|
HS Code |
715610 |
| Chemical Formula | C6H7NO2S2 |
| Molar Mass | 189.26 g/mol |
| Appearance | Solid |
| Solubility In Water | Poorly soluble |
| Melting Point | 155 - 158 °C |
| Odor | Characteristic sulfur - like odor |
| Pka Value | Around 3.8 |
| Density | Approx. 1.4 g/cm³ |
| Stability | Stable under normal conditions |
As an accredited 2-Mercapto-4-Methyl-Thiazole Acetic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 500g of 2 - Mercapto - 4 - Methyl - Thiazole Acetic Acid in a sealed plastic container. |
| Shipping | 2 - Mercapto - 4 - Methyl - Thiazole Acetic Acid is shipped in properly sealed, corrosion - resistant containers. It adheres to strict chemical shipping regulations to prevent spills and ensure safe transport due to its chemical nature. |
| Storage | 2 - Mercapto - 4 - Methyl - Thiazole Acetic Acid should be stored in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air, which could potentially lead to degradation. Store it separately from incompatible substances like strong oxidizers to avoid chemical reactions. |
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In a typical batch synthesis of a third-generation cephalosporin intermediate, (2-mercapto-4-methyl-1,3-thiazol-5-yl)acetic acid is condensed with a protected 7-amino-3-chloromethylceph-3-em-4-carboxylate salt in anhydrous N,N-dimethylacetamide maintained at −8 °C to −2 °C. The alkylation requires 1.05 to 1.20 molar equivalents of the thiol acid and is initiated by dropwise addition of 1.3 equivalents of triethylamine over 90 minutes under a dry nitrogen sweep. Agitation continues for 5–7 hours, after which the reaction mass is quenched into 0.5 M hydrochloric acid pre-cooled to 0 °C. The crude thioether precipitates as an off-white solid, isolated on a Nutsche filter and washed with chilled deionized water until the filtrate chloride content falls below 50 ppm. Recrystallization from isopropanol/water (3:1 v/v) yields a product with an HPLC purity typically exceeding 99.2 area-% and a residual heavy-metal profile compliant with ICH Q3D Option 1 limits. All solvents employed in the final isolation must meet the concentration caps stipulated by ICH Q3C: the isopropanol ceiling is 5000 ppm, dimethylacetamide 1090 ppm, and triethylamine 320 ppm. During scale-up in a 1000 L glass-lined reactor, the exotherm is managed by jacket cooling at a rate not exceeding 0.5 °C/min; excursions above +5 °C promote di-alkylation impurities that are difficult to purge without preparative chromatography. The resulting 3-[(4-methyl-2-sulfanyl-1,3-thiazol-5-yl)methylthio]cephem nucleus is a direct penultimate precursor to a range of injectable cephalosporin active pharmaceutical ingredients whose marketing authorization requires a Certificate of Suitability (CEP) demonstrating compliance with Ph. Eur. monograph 01/2023:0698 and the ICH Q7 GMP guidelines for sterile API manufacture.
Pre-drying the wet cake in a vacuum tray dryer at 45 °C and 20 mbar for 16 hours reduces the LOD to <0.3 %, a moisture threshold below which hydrolytic ring-opening of the β-lactam is kinetically suppressed during ambient storage in double polyethylene liners inside fiber drums. Shipment compliance is routinely verified against a TAMC of <100 CFU/g and an endotoxin level of <0.05 EU/mg by the Limulus amebocyte lysate method per Ph. Eur. 2.6.14. What Defines the Operational Window for Acid Pickling Inhibitor Formulations?Gravimetric evaluation conducted in accordance with ASTM G31-12a on AISI 1018 low-carbon steel coupons immersed in 1 M HCl reveals that (2-mercapto-4-methyl-1,3-thiazol-5-yl)acetic acid delivers a mass-loss inhibition efficiency exceeding 93 % at a dosing rate of 100 mg·L⁻¹ and a bulk fluid temperature of 30 °C. The chemisorption process, confirmed by a Langmuir isotherm fit with a regression coefficient R²>0.998, involves simultaneous coordination of the endocyclic thiazole nitrogen and the exocyclic thiol sulfur to the iron surface, forming a nano-scale barrier film of approximately 2–4 nm thickness as measured by variable-angle spectroscopic ellipsometry. When the pickling bath temperature exceeds 65 °C, the equilibrium shifts toward desorption, and the inhibition efficiency decays to 61–68 % at 80 °C; the compound must therefore be partitioned into low-temperature cleaning stages or co-formulated with a synergistic propargyl alcohol derivative to extend the thermal stability ceiling. Potassium iodide at 5 mM exhibits a pronounced synergistic effect, elevating the charge transfer resistance from 940 Ω·cm² to 2180 Ω·cm² in EIS spectra acquired at 10 mV AC amplitude and 0.01–100 kHz frequency sweep. Tafel polarization curves indicate mixed-type inhibition with a slight anodic predominance, shifting the corrosion potential by less than ±20 mV. No protection is afforded in oxidizing acids such as 3 M HNO₃ or in aerated sulfamic acid strippers, because the thiol moiety is rapidly oxidized to disulfide, rendering the molecule surface-inactive. Effluent discharge limits for spent bath dumps are governed by regional ZDHC Manufacturing Restricted Substances List thresholds; typical treatability via alkaline hydrolysis followed by activated sludge shows a DOC reduction of 87–92 % at a hydraulic retention time of 18 hours.
Brightener Carrier and Surface Leveler in Acidic Copper Plating SystemsIn via-fill and pattern-plating electrolytes for high-density interconnect printed circuit boards, the compound is co-adsorbed onto the cathode alongside polyethylene glycol (Mn 6000, 300 µM), bis-(sodium sulfopropyl)-disulfide (SPS, 20 µM), and chloride ion (50 ppm) in a base solution containing 200 g/L CuSO₄·5H₂O and 60 g/L H₂SO₄. A dithiocarbamate-like adsorption mechanism, driven by the thiol anchor, moderates the boundary-layer ohmic resistance and suppresses Cu⁺ accumulation at the diffusion layer, enabling a 1.5-fold extension of the bright range in the low-current-density zone of a Hull cell panel plated at 2 A for 5 minutes. The effective working concentration spans 2–10 mg/L; below 1 mg/L the leveling action is lost and surface roughness measured by atomic force microscopy climbs beyond 45 nm Ra, while above 15 mg/L the plating current efficiency drops below 82 % and the ductility of the deposit, assessed by the bend test of IPC-TM-650 2.4.3, fails after 3 cycles. Cyclic voltammetric stripping on a rotating disk electrode at 2500 rpm is the standard process control tool; the ratio of the stripping peaks at −0.1 V and +0.3 V versus SCE must be maintained between 0.65 and 0.80 to avoid via mouse-bite or corner cracking. Freshly made-up baths require a dummy plating run at 0.5 ASD for 1 Ah/L to condition the anode film and remove organic bleed-out that otherwise generates copper whiskers. Conformity to IPC-4552A for electroless copper/electrolytic copper integrity and to the RoHS 2011/65/EU recast appendix for restricted substances must be validated on each final board lot by XRF thickness mapping and cross-sectional micrography at 500×. When Gold Nanoparticle Monodispersity Depends on Ligand Exchange KineticsAqueous reduction of tetrachloroauric acid trihydrate (0.25 mmol) in the presence of (2-mercapto-4-methyl-1,3-thiazol-5-yl)acetic acid at a Au:ligand molar ratio of 1:2.5 using ice-cold 0.1 M sodium borohydride (10 mL bolus addition) produces citrate-free gold sols with a localized surface plasmon resonance peak locked at 522 ± 2 nm. The mercaptoacetic acid moiety chelates the gold surface through the sulfur headgroup while the carboxylate tail, fully deprotonated at pH > 7.2, imparts a zeta potential of −38 mV to −45 mV that suppresses aggregation through electrostatic repulsion for over 18 months when stored at 4 °C in the dark. Mean core diameters obtained from transmission electron microscopy image analysis of 300 particles range from 3.8 nm to 6.2 nm with a coefficient of variation below 12 %; larger ratios (>1:4) induce secondary ligand intercalation and broaden the distribution to ±4.1 nm standard deviation. The ligand shell withstands displacement by dithiothreitol up to 10 mM but is quantitatively stripped by a 0.01 M potassium cyanide solution within 30 seconds, a property exploited for post-synthetic metal core etching in hollow nanostructure fabrication. Cytotoxicity screening against HepG2 cells via the MTT assay per ISO 10993-5:2009 shows no statistically significant viability reduction up to 200 µg Au/mL, qualifying the conjugate for lateral flow immunoassay label development. When recovering mercury from chlor-alkali brine purge streams, a stoichiometric excess of the sodium salt of (2-mercapto-4-methyl-1,3-thiazol-5-yl)acetic acid is dosed at a molar ratio of 2.1 relative to total dissolved Hg²⁺ species while the stream pH is tightly held between 4.0 and 5.5 with 0.1 M acetate buffer. The resulting amphiphilic mercaptide precipitate, Hg(C₆H₆NO₂S₂)₂, forms micronic agglomerates that are removed on a recessed-plate filter press operating at 6 bar with a 25 µm polypropylene cloth. Filtrate total mercury levels, determined by cold-vapor atomic fluorescence spectroscopy following EPA SW-846 Method 7470A, drop from an inlet concentration of 12–45 mg/L to below 0.015 mg/L, consistently under the 0.05 mg/L North American Metal Finishing categorical effluent guideline. Sludge leachability, assessed by the Toxicity Characteristic Leaching Procedure (EPA SW-846 Method 1311), yields a mercury extract value below 0.025 mg/L, allowing disposal as non-hazardous solid waste provided the thiol loading does not exceed 3 % w/w of the filter cake mass. Overdosing above a molar ratio of 3.5 causes partial re-dissolution of the floc and elevates the chemical oxygen demand of the clarified overflow above 800 mg/L, necessitating post-carbon polishing. Chelation-UV Derivatization Strategy for sub-ppb Mercury SpeciationReversed-phase ion-pair chromatography of Hg²⁺, CH₃Hg⁺, and C₂H₅Hg⁺ in surface water is achieved by pre-column derivatization with (2-mercapto-4-methyl-1,3-thiazol-5-yl)acetic acid at 2.5 mM in 50:50 v/v acetonitrile‑ammonium acetate buffer (pH 4.5). The ternary mercury chelates exhibit a maximal UV absorbance at 342 nm with apparent molar absorptivities of (2.4–2.8)×10⁴ L·mol⁻¹·cm⁻¹, permitting a method detection limit of 0.18 µg Hg/L when 500 µL of sample is injected onto a 150 × 4.6 mm C18 column thermostated at 40 °C. Isocratic elution at 1.0 mL/min with a mobile phase containing 5 mM tetrabutylammonium hydrogen sulfate resolves the methyl‑ and ethyl‑mercury adducts within 12 minutes with a resolution factor Rₛ > 1.8. The chelation reaction proceeds quantitatively at room temperature in 5 minutes, but an excess of free Cu²⁺ above 50 µg/L quenches the signal via competitive thiol oxidation; a masking cocktail of 1 mM EDTA and 0.5 mM 1,10-phenanthroline is therefore added to each calibration standard and field sample. The protocol aligns with the performance criteria of EPA Method 1631E for low-level mercury, though it does not substitute the direct purge-and-trap fluorescence technique; it is instead used as an orthogonal confirmation tool for speciation discrepancy investigations in freshwater sediment porewater studies. During Banbury compounding of a radial truck tire innerliner masterbatch based on 100 phr bromobutyl rubber X_Butyl® BB 2030, replacement of 0.3 phr of N-cyclohexyl-2-benzothiazolesulfenamide with (2-mercapto-4-methyl-1,3-thiazol-5-yl)acetic acid extends the moving-die rheometer scorch time t₅ at 160 °C by 16 to 22 seconds, as recorded following ISO 6502:2018. The cure reversion onset, measured at the torque decay inflection point, shifts from 4.7 min to 5.1 min, while the maximum torque MH is preserved within 2 % of the control. The acid functions as a transient vulcanization retarder that decomposes above 145 °C, liberating a thiazole-sulfur fragment that subsequently participates in the sulfidation of the accelerator complex; this dual behavior eliminates the need for separate prevulcanization inhibitor additions and reduces the overall N-nitrosamine-generating potential of the compound by cutting the secondary amine accelerator inventory. Process safety data obtained on a 1.5 L internal mixer equipped with water-circulated rotors show a Mooney scorch t5 at 127 °C of 8.4 ± 0.5 min versus 5.1 ± 0.4 min for the zero-filler control, enabling a broader processing window on pin-barrel cold-feed extruders. Pre-drying of the chemical at 60 °C for 3 hours in a dehumidified air dryer is mandatory when the ambient relative humidity exceeds 65 %, otherwise moisture-induced hydrolysis generates a carboxylic acid–free mercaptothiazole that acts as a potent premature sulfur donor and reduces the induction period unpredictably. Building Block for 2-Substituted 4-Methylthiazole-Based Fungicides via HydrazinolysisRefluxing (2-mercapto-4-methyl-1,3-thiazol-5-yl)acetic acid methyl ester with 1.25 molar equivalents of hydrazine hydrate (80 % aqueous) in ethanol for 7 hours furnishes the corresponding acetohydrazide in 93–96 % isolated yield after crystallization from 2:1 ethanol‑water. Condensation of this hydrazide with substituted benzaldehydes under Dean‑Stark dehydration in toluene with 0.5 mol% p-toluenesulfonic acid yields Schiff bases that are subsequently cyclized with ethyl acetoacetate in glacial acetic acid at 110 °C to construct the pyrazoline‑thiazole biheterocyclic scaffold. The penultimate intermediates exhibit in vitro mycelial growth inhibition against Rhizoctonia solani exceeding 82 % at 25 mg a.i./L in potato dextrose agar assays, a level comparable to the commercial contact fungicide flutolanil in the same screen. Pilot-scale acylation of the free thiol with acetyl chloride in the presence of triethylamine at 0 °C converts the mercapto group into a pro-pesticide thioester that delays metabolic degradation in leaf tissue, increasing the foliar half-life from 2.3 days to 6.8 days as determined by radio‑TLC tracking of ¹⁴C-labeled deposit. Regulatory pre-registration requires the five-batch analysis report to confirm an active ingredient purity floor of 97.0 % and to quantify the dimethylformamide, dichloromethane, and toluene residue levels against FAO Specification pH 5–8 and CIPAC Handbook J limits. The hydrazide route must be executed in a dedicated, flameproof facility because the hydrazine‑ethanol vapor mixture forms a flammable atmosphere between 2.9 % and 15.4 % Lower Explosive Limit, mandating continuous LEL monitoring and nitrogen inertization of the reactor headspace. |
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In rubber compounding operations where thick cross-section articles such as engine mounts and bridge bearings demand prolonged flow under high shear without premature crosslinking, the substitution of a conventional thiazole accelerator with 2-mercapto-4-methyl-thiazole acetic acid (CAS 29490-19-5) shifts the scorch–cure rate balance decisively toward processing safety. The molecule incorporates a carboxymethylthio substituent on the thiazole ring, rendering the active sulfurating complex release temperature-dependent and markedly retarding scorch initiation at mixing and calendering temperatures below 110°C. At typical cure temperatures of 150–170°C, the accelerator dissociates to release 2-mercapto-4-methylthiazole, which then participates in the zinc-mediated sulfur crosslinking network. Comparative Mooney scorch measurements (ASTM D1646, large rotor at 121°C) have shown t5 values exceeding 38 minutes for an NR/BR (70/30) truck tire sidewall formulation at a loading of 0.8 phr, versus 21 minutes for an equal weight of 2-mercaptobenzothiazole (MBT) under identical mixing conditions in a 1.5-liter intermeshing internal mixer with ram pressure 0.6 MPa.
The product is supplied as a white to off-white crystalline powder with a characteristic thiazolic odor. Its systematic chemical name is 2-[(4-methyl-1,3-thiazol-2-yl)thio]acetic acid (synonyms: (4-methylthiazol-2-ylthio)acetic acid, MMT-acetic acid). The molecular formula is C₆H₇NO₂S₂ and the molecular weight is 189.26 g/mol. Specifications established through quality control protocols are as follows.
| Parameter | Method | Typical Value |
|---|---|---|
| Purity (HPLC area%) | In-house HPLC, UV detection 254 nm | ≥98.5% |
| Melting range | Differential scanning calorimetry (onset) | 152–155°C |
| Moisture content | Karl Fischer titration | ≤0.5% |
| Ash (sulfated) | Ignition at 800°C | ≤0.2% |
| Particle size (d₅₀) | Laser diffraction | 10–30 µm |
When evaluated in a standard accelerated sulfur formulation based on SMR CV60 natural rubber (100 phr), N330 carbon black (50 phr), zinc oxide (5 phr), stearic acid (2 phr), and sulfur (2.25 phr), the addition of 0.7 phr of the product resulted in a Mooney scorch time (MS t5, 121°C) of 42.5 minutes according to ASTM D1646, while a matching MBT formulation reached t5 at 23.1 minutes. Moving-die rheometer traces (ISO 6502, 160°C, arc 0.5°) exhibited a minimum torque ML of 2.1 dNm and a maximum torque MH of 14.8 dNm for the acetic acid derivative, compared to MH 15.6 dNm for MBT, indicating a negligible sacrifice in crosslink density. The scorch safety margin (t2 – t5) widened by approximately 6 minutes under production-relevant reversion-prone conditions.
Unlike sulfenamide accelerators such as N-cyclohexyl-2-benzothiazole sulfenamide (CBS) that rely on thermal cleavage of the S–N bond to liberate the active mercaptobenzothiazole and a secondary amine, this product’s protective group is a carboxymethyl moiety attached via a thioether linkage. The S–C bond cleavage requires a higher activation energy, delaying the onset of active accelerator species until the compound reaches the cure temperature plateau. Furthermore, the released glycolic acid does not nucleophilically attack the zinc stearate complex, whereas amines from sulfenamides can compete for zinc ions, occasionally leading to modulus fluctuations. In injection molding of large elastomeric bushings, this difference translates to a critical processing window extension of 8–12°C in the nozzle zone (determined on a 500-ton horizontal injection press with a 4-zone barrel temperature profile 70/80/90/100°C). Scalding at the gate was eliminated even when hold time was increased by 15%.
On a 90 mm cold-feed pin-extruder with a 12:1 L/D ratio processing a carbon-black-filled EPDM compound, the replacement of a thiuram/MBT accelerator package with 0.6 phr of 2-mercapto-4-methyl-thiazole acetic acid and 1.0 phr of a sulfur donor eliminated porosity in the cured sponge profile at haul-off speeds of 18 m/min. Die swell was reduced from 38% to 31% as measured by laser micrometer, attributed to absence of pre-crosslinked gel particles that form when MBT scorches in the screw compression zone. Continuous production of 2,500 meters of profile showed less than 0.5% surface defect incidence, measured against a 2% defect rate with the standard package.
In silica-filled tread formulations containing a bifunctional silane coupling agent, the ethanol liberated during the silanization reaction does not prematurely activate this accelerator, whereas sulfenamides can undergo hydrolysis-driven decomposition. Differential scanning calorimetry of the pure product places the onset of thermal decomposition at 210°C, providing a substantial safety margin above typical dump temperatures. Single-stage mixing trials in a 1.6-liter tangential internal mixer with a ram pressure of 0.55 MPa and a rotor speed of 50 rpm achieved a dump temperature of 148°C without any scorch indication. When the batch temperature inadvertently overshot to 153°C, the Mooney relaxation (MLRA) decay time remained above the critical threshold of 30 seconds, confirming that a 5°C excursion does not trigger catastrophic viscosity build-up. For downstream processing, a two-roll mill set at a front-roll temperature of 60°C and a friction ratio of 1:1.2 maintained a smooth bank without crumbling, allowing incorporation of curatives at 0.8–1.0 phr without pre-scorch.
When fabricating EPDM door seals by continuous microwave curing, the absence of amine-generating accelerators significantly reduced the susceptibility to post-cure discoloration. Laboratory aging per ISO 188 at 100°C for 168 hours on a formulation containing 1.2 phr of the product showed a ΔE color shift (CIELAB) of 1.8 units, compared to 4.3 units for a CBS-containing counterpart. Additionally, dynamic mechanical analysis (DMA) at 10 Hz recorded a tan δ peak temperature identical to that of the MBT-based compound, confirming no plasticizing effect from the acetic acid moiety.
Synergistic activation is observed when the product is paired with a small amount of a zinc dithiocarbamate; addition of 0.3 phr zinc dibutyldithiocarbamate reduced the optimum cure time (t90) by 2.7 minutes without shortening the scorch time below 28 minutes. However, excessive zinc oxide loadings above 7 phr in such a system lead to the formation of ionic zinc carboxylate bridges that raise Mooney viscosity by approximately 12 MU and reduce elongation at break. The processing window thus narrows to a stearic acid/zinc oxide molar ratio of 1.8–2.2. Published data for this specific configuration is limited, but plant trials indicate that a ratio of 2.0 yields the best balance of green strength and cure rate on a continuous salt-bath curing line operating at 230°C.
A direct comparison of acceleration performance in a model NR tread compound (SMR CV60 100 phr, N330 45 phr, oil 5 phr, ZnO 4 phr, stearic acid 2 phr, sulfur 2.0 phr) at a loading of 0.7 phr is provided below.
| Accelerator Type | MS t5 at 121°C (min) | t90 at 160°C (min) | MH−ML (dNm) | Tensile Strength (MPa) ASTM D412 |
|---|---|---|---|---|
| 2-Mercapto-4-methyl-thiazole acetic acid | 43 | 11.2 | 12.6 | 24.8 |
| 2-Mercaptobenzothiazole (MBT) | 24 | 8.9 | 13.5 | 25.3 |
| CBS (sulfenamide) | 33 | 9.4 | 12.9 | 24.1 |
The product is hygroscopic above 60% relative humidity; pre-drying in a vacuum oven at 50°C for 2 hours is recommended prior to use in moisture-sensitive polyurethane coupling. It is incompatible with strong aqueous alkalis due to salt formation; avoid blending with sodium hydroxide or potassium hydroxide masterbatches. For food-contact rubber applications, migration testing under EU Regulation 10/2011 must be performed because the substance is not explicitly listed in FDA 21 CFR 177.2600. Compliance with REACH (EC 1907/2006) is confirmed through a pre-registration dossier at a tonnage band of 1–10 tonnes/year.