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HS Code |
983047 |
| Chemical Formula | C8H10N4S |
| Molecular Weight | 194.26 g/mol |
| Appearance | Solid (usually) |
| Odor | Typically has a characteristic odor |
| Melting Point | Specific value would require literature search |
| Boiling Point | Specific value would require literature search |
| Solubility In Water | Limited solubility likely |
| Solubility In Organic Solvents | May be soluble in some organic solvents like ethanol |
| Density | Specific value would require literature search |
| Stability | Can decompose under certain conditions |
As an accredited 4-Methyl-2-Hydrazino Benzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 500g of 4 - Methyl - 2 - Hydrazino Benzothiazole packaged in air - tight plastic bags. |
| Shipping | 4 - Methyl - 2 - Hydrazino Benzothiazole is shipped in properly sealed, corrosion - resistant containers. It follows strict chemical transport regulations to ensure safe transit, with careful handling to prevent spills and exposure during shipping. |
| Storage | Store 4 - Methyl - 2 - Hydrazino Benzothiazole in a cool, dry, well - ventilated area away from heat sources and open flames. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air. Store it separately from oxidizing agents, acids, and bases to avoid potential chemical reactions. |
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In continuous steel pickling lines operating with 15–20 wt% hydrochloric acid at bath temperatures between 60°C and 80°C, the heterocyclic hydrazine 4-methyl-2-hydrazino benzothiazole is metered into the recirculation loop via a calibrated diaphragm dosing pump at concentrations of 0.05–0.5 wt% relative to the acid inventory, with the narrow optimum typically falling at 0.15–0.25 wt% once iron ion build-up exceeds 80 g/L. The compound adsorbs onto the freshly descaled carbon steel surface through the thiazole nitrogen and the hydrazino terminal, forming a monomolecular inhibitor film that suppress both the cathodic hydrogen evolution and the anodic metal dissolution reactions. Weight-loss coupon measurements per ASTM G31-72(2021) in unstirred 18% HCl at 70°C demonstrate inhibitor efficiency exceeding 97% when the dosing is maintained above 0.2 wt%, while electrochemical impedance spectroscopy following the guidelines of ISO 17475:2005 confirms a charge-transfer resistance increase from 12 Ω·cm² to over 850 Ω·cm². Production-scale experience on push-pickling lines with a throughput of 120 metric tons/hour reveals that dosing must be dynamically adjusted whenever the acid temperature deviates by more than ±5°C from the 75°C setpoint: below 70°C the inhibitor film builds too slowly to protect against shallow pitting, while above 80°C the molecule undergoes exothermic decomposition that generates transient sulfidic byproducts, detectable as a rise in the free sulfide concentration measured by methylene blue spectrophotometry (EPA 376.2). Conformance to environmental discharge limits relies on compliance with ISO 14001:2015 management systems and, where relevant, the EU Industrial Emissions Directive (2010/75/EU) because spent acid regeneration plants must destroy residual organic inhibitor before the iron oxide recovery cycle. The finished steel strip, after rinsing and drying, enters a four-high cold rolling mill or a hot-dip galvanizing bath (for production of DX51D+Z or DX54D+Z grades per EN 10346:2015), where any residual surface carbon from uncleaved inhibitor can create wetting defects; therefore, the final rinse stage is maintained at pH 10–11 with a hydroxide-based alkalinity source to hydrolyse adsorbed species. In integrated mills that recirculate rinse water, the inhibitor’s biodegradation half-life under those alkaline oxidative conditions, as measured by manometric respirometry (OECD 301F), becomes the controlling parameter for bleed-and-feed rate settings. How Does the Hydrazinothiazole System Accelerate Vulcanisation in Diene Rubber Compounds?When 4-methyl-2-hydrazino benzothiazole is incorporated into a natural rubber (Hevea brasiliensis, technically specified grade SMR CV60) or styrene-butadiene rubber masterbatch during the second pass of an internal mixer, the compound acts not as a classical sulfenamide donor but as a temperature-activated scorch modifier that releases hydrazine radicals above 130°C. Addition levels range from 0.3 phr to 1.2 phr in a typical sulfur-cure system also containing 2.5 phr zinc oxide and 1.0 phr stearic acid; the formulation crosses the threshold into reversion sensitivity at doses exceeding 1.5 phr because excess hydrazine fragments attack polysulfidic crosslinks during the post-cure cooling stage. Production-scale mixing on an intermeshing twin-screw extruder with L/D 48:1 and segmented screw configuration (screw speed 180–250 rpm, barrel temperature profile 70→90→110→90°C) achieves a Mooney viscosity ML(1+4)100°C of 52±3 MU when 0.6 phr of the compound is pre-dispersed in an ethylene-vinyl acetate binder wax. Curing is carried out on a multi-daylight hydraulic press at 155°C to a rheometric t90 typically between 4.5 and 7.2 minutes, as determined by an oscillating disc rheometer conforming to ISO 6502-2:2018; the shape of the cure curve reveals a pronounced marching modulus when the hydrazine compound is under-weighed below 0.2 phr, indicative of insufficient crosslink precursor generation. Compliance for exported vulcanizates destined for repeated-use food-contact applications demands full traceability of the accelerator system under FDA 21 CFR §177.2600 and migration testing per EN 1186-1:2002 with simulant A (ethanol 10% v/v) at 40°C for 10 days. The finished articles—high-pressure hydraulic hose inner tubes meeting SAE J517 100R7 specifications, ethylene propylene diene monomer automotive weatherstrips, and steam-resistant conveyor belt covers for agri-food processing—exhibit an extended fatigue life (DeMattia flex crack growth below 1.2 mm after 150 kcycles) when the additive is used at the bottom end of its range, because the liberated hydrazine fragments scavenge free radicals that would otherwise initiate oxidative chain scission at the rubber-carbon black interface. Chromophoric Azomethine Formation in Disperse Dye SynthesisAttack on the terminal hydrazino group by sodium nitrite in 30% sulfuric acid at 0–5°C converts 4-methyl-2-hydrazino benzothiazole into the corresponding diazonium salt, which is immediately coupled with tertiary-aniline or pyridone-based components to yield monoazo disperse dyes with molar extinction coefficients ranging from 28,000 to 45,000 L·mol⁻¹·cm⁻¹ in the 480–560 nm region. The molar ratio of diazo component to coupler is kept slightly substoichiometric at 1:0.98 to minimise unreacted coupler carryover; coupling pH is buffered to 4.5–5.5 with sodium acetate, and the resulting pigment cake is washed on a plate-and-frame filter press to a conductivity below 50 µS/cm before spray-drying at an inlet temperature of 190°C. Batches produced on a 5,000 L glass-lined reactor equipped with an anchor agitator (60 rpm) routinely exhibit a dye strength variability of ±2.5% against the internal reference standard, measured by transmission spectrophotometry on a polyester film dyed in a high-temperature exhaust process at 130°C and 2 bar. Compliance with the Zero Discharge of Hazardous Chemicals (ZDHC) Manufacturing Restricted Substances List requires continuous monitoring of aromatic amine release during the reductive cleavage test, performed according to EN 14362-1:2017, because even trace amounts of unreacted hydrazino precursor can generate free 4-methylbenzothiazole-2-amine under the citrate-buffered dithionite conditions used to simulate textile metabolism. The finished disperse dye preparations—sold as low-dusting granules for exhaust dyeing of polyethylene terephthalate sportswear fabrics or as liquid brands for continuous thermosol pad-steam ranges—meet the fastness benchmarks specified under ISO 105-C06 (washing at 60°C) and ISO 105-B02 (xenon arc lightfastness, grade 6) when the dye is applied at 1.0–2.5% owf and aftertreated with a reduction clearing step in alkaline sodium hydrosulfite. When Thermal Oxidative Chain Scission Threatens Flexible Polyurethane FoamBlock copolymerization of toluene diisocyanate (TDI 80/20) and a 3,000 MW glycerol-initiated trifunctional polyether polyol in a low-pressure continuous slabstock foaming line (output 250 kg/min) generates an exotherm that pushes the core temperature past 160°C within the first hour of block maturation; at this temperature, the polyether soft segments are vulnerable to auto-oxidation unless a sacrificial hydrogen-donor stabilizer is homogeneously dissolved in the polyol side. 4-Methyl-2-hydrazino benzothiazole is pre-dispersed at 0.08–0.25 wt% in the polyol blend through a high-shear rotor-stator disperser operating at 3,000 rpm for 45 minutes; the 0.08 wt% lower limit is dictated by the need to suppress discolouration to a yellowness index below 15 (measured per ASTM E313-20 on a 50 mm compressed slice) after 7-day heat-ageing in a forced-air oven at 140°C. Foams produced with 0.15 wt% of the additive retain 85% of their original tensile strength (ISO 1798:2008) after the humid-ageing protocol (85°C / 95% RH for 200 hours) compared with 48% retention in the unstabilised control; this is attributed to the two-stage radical-chain-breaking mechanism in which the hydrazino group transfers a hydrogen atom to peroxy radicals and the resulting hydrazyl radical rearranges to a stable aminoxyl species detectable by electron paramagnetic resonance spectroscopy. Equipment-specific processing constraints arise because the hydrazine additive lowers the activation energy of the tin-catalysed gel reaction (dibutyltin dilaurate, 0.22 pphp), necessitating a compensatory reduction in catalyst level of 8–12% to maintain a cream time of 12±1 seconds on an electronic foam qualification unit. For flammability-compliant grades that incorporate melamine or chlorinated phosphate flame retardants, the addition limit is derated to 0.10 wt% to avoid synergistic nitrosamine formation under combustion conditions, as measured by the cone calorimeter smoke toxicity protocol described in ISO 5659-2:2017. Finished foam blocks, trimmed to 220 × 220 × 120 cm, are destined for automotive seating assemblies certified under FMVSS 302 and for upholstered furniture meeting the California Technical Bulletin TB 117-2013 smoulder resistance requirements.
Analytical Derivatization of Volatile Carbonyls for HPLC-UV QuantitationIn environmental compliance laboratories tracking formaldehyde, acetaldehyde, and acrolein emissions from wood-based panel products under ISO 16000-3:2022 or from stationary source stacks per EPA Method 0011, 4-methyl-2-hydrazino benzothiazole serves as a pre-column derivatization agent dissolved in acetonitrile at a working concentration of 2.0 mg/mL. A volume of 100 µL of the reagent solution is combined with 1.0 mL of the aqueous or impinger-trapped sample and allowed to react at 40°C for 30 minutes in an amber autosampler vial; the nucleophilic addition-elimination forms the corresponding hydrazone, which exhibits an absorption maximum at 342 nm with a molar absorptivity of 3.2×10⁴ L·mol⁻¹·cm⁻¹. Chromatographic separation on a 150 mm × 4.6 mm C18 column (5 µm particle size) using isocratic elution with methanol–water 70:30 at 1.0 mL/min resolves the formaldehyde-hydrazone, acetaldehyde-hydrazone, and excess reagent within 12 minutes, achieving a detection limit of 0.8 µg/L for formaldehyde based on a signal-to-noise ratio of 3:1. Method validation consistent with the ICH Q2(R2) guideline demands assessment of the hydrazone’s stability in solution: bench-top experiments confirm that peak area drifts below 2.5% over 8 hours when samples are kept at 4°C and shielded from ambient light, but degradation accelerates sharply at room temperature if the pH of the injection solvent falls below 3.0 or rises above 8.5. The derived hydrazones are amenable to post-column mass spectrometric confirmation (LC-MS/MS in positive electrospray mode) for forensic indoor air investigations where isobaric interferences from nitrogen-containing tobacco-smoke constituents must be distinguished, and the protocol is cited in technical annexes of the German Committee for Indoor Guide Values (AgBB) evaluation scheme for construction products. Acid-Catalysed Cyclocondensation Yielding Triazolothiazole FungicidesHeating 4-methyl-2-hydrazino benzothiazole with one equivalent of a substituted aromatic aldehyde in glacial acetic acid (10 volumes) containing 0.5 mol% p-toluenesulfonic acid at reflux (≥118°C) for 4–6 hours generates the corresponding hydrazone intermediate, which undergoes an oxidative cyclisation upon addition of ferric chloride hexahydrate (1.2 equivalents) to furnish the 3-substituted-7-methyl-1,2,4-triazolo[3,4-b]benzothiazole core; the overall isolated yield across a 200 mmol scale in a jacketed 2 L three-neck flask with overhead stirring typically falls within 68–74% after recrystallisation from dimethylformamide–water 1:1. Process safety assessments carried out according to OSHA 29 CFR 1910.119 (Process Safety Management) demand continuous monitoring of the off-gas stream for hydrazine vapour using a photoionisation detector set to 10.6 eV alarm threshold, because the exothermic ring-closure step can liberate free hydrazine if the oxidant charge is front-loaded rather than divided into three equal portions added at 30-minute intervals. The resulting triazolothiazole products are screened as succinate dehydrogenase inhibitor (SDHI) lead candidates in an early-stage discovery programme targeting Fusarium graminearum and Botrytis cinerea, with primary in-vitro ED₅₀ values measured on pesticide research-grade water-agar plates according to EUCASO EP 1/170 2024 guidelines; regulatory data package compilation for eventual registration under Regulation (EC) 1107/2009 requires that the hydrazino starting material is demonstrated to be below the 0.1% w/w residual limit in the technical-grade active ingredient, verified by a validated HPLC-UV method with a limit of quantification of 0.01%. The commercial form—a 250 g/L suspension concentrate formulated with a naphthalenesulfonate dispersant and a xanthan gum rheology modifier—is applied as a foliar spray at a rate of 0.8–1.2 L/ha in vineyard protection programmes against grey mould.
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| Property | MHB‑4M | MBT | MBTS |
|---|---|---|---|
| Mooney scorch t₅, 140 °C [min] (ASTM D1646) | 18.7 | 14.2 | 22.3 |
| Cure time t₉₀, 160 °C [min] (MDR, ASTM D5289) | 6.2 | 4.5 | 6.8 |
| Tensile strength [MPa] (ISO 37) | 23.4 | 25.1 | 24.8 |
| Inhibition efficiency 1 M HCl, 200 ppm, AISI 1018, 6 h (ASTM G31) | 95.4 % | not assessed | not assessed |
| Contact angle on inhibited steel [°] (ASTM D7334) | 89 | — | — |