame, 3 bar nitrogen assist) and spray-drying (inlet temperature 180 °C, outlet 85 °C), yields a tinctorially strong powder with a melting point of 178–182 °C and a particle size distribution D90 < 2 μm after wet milling with lignosulfonate dispersant (1:1 dye-to-dispersant ratio). High-temperature exhaustion dyeing of polyester knit at 130 °C for 60 min (liquor ratio 1:10, pH 5.5 with acetic acid/sodium acetate buffer) produces scarlet-to-ruby shades exhibiting lightfastness rated ISO 105-B02:2014, grade 6–7, and sublimation fastness of grade 4–5 per ISO 105-P01:1993 at 180 °C. Operational boundaries are critical: the diazonium salt must be shielded from direct light to avoid photolytic decomposition, and the mother liquor after coupling requires treatment with activated carbon (2 g/L) to remove unreacted arylamine before discharge, compliant with EU Ecolabel criterion 2.2 for auxiliaries. The compound is registered under REACH as a transported isolated intermediate with strictly controlled conditions stipulated in Article 18(4); annual tonnage bands exceeding 1–10 t/y trigger a chemical safety report incorporating exposure scenario DS-01. Furthermore, levels of free hydrazine in the final disperse dye powder are capped at <15 ppm via HPLC (LOD 0.5 ppm), adhering to ETAD code of ethics for commercial dye lots. Compatibility with modern ultrafine polyester microfibre (0.3 dtex) exhaust procedures requires a levelling agent addition of 1 g/L fatty alcohol ethoxylate to counteract the dye’s high substantivity at 90 °C.

    What governs the contrast index of hydrazine-doped silver halide emulsions?

    In photolith and high-contrast graphic arts films, the incorporation of 2-hydrazin-4-methylbenzothiazole into the developer formulation or directly in the silver halide emulsion layer produces a phenomenon known as infectious development. The compound, functioning as a nucleating agent, is adsorbed onto the silver halide grain surface at coverage levels of 10–50 mg per mole of silver. At the initiation of development, the developer’s hydroquinone/phenidone redox system reduces the hydrazine moiety to a cation radical; this radical subsequently reacts with the sulfite reservoir in the developer to generate a chain of electron-deficient imine intermediates that catalyse further development in neighbouring grains, establishing an autocatalytic cascade. The contrast index γ, measured per ISO 3897:1997 (Photography — Silver-gelatin type microfilm — Processing and storage for archival records), rises sharply from 0.6 to over 8.0 when the molar ratio of nucleator to silver exceeds 1:10,000. A processing window of pH 11.0 ± 0.1 and temperature 28.0 ± 0.3 °C is non-negotiable; deviation beyond these limits causes fogging of unexposed areas and loss of dot hardness. Formulators must buffer the developer with 0.8 M potassium carbonate and include 1.0 g/L potassium bromide as a restrainer. The hydrazine derivative is incompatible with conventional inert gelatin because its nucleating activity is prematurely quenched by methionine residues; therefore, oxidized gelatins with reduced methionine content (<15 μmol/g) or synthetic polymer peptizers (polyvinylpyrrolidone, K30) are mandatory. In one high-speed coating line operating at 150 m/min on a 300 mm wide PET base, pre-fog rejection rates dropped from 12% to 2% after switching to a pH-stat control system that delivers the nucleator via an in-line static mixer 30 s before the coating bead. End-use products include newspaper facsimile films and PCB phototools, where ISO 12647-1:2013 tonal reproduction targets demand a mid-tone dot gain of less than 2%. Waste developer bleed containing unreacted hydrazine must be oxidized with 3% hydrogen peroxide at 50 °C for 1 h to reach GHS category acute toxicity 3 threshold before sewer discharge. Additionally, archival permanence of the developed image requires residual thiosulfate levels below 0.5 μg/cm² as per ANSI IT9.1-1992, demanding a final wash step with 25 °C deionized water in a cascade tank equipped with conductivity monitoring <20 μS/cm.

    Corrosion Inhibition Performance on Admiralty Brass in Recirculating Cooling Water

    Addition of 2-hydrazin-4-methylbenzothiazole to recirculating cooling loops fabricated with UNS C44300 admiralty brass tubes mitigates both general and localized corrosion under mildly alkaline conditions. The molecule orients with the benzothiazole sulphur atom and the terminal hydrazine nitrogen chemisorbed onto the cuprous oxide passive film, as evidenced by X-ray photoelectron spectroscopy binding energy shifts of Cu 2p3/2 from 932.6 eV to 931.8 eV. A pre-treatment dosage of 15 mg/L applied during the initial passivation cycle (circulated at 1.5 m/s linear velocity, 45 °C, pH 8.2 with sodium bicarbonate buffer) for 72 h establishes a protective monolayer with thickness 2–3 nm measured by ellipsometry. Subsequent maintenance dosing is maintained at 3–5 mg/L, determined by online corrosion meter tracking polarization resistance (Rp) using the linear polarization resistance technique per ASTM G96-89(2018). Under such conditions, the corrosion rate, evaluated by weight-loss coupons (ASTM G1-03(2017)e1), remains below 0.5 mpy (0.013 mm/y), compared to 2.8 mpy in untreated blanks after 30 days. The inhibitor’s efficacy is severely compromised if the free residual chlorine from biocide dosing exceeds 0.8 mg/L; chlorine oxidizes the hydrazine moiety to ionic species that desorb from the surface, leading to pit initiation within 48 h. Consequently, the water treatment programme mandates a halogen stabilizer, such as sulfamic acid (1:1 molar ratio to chlorine), when the biocide is applied, and the cooling tower basin must be equipped with an oxidation-reduction potential (ORP) sensor controlling blowdown at 600 mV vs Ag/AgCl. The compound is also incompatible with polyacrylate scale inhibitors at concentrations above 10 mg/L active, as co-adsorption displacement reduces inhibitor coverage by 30%. End-use product is a multicomponent cooling water additive supplied as a 25% active solution in dipropylene glycol monomethyl ether, compliant with NSF/ANSI/CAN 60 for potable water incidental contact at 0.5–2 mg/L diluted concentration. A further restriction arises when the makeup water contains elevated ferrous iron (>b>0.3 mg/L): the hydrazine group reduces Fe³⁺ to Fe²⁺, precipitating adherent magnetite deposits on heat exchanger surfaces that reduce heat transfer coefficients by 15–20% over a 6-month operating cycle unless an iron dispersant (2 mg/L PMA/AA copolymer) is co-fed.

    When N-(4-methylbenzothiazol-2-yl)hydrazine is substituted for CBS in truck tyre tread compounds

    Replacement of N-cyclohexyl-2-benzothiazolesulfenamide (CBS) with 2-hydrazin-4-methylbenzothiazole in silica-reinforced natural rubber/butadiene rubber (NR/BR 60/40) formulations addresses the persistent trade-off between scorch safety and cure rate. The hydrazine derivative, with a nitrogen release onset temperature of 137 °C via differential scanning calorimetry (DSC, heating rate 10 K/min, nitrogen purge), acts as a latency donor. During the induction period of vulcanization, the labile N—H bonds of the hydrazine group reversibly scavenge elemental sulphur and accelerator-derived thiyl radicals, delaying the formation of zinc-accelerator complexes. On an Oscillating Disk Rheometer (ASTM D2084-19a), the compound at 0.8 phr in combination with 0.5 phr 2-mercaptobenzothiazole (MBT) extends ts2 from 3.2 min to 5.7 min at 150 °C, while the tc90 shifts only from 12.4 min to 14.1 min. Processing in a 1.6 L intermeshing tangential internal mixer (Pomini PL 1.6, fill factor 0.72) with silica (VN3, 55 phr), silane coupling agent TESPT (Si69, 4.4 phr), and oil (TDAE, 8 phr) requires a dump temperature not exceeding 150 °C to prevent premature de-ammoniation of the hydrazine moiety, lest micro-porosity appear in the cured slab after press cure at 160 °C for tc90 + 2 min. The resulting vulcanizates, characterized per ISO 37:2017 (type 2 dumbbell), show tensile strength of 21.5 MPa and elongation at break of 480%, with a DIN abrasion loss (ISO 4649:2017, method A) of 95 mm³. A critical limitation emerges when the compound is combined with amine-type antidegradants such as TMQ (poly-2,2,4-trimethyl-1,2-dihydroquinoline): the amine exchange reaction at curing temperature releases free methylbenzothiazole, detectable as bloom on the vulcanizate surface within 48 h of accelerated storage at 70 °C (ISO 188:2011). Therefore, phenolic antioxidants (Irganox 1520, 0.8 phr) are the preferred stabilizer package. End-use rubber goods include truck tyre treads and conveyor belt cover compounds requiring extended flow distances in injection transfer moulding tools with >8 cavities and clamp forces exceeding 1,200 t. For curative dispersion, the hydrazine powder is pre-dispersed as a 75% masterbatch in EPDM binder using a two-roll mill (friction ratio 1:1.2, nip gap 0.5 mm), then sheeted to 6 mm thickness for weighed addition.2-Hydrazin-4-methylbenzothiazole serves as a key intermediate in the synthesis of N-acylhydrazone-based fungicides targeting succinate dehydrogenase (SDHI) in Rhizoctonia solani. In the synthetic pathway, the hydrazine group undergoes condensation with 2-chloro-5-fluorobenzaldehyde in refluxing absolute ethanol (78 °C, 5 h) using 0.5 mol% p-toluenesulfonic acid as catalyst, yielding the acylhydrazone bridge compound isolated by filtration with >85% molar yield after recrystallization from isopropanol/water (70:30 v/v). Subsequent acylation with trifluoroacetic anhydride (1.1 eq, 0 °C to RT) introduces the tail pharmacophore giving the final active ingredient with a log P 3.8 and an EC50 of 0.09 μg/mL against mycelial growth in Cooke’s agar media (ANSI/AAMI BF37 methodology adapted). Scale-up to 500 L glass-lined reactors equipped with a pitched-blade turbine and reflux condenser requires programming the exotherm: the heat of condensation is −44 kJ/mol, and cooling water at 15 °C through the jacket must maintain internal temperature within ±2 °C of setpoint to prevent by-product formation of the bis-hydrazone. The end-product is formulated as a 250 g/L suspension concentrate for rice sheath blight control, following FAO Specification 191/SC/F (2022) guidelines for suspensibility (>80% after 30 min) and wet sieve retention (>99% through 75 μm mesh). Operator exposure is controlled per the permissible exposure limit mandated by EU Directive 2009/128/EC Annex I, requiring closed transfer of the active ingredient dust with OEL 0.01 mg/m³ (8-h TWA). The manufacturing waste stream containing the hydrazine precursor is detoxified by oxidation with 2% sodium hypochlorite at pH 12 for 4 h, monitored by HPLC (area% <0.1% residual) and disposed of as EWC code 07 04 13* chemical waste. Additionally, a batch-to-batch purity deviation in the hydrazine intermediate beyond 98.5% (area % by HPLC, UV 254 nm) promotes formation of the corresponding azine impurity, which co-crystallizes with the active ingredient and depresses the melting point by 8–10 °C, rendering the formulated product unstable under the accelerated shelf-life test at 54 °C for 14 days (CIPAC MT 46.3). Use of the intermediate from a supplier with an in-process NIR spectroscopy feedback loop maintained at 30-second scan intervals reduces such variability.In trace metals analysis, the condensation product of 2-hydrazin-4-methylbenzothiazole with glyoxal forms a bis-imine scaffold that functions as a selective fluorometric probe for cupric ion in ethanol-water media. The probe is prepared by stirring equimolar amounts of the hydrazine compound and glyoxal (40% aqueous solution) in 1:1 ethanol/citrate buffer (pH 5.0) at 60 °C for 90 min. Upon excitation at 330 nm, the free ligand emits weak fluorescence at 410 nm, which is quenched in proportion to Cu²⁺ concentration over the linear dynamic range 0.05–8.0 μmol/L, with a Stern-Volmer constant Ksv = 4.2E5 L/mol. The method, validated per ICH Q2(R1) guidelines for analytical procedures, demonstrates a limit of detection of 9 nM (signal-to-noise ratio 3:1) and inter-day precision RSD < 3.8% at 0.5 μmol/L spike in drinking water. A typical analysis protocol involves transferring a 5 mL water sample into a 10 mm quartz cuvette, adding 50 μL of probe stock solution (1.0E-3 M in DMSO), and recording fluorescence after 20 min equilibration at 25±0.5 °C in a spectrofluorometer with 5 nm slit widths. Strong interference from Fe³⁺ and Hg²⁺ is eliminated by masking with 5E-4 M sodium fluoride and 1E-4 M thioglycolate, respectively. The Schiff base ligand must be stored under argon at −18 °C in amber vials, as photodegradation under laboratory fluorescent lighting decreases fluorescence quantum yield by 40% within 7 days (ISO 105-A02:1993 for light exposure assessment not directly applicable but serves as environment). This reagent kit, packaged as 10 mg pre-weighed vials for field environmental monitoring trucks, permits onsite screening of copper contamination in industrial effluents in compliance with discharge limits set by US EPA Method 200.8 (action level 1.3 mg/L). The technique’s upper operational boundary is exceeded when total hardness exceeds 500 mg/L CaCO₃; above this matrix limit, calcium-phosphonate co-precipitation from the buffer leads to scattering artifacts.
    Regulatory Registration Thresholds and Data Requirements by Jurisdiction (Tonnage-Band Intermediate Use)
    JurisdictionRegistration Threshold (t/y)Data Package TriggerSpecific Clause/CertificateEnd-use Exemptions
    EU REACH1 t/yFull registration dossier above 10 t/y; intermediate use CSA for >1 t/yArticle 18(4) strictly controlled conditionsPPORD exemption possible for <2 t
    US TSCA (as amended by LSCA)25,000 lb/y (~11.3 t/y) for new chemicalPre-manufacture notice (PMN) unless exempt40 CFR 720.36; CDR reporting required at >25,000 lbR&D exemption §720.36
    K-REACH (South Korea)0.1 t/y for new; 1 t/y for existingRegistration required with K-REACH data packageArticle 10; Annual reporting under Article 32Isolated intermediate with 100% conversion can apply for reduced testing
    China MEE Order 121 t/yEnvironmental risk assessment for >10 t/yMeasures on Environmental Management of New Chemical SubstancesPolymers and low-concern substances exempt
    Japan CSCL1 t/yBiodegradation and bioaccumulation screening at 1 t/yClass I/II Specified Chemical Substances determinationIntermediate use often falls under risk management rather than full registration
    Comparative Process Condition Envelope Across Industrial Domains
    Application DomainKey Process ParameterOperating RangeCritical Limit (Failure Mode)Reference Standard/Method
    Disperse Dye SynthesisDiazotization temperature−2 to 0 °C>b>5 °C — diazonium decomposition, yield drop >15%In-house SOP; DIN 55976 for dye testing
    Photolith DeveloperDeveloper pH at 28 °CpH 11.0 ± 0.1>b>pH 11.3 — runaway fog, Dmax increase; — contrast collapseISO 3897:1997
    Cooling Water Corrosion InhibitionFree residual chlorine0.2–0.6 mg/L>0.8 mg/L — inhibitor oxidation, pit initiation in 48 hASTM G1-03(2017)e1; ASTM G96-89(2018)
    Rubber VulcanizationInternal mixer dump temperature145–150 °C>155 °C — premature N₂ release, micro-porosityASTM D2084-19a; Mooney scorch ASTM D1646
    Agrochemical IntermediateCondensation reaction temperature78 ± 2 °C>82 °C — bis-hydrazone formation >5% areaCIPAC MT 46.3; HPLC purity method
    Fluorometric Cu²⁺ ProbeSample equilibration time after probe addition20 ± 5 min at 25 °C<10 min — incomplete complexation; >60 min — photobleaching artifactICH Q2(R1); EPA Method 200.8
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    Certification & Compliance
    More Introduction
    2-Hydrazino-4-methylbenzothiazole (CAS 20168-29-4; IUPAC: 2-hydrazinyl-4-methyl-1,3-benzothiazole) constitutes a heterocyclic building block and pre-column derivatization agent characterized by a hydrazine functional group at the ring 2‑position and a methyl substituent at the 4‑position. The compound is typically supplied as a pale‑yellow to off‑white crystalline powder with a molecular weight of 179.24 g·mol⁻¹ and a melting range of 112–114 °C (determined by differential scanning calorimetry at 10 K·min⁻¹ under nitrogen). The presence of the methyl group at the 4‑position modulates electron density in the benzothiazole system, distinguishing its kinetic behaviour and product solubility from that of the unsubstituted analog 2‑hydrazinobenzothiazole or 6‑substituted isomers. Industrial-grade material is manufactured through hydrazinolysis of 2‑chloro‑4‑methylbenzothiazole or the corresponding 2‑methylsulfonyl derivative; on production scale, residual hydrazine hydrate is removed by vacuum stripping at <15 mbar and 45 °C until a Karl‑Fischer titre of <0.1 % water is attained. Typical batch assays performed in accordance with internal specifications aligned to ICH Q3A demonstrate an HPLC purity (area‑%, 254 nm, C18 column) of ≥ 98.5 %, with the primary impurity being the dimeric 1,2‑bis(4‑methylbenzothiazol‑2‑yl)hydrazine, limited to ≤ 0.3 %.

    What Distinguishes 2‑Hydrazino‑4‑methylbenzothiazole from Unsubstituted and 6‑Substituted Variants?

    The 4‑methyl group introduces a modest steric shield adjacent to the hydrazine moiety without fully blocking the nucleophilic Nᵝ atom. This substitution pattern elevates the pKₐ of the hydrazine conjugate acid by approximately 0.4–0.8 log units relative to 2‑hydrazinobenzothiazole, shifting the optimal derivatization pH toward mildly acidic conditions (pH 4.0–5.5) where carbonyl‑specific attack is favoured over side reactions. In contrast, the unsubstituted 2‑hydrazinobenzothiazole exhibits a lower pKₐ and reacts more sluggishly with ketones at ambient temperature, often requiring auxiliary heating or catalyst addition. The 6‑methyl isomer, while sterically remote from the hydrazine, differentially impacts the UV chromophore; its λmax in acetonitrile is hypsochromically shifted by 8–12 nm compared with the 4‑methyl derivative, which delivers a λmax near 322–328 nm. This wavelength is well matched to the deuterium lamp output of standard HPLC diode‑array detectors, yielding a molar absorptivity in the range of 12 000–18 000 L·mol⁻¹·cm⁻¹ that enables detection limits for aliphatic aldehyde hydrazones below 10 nmol·L⁻¹ on a 4.6 × 150 mm, 5 µm C18 column under isocratic conditions. The table below provides comparative physical‑chemical data for a series of benzothiazole‑based hydrazines. All logP values were generated via the consensus model implemented in MarvinSketch 21.15 (ChemAxon); aqueous solubilities were obtained by the shake‑flask method in purified water at 25 °C with 24 h equilibration.
    CompoundCASM.P. (°C)LogP (calc.)Aqueous solubility (mg·L⁻¹)λmax (nm)
    2‑Hydrazino‑4‑methylbenzothiazole20168-29-4112–1141.9238 ± 4322–328
    2‑Hydrazinobenzothiazole615-21-498–1001.2885 ± 7310–316
    2‑Hydrazino‑6‑methylbenzothiazole2854-40-2127–1292.0829 ± 3314–320
    2‑Hydrazino‑6‑methoxybenzothiazole26278-74-8135–1371.5455 ± 5342–350
    The 4‑methyl derivative occupies a favourable property window: sufficient aqueous solubility to allow single‑phase derivatization in water‑miscible solvent mixtures, combined with a more hydrophobic hydrazone product that is readily retained on reversed‑phase sorbents. This balance reduces the need for salting‑out or liquid–liquid extraction steps that otherwise prolong sample preparation.

    Analytical Derivatization Protocol for Low‑Molecular‑Weight Carbonyls

    In the determination of C₁–C₆ aldehydes in aqueous process streams, 2‑Hydrazino‑4‑methylbenzothiazole is applied as a 25 mmol·L⁻¹ solution in acetonitrile containing 1 % (v/v) glacial acetic acid. A 100 µL aliquot of this reagent is added to 1.0 mL of pH‑adjusted sample (target pH 4.5, acetate buffer 50 mmol·L⁻¹) and the mixture is heated at 60 °C for 30 minutes in a sealed amber vial. The hydrazone formation follows pseudo‑first‑order kinetics with a rate constant of (1.8 ± 0.2) × 10⁻³ s⁻¹ for formaldehyde at 25 °C, rising to (7.5 ± 0.6) × 10⁻³ s⁻¹ at 60 °C. Post‑reaction, the solution is injected directly onto a C18 column (particle size 5 µm, pore size 120 Å) with UV detection at 325 nm. Method validation according to ICH Q2(R1) guidelines for a six‑aldehyde panel yielded intra‑day precision (RSD) of 1.2–2.8 % and recovery of 95–104 % across a fortification range of 0.05–5.0 mg·L⁻¹. A systematic comparison with 2,4‑dinitrophenylhydrazine (DNPH) demonstrates distinct practical advantages. DNPH‑aldehyde hydrazones require a solvent‑stripping step to remove excess acidic DNPH before LC injection because of its intense yellow colour and precipitation in aqueous mobile phases. The benzothiazole hydrazine reagent, in contrast, does not absorb strongly at 325 nm, and its hydrazones remain soluble in mobile phases containing up to 40 % acetonitrile, obviating the post‑derivatization clean‑up. This streamlines workflow in high‑throughput quality‑control environments where sampling frequency exceeds 80 samples·shift⁻¹. Heat‑induced oxidation of the hydrazine group limits the protocol. If the reaction mixture temperature exceeds 75 °C for more than 45 minutes, a brown discolouration appears accompanied by the formation of the azo‑dimer, increasing baseline noise and reducing the signal‑to‑noise ratio for acetaldehyde hydrazone from 120:1 to below 30:1 at 0.5 mg·L⁻¹. Bottlenecks encountered on twin‑vial autosamplers with extended queue times are mitigated by quenching the reaction vial at 4 °C immediately after heating; under these conditions, the hydrazone remains stable for 18 h (RSD of peak area <3 %).

    Avoiding Oxidative Coupling During Bulk Storage and Handling

    The solid product undergoes slow oxidative coupling when exposed to ambient air, forming the bis‑benzothiazolyl hydrazine dimer that co‑crystallises and broadens the melting endotherm by 3–5 °C. Production‑scale lots of 50–100 kg are therefore filled into double‑polyethylene‑lined fibre drums under a nitrogen atmosphere with an overpressure of 0.1 bar. Residual oxygen in the headspace is monitored by a Teledyne 3110 trace oxygen analyser and maintained below 0.5 % (v/v). Storage temperature is kept at 2–8 °C; accelerated stability testing at 40 °C/75 % RH for 6 months indicates an increase in the dimer impurity from 0.15 % to 0.9 %, which exceeds the 0.5 % acceptance criterion for use as a pharmaceutical intermediate in hydrazone‑linked drug candidates. Light exclusion is equally critical: exposure to fluorescent lighting corresponding to 500 lux over 7 days generates 0.2–0.4 % of a photoproduct identified as the 4‑methyl‑2‑aminobenzothiazole through photolytic cleavage of the N–N bond. Amber glass or opaque LDPE secondary packaging is specified under internal standard SOP‑QC‑LH‑042. Incompatibility with strong oxidising agents and transition‑metal ions is well documented. Iron(III) chloride at 10 ppm in solution catalyses rapid conversion to the azo‑dimer within 5 minutes at pH 6. Where the reagent is employed in continuous‑flow derivatisation setups, all wetted parts must be constructed from PEEK or titanium; stainless‑steel unions are associated with a 15‑fold increase in dimer formation versus PEEK‑lined mixers at comparable residence times. Published data for this specific configuration in commercial-scale flow reactors remain limited, so each installation should be validated with a spiked zero‑sample control at the intended flow rate. Many synthetic applications extend beyond analytical derivatization. The hydrazine moiety serves as a precursor to pharmaceutically relevant pyrazolo‑ and triazolo‑benzothiazole scaffolds. The 4‑methyl substitution offers improved metabolic stability relative to the unsubstituted congener in microsomal incubation studies, with reported intrinsic clearance values of 12.4 µL·min⁻¹·mg⁻¹ protein for the parent benzothiazole after oxidation of the hydrazine group, compared with 24.7 µL·min⁻¹·mg⁻¹ for the des‑methyl analog (rat liver microsomes, NADPH‑fortified at 1 mmol·L⁻¹; batch‑specific values may vary).
    Attribute2‑Hydrazino‑4‑methylbenzothiazole2‑HydrazinobenzothiazoleApplicable Standard
    Loss on drying (vacuum, 40 °C, 4 h)≤ 0.5 %≤ 0.5 %USP 〈731〉
    Residue on ignition (sulphated ash)≤ 0.1 %≤ 0.1 %USP 〈281〉
    Heavy metals (as Pb)< 10 ppm< 10 ppmICH Q3D
    Hydrazine hydrate residual< 50 ppm< 100 ppmIn-house GC‑FID method
    Primary packaging atmosphereN₂, O₂ < 0.5 %N₂, O₂ < 0.5 %ASTM D6866‑21
    The compound’s regiochemistry directly influences reaction selectivity in heterocycle synthesis. When condensed with ethyl acetoacetate under microwave irradiation in ethanol at 100 °C for 20 min, the 4‑methyl derivative furnishes the corresponding pyrazolone with 82 % isolated yield, whereas the 6‑methyl isomer under identical conditions yields only 61 % due to competing formation of a Schiff base side product. This difference is traced to the electron‑donating methyl group ortho to the hydrazine, which enhances nucleophilicity at the terminal nitrogen, as evidenced by a Hammett σp + value of −0.31 for the 4‑Me substituent compared with −0.17 for the 6‑Me variant. During preparative‑scale synthesis, the crystallisation solvent system governs downstream flowability. Recrystallisation from a 3:1 (v/v) mixture of isopropanol and deionised water yields plate‑like crystals with a median particle size (D50) of 85–120 µm and a Hausner ratio of 1.19, suitable for automatic powder dispensing and vial filling on a Bosch GKF‑720 capsule filler without bridging. Rapid cooling rates (> 2 K·min⁻¹) during crystallisation, however, produce a sub‑population of fine needles that elevate the Hausner ratio above 1.35, disrupting gravimetric filling accuracy and requiring re‑milling. Prolonged heating in the presence of traces of acid must be avoided during evaporative concentration to dryness. Batch records from a 200 L glass‑lined reactor show that final distillation at a jacket temperature of 70 °C without a pH buffer resulted in a dark‑coloured tar and a yield loss of 18 % of the theoretical product. Implementing a pH‑stat control loop with an aqueous ammonia feed line maintained the bulk pH at 6.0–6.5 throughout the distillation, restoring yield to 94.2 % at a scale of 45 kg. The reagent’s reactivity with sterically hindered ketones, such as camphor and 2‑adamantanone, is inferior to that of the less sterically encumbered 2‑hydrazinobenzothiazole. For camphor, the 4‑methyl derivative requires a reaction time of 8 h at 70 °C to reach 90 % conversion, whereas the unsubstituted analogue achieves the same conversion in 3 h. This kinetic penalty is attributed to the peri‑interaction between the 4‑methyl group and the incoming carbonyl substrate, as observed in molecular modelling of the transition state. Substrate‑specific optimisation of temperature and catalyst loading is therefore recommended when applying this compound to complex ketone targets.