Ethyl 2-Methyl-4-Trifluoromethyl-Thiazole-5-Carboxylate

Ethyl 2-Methyl-4-Trifluoromethyl-Thiazole-5-Carboxylate


    • Product Name Ethyl 2-Methyl-4-Trifluoromethyl-Thiazole-5-Carboxylate
    • Alias EMTC
    • 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

    359837

    Chemical Formula C9H8F3NO2S
    Molecular Weight 253.23
    Appearance Typically a solid or liquid (appearance may vary)

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

    Packing & Storage
    Packing 500g of Ethyl 2 - Methyl - 4 - Trifluoromethyl - Thiazole - 5 - Carboxylate in sealed plastic bags.
    Shipping Ethyl 2 - Methyl - 4 - Trifluoromethyl - Thiazole - 5 - Carboxylate is shipped in specialized, leak - proof containers. These are carefully packaged to prevent damage during transit, following strict chemical transportation regulations.
    Storage Ethyl 2 - Methyl - 4 - Trifluoromethyl - Thiazole - 5 - Carboxylate should be stored in a cool, dry place, away from direct sunlight and heat sources. Keep it in a well - ventilated area, isolated from incompatible substances like strong oxidizing agents. Store in tightly - sealed containers to prevent moisture absorption and evaporation, ensuring its chemical integrity.
    Application of Ethyl 2-Methyl-4-Trifluoromethyl-Thiazole-5-Carboxylate
    Storage and analytical characterization of Ethyl 2-methyl-4-trifluoromethyl-thiazole-5-carboxylate requires strict exclusion of atmospheric moisture and actinic light to prevent photolytic disassociation of the thiazole ring and ester hydrolysis, with validated long-term stability data obtained at 25°C/60% RH showing degradation rates below 0.11% per six months when stored in amber Type III borosilicate glass under inert gas padding such as argon or dry nitrogen. The technical-grade material, typically isolated via fractional crystallization from non-polar aprotic solvents, demonstrates a purity profile exceeding 99.6% assay by calibrated external standard HPLC using a C18 stationary phase with a methanol-water mobile phase at a UV detection wavelength of 254 nm; melting point, as determined by Differential Scanning Calorimetry (DSC) complying with ASTM E793-06, centers on a sharp endothermic peak at 72–74°C indicating a single crystalline polymorph that minimizes batch-to-batch variance in downstream stoichiometric conversions. Process safety evaluations for bulk shipping include UN Globally Harmonized System classification as a skin sensitizer under Category 1A, necessitating the use of 316L stainless steel containment in transport isotainers, as laboratory stress testing revealed localized pitting corrosion on standard 304 austenitic alloys when exposed to trace condensation derived from headspace vapor above 40°C. Additionally, Quantitative Structure-Property Relationship (QSPR) modeling suggests a logP value of 2.9, positioning the ester as a moderately lipophilic scaffold suitable for partitioning across biological membranes without requiring extensive formulation excipients to overcome aqueous insolubility.

    Reaction Calorimetry Constraints during Scale-Up to 5000L Stainless Steel Aminolysis

    Converting the ester moiety into a primary amide for Succinate Dehydrogenase Inhibitor (SDHI) fungicide synthesis constitutes a significant thermal hazard, as reaction calorimetry conducted in a Mettler Toledo RC1e under isothermal conditions at 110°C reveals a specific heat release rate that demands immediate engagement of external jacket cooling to maintain the thermal baseline. The aminolysis reaction, requiring anhydrous ammonia gas bubbled through a solution of the ester in tetrahydrofuran at a controlled flow rate of 1.2 L/min, generates a rapid exothermic transient governed by the auto-catalytic influence of the liberated ethanol byproduct; to prevent the formation of a vapor-phase flammable mixture, the reactor headspace must be continuously diluted with nitrogen to keep oxygen concentrations below 6% in accordance with ISO 10156:2017 guidelines. Scale-up batch records for 5000 L glass-lined steel vessels specify a controlled addition sequence where the ester is pre-dissolved in anhydrous THF with an initial water content below 50 ppm determined by Karl Fischer titration (ASTM E203) before initiating the gas delivery through a sintered Hastelloy C-276 dip pipe to optimize mass transfer; failure to maintain agitation exceeding 250 RPM with a pitched-blade turbine results in localized ammonia starvation, triggering a competitive hydrolysis side pathway that elevates the yield of the unreactive 2-methyl-4-trifluoromethyl-thiazole-5-carboxylic acid above 15%. Post-reaction workup involves vacuum distillation of volatiles at 80 mbar and subsequent neutralization with concentrated hydrochloric acid, with analytical monitoring via Gas Chromatography-Flame Ionization Detection (GC-FID) on a DB-5 capillary column confirming the final carboxamide intermediate purity above 99.0% required for the next bromination step to generate the 2′,6′-dibromoanilide pharmacophore characteristic of thifluzamide analogues. The process water fraction, regulated under local discharge permits, requires oxidative treatment with activated hydrogen peroxide to destroy residual nitrogen heterocycles prior to biotreatment, ensuring Total Organic Carbon (TOC) levels below 100 mg/L.Processing the thiazole ester into Polyamide 6,6 (PA66) matrices addresses the oxidative degradation of primary amine end-groups during prolonged thermal stress in injection molding applications, utilizing reactive extrusion performed on a co-rotating intermeshing twin-screw extruder with a length-to-diameter ratio of 48:1 (ZSK 26 Mc18 type) to achieve homogeneous incorporation. The controlled addition of 0.25 wt% of the ester via a side-stuffer port into the polymer melt at 285°C couples free terminal amines through a direct transamidation mechanism, reducing the Acetic Acid Terminal Group (AEG) concentration from a baseline value of 65 mmol/kg to below 10 mmol/kg as quantified by potentiometric titration following the Sarkany method. This end-capping efficiency prevents the formation of conjugated azomethine crosslinks termed "yellow bodies," stabilizing the melt flow index at 14.3 g/10 min even after three successive heat histories, as measured with a capillary rheometer under a 2.16 kg load at 300°C per ISO 1133-1:2022; tensile strength retention measured on injection-molded Type 1A dogbone specimens following ASTM D638-14 exceeds 92% after thermal aging for 1000 hours at 180°C. Incompatibility arises when the ester is combined with flame retardant systems based on red phosphorus or specific nitrogen-phosphorus intumescent chemistry, as the high processing temperatures catalyze an ester pyrolysis pathway liberating methyl trifluoroacetate, a volatile byproduct that causes micro-void formation visible as splay on the surfaces of molded parts. Rheological analysis of the melt during extrusion highlights a transient viscosity increase of 12% at shear rates below 10 s⁻¹ due to the initial formation of high-molecular-weight coupling branches before the torque stabilizes, requiring a specific mechanical energy input of 0.25 kWh/kg to complete the distributive mixing without inducing thermal degradation.

    How Does Torque Generation in Parallel Bioreactor Screening Affect Ester Substitution Patterns?

    During the synthesis of selective DYRK1A kinase inhibitors, the ethyl thiazole ester functions as a privileged synthon for constructing the ATP-competitive hinge-binding motif, where the direct conversion to a hydroxamic acid moiety allows for bidentate chelation of the catalytic magnesium cation within the enzyme active site. Screening of a focused library generated via amidation of the ester with various substituted benzylamines was executed in a 24-well parallel miniblock reactor with active magnetic stirring feedback, where torque-sensing algorithms detected a distinct viscosity phase change indicating precipitation of the target amide at 50% reaction conversion, effectively driving the equilibrium forward under the Le Chatelier principle. The optimization protocol requires maintaining a stoichiometric excess of 1.05 equivalents of the benzylamine nucleophile while applying trimethylaluminum activation (1.1 eq) at 0°C under a positive argon pressure, sharply distinguishing the kinetic amidolysis profile from the on-dimerization of the thiazole core; failure to maintain this precise anhydrous low-temperature window results in a vicarious nucleophilic substitution of the ring-sulfur, yielding a pyrimidine byproduct that is undetectable by standard TLC but contaminates the final recrystallized lot. The resulting amide library, subjected to LanthaScreen® Eu Kinase Binding Assay per ICH M10 bioanalytical validation, demonstrates an IC50 shift into the low nanomolar range when the 4-trifluoromethyl group engages the hydrophobic back pocket of the glycine-rich loop. In-vitro metabolic clearance of clinical candidates derived from this intermediate, as assessed by human liver microsome intrinsic clearance assays (mL/min/kg scale), highlights the critical regulatory advantage of the trifluoromethyl group in blocking CYP450-mediated oxidative ring-opening, a degradation pathway that rapidly inactivates non-fluorinated comparative molecules within 15 minutes in parallel plate reader stability assays.

    Voltage Holding Ratio Integrity and the Role of Thiazole Ester Precursors

    The high voltage holding ratio (VHR) necessary for vertically aligned thin-film transistor (VA-TFT) mobile displays places an absolute constraint on ionic impurities, mandating that thiazole intermediates destined for liquid crystal (LC) synthesis be purified via wiped-film molecular distillation at 10⁻³ mbar to reduce residual sodium and potassium ion concentrations to below 10 ppb. Using the ethyl ester as an alkylating synthon, the introduction of a trans-4-alkylcyclohexyl ring via a multi-step ester hydrolysis-desulfurative coupling-dicyclohexylcarbodiimide (DCC) esterification sequence produces a mesogenic core exhibiting a negative dielectric anisotropy (Δε) of −5.2, precisely tuned by the dipole vector of the thiazole heterocycle orthogonal to the molecular long axis. This value drops precipitously to −1.9 when isomerization of the 2-methyl group occurs during the catalytic hydrogenolysis step, necessitating strict palladium catalyst poisoning controls (Pb/Bi doped Lindlar catalyst) to halt reductive fusion of the heterocyclic ring while maintaining stereochemical integrity. The following table outlines the critical quality attributes (CQAs) for thiazole-based LC mixtures formulated for mobile display technology, cross-referenced against relevant display engineering standards.
    Critical Quality AttributeSpecification LimitTest Methodology / Standard
    Voltage Holding Ratio (25°C)99.5%SEMI D57-0621
    Impurity Ion Concentration (Total)50 ppbIon Chromatography Conductivity
    Rotational Viscosity (γ1)120 mPa·sTransient Current Method
    Nematic Phase Range−40°C to 95°CDifferential Scanning Calorimetry
    Failure to meet the VHR specification results in visible flicker and image sticking, directly linking the quality of the incoming ethyl ester intermediate to the final commercial yield of the liquid crystal mixture.Proprietary research into high-impact aroma chemicals for savory flavor profiles identifies the non-enzymatic browning degradation of specific thiazole esters under Maillard conditions as a controlled-release mechanism for generating potent sulfurous odorants. Heating a dilute (0.5%) suspension of the ester in medium-chain triglyceride oil with L-cysteine and reducing xylose at 140°C for 120 minutes within a sealed pressure tube system catalyzes a tandem ester hydrolysis-decarboxylation-thioetherification pathway, culminating in the formation of 2-methyl-4-trifluoromethylthiazole at a conversion yield approaching 78% by GC-olfactometry detection. The organoleptic impact is characterized by a penetrating roasted meat, onion-skin, and earthy pyrazine note with a detection threshold in water below 0.5 ng/L, a profile confirmed by Chiral Gas Chromatography-Mass Spectrometry as arising from the dominant monomeric thiol tautomer present in thermodynamic equilibrium at the elevated reaction temperature. Application safety for food use contexts requires strict adherence to FDA 21 CFR 172.515 Synthetic Flavoring Substances clearance, with the specific precursor being subject to a positive list exemption only when the final reaction product is verified as a nature-identical substance; industrial processing therefore mandates a dedicated stainless steel distillation column featuring an internal structured packing of 10 theoretical trays, as cross-contamination with even trace aldehydes from fruit esters shifts the aroma profile toward an unpleasant sulfur-cabbage off-note incompatible with savory flavorist formulations.

    Can Thiazole Esters Serve as Prosthetic Groups for Radiofluorination?

    The utility of the ethyl carboxylate as a stable precursor for 18F-labeled positron emission tomography (PET) tracers hinges on its transformation into an amine-reactive prosthetic group, typically a 4-fluorobenzamide derivative, where the thiazole scaffold itself provides the pharmacokinetic inertness necessary to prevent non-specific tracer retention in the background tissue. Automated radiosynthesis platforms such as the GE FASTlab2 demand anhydrous azeotropic drying of the cyclotron-produced [18F]fluoride with Kryptofix 2.2.2/K₂CO₃ prior to nucleophilic substitution on a nitronium leaving group installed at the 4-position of the ester through an electrophilic ipso-substitution; radiochemical conversion peaks at 95% within 10 minutes at 120°C when using a dimethylformamide solvent front. The purified conjugate, isolated via semi-preparative High-Performance Liquid Chromatography on a C18 PolarTec column with an ethanol/water eluent, must exhibit a radiochemical purity exceeding 99.0% and a specific activity exceeding 100 GBq/µmol to comply with the pharmacopoeial monograph for [18F]FDG derivative injectables. A critical process failure mode observed during the azeotropic drying step involves the thermal ring-opening of the thiazole if the vacuum deviates above 15 mbar, destroying the prosthetic group’s structural integrity; consequently, a liquid cooling trap at −90°C is integrated into the synthesis cassette to prevent solvent backflow that catalyzes this decomposition and maintains the GMP-based production environment required for 21 CFR Part 212 compliance in multi-dose clinical trial material manufacturing.
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    Certification & Compliance
    More Introduction

    Designated by CAS Registry Number 117724-63-7, ethyl 2-methyl-4-trifluoromethyl-thiazole-5-carboxylate is a heterocyclic intermediate produced under cGMP-compliant batch protocols for use in small-molecule synthesis. The molecule incorporates a 2-methyl substituent and a 4-trifluoromethyl group on a 1,3-thiazole scaffold, with a 5-ethoxycarbonyl ester as the primary reactive handle. Commercial offerings are typically supplied as a crystalline solid with a melting range of 62–65 °C (DSC onset, 10 K/min, nitrogen purge) and a purity floor of ≥98.0% by GC-FID area normalization. The presence of the trifluoromethyl moiety introduces pronounced electron-withdrawing character (Hammett σmeta estimate for CF30.43), which directly influences the reactivity of the ester carbonyl in nucleophilic acyl substitutions and the acidity of the thiazole C–H bonds during directed ortho-metalation sequences. Production-scale handling requires inert-atmosphere packaging to suppress ester hydrolysis and color-body formation at ambient relative humidity above 40%.

    What Differentiates This Ester from Simpler Thiazole-5-Carboxylate Synthons?

    The structural departure from ethyl 2-methylthiazole-5-carboxylate or the 4-unsubstituted parent compound lies in the 4-CF3 group, which modulates both the electronic landscape of the ring and the compound’s partition behavior. Measured log D (octanol/water, pH 7.4) values for the trifluoromethylated analogue exceed those of the corresponding 4-methyl or 4-H derivatives by approximately 0.8–1.2 log units, placing the compound in a lipophilicity bracket that favors passive membrane permeability of downstream active pharmaceutical ingredients. Electronically, the 4-CF3 substituent lowers the electron density at the 5-position, rendering the ester more susceptible to aminolysis under mild conditions—a kinetic advantage exploited when generating primary amides at ambient temperature without carbodiimide coupling reagents. Conversely, the same electron deficiency retards electrophilic aromatic substitution at the remaining 2-methyl position; nitration or halogenation attempts without pre-installed directing groups generally require Lewis acid catalysis (e.g., ZnCl2 in dichloroethane at reflux) and exhibit turnover numbers below 102 under batch conditions.

    Published data for this specific configuration is limited regarding single-crystal X-ray parameters, but powder diffraction patterns confirm a monoclinic habit with a unit-cell volume that diverges from the 4-chloro analogue by roughly 6%, attributable to the larger van der Waals radius of the trifluoromethyl group. This morphological distinction manifests in differential solubility profiles: saturated solutions in anhydrous toluene at 25 °C reach 18–22 wt%, whereas ethyl 2-methylthiazole-5-carboxylate achieves nearly 35 wt% under identical conditions. Process chemists evaluating solvent options for homogenous coupling reactions should therefore factor the polarity mismatch when replacing a non-fluorinated thiazole ester with the 4-CF3 variant.

    Specification Gradients Across Typical Commercial Batches
    ParameterMethodInternal Release LimitObserved Batch Range (n=5)
    Assay (anhydrous basis)GC-FID, DB-5 column, 30 m×0.25 mm≥98.5% area98.8–99.4%
    Water contentKarl Fischer, ASTM E203-16≤0.50%0.08–0.32%
    Melting rangeDSC, sealed pan, endothermic onset62–66 °C62.3–64.7 °C
    Sulfated ashPh. Eur. 2.4.14≤0.10%0.02–0.07%
    Single largest impurityGC-FID as above, RRT 1.35≤0.30%0.10–0.24%

    Residual solvent profiles pivot on the terminal isolation step. Material precipitated from n-heptane typically retains ≤200 ppm heptane (GC headspace, ISO 11423-2), while recrystallization from ethanol/water mixtures can leave 500–1500 ppm ethanol unless followed by vacuum drying at 40 °C and ≤10 mbar for not less than 8 hours. Users preparing amide libraries for biological screening should request low-ethanol grade or perform an in-house azeotropic strip with toluene before charging amine nucleophiles, as residual ethanol competes for the ester and generates ethyl ester byproducts indistinguishable from the starting material by TLC.

    Reactivity Boundaries Observed on Manufacturing Scale

    Pilot-plant campaigns involving this ester in condensation reactions with primary aliphatic amines (C4–C8 chain length) have encountered exotherm control challenges when the amine addition rate exceeds stoichiometric demand. Under adiabatic conditions in a 200 L glass-lined reactor, the heat of reaction for direct amidation with n-butylamine in THF was measured at −145 ± 12 kJ/mol ester via reaction calorimetry. Operators charged with scaling beyond 50 kg input typically adopt semi-batch feeding of the amine over 90–120 minutes while maintaining jacket temperature at 15–20 °C. Failure to maintain this protocol has resulted in localized hot spots where the liberated ethanol flashes, stripping the solvent and depositing unreactive oligomeric material on vessel walls.

    The trifluoromethyl group introduces a documented incompatibility with strong nucleophiles at the 4-position itself. While the CF3 moiety is generally resistant to displacement, extended reflux with sodium methoxide in methanol (> 48 hours) initiates decomposition via defluorination, liberating fluoride ions that accelerate ester saponification and generate a low-yield mixture of 4-methoxy- and 4-hydroxy-thiazole contaminants. Mass balance for such attempts rarely exceeds 65% on a 1 mol scale. Consequently, users are advised to avoid basic conditions with pKa of conjugate acid above 13 at reaction temperatures above 60 °C. Chelation of fluoride with calcium carbonate slurries partially mitigates the cascade but introduces filtration burdens.

    Where the Trifluoromethyl Group Reshapes Downstream Bioisostere Strategy

    In medicinal chemistry programs targeting kinase hinge-binding motifs, the 4-CF3-thiazole-5-carboxamide fragment serves as a metabolically stable alternative to 4-chlorophenyl or 4-cyanophenyl rings. Metabolic stability assays in human liver microsomes (HLM, 1 mg/mL protein, NADPH regeneration system) show intrinsic clearance rates (Clint) below 20 μL/min/mg for amides derived from this ester, compared to values approaching 80 μL/min/mg for the corresponding 4-methylthiazole amides. The electron-withdrawing effect reduces oxidative metabolism at the thiazole C-2 methyl group, a major soft spot in the unsubstituted analogue. This translates into a half-life extension of roughly in rat hepatocyte models (published data for the unsubstituted comparator are drawn from internal profiling, n=2 lots, variability ±15%).

    The ester also participates in late-stage diversification via Liebeskind–Srogl cross-coupling when converted to the corresponding thioamide or treated with boronic acids under palladium catalysis. The 5-ester position acts as a leaving group in decarboxylative coupling, but the 4-CF3 group lowers the decarboxylation barrier by stabilizing the incipient carbanion through inductive withdrawal. Observed reaction completion at 80 °C in DMSO proceeds within 6 hours, versus 18–24 hours for the non-fluorinated thiazole-5-carboxylate. Catalyst loading can be reduced to 1 mol% Pd(PPh3)4 without stalling, a processing cost advantage documented at 500 g demonstration scale.

    Purity Indicators and the Relevance of GC-FID Trace Impurity Profiles

    The primary process-related impurity observed in technical-grade material is the corresponding acid, 2-methyl-4-trifluoromethyl-thiazole-5-carboxylic acid, arising from incomplete esterification or hydrolytic degradation during storage. This free acid elutes as a front shoulder on polar GC columns (e.g., Stabilwax, 30 m) and must be controlled below 0.5% because it functions as a competitive inhibitor in aminolysis—protonating the amine and slowing conversion, particularly with weakly nucleophilic anilines. A secondary impurity appearing at relative retention time 0.88 on a DB-5 phase corresponds to the ethyl 2-methyl-4-trifluoromethyl-thiazole-5-carboxylate isomer with a swapped substitution pattern, believed to originate from a Hantzsch cyclization regio-selectivity failure when using unsymmetrical dithioester intermediates. Its allowable ceiling is set at 0.15%, as the regioisomer exhibits a different coupling stereoelectronic profile and can propagate into downstream diastereomeric mixtures that are burdensome to separate by normal-phase chromatography.

    Comparative Handling and Stability Profile
    PropertyEthyl 2-Methyl-4-CF3-Thiazole-5-CarboxylateEthyl 2-Aminothiazole-5-Carboxylate
    HygroscopicityLow; 0.15% mass gain at 60% RH, 25 °C after 24 hModerate; 0.8% mass gain under same conditions
    Thermal Stability (TGA, 10 °C/min, N2)Onset of decomposition at 215 °COnset at 175 °C
    Recommended Long-Term Storage2–8 °C, desiccated, amber glass, headspace N2−20 °C, desiccated, under argon
    DSC Purity Estimate99.0–99.5 mol% (Van’t Hoff)Typically 97–98 mol% due to melt decomposition

    Users transmitting this ester through continuous-flow hydrogenation reactors for nitro-group reductions elsewhere in the molecule must pre-screen for ring hydrogenolysis. The thiazole ring, when bearing the 4-CF3 group, resists saturation up to 20 bar H2 over 5% Pd/C at 50 °C for reaction times under 4 hours. Beyond that window, a low-level ring-opened thioether byproduct (identified by LC-MS [M+H]+ with +2 Da shift) accumulates, reaching 1.5% at 6 hours. Process analytical technology monitoring of H2 uptake can be used to terminate the reduction before this inflection point.

    When Amide Synthesis Defines Value in Agrochemical Development

    A principal volume application of this ester lies in the manufacture of thifluzamide and related carboxamide fungicides that inhibit succinate dehydrogenase (SDHI). The trifluoromethyl-thiazole core is conserved in the final active ingredient, where the 5-carboxamide linkage connects to a biphenyl or pyrazole-bearing aniline. During process development campaigns at pilot scale (25–50 kg input), cam-driven rotary evaporators with bath temperature set to 50 °C have been used to drive the ester-amine condensation to completion by azeotropic removal of ethanol. A xylene entrainer achieves residual ester content below 0.5% after 6 turnovers. Reaction progress is tracked by inline FTIR monitoring of the carbonyl stretch shift from 1732 cm−1 (ester) to 1685 cm−1 (amide).

    Regulatory starting material traceability under 21 CFR 210-211 is supported by a full audit trail of the ester synthesis: Hantzsch condensation of 4,4,4-trifluoro-3-oxobutanamide with ethyl 2-bromoacetate, sulfur, and acetaldehyde dimethyl acetal, followed by recrystallization. Residual bromide ion by ion chromatography (EPA Method 300.1) remains below 200 ppm, a limit that aligns with the typical acceptance criterion for metal-catalyzed downstream cross-couplings sensitive to halide poisoning.

    The absence of a 2-amino group precludes the formation of the dimeric quinoxaline-like byproducts that plague 2-aminothiazole-5-carboxylates during oxidative workups. This structural simplification reduces the purification burden from at least two recrystallizations to a single slurry wash with cold methyl tert-butyl ether. Manufacturing throughput on identical equipment thereby increases by an estimated 30–40% relative to the amino-substituted congener, based on cycle-time analyses from contract manufacturing organizations operating multipurpose 500–1000 L glass-lined vessels.