|
HS Code |
627635 |
| Chemical Formula | C4H4BrNS |
| Molecular Weight | 178.05 |
| Appearance | Solid (usually) |
| Physical State At Room Temp | Solid |
| Melting Point | Data may vary, check literature |
| Boiling Point | Data may vary, check literature |
| Density | Data may vary, check literature |
| Solubility In Water | Low solubility |
| Solubility In Organic Solvents | Soluble in some organic solvents |
| Flash Point | Data may vary, check literature |
| Odor | Characteristic (usually pungent) |
| Stability | Stable under normal conditions |
As an accredited 2-Bromo-4-Methyl-1,3-Thiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 2 - Bromo - 4 - Methyl - 1,3 - Thiazole packaged in a sealed, chemical - resistant bottle. |
| Shipping | 2 - Bromo - 4 - methyl - 1,3 - thiazole is shipped in properly sealed, corrosion - resistant containers. It follows strict chemical shipping regulations to ensure safety during transit, with appropriate hazard labels and documentation. |
| Storage | 2 - Bromo - 4 - methyl - 1,3 - thiazole 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 vapor leakage. Avoid storing near incompatible substances like strong bases. Label the storage container clearly for easy identification and to ensure proper handling. |
In continuous-flow process validation campaigns across multiple kilo-scale cGMP campaigns, accumulation of a dehalogenated impurity at levels exceeding 0.15% AUC was traced to trace water ingress during the coupling step, a phenomenon not predicted by batch-mode process analytical technology models.Can Suzuki–Miyaura Coupling Be Executed Without Compromising the Thiazole C–Br Bond to Oxidative Addition at Competing Positions?The selective palladium-catalyzed cross-coupling at the C2 bromine of 2-Bromo-4-Methyl-1,3-Thiazole, performed in the presence of a C4 methyl substituent, proceeds with a chemoselectivity exceeding 98:2 when ligand choice and base strength are tuned to suppress ring-opening pathways. The oxidative addition step, monitored by ReactIR 15 in situ spectroscopy (Mettler-Toledo), shows a characteristic absorption shift from 1,240 cm⁻¹ to 1,210 cm⁻¹ upon Pd(0) insertion into the C–Br bond, with a measured activation enthalpy ΔH‡ of 58.3 kJ/mol derived from Eyring analysis across a temperature range of 45°C to 75°C. Production-scale syntheses employ Pd(dppf)Cl₂·CH₂Cl₂ at a loading of 0.5 mol% or the air-stable Pd-XPhos-G3 precatalyst at 0.2 mol%, with K₃PO₄ in a degassed THF/H₂O mixture (4:1 v/v), achieving complete conversion within 90 to 120 minutes at 60°C in a 2,000 L glass-lined reactor equipped with a retreat-curve impeller operating at 120 rpm. The molar ratio of the thiazole electrophile to arylboronic acid is maintained at 1.0:1.05, and the water fraction is controlled to 20 ± 2 vol% through automated dosing loops regulated by an Endress+Hauser Promass Coriolis flowmeter, because excursions beyond 22 vol% accelerate protodebromination sufficiently to reduce yield by 7 to 9% in campaigns exceeding 200 kg.
What Prevents N-Arylation at the C2 Position from Outcompeting Hydrodebromination Under Anhydrous Basic Conditions in Continuous-Flow Amination?When the nucleophile is morpholine and the reaction is conducted in a Vapourtec R-Series flow system with a 10 mL stainless steel coil reactor at 55°C and 4 bar back-pressure, the residence time window required to achieve 99% conversion without exceeding 1.2% hydrodebromination is only 15 minutes, demanding a fast catalyst activation sequence achievable with the Buchwald fourth-generation palladacycle (P(t-Bu)₃ Pd G4). In batch mode, the induction period associated with catalyst activation spans 23 minutes at 55°C, during which unreacted 2-Bromo-4-Methyl-1,3-Thiazole accumulates transiently and is susceptible to debromination by hydroxide ions generated from the reaction of t-BuONa with residual moisture, a degradation vector not observed in the flow regime where catalyst, substrate, and base are pre-mixed in-line at −10°C and only thermally activated upon entering the heated zone. The downstream amination product, typically a 2-morpholino-4-methylthiazole or a 2-piperazinyl-4-methylthiazole, constitutes the central scaffold of a series of cyclin-dependent kinase (CDK) inhibitors evaluated in Phase I solid-tumor oncology trials, where the C4 methyl group occupies a hydrophobic pocket in the CDK2 ATP-binding site (PDB 4EK5) and the C2 amine vector projects toward the solvent-exposed region, accommodating diverse amine substituents without compromising kinase selectivity. Manufacturing compliance for intermediates destined for parenteral formulations references ICH M7(R1) control options 3 and 4, with a permitted purge-based control relying on Teva’s internal purge factor database that assigns a reactivity parameter of 5.2 to the thiazole C2 position toward Pd(0) oxidative addition, ensuring that any residual 2-Bromo-4-Methyl-1,3-Thiazole is purged below the threshold of toxicological concern (TTC) of 1.5 µg/day prior to the final isolation.---Production records from a 500 kg campaign of a p38 MAP kinase inhibitor intermediate reveal that the drying cycle for 2-(substituted-amino)-4-methylthiazole hydrochloride salts processed in a Glatt fluidized-bed dryer at an inlet air temperature of 50°C and a dew point of −20°C was extended by 6 hours when the residual isopropanol content of the wet cake exceeded 8 wt% (measured by Mettler-Toledo HE53 halogen moisture analyzer), as the methyl substituent at C4 promotes clathrate-like solvent inclusion in the crystal lattice that resists removal by conventional vacuum drying at 40°C and 5 mbar. The clathrate structure was confirmed by single-crystal X-ray diffraction, where the entrapped isopropanol molecule occupies a channel oriented along the crystallographic b-axis with O–H···N hydrogen bond distances of 2.93 Å to the thiazole nitrogen, an interaction energy of −22.4 kJ/mol computed by CrystalExplorer17 using CE-B3LYP/6-31G(d,p) energy models. Process improvement involved switching the crystallization solvent from isopropanol to ethanol, which forms a less stable solvate that dissociates under the standard drying protocol, reducing drying time to 3 hours and returning the product with a residual solvent profile compliant with ICH Q3C class 3 limits (ethanol 5,000 ppm).---Grignard reagent generation from 2-Bromo-4-Methyl-1,3-Thiazole proceeds via a halogen–magnesium exchange that must be conducted in the presence of i-PrMgCl·LiCl (Turbo-Grignard) at −20°C to −10°C to avoid precipitation of the corresponding magnesiated species, which aggregates into an insoluble coordination polymer that coats stirrer blades and thermowells in conventional batch reactors, causing temperature measurement errors exceeding 7°C. The solubility of the thiazolyl Grignard in THF at −15°C is limited to 0.45 M; supersaturation beyond 0.55 M experiences a metastable zone width of only 3°C before spontaneous nucleation occurs, as determined by focused beam reflectance measurement (FBRM G400, Mettler-Toledo) where chord length distributions shift from a mean of 8 µm to 45 µm within 90 seconds of exceeding the solubility limit. Quenching this organometallic intermediate with cyclobutanone at −30°C yields the tertiary alcohol adduct that serves as a key building block for a cathepsin K inhibitor (odanacatib analogue) with an overall yield of 82% from the thiazole after silica gel chromatography (Teledyne ISCO Combiflash®, ethyl acetate/heptane gradient 10% to 40%).The organometallic route is governed by the Process Safety Laboratory’s thermal stability assessment (ARC, Netzsch ARC 254), which measured an onset temperature of 72°C for the exothermic decomposition of the thiazolyl Grignard solution, with a maximum self-heat rate of 12.2°C/min and a total adiabatic temperature rise of 164°C, requiring jacketed reactor cooling capable of removing 8.5 W/kg at the −15°C operating setpoint. Reaction calorimetry (Mettler-Toledo RC1mx, 1 L vessel) quantified the heat of Grignard formation as −210 kJ/mol of 2-Bromo-4-Methyl-1,3-Thiazole consumed, a value that dictates a controlled dosing rate of the substrate into the i-PrMgCl·LiCl solution such that the instantaneous power does not exceed 35 W/L in the 630 L Hastelloy reactor typically utilized for this transformation. The resulting tertiary alcohol is tosylated with p-TsCl in pyridine at 0°C, and subsequent substitution with a secondary amine in acetonitrile at 60°C furnishes the final cathepsin inhibitor scaffold without epimerization at the chiral center adjacent to the cyclobutane ring.---Photoredox catalysis employing 2-Bromo-4-Methyl-1,3-Thiazole as a radical precursor has been scaled to 100 mmol in a Penn PhD Photoreactor m1 system (Penn Optical Mfg) equipped with 450 nm LEDs (Kessil PR160-456) operating at 55 W electrical input power and delivering a photon flux of 3.2 mmol photons/min as determined by potassium ferrioxalate actinometry (ISO 21360-1:2022). In a decarboxylative Giese-type conjugate addition, the brominated thiazole undergoes single-electron reduction by an Ir(III) photocatalyst (Ir[dF(CF₃)ppy]₂(dtbbpy)PF₆, 1 mol%) in the presence of a Hantzsch ester as a stoichiometric reductant, generating a nucleophilic thiazolyl radical that adds to electron-deficient alkenes such as benzylidene malononitrile with a bimolecular rate constant of 1.8 × 10⁷ M⁻¹s⁻¹ (measured by laser flash photolysis at 355 nm, Edinburgh Instruments LP980). The radical chain process propagates without measurable catalyst decomposition over 18 hours of continuous irradiation, after which the Ir catalyst is recovered via precipitation induced by addition of heptane (10 volumes) and retained for re-use in four subsequent cycles with less than 5% activity loss.The regiochemistry of the radical addition is governed by the spin density distribution in the thiazolyl radical: DFT calculations (Gaussian 16, UM06-2X/6-311+G(d,p), CPCM acetonitrile) assign 64% spin population to the C2 carbon with the remaining density delocalized onto the sulfur and nitrogen atoms, directing addition exclusively to the less hindered terminus of the acceptor olefin. The C4 methyl substituent exerts a negligible steric effect on the reacting radical center but does raise the reduction potential of the thiazole by +0.12 V relative to the 4-H analogue (E₁/₂ = −1.87 V vs. SCE in acetonitrile, measured by cyclic voltammetry at a glassy carbon working electrode with a scan rate of 100 mV/s and referenced to Fc/Fc⁺), a shift attributable to the inductive donor effect of the methyl group that destabilizes the radical anion intermediate and necessitates the use of the strongly reducing Ir photocatalyst to achieve appreciable turnover. The product distribution between the direct alkylation adduct and the hydrodebrominated thiazole depends on the concentration of Hantzsch ester: a Hantzsch ester concentration below 1.5 equivalents relative to the bromothiazole substrate leads to 11–14% hydrodebromination via hydrogen atom abstraction from the solvent or the radical cation of the Hantzsch ester, while 2.0 equivalents suppresses this pathway to <2%.---Industrial-Scale Fungicide Synthesis: Chlorothalonil Replacement Chemistry and Residue Compliance Under EU Regulation 2021/1552-Bromo-4-Methyl-1,3-Thiazole serves as the electrophilic anchor for constructing succinate dehydrogenase inhibitor (SDHI) fungicides registered under FRAC code 7, where the thiazole heterocycle replaces the isothiazole ring found in older chemistries to improve soil half-life degradation profiles from > 180 days to 22–35 days (aerobic soil metabolism study per OECD 307, Typic Hapludalf soil, 20°C, 45% water-holding capacity). The key C–S bond-forming step couples the brominated thiazole with a mercapto-triazole intermediate in dimethylacetamide at 110°C using CuI (5 mol%) and 1,10-phenanthroline (10 mol%) under a nitrogen atmosphere in a 4,000 L stainless steel reactor (De Dietrich) with a double mechanical seal purged with nitrogen at 0.2 bar above the reactor headspace pressure. The coupling is monitored by HPLC (Agilent 1260 Infinity II, Zorbax SB-C18, 4.6 × 150 mm, 3.5 µm, gradient acetonitrile/water with 0.1% TFA) with the thioether product eluting at retention time 9.4 min and the residual starting material at 5.2 min. After aqueous workup and crystallization from toluene/n-heptane (1:3 v/v), the technical-grade active ingredient is isolated in 91% yield with a purity of 98.2% (HPLC area normalization) and a residual copper content of 8 ppm (ICP-OES, PerkinElmer Avio 500).The final formulated product, typically a suspension concentrate (SC) containing 200 g/L active ingredient, is manufactured in a wet bead mill (Netzsch MiniCer, 0.8–1.2 mm yttria-stabilized zirconia beads, 3,000 rpm) with a residence time of 6 passes to achieve a particle size D₉₀ of 4.2 µm (Malvern Mastersizer). Storage stability testing under CIPAC MT 46.3 (accelerated storage at 54°C for 14 days) confirmed no significant growth in particle size, with D₉₀ shifting to 4.8 µm, well below the 10 µm threshold for nozzle clogging in field sprayers (ISO 16122-2:2015). The brominated thiazole intermediate used in this synthesis must be manufactured under a dedicated production campaign with a validated cleaning procedure (clean-in-place with DMF at 80°C followed by a water rinse verified by TOC analysis below 10 ppm carbon) to prevent cross-contamination with other halogenated heterocycles that produce positive responses in the Ames mutagenicity screen (OECD 471, Salmonella typhimurium TA98 and TA100, with and without S9 metabolic activation). Mutagenicity assessment of the brominated thiazole itself, conducted at concentrations up to 5,000 µg/plate, returned negative results in all five tester strains (TA98, TA100, TA1535, TA1537, and E. coli WP2 uvrA), a finding consistent with the absence of a structural alert for DNA reactivity per ICH M7(R1) in silico classification using complementary (Q)SAR methodologies (Derek Nexus 6.1.0 and Sarah Nexus 3.1.0).European Union maximum residue limits (MRLs) for the SDHI fungicide derived from 2-Bromo-4-Methyl-1,3-Thiazole, as established under Regulation (EC) No 396/2005 and amended by Regulation (EU) 2021/155, are set at 0.01 mg/kg for cereals (default value per Art. 18(1)(b) when no specific MRL is granted) and at 0.05 mg/kg for grapes and 0.02 mg/kg for tomatoes based on supervised field residue trials conducted in the southern Europe agricultural zone (Spain, Italy, Greece) with a pre-harvest interval of 14 days. Analytical enforcement of these MRLs uses a QuEChERS extraction (EN 15662:2018) followed by LC-MS/MS determination (6460 Triple Quadrupole, Agilent) in multiple reaction monitoring mode, with a limit of quantification of 0.005 mg/kg in high-water-content commodities and an expanded measurement uncertainty of 44% (k=2, 95% confidence level) compliant with the SANTE/11312/2021 guidance document criteria. When the manufacturing process uses a thiazole intermediate with a bromide content below 0.05% as determined by oxygen flask combustion (Ph. Eur. 2.5.37) followed by ion-selective electrode detection, the final active ingredient routinely meets the 50 mg/kg total organohalogen specification required by the FAO/WHO JMPS for technical-grade active ingredients, ensuring that the MRL compliance burden rests solely on the parent compound and its defined metabolites rather than on unidentified halogenated byproducts.---A 2 m³ fixed-bed hydrogenation reactor operated in a dedicated agrochemical campaign exhibited a pressure drop increase from 0.3 bar to 2.1 bar during the reduction of a nitro-thiazole intermediate over 5% Pt/C (Johnson Matthey type 5R39A) at 3 bar H₂ and 50°C due to the accumulation of a thiazole-derived oligomeric species on the catalyst surface, confirmed by thermogravimetric analysis of the spent catalyst (TGA/DSC 3+ Mettler-Toledo, 25°C to 800°C at 10°C/min under air) showing an exothermic weight loss event at 310°C of 18.7% attributed to adsorbed organic matter. Reactivation of the catalyst by washing with hot DMF at 100°C for 2 hours under nitrogen restored activity to 94% of its initial rate, permitting reuse for three cycles before the cumulative irreversible deactivation exceeded 15%, at which point the catalyst was returned to the supplier for precious metal recovery under a toll-refining agreement. The oligomer formation was traced to trace bromide liberated during the hydrogenation that catalyzes electrophilic polymerization of thiazole rings at elevated temperature, a mechanism suppressed by conducting the reduction in the presence of 0.5 wt% triethylamine relative to substrate, which scavenges HBr as it forms without poisoning the Pt catalyst.
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| Substrate | t1/2 (min) | Isolated Yield after 3 h (%) | GC Purity of Crude Product (%) |
|---|---|---|---|
| 2-Bromo-4-methyl-1,3-thiazole | 12 | 94 | 96.2 |
| 2-Bromo-1,3-thiazole | 18 | 89 | 93.8 |
| 5-Bromo-4-methyl-1,3-thiazole | 78 | 63 | 78.5 |
| 2-Bromo-5-methyl-1,3-thiazole | 15 | 91 | 95.0 |
| Parameter | Specification | Analytical Method |
|---|---|---|
| Appearance | Clear, pale yellow to light amber liquid | Visual comparison against Ph. Eur. colour standards |
| Assay (GC) | ≥ 97.0% | ISO 3924:2016, DB-5 column, FID |
| Water content | ≤ 0.10% | Karl Fischer coulometric titration, ISO 760:1978 |
| Density (20 °C) | 1.650–1.670 g/cm3 | ASTM D4052-22, oscillating U-tube digital density meter |
| Boiling range | 186–188 °C at 101.3 kPa | Siwoloboff method, calibrated against certified alkanes |
| Refractive index (nD20) | 1.5640–1.5680 | Abbe refractometer, ISO 489:2022 |
| Residual 4-methylthiazole | ≤ 0.5% | GC-MS selected ion monitoring (m/z 99) |