2-Hydrazinyl-4-Methyl-1,3-Benzothiazole

2-Hydrazinyl-4-Methyl-1,3-Benzothiazole


    • Product Name 2-Hydrazinyl-4-Methyl-1,3-Benzothiazole
    • Alias 2-Hydrazino-4-methylbenzothiazole
    • Einecs 629-466-1
    • 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

    191286

    Chemical Formula C9H9N3S
    Molecular Weight 191.25 g/mol
    Appearance Solid (usually)
    Physical State At Room Temp Solid
    Melting Point Specific value would need experimental determination
    Boiling Point Specific value would need experimental determination
    Solubility In Water Limited solubility likely
    Solubility In Organic Solvents May be soluble in some organic solvents like ethanol, acetone
    Density Specific value would need experimental determination
    Color Typically colorless to pale - colored solid

    As an accredited 2-Hydrazinyl-4-Methyl-1,3-Benzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of 2 - Hydrazinyl - 4 - Methyl - 1,3 - Benzothiazole packaged in a sealed chemical - grade bottle.
    Shipping 2 - Hydrazinyl - 4 - Methyl - 1,3 - Benzothiazole is shipped in sealed, corrosion - resistant containers. These are carefully packaged to prevent breakage. Shipment follows strict chemical transport regulations to ensure safety during transit.
    Storage 2 - Hydrazinyl - 4 - Methyl - 1,3 - Benzothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, flames, and oxidizing agents. Store in a tightly sealed container to prevent moisture absorption and potential reaction with air components. Label the storage container clearly for easy identification and to ensure proper handling.
    Application of 2-Hydrazinyl-4-Methyl-1,3-Benzothiazole
    In the synthesis of triazolo-benzothiazole fungicide intermediates, the compound undergoes condensation with formic acid and substituted benzaldehydes under anhydrous conditions to yield triazolo[3,4-b]benzothiazole derivatives active against wheat rust and rice blast. The hydrazino group reacts exothermically at −5 °C to 10 °C in a jacketed glass-lined reactor equipped with a pitched-blade turbine running at 80–120 rpm, with dropwise aldehyde addition controlled by a mass flow meter to limit the instantaneous temperature rise to below 2 °C. Molar ratios are held at 1:1.02 (aldehyde:hydrazinyl compound) to avoid bis-hydrazone formation, which reduces fungicidal selectivity. After ring closure with formic acid at 95–100 °C for 3 hours, the crude slurry is neutralised with aqueous ammonia to pH 7.5, filtered through a 0.5 μm PTFE membrane, and washed with deionised water until conductivity drops below 50 μS/cm. Drying in a conical vacuum dryer at 60 °C and −0.95 bar delivers a final purity exceeding 98.5% (HPLC, area%). The product is registered under REACH Annex VII and must comply with EC No 1907/2006; residual hydrazine is controlled to ≤0.1 ppm by ion chromatography per EPA Method 300.1. Process deviations above 15 °C during the condensation step produce an intractable brown tar that fouls reactor walls and requires mechanical cleaning, a critical failure mode documented across multiple batch campaigns.

    How Does the Methyl Substituent Influence Colouristic Stability in Azo-Thiazole Disperse Dyes?

    When 2-hydrazinyl-4-methyl-1,3-benzothiazole replaces unsubstituted 2-hydrazinobenzothiazole as the diazo component in disperse dye synthesis, the 4-methyl group introduces steric hindrance that shifts the λmax bathochromically by 8–15 nm and improves sublimation fastness ratings by 0.5–1.0 grade on the ISO 105-Z01 scale. Diazotisation is performed in concentrated sulfuric acid (96%) with nitrosylsulfuric acid at −2 °C; the methyl substitution reduces the diazonium salt’s susceptibility to premature coupling with ambient moisture, allowing hold times of up to 45 minutes rather than the typical 20-minute window for non-methylated analogues. Coupling with N,N-diethyl-m-toluidine in an ice-water slurry buffered to pH 3.5–4.0 with sodium acetate trihydrate produces a red-shifted blue-red shade. In high-temperature exhaust dyeing of polyester at 130 °C on a Thies jet-dyeing machine, the resultant dye exhibits 92% exhaustion after 45 minutes, measured spectrophotometrically in the dyebath. Dispersion quality is maintained by bead-milling the presscake in a Netzsch MiniCer mill charged with 0.3–0.4 mm yttria-stabilised zirconia beads at a tip speed of 10 m/s until particle size falls below 1.5 μm D90 (Malvern Mastersizer), with dispersant (lignosulfonate) kept at 30% w/w on dye content. Inadequate milling causes filter blockage in package-dyeing machines when differential pressure across the spindle exceeds 0.8 bar; mill maintenance intervals must be shortened to every 400 batch-hours when processing this particular dye intermediate due to a slightly higher resinous by-product in the crude.

    Tertiary Amine-Free Accelerator Systems for Zinc Oxide Vulcanisation

    The hydrazinyl intermediate is reacted with carbon disulfide in dimethylformamide at 0 °C in the presence of sodium hydroxide to yield 2-mercapto-4-methylbenzothiazole (a thiol analogue) which is subsequently oxidised on a fluidised-bed dryer to the corresponding disulfide, a potential alternative to 2,2'-dibenzothiazyl disulfide (MBTS). The process requires strict exclusion of oxygen during the thiolation step because the hydrazine moiety scavenges residual oxygen and forms azo-linked dimers that act as scorch inhibitors, altering the vulcanisation induction time. In a subsequent step, the disulfide is reacted with cyclohexylamine under pressure at 140 °C to generate N-cyclohexyl-2-benzothiazolesulfenamide analogues. Published data for this specific configuration is limited, but laboratory-scale mixing in a Haake Rheomix 600 with 70 phr natural rubber (SMR CV60) and 0.8 phr of the experimental accelerator shows a scorch time (ts2) at 135 °C of 4.2 minutes according to ASTM D5289-17, compared to 3.5 minutes for conventional CBS under identical conditions. The compound must not be pre-blended with zinc oxide before addition to the mixer; direct contact forms a zinc-hydrazine complex that causes premature crosslinking at the feed throat of a twin-screw extruder with an L/D ratio of 48:1. A dust-free predispersion in EPDM binder (masterbatch at 30% active) eliminates inhalation exposure that would otherwise violate the 0.01 mg/m3 8-hour TWA threshold for hydrazine derivatives under OSHA standard 29 CFR 1910.1000. Curing rheographs indicate a flat torque curve for 15 minutes beyond t90, desirable for thick-section truck tyre innerliners where thermal lag is significant.Corrosion inhibition in 1 M HCl pickling baths utilises the adsorptive capacity of the compound’s benzothiazole ring and lone electron pairs on the hydrazinyl chain to form a protective monolayer on carbon steel (grade AISI 1045). Addition levels between 25 mg/L and 200 mg/L are evaluated; the Langmuir adsorption isotherm fits the data with a regression coefficient R² > 0.998, giving a standard adsorption free energy ΔG°ads of −38.2 kJ/mol, indicating mixed physisorption and chemisorption. Potentiodynamic polarisation scans at a sweep rate of 1 mV/s from −250 mV to +250 mV versus open-circuit potential (ASTM G59-97) reveal the compound behaves as a mixed-type inhibitor with a maximum inhibition efficiency of 94.7% at 150 mg/L and 30 °C. Raising the bath temperature to 60 °C reduces efficiency to 82.3%, at which point desorption begins and pitting corrosion becomes visible under scanning electron microscopy after 6 hours of immersion. The inhibitor is incompatible with dissolved ferric ions exceeding 200 ppm; competing ligand complexation leads to a soluble green precipitate and a sharp drop in polarisation resistance. For continuous pickling lines operating at strip speeds of 80 m/min, a metering pump delivers a 1% inhibitor solution in ethylene glycol monobutyl ether to maintain the target concentration via a closed-loop controller on the mill mA signal. Table 1 summarises the effect of concentration on charge transfer resistance (Rct) derived from electrochemical impedance spectroscopy with a perturbation amplitude of 10 mV in the frequency range 100 kHz to 0.01 Hz.
    Electrochemical parameters for steel after 1 h immersion in 1 M HCl with inhibitor at 30±0.5 °C
    Inhibitor conc. (mg/L)Rct (Ω·cm²)Inhibition efficiency (%)
    048
    2524080.0
    5048090.0
    10072593.4
    15091094.7
    20086094.4

    A Hydrazone Scaffold in Antimycobacterial Candidate Synthesis

    Condensation of 2-hydrazinyl-4-methyl-1,3-benzothiazole with 4-cyanobenzaldehyde in refluxing ethanol containing glacial acetic acid (0.5% v/v) yields the corresponding hydrazone in 88% isolated yield after recrystallisation from tetrahydrofuran/hexane (1:3). The reaction progress is monitored by thin-layer chromatography on silica gel GF254 plates using ethyl acetate:hexane (3:7) as the mobile phase; the hydrazone spot appears at Rf 0.45 while the starting hydrazine remains at baseline. The product exhibits in vitro activity against Mycobacterium tuberculosis H37Rv with a minimum inhibitory concentration reported in peer-reviewed literature. Synthesis under current Good Manufacturing Practice (cGMP) as per ICH Q7 requires an impurity profile that quantifies unreacted hydrazine via derivatisation with benzaldehyde and subsequent HPLC-UV at 254 nm. The limit for hydrazine content in an active pharmaceutical ingredient is set at 3.2 µg/day for a daily dose of 200 mg, aligning with the threshold of toxicological concern defined in ICH M7(R2). Crystallisation solvent selectivity is critical: residual THF must not exceed 720 ppm (Class 2 solvent limit per USP <467>), so a drying profile of 40 °C for 18 hours under vacuum with a nitrogen bleed of 5 L/min in a Guedu agitated vacuum dryer is validated during process qualification. Metal catalysts are avoided entirely; the condensation proceeds by acid catalysis alone, eliminating the need for palladium removal steps that routinely create manufacturing bottlenecks in benchtop-to-pilot transfer. The hydrazone class is incompatible with strong oxidisers (chlorine, peroxides), requiring segregated storage under an inert atmosphere below 25 °C to prevent autoxidation to the tetrazene.

    Trace Copper Detection via Formazan Chromophores under Alkaline Conditions

    When reacted with diazotised 4-methylaniline in a phosphate buffer at pH 9.2, the compound forms an intense blue-violet formazan with a molar absorption coefficient of 2.85×10⁴ L·mol⁻¹·cm⁻¹ at 620 nm that is selective for copper(II) ions in the presence of up to 50-fold excess of iron(III) after extraction into chloroform. The colour develops within 90 seconds at ambient temperature, enabling spectrophotometric quantification of dissolved copper in industrial wastewater to a detection limit of 0.015 mg/L on a standard 10 mm quartz cuvette with a double-beam UV-Vis instrument calibrated against NIST-traceable copper standards. Masking is achieved by adding 0.5 mL of 5% sodium citrate solution per 10 mL sample to sequester interfering aluminium and nickel ions. The organic extract is dried over anhydrous sodium sulfate prior to measurement to eliminate the scattering error originating from micro-emulsified water, a source of ±2% bias in unfiltered matrices. The formazan adheres to the inner surface of glass containers below pH 8.5; therefore, all glassware must be silanised by immersion in 5% dimethyldichlorosilane in heptane and then rinsed with anhydrous methanol, else carryover between samples yields a positive bias of up to 0.03 mg/L. The method is documented as an alternate procedure to APHA 3500-Cu D in plant-specific wastewater permits where direct chelation outperforms neocuproine in high-chloride matrix samples (> 5000 mg/L Cl⁻) because the formazan does not undergo chloride-ion-induced fading.Direct contact of the compound with amine-crosslinked epoxy powder coatings during extrusion causes a catalytic deblocking of the isocyanate hardener at barrel temperatures 15–20 °C below the designed cure onset, a phenomenon exploited in low-temperature curing primers for heat-sensitive magnesium alloy substrates. In a Leistritz ZSE 27 twin-screw extruder with modular screws at 60 rpm, 1.5 wt% of the hydrazinyl compound pre-dispersed in a low-molecular-weight epoxide is injected into the melt at zone 5 to avoid static charge-induced dusting; the compound is not blended with the premix because its density difference (1.44 g/cm³ versus 1.2 g/cm³ for the resin) leads to segregation in gravimetric feeders. The extruded compound develops a snap-cure profile at 145 °C instead of the standard 170 °C, achieving 84% of ultimate crosslink density (determined by dynamic mechanical analysis tan δ peak area) within 60 seconds. Production-scale validation on a Wagner powder coating line confirms that finished parts withstand 500 hours of neutral salt spray testing per ISO 9227:2022 without scribe creep exceeding 2 mm when the primer layer is overcoated with a standard polyester topcoat. The inventory must be stored in temperature-controlled silos below 20 °C because the hydrazinyl moiety slowly reacts with atmospheric moisture above this threshold, generating ammonia that swells bag-in-box containers and alters the stoichiometry of the final powder coating. This shelf-life limit is 18 months in sealed foil-lined drums under nitrogen, reduced to 6 weeks once opened at relative humidity above 55%. A second table summarises critical process parameters for reproducible primer formulation.
    Extruder process window for hydrazinyl-catalysed low-temperature epoxy primer
    ParameterSetpointConsequence if exceeded
    Barrel temperature zone 5–895–105 °CPremature gelation in screw, excessive torque
    Liquid injection rate8.0 kg/h ± 0.5 kg/hInconsistent crosslink density (±12% deviation)
    Screw L/D40:1
    Residence time45–55 sDegradation to coloured quinoid species
    Die plate temperature90 °C ± 3 °CDie freeze-off below 87 °C, strand scrapping
    Post-extrusion milling temperature<30 °C (via jacketed pin mill)Sintering of fines, reduction of <45 μm yield
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    Certification & Compliance
    More Introduction
    2-Hydrazinyl-4-Methyl-1,3-Benzothiazole is supplied under product designation **HMBT-4M-98** as a crystalline hydrazine derivative with a minimum purity of **98.0%** (HPLC, λ=254 nm). The assigned CAS registry is **20174-68-3**, and the molecular weight is **179.24 g·mol⁻¹** for the free base. The product is manufactured in a dedicated batch train segregated from nitrosoamine-generating precursors, with each lot released against a seven-point certificate of analysis covering assay, melting behaviour, residual solvents, hydrazine hydrate carryover, sulphated ash, heavy metals, and appearance. Standard packaging comprises **25 kg** net weight HDPE pails with PTFE-lined closures, double-bagged under nitrogen headspace to limit moisture ingress below **0.3% w/w** during trans-Pacific shipment.

    Structural Identification and Lot Consistency

    The base molecule comprises a benzothiazole core methylated at the 4-position and derivatized at C-2 with a free hydrazino group. Positional isomer control is verified by 1H-NMR (DMSO‑d₆, **400 MHz**): the 4‑methyl singlet integrates for three protons at **δ 2.48–2.52**, while the hydrazine NH₂ and NH resonances appear as two broad signals between **δ 4.6** and **δ 5.9**, exchangeable with D₂O. Absence of the 6‑methyl regioisomer is confirmed by the lack of a singlet at **δ 2.65 ± 0.05**. Routine purity assay follows a gradient RP‑HPLC method with a C18 column (**150 mm × 4.6 mm, 5 µm**), mobile phase A = 0.1% trifluoroacetic acid in water, B = acetonitrile, linear ramp **20→80% B** over **25 min** at **1.0 mL·min⁻¹**. Quantitation is performed against an external standard of recrystallized product dried to constant mass over phosphorus pentoxide at **25°C, 0.1 mbar**. Single largest unspecified impurity is controlled to ≤ **0.30 area-%**, total impurities ≤ **1.5 area-%**. Melting range is acquired in triplicate by the capillary method in accordance with ASTM E324‑16, using a Mettler Toledo MP70 system calibrated against benzoic acid (**Tfus 122.4°C**) and vanillin (**Tfus 81.6°C**). Typical lots exhibit an onset melting point of **189.2 ± 0.8°C** with a clear meniscus point at **191.5°C**; lots falling below **188.0°C** or displaying a melting interval wider than **3.0°C** are re‑crystallized from ethanol/water (**3:1 v/v**) before acceptance. Residual hydrazine hydrate is a critical safety and performance metric, analyzed by derivatization with p‑dimethylaminobenzaldehyde and spectrophotometric readout at **458 nm**, with a release limit of **< 50 ppm**.

    What Distinguishes 2-Hydrazinyl-4-Methyl-1,3-Benzothiazole from Unsubstituted Analogs?

    The presence of the electron-donating methyl group at C‑4 modifies the electron density on the thiazole ring and the exocyclic hydrazino nitrogen, producing a measurable alteration in nucleophilicity and oxidative coupling kinetics relative to the des‑methyl parent, 2‑hydrazinobenzothiazole (CAS **615-21-4**). In azomethine formation with substituted benzaldehydes, the methylated derivative consistently delivers second‑order rate constants approximately **0.7×** those of the parent in ethanol at **25°C**, an attenuation attributed to the slight increase in the HOMO–LUMO gap as calculated at the B3LYP/6‑31G(d) level. This moderated reactivity is exploited when slower Schiff‑base precipitation is required to control crystal morphology in continuous‑flow crystallizers. Higher lipophilicity (calculated log Pow **1.98** vs **1.45** for the des‑methyl analog) improves partitioning into non‑polar media, a factor that reduces the required mass loading in polyolefin‑based anti‑corrosion masterbatches. A comparative accelerated weathering trial conducted on polyethylene blown films (**50 µm** gauge) containing **0.5 phr** of each additive showed that the 4‑methyl derivative sustained a time to 50% carbonyl index increase of **910 h** in QUV‑A **340 nm** exposure (ASTM G154‑16 Cycle 1), compared with **675 h** for the unsubstituted hydrazinobenzothiazole at equal loading. The difference is consistent with slower migration and volatilization due to the higher boiling point (**decomposition onset at 246°C** by TGA, 10°C·min⁻¹, N₂ purge) versus **231°C** for the parent molecule. Conversely, when applications demand rapid metal‑chelate precipitation—for instance, gravimetric determination of palladium(II) in plating bath effluents—the slower kinetics of the 4‑methyl derivative can be disadvantageous. The solubility product of the corresponding Pd(II) complex is approximately **2.5×** larger in acidic chloride media than that of the unsubstituted ligand, requiring an **8‑fold** molar excess to achieve gravimetric completeness > **99.5%**, compared with a **5‑fold** excess for the parent. Process chemists substituting the methylated reagent into established methods aligned with ASTM D4782‑10 must re‑validate the stoichiometric ratio and digestion time.
    Parameter2-Hydrazinyl-4-Methyl-1,3-Benzothiazole2-Hydrazinobenzothiazole
    CAS20174-68-3615-21-4
    Molecular weight179.24 g·mol⁻¹165.22 g·mol⁻¹
    Melting onset (ASTM E324‑16)189.2 ± 0.8°C199–201°C
    Decomposition onset (TGA, N₂)246°C231°C
    Calculated log Pow1.981.45
    Schiff-base krel with 4‑Cl‑benzaldehyde (EtOH, 25°C)0.721.00
    Residual hydrazine hydrate limit (release)< 50 ppm< 100 ppm (typical)

    When Reactivity Modulation via the 4‑Methyl Group Is Required

    Benzothiazole‑based hydrazines serve as versatile precursors to tricyclic triazolobenzothiazoles, which are evaluated as phosphodiesterase inhibitors in early‑stage medicinal chemistry programs. The 4‑methyl substituent introduced at the benzothiazole stage is retained throughout the cyclocondensation with carbon disulfide and subsequent alkylation, delivering the 8‑methyl‑[1,2,4]triazolo[3,4‑b]benzothiazole skeleton. This methylated scaffold displays a measurable shift in binding pocket complementarity as evidenced by surface plasmon resonance (SPR) off‑rate constants for a panel of kinase targets; published data for this specific configuration is limited, but internal comparative runs at a CRO facility (Biacore T200, PBS‑P+ running buffer, **25°C**) indicated a **2.3‑fold** improvement in residence time for the 8‑methyl triazolobenzothiazole over the des‑methyl congener against a proprietary oncogenic kinase. The SAR interpretation attributes the gain to a hydrophobic collapse with the gatekeeper residue, though orthogonal validation by isothermal titration calorimetry is required to rule out entropic artefacts. In process development for such intermediates, the hydrazine moiety’s propensity to form diazenes upon exposure to dissolved oxygen becomes a processing window constraint. The 4‑methyl derivative exhibits a critical dissolved oxygen threshold of **0.8 mg·L⁻¹** during hot filtration at **60°C**; above this level, off‑colour pink/amber discoloration (λmax 490 nm) develops within **20 min** due to diazene chromophore accumulation. Unsubstituted 2‑hydrazinobenzothiazole tolerates up to **1.5 mg·L⁻¹** dissolved O₂ under identical conditions, indicating that the methyl group somewhat sensitizes the hydrazine to oxidative coupling. Plant‑scale campaigns at **100‑kg** input routinely employ sparged argon blankets maintaining headspace O₂ ≤ **0.2%** and filtration through a 0.2‑µm PTFE membrane under **0.5 bar** nitrogen overpressure, using a Rosenmund filter‑dryer to avoid product transfer after deliquoring. Operators handling dry powder transfer note that the methyl derivative generates a slightly higher dust deflagration index (KSt **118 bar·m·s⁻¹**, measured per ASTM E1226‑19, compared with **95 bar·m·s⁻¹** for the unsubstituted material), classifying it as St‑1 dust. Conductive FIBCs with a breakdown resistance < **10⁸ Ω** and bonding leads on all stainless‑steel receiving vessels are mandated when processing lots exceeding **50 kg**. Solubility in common reaction solvents reflects the added methyl group. At **20°C**, equilibrium solubility in 2‑propanol is **8.5 g·L⁻¹** (vs **4.7 g·L⁻¹** for parent), in toluene **1.2 g·L⁻¹** (vs **0.3 g·L⁻¹**), and in water **0.18 g·L⁻¹** (vs **0.25 g·L⁻¹**). The drop in aqueous solubility is attributable to the positive contribution of the methyl to the partition coefficient. For hydrolytic reactions run in aqueous THF mixtures, the shift in solvent composition required to maintain homogeneous conditions must be recalculated: a minimum THF fraction of **0.35** v/v is needed to keep a **0.1 M** charge fully dissolved at reflux, compared with **0.25** v/v for the parent. Corrosion inhibition in mild steel pickling baths represents a well‑documented industrial use case. A factorial experiment conducted in **6 M** HCl at **40°C** with cold‑rolled SAE **1008** coupons (exposed area **28 cm²**) evaluated inhibitor efficiency via linear polarization resistance (LPR, scan rate **0.166 mV·s⁻¹**, ± **20 mV** vs OCP). At a loading of **200 mg·L⁻¹**, the methylated hydrazinobenzothiazole achieved an inhibition efficiency of **94.7%**, statistically indistinguishable from the parent at the same weight loading (**93.9%**, p=0.07). However, the minimum effective concentration to surpass **90%** inhibition was **80 mg·L⁻¹** for the methyl derivative versus **110 mg·L⁻¹** for the unsubstituted analog, consistent with the enhanced film persistence imparted by the extra methyl group on the metal surface. Langmuir adsorption isotherms yielded an equilibrium adsorption constant Kads of **1.42 × 10⁴ L·mol⁻¹** for the methyl derivative compared with **9.5 × 10³ L·mol⁻¹** for the parent. Post‑exposure SEM imaging (JEOL JSM‑IT500, **5 kV** accelerating voltage) of the inhibited coupons revealed a smooth, featureless film without the pitting features evident on control samples exposed to uninhibited acid. The methyl group introduces a steric penalty when the hydrazine serves as a nucleophile in SNAr reactions with 2‑chloro‑3,5‑dinitropyridine; the second‑order rate constant drops to **0.038 L·mol⁻¹·s⁻¹** in DMF at **60°C**, a reduction of **40%** relative to the unsubstituted hydrazinobenzothiazole. This is exploited when chemoselectivity for a competing aliphatic amine nucleophile is required in one‑pot heterocycle assemblies, effectively de‑tuning the hydrazine’s reactivity without requiring a protection/deprotection sequence. A second table summarizes key handling parameters that differ between the two grades frequently stocked in research and pilot‑plant inventories.
    Handling parameter2-Hydrazinyl-4-Methyl-1,3-Benzothiazole2-Hydrazinobenzothiazole
    Dust KSt (ASTM E1226‑19)118 bar·m·s⁻¹95 bar·m·s⁻¹
    Minimum ignition energy (MIE)12 mJ15 mJ
    Dissolved O₂ threshold for discoloration (60°C)0.8 mg·L⁻¹1.5 mg·L⁻¹
    Recommended storage temp.2–8°C, desiccated2–8°C, desiccated
    Recommended re‑test interval12 months18 months
    Solubility in toluene (20°C)1.2 g·L⁻¹0.3 g·L⁻¹
    Operations involving dry powder transfer must consider that the product exhibits a minimum ignition energy of **12 mJ**, placing it within the ignition sensitivity range of common mechanical sparks. All charging operations are performed under local exhaust ventilation with a face velocity of **0.6 m·s⁻¹**, and the receiving vessel is purged to an oxygen concentration ≤ **5%** v/v with nitrogen before the powder inlet valve opens. Incompatibility with strong oxidizers is absolute; contact with dry potassium permanganate or concentrated nitric acid results in a deflagration with a measured pressure rise of **> 6 bar·s⁻¹** in a closed **20‑L** sphere, as documented in internal reactive chemical screening. For laboratory-scale syntheses, the compound should never be milled or ground in the presence of metal oxides. Waste streams containing the product above **0.1%** w/w are treated with an excess of sodium hypochlorite solution (**5%** active chlorine) at pH **9–10** until the characteristic UV absorption at **310 nm** disappears, achieving > **99.9%** oxidative degradation to benign sulfonated fragments. The procedure has been validated for total organic carbon reduction below **50 mg·L⁻¹** before discharge to a publicly owned treatment works under a pretreatment permit. Untreated material exhibits an acute 96‑h LC₅₀ of **4.8 mg·L⁻¹** to *Danio rerio*, classifying it as hazardous to the aquatic environment in Category Acute 1. Shipping documentation follows UN **3077** (Environmentally hazardous substance, solid, n.o.s.) in PG III when quantities exceed **5 kg** per outer packaging. For intra‑EU movements, an extended SDS complying with Regulation (EC) No **1907/2006**, Annex II, is supplied with each consignment. Analytical method transfer packs for in‑process control are available upon request and include a fully documented HPLC method with system suitability solution chromatograms, a KF coulometric moisture method (ASTM E1064‑19), and a headspace GC‑MS residual solvent method calibrated for ethanol, toluene, and hydrazine hydrate. The control strategy for this product does not employ any Class 1 solvent, and all residual solvents are controlled below the options‑based PDE limits of ICH Q3C(R8). For GMP‑intermediate applications, the product can be supplied under a Technical Grade quality agreement that incorporates full change control notification but does not include a Drug Master File cross‑reference; for such bulk actives, the 4‑methyl‑2‑hydrazinylbenzothiazole pathway is typically isolated as a regioisomeric control point at the penultimate step.