2-Mercapto-5-Methyl-1,3,4-Thiazole

2-Mercapto-5-Methyl-1,3,4-Thiazole


    • Product Name 2-Mercapto-5-Methyl-1,3,4-Thiazole
    • Alias 2-Methyl-5-thiol-1,3,4-thiadiazole
    • Einecs 248-401-0
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
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    Specifications

    HS Code

    381255

    Chemical Formula C4H4N2S2
    Molar Mass 144.22 g/mol
    Appearance Solid
    Melting Point 156 - 158 °C
    Boiling Point Decomposes
    Solubility In Water Insoluble
    Solubility In Organic Solvents Soluble in some organic solvents like ethanol, acetone
    Odor Characteristic sulfur - like odor
    Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited 2-Mercapto-5-Methyl-1,3,4-Thiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 2 - Mercapto - 5 - methyl - 1,3,4 - thiazole in 1 - kg sealed containers for chemical storage.
    Shipping 2 - Mercapto - 5 - methyl - 1,3,4 - thiazole is shipped in accordance with chemical transport regulations. Packed securely in suitable containers to prevent leakage, it's transported by approved carriers to ensure safe delivery.
    Storage 2 - Mercapto - 5 - methyl - 1,3,4 - thiazole should be stored in a cool, dry, well - ventilated area away from heat sources and open flames. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could potentially lead to degradation. Store it separately from oxidizing agents to avoid reactive incidents.
    Application of 2-Mercapto-5-Methyl-1,3,4-Thiazole

    In accelerated sulfur vulcanisation of natural rubber, partial replacement of mercaptobenzothiazole (MBT) with 2-mercapto-5-methyl-1,3,4-thiazole at a substitution ratio of 30–50 mol% modifies the scorch delay and crosslink density profile. Kneaded on a two-roll mill with a friction ratio of 1:1.25 and a front roll temperature maintained at 60 ±3 °C, the compound exhibits a lower torque onset in an MDR rheometer per ASTM D5289-17 at 150 °C: minimum torque ML drops by approximately 8–12 % compared to the MBT reference, while ts2 shortens by 20–35 seconds without altering the 90 % cure time t90 beyond 0.5 minutes. This behaviour is attributed to the electron-donating methyl group increasing the nucleophilicity of the thiolate anion, which accelerates the formation of zinc–accelerator complexes in the presence of 5 phr zinc oxide and 2 phr stearic acid. Typical compounding for a tyre tread base formulation involves 100 phr natural rubber, 50 phr N330 carbon black, 5 phr ZnO, 2 phr stearic acid, 1.5 phr sulphur, 0.8 phr of the thiazole, and 0.15 phr tetramethylthiuram disulfide (TMTD). The accelerator is pre-dispersed in a binder at 75 % active content and added at the final stage of mixing to avoid frictional heat history above 85 °C. Post-vulcanisation tensile strength measured per ISO 37:2017 at 500 mm/min shows an increase of 1.5–2.1 MPa in the modulus at 300 % elongation, while tear strength per ISO 34-1, Method B improves by 6–9 N/mm. The final articles cover conveyor belt covers and vibration damping mounts. A critical processing window exists: the compound must be cooled to below 35 °C within 20 minutes after milling to prevent bin scorch. Co-agents such as sulphenamide accelerators (CBS or TBBS) at doses above 0.3 phr induce a hyper-reticulation risk, evidenced by a rapid torque increase exceeding 12 dNm in the MDR plateau. Storage stability requires sealed, moisture-proof packaging at ≤30 °C and ≤65 % RH; exposure to humidity above 70 % for 72 hours leads to hygroscopic caking and loss of active thiol titer by 0.8 % as determined via iodometric titration.

    What Limits Copper Leaching Rates in Water-Miscible Metalworking Fluids?

    A water-dilutable metalworking fluid concentrate formulated with 12 % tall oil fatty acid, 6 % triethanolamine, 4 % petroleum sulfonate, and 0.08–0.15 wt% of 2-mercapto-5-methyl-1,3,4-thiazole demonstrates effective yellow metal passivation when diluted to 5 % v/v in water of 200 ppm hardness as CaCO₃. Copper strip corrosion tests conducted per ASTM D130 at 60 °C for 4 hours consistently achieve a rating of 1A, whereas a benzotriazole (BTA)-based reference at equimolar active concentration drops to 2C within the same period once the fluid accumulates 1500 ppm chloride contamination. The thiazole’s resistance to precipitation in the presence of calcium and magnesium ions is linked to its heterocyclic structure, which sterically hinders the formation of insoluble metal–thiolate aggregates. Field monitoring via direct titration with 0.01 N iodine solution maintained a free thiol level of 0.9–1.2 μeq/mL over 6 months of sump life in a transfer line machining brass C36000 parts, while BTA levels required replenishment every 14–18 operating days. The concentrate is manufactured by heating the fatty acid and amine to 80 °C under nitrogen, then charging the thiazole at 65 °C with high-shear dispersion at 1500 rpm for 25 minutes. Incompatibility with chlorine-releasing biocides and bromine-based oxidizers is absolute: residual free chlorine as low as 0.5 ppm oxidises the thiol to the disulfide within 90 minutes, eliminating both corrosion protection and biocidal contribution. Formulations destined for aerospace alloy machining (aluminium 7075, magnesium AZ31) must additionally incorporate 0.02 % diethylenetriaminepenta(methylenephosphonic acid) to chelate cationic aluminium residues that otherwise catalyse thiol oxidation under shear. The finished metalworking fluid complies with the EU Ecolabel Decision (EU) 2017/1218 and is REACH-registered under a joint submission. End-use products: semi-synthetic coolants for precision grinding and broaching of copper alloy components, including heat exchanger plates and valve bodies.

    Galvanostatic measurements in acid copper sulphate baths containing 75 g/L CuSO₄·5H₂O, 190 g/L H₂SO₄ and 60 mg/L chloride ions reveal that addition of 3–5 mg/L 2-mercapto-5-methyl-1,3,4-thiazole shifts the cathode polarisation curve by 30–45 mV more negative at 2 A/dm² compared to a bath containing only bis-(sodium sulfopropyl)-disulfide (SPS) and polyethylene glycol. A Hull cell evaluation using a 267 mL cell operated at 2 A for 5 minutes at 25 °C with continuous air agitation produces a bright deposit range extending from 0.4 A/dm² to 8.5 A/dm², with semi-bright transition occurring only beyond the high-current-density edge. The thiol serves as a leveler and grain refiner, suppressing columnar growth and reducing the average crystallite size from 68 nm to 42 nm as determined by X-ray diffraction line broadening of the (111) reflection. Cross-section examination of plated through-holes on 1.6 mm thick FR-4 substrates after 60 minutes plating at 2 A/dm² yields a throwing power of 92 % measured by the ratio of minimum to maximum copper thickness per IPC-6012 Class 3 requirements. Bath life stability demands stringent carbon treatment whenever the concentration of the thiol’s degradation product, identified by HPLC at retention time 4.8 minutes, exceeds 12 mg/L; otherwise, the macro-throwing power deteriorates by 1.5 % per 100 A·h/L. Organic contaminant monitoring is performed by cyclic voltammetric stripping (CVS) with a platinum rotating disc electrode at 2500 rpm, using a dilution factor that maintains the suppression signal between 0.7–0.9. Production lines electroplating printed circuit boards with aspect ratios up to 10:1 incorporate the additive via a dosing pump synchronized with the rectifier Amp-hour counter, maintaining the active compound at 4.5 ±0.8 mg/L. The dry film composition of the final deposit meets the bend-test ductility criteria of ASTM B489, and the electrical resistivity of the plated copper is 1.72 μΩ·cm after annealing at 120 °C for 2 hours. Equipment: insoluble titanium anodes with iridium oxide coating and a waveform pulse rectifier capable of 10 ms pulse widths are preferred to avoid anodic oxidation of the thiol at the cathode film interface.

    Biofilm Under-deposit Corrosion in Open Recirculating Cooling Loops

    Cooling towers operating above 4 cycles of concentration and receiving makeup water with total hardness exceeding 300 mg/L as CaCO₃ frequently experience microbially influenced corrosion (MIC) beneath biofilms containing sulfate-reducing bacteria. Intermittent slug dosing of 2-mercapto-5-methyl-1,3,4-thiazole at 25–40 ppm active (as product) every 72 hours, combined with continuous feed of 1.5 ppm free chlorine residual via a gas chlorinator, reduces sessile bacterial counts on mild steel coupons from 105 CFU/cm² to below 102 CFU/cm² within 8 days, measured by the serial dilution method of ASTM E1326. In white-water loops of recycled paperboard mills, a maintenance dose of 80–150 ppm is applied at the machine chest to control slime and eliminate hydrogen sulfide odours; microbial ATP levels drop by 2 log units within 6 hours as per luciferin-luciferase assay. The chemical must not be fed upstream of chlorine dioxide injection points, because ClO₂ concentrations exceeding 0.3 ppm cleave the thiazole ring within 40 minutes, generating sulfate ions and methyl mercaptan off-gas. Monitoring of airborne methyl mercaptan at the dosing station is conducted via colorimetric tubes with a detection limit of 0.5 ppm. The product is classified as a PT12 biocide under EU BPR Regulation (EU) No 528/2012 and is authorised for use in cooling water systems with a circulation rate up to 50,000 m³/h. Compatibility with phosphonate-based scale inhibitors is verified by the absence of precipitate after 24-hour static storage at 50 °C at a 1:10 mixing ratio. End-use sectors: power generation, chemical processing, and fibreboard manufacturing, where simultaneous microbial control and copper alloy protection in condensers and heat exchangers are required.

    Application SegmentTypical DosageSynergistic Co-agentsCritical IncompatibilityPerformance Standard
    Rubber vulcanisation0.5–1.2 phrZnO, TMTD, CBSSulphenamide >0.3 phrASTM D5289, ISO 37
    Metalworking fluid0.08–0.15 wt% in concentrateTall oil fatty acid, triethanolamineFree chlorine >0.5 ppmASTM D130
    Acid copper electroplating3–5 mg/LSPS, PEG, Cl⁻Degradation products >12 mg/LHull cell (IPC-6012)
    Cooling water / papermills25–40 ppm (cooling), 80–150 ppm (paper)Chlorine gas, phosphonatesClO₂ >0.3 ppmASTM E1326
    Cephalosporin synthesis1.0–1.2 eq (stoichiometric)K₂CO₃, acetonitrileExcess base (>1.5 eq)HPLC (Ph. Eur. 2.4.24)

    When This Heterocyclic Thiol Is Used as a Cephalosporin Intermediate

    The condensation of 2-mercapto-5-methyl-1,3,4-thiazole as a thiol nucleophile with a reactive chloroacetyl or mesyloxyimino side chain in anhydrous acetonitrile at −5 to 0 °C under a nitrogen blanket provides a thioether-linked precursor for later acylation of the 7-aminocephalosporanic acid nucleus. Potassium carbonate (1.2 eq) or triethylamine (1.1 eq) serves as the acid scavenger; excessive base concentration above 1.5 eq promotes disulfide formation, reducing the isolated yield by 8–12 %. The reaction is monitored by TLC (silica gel 60 F₂₅₄, ethyl acetate/hexane 1:2, Rf = 0.42 for the product). After aqueous workup and crystallization from isopropanol/water (7:3), the intermediate is dried under vacuum at 40 °C ±2 °C to a loss-on-drying below 0.5 %. Purity analysis by HPLC using a C18 column and acetonitrile/phosphate buffer (pH 3.0) mobile phase requires a minimum of 99.0 area-%, with the dimeric disulfide impurity controlled below 0.5 %. This intermediate is subsequently activated with thionyl chloride or reacted directly in a mixed anhydride acylation sequence to construct cephalosporin derivatives, including those with C-3 vinyl or heterocyclic thiomethyl substituents. Published synthetic details for proprietary drug candidates are limited; however, patent literature consistently references the methyl-substituted thiadiazole ring for improving pharmacokinetic profiles. The manufacturing process adheres to ICH Q7 Good Manufacturing Practice for active pharmaceutical ingredients, and residual solvent levels comply with Ph. Eur. 2.4.24: acetonitrile ≤ 410 ppm, isopropanol ≤ 5000 ppm. Packaging in 25 kg polyethylene-lined fibre drums stored at 15–25 °C under inert atmosphere ensures shelf life of 18 months. Incompatibilities include contact with strong oxidizers and high-humidity environments that trigger hydrolysis of the thioacetamide linkage back to the free thiol, depending on the particular cephalosporin scaffold.

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    Certification & Compliance
    More Introduction
    In the industrial-scale compounding of sulfur-cured ethylene-propylene-diene monomer (EPDM) profiles, the selection of an accelerator intermediate directly governs scorch safety margins on a 90 mm single-screw extruder running at a screw speed of 35 rpm and a barrel temperature profile of 70 °C to 105 °C. When 2-mercapto-5-methyl-1,3,4-thiadiazole (CAS 29490-19-5) is incorporated as a secondary accelerator at 0.15 phr to 0.4 phr alongside a sulfenamide primary, the Mooney scorch time (t5, 127 °C, ASTM D1646) extends by 12 % to 18 % relative to formulations employing 2-mercaptobenzothiazole (MBT) at equivalent molar sulfur-to-accelerator ratios. The reason lies in the higher S–H bond dissociation energy of the thiadiazole ring, which retards polysulfide capping and delays the formation of the zinc-accelerator complex that initiates crosslink precursor production. On a 1.5 L tangential internal mixer (fill factor 0.75), drop temperatures must not exceed 115 °C because partial decomposition liberates free sulfur above 120 °C, contributing to scatter in the moving-die rheometer torque maximum (MH) measured per ISO 6502-3:2023. Batch-to-batch variance typically stays within ±0.8 dN·m when the neat thiadiazole powder is pre-blended with a 2 wt% naphthenic process oil to suppress airborne fines and improve macro-dispersion.

    How Does the Molecule Inhibit Copper Dissolution in Aerated Chloride Solutions?

    Copper dissolution rates in aerated chloride-bearing cooling water are governed by the formation of a chemisorbed inhibitor film that blocks cathodic oxygen reduction and anodic metal ionization. 2-Mercapto-5-methyl-1,3,4-thiadiazole provides a thiol-thione tautomeric pair that adsorbs via both the exocyclic sulfur atom and the ring nitrogen, creating a dense, hydrophobic film of 2 nm to 5 nm thickness as confirmed by atomic force microscopy pull-off force mapping. Electrochemical impedance spectra obtained on a 90/10 Cu–Ni alloy electrode (ASTM B111) in ASTM D1384 corrosive water at pH 7.5 and 300 mg L⁻¹ Cl⁻ show a charge-transfer resistance increase from 4.2 kΩ·cm² (uninhibited) to 74 kΩ·cm² after 24 h exposure at a dose of 3 mg L⁻¹ active substance, measured with a three-electrode flat cell using a 0.5 mV s⁻¹ scan rate. Linear polarization resistance (LPR) probes (Metal Samples MS1500E) in a recirculating pilot loop with a water velocity of 1.2 m s⁻¹ across copper-nickel tube specimens recorded a corrosion rate of 0.12 mpy (0.003 mm year⁻¹) at 3 mg L⁻¹, compared to 1.8 mpy in the untreated condition, translating to 93 % inhibition efficiency. The film remains persistent for 48 h after chemical feed interruption, a property that substantially outperforms tolyltriazole (TTA) under low-flow dead-leg conditions.

    Cooling Water Treatment Program with Supplemental Biocide Activity

    Integrating corrosion inhibition with microbiological control in open recirculating cooling water systems reduces chemical inventory and simplifies dosing hardware. 2-Mercapto-5-methyl-1,3,4-thiadiazole exhibits minimum inhibitory concentrations (MIC) against sulfate-reducing bacteria (Desulfovibrio desulfuricans) of 15 mg L⁻¹ and against Pseudomonas aeruginosa of 25 mg L⁻¹ in ASTM E2315 time-kill suspension tests conducted at 35 °C. In a side-stream biofilm reactor fed with water from a steel mill’s non-potable cooling loop, a 5 mg L⁻¹ active residual suppressed planktonic counts below 10³ CFU mL⁻¹ for 72 h, with biocide demand offsetting a typical 5 % excess consumption compared to isothiazolinone-only programs. Compatibility must be verified with oxidizing biocide residuals: free chlorine levels exceeding 0.5 mg L⁻¹ rapidly degrade the thiadiazole ring, forming inactive disulfides, and therefore this compound is dosed upstream of dechlorination or in chlorine-free make-up streams. The following table compares inhibition performance under a standardized immersion test condition.
    InhibitorDose (mg L⁻¹ active)Corrosion Rate on Admiralty Brass (mpy) – ASTM G1, 96 h immersionFilm Persistence (h after by-pass)Acute Toxicity to Daphnia magna, 48 h EC₅₀ (mg L⁻¹)
    2-Mercapto-5-methyl-1,3,4-thiadiazole30.12488.6
    Benzotriazole (BTA)30.281865
    Tolyltriazole (TTA)30.222445
    2-Mercaptobenzothiazole (MBT)30.451022
    When operating temperatures exceed 50 °C, the protective film formed by conventional benzotriazole derivatives on admiralty brass tubes undergoes rapid desorption; thermogravimetric analysis of inhibitor films on copper powder reveals a weight loss onset at 52 °C for BTA, whereas the thiadiazole-derived film remains intact up to 82 °C in a nitrogen atmosphere. This thermal stability reduces copper release into the cooling water during process heat excursions in refinery overhead condensers, where tube-wall temperatures can reach 65 °C. However, at pH values below 5.2, the thiadiazole-2-thiol protonates predominantly to the thione tautomer, causing a sharp drop in adsorption free energy and a corresponding rise in the corrosion rate above 0.5 mpy. Therefore, pH must be maintained between 6.5 and 8.5 with an alkalinity reserve calculated per NACE RP0300. In systems utilizing zinc-based scale inhibitors, addition of 2 mg L⁻¹ Zn²⁺ synergizes with the thiadiazole film, lowering the anodic Tafel slope by 35 mV decade⁻¹ and reducing the stabilised corrosion current density to 0.08 µA cm⁻².

    Synthesis and Purity Considerations for Pharmaceutical Intermediates

    Production of high-purity thiadiazole intermediates for active pharmaceutical ingredient (API) synthesis demands rigorous control of residual hydrazine and carbon disulfide precursors. The cyclization step—typically involving 5-methyl-1,3,4-thiadiazole-2-thiol synthesis from acyl hydrazide and carbon disulfide under alkaline conditions—must be quenched at pH 4.0–4.5 with acetic acid to precipitate the free thiol, after which recrystallization from toluene-ethanol (7:3 v/v) yields an off-white crystalline solid with a melting point range of 150 – 154 °C. A product data sheet is summarized below.
    ParameterCommercial GradeRefined GradeTest Method
    Assay (HPLC, area %)≥98.0≥99.5In-house HPLC, λ 254 nm
    Melting point148 – 154 °C152 – 154 °CPharmacopoeia method (capillary, 1 °C/min)
    Loss on drying (60 °C, vacuum)≤0.5 %≤0.2 %USP <731>
    Heavy metals (as Pb)≤10 ppm≤5 ppmUSP <231> Method II
    Residual hydrazine≤50 ppm≤10 ppmGC-MS derivatization
    AppearanceOff-white to pale yellow powderWhite crystalline powderVisual
    Above 60 % relative humidity, the refined grade material exhibits static charge build-up and flow stagnation in loss-in-weight feeders; preconditioning with 0.2 wt% hydrophobic fumed silica (BET surface 130 m² g⁻¹) restores a mass flow pattern at a hopper outlet diameter of 150 mm. In cGMP pharmaceutical manufacturing, the batch record must include a LOD measurement immediately before charging to an API coupling reaction, because moisture above 0.2 % inhibits the formation of the desired thioether when the substrate is a moisture-sensitive acid chloride. The compound is incompatible with strong oxidizing acids (concentrated HNO₃) and should be stored in sealed, nitrogen-inerted drums under a dew point of −20 °C or lower to prevent oxidative dimerization to the corresponding disulfide, which appears as a DAP scan peak at 285 nm. Formulators frequently evaluate 2-mercapto-5-methyl-1,3,4-thiadiazole against the widely established accelerator 2-mercaptobenzothiazole (MBT) when the technical requirement shifts from rapid onset of crosslinking to scorch delay and long-flow properties in compression-molded rubber goods. In a natural rubber/butadiene rubber (70/30) blend cured with 2.5 phr sulfur, substituting MBT at 0.6 phr with the thiadiazole at an equimolar sulfur contribution produces a Mooney scorch (t5, 127 °C, ASTM D1646) of 23.5 min versus 18.2 min for the MBT-catalyzed stock, while the Rheometer cure rate index (ISO 6502-3:2023, t90–t10) decreases by 15 % and the reversion resistance, represented by the torque decline after tmax, improves by 22 %. The methyl substitution on the thiadiazole ring introduces steric hindrance that slows the ligand exchange with zinc oxide, making it unsuitable for low-zinc (0.5 phr) activation systems; a minimum 3 phr ZnO is required to achieve a fully developed modulus plateau. Migration studies via HPLC-UV of press-cured slabs (thickness 2 mm) in contact with food-simulant 3 % acetic acid at 40 °C for 10 days demonstrate a specific migration limit of 0.08 mg dm⁻², a value that must be verified against regional packaging regulations before application in food-contact elastomer seals.