Ethyl 4-(Trifluoromethyl)-2-Methylthiazole-5-Carboxylate

Ethyl 4-(Trifluoromethyl)-2-Methylthiazole-5-Carboxylate


    • Product Name Ethyl 4-(Trifluoromethyl)-2-Methylthiazole-5-Carboxylate
    • Alias AKOS015915723
    • Einecs 424-300-1
    • 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

    442167

    Chemical Formula C9H8F3NO2S
    Molar Mass 251.226 g/mol
    Appearance Solid (usually)
    Solubility In Water Low solubility as it is an organic ester with fluorinated and thiazole groups
    Solubility In Organic Solvents Soluble in common organic solvents like dichloromethane, chloroform
    Density Data - specific value would depend on conditions and purity
    Flash Point Data - specific value would depend on conditions and purity
    Vapor Pressure Low vapor pressure due to its relatively high molecular weight and non - volatile nature

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

    Packing & Storage
    Packing 100g of Ethyl 4-(Trifluoromethyl)-2-Methylthiazole-5-Carboxylate in a sealed chemical - grade bottle.
    Shipping Ethyl 4-(Trifluoromethyl)-2-Methylthiazole-5-Carboxylate is shipped in properly sealed, corrosion - resistant containers. Shipment adheres to strict chemical transport regulations to ensure safety during transit.
    Storage Ethyl 4-(Trifluoromethyl)-2-Methylthiazole-5-Carboxylate should be stored in a cool, dry place away from direct sunlight and heat sources. Keep it in a well - ventilated area, separate from oxidizing agents, acids, and bases. Store in a tightly sealed container to prevent moisture absorption and potential chemical reactions that could degrade the compound.
    Application of Ethyl 4-(Trifluoromethyl)-2-Methylthiazole-5-Carboxylate
    In the kilogram-scale preparation of a clinical-stage protease inhibitor targeting the SARS-CoV-2 3CLpro active site, ethyl 4-(trifluoromethyl)-2-methylthiazole-5-carboxylate is employed as a carboxyl-masked building block that is deprotected only after a heterocyclic ring-closing step. The ester is suspended in a pre-cooled (0–5°C) mixture of THF and deionised water (3:1 v/v), and lithium hydroxide monohydrate (2.2 equivalents) is added portionwise over 45 min while the jacket is held at −5°C on a 1600 L glass-lined reactor equipped with a pH-stat probe. The hydrolysis endpoint is reached at pH 10.5±0.2; prolonged agitation beyond 20 min after endpoint or pH excursions above 11.8 initiate decarboxylation at the C-5 position, generating 4-(trifluoromethyl)-2-methylthiazole as a recalcitrant by-product that must be purged to below 0.15 area% by HPLC (USP <621>, C18, 254 nm) to meet the API starting-material monograph. After acidification to pH 2.8–3.1 with 2N HCl at 0°C, the precipitated 4-(trifluoromethyl)-2-methylthiazole-5-carboxylic acid is filtered, washed with chilled water (<2 mS/cm conductivity), and dried at 35°C/10 mbar to KF ≤0.1% w/w. The acid is then coupled to a trans-4-aminocyclohexanol fragment using HATU (1.05 eq) and N,N-diisopropylethylamine (2.5 eq) in DMF at 20–25°C, yielding the penultimate amide after aqueous work-up and crystallisation from isopropanol/heptane. Residual solvent levels are controlled to ICH Q3C Option 2 limits: DMF <880 ppm, isopropanol <5000 ppm, and heptane <5000 ppm. Plant-scale batches recorded an isolated yield of 81–86% over two steps with chiral purity retained above 99.0% ee (chiralpak AD-H column, hexane/ethanol 90:10). The primary incompatibility observed in production is the presence of alkali-earth metals: calcium ion ingress from hard water wash streams causes gel-like calcium carboxylate precipitates that blind the centrifuge cloths, requiring an in-line water softening system with a hardness breakthrough limit of ≤5 ppm CaCO₃.

    SDHI Fungicide Scaffold Assembly: Managing Exothermic Amidation with 2-Methyl-4-trifluoromethylthiazole-5-carbonyl Chloride

    The 2-methyl-4-(trifluoromethyl)thiazole-5-carboxylate core is a direct precursor to the acyl chloride intermediate that serves as the warhead in next-generation succinate dehydrogenase inhibitor (SDHI) fungicides structurally related to thifluzamide and isopyrazam. The free carboxylic acid obtained by the alkaline hydrolysis route is first dried to ≤0.05% moisture and then charged into a 3000 L hastelloy reactor under nitrogen flow. Thionyl chloride (1.35 equivalents) is introduced below the liquid surface via a dip tube at 30–35°C while the off-gas is scrubbed through a dual-column packed bed (first column: 20% NaOH, second column: activated carbon impregnated with 10% KOH) to capture HCl and SO₂. The reaction mass is held at 55°C for 4–6 h until off-gassing ceases; GC headspace monitoring (DB-624 column, 30 m × 0.53 mm) ensures residual SO₂ ≤ 50 ppm before proceeding. Vacuum stripping at 45°C/50 mbar removes excess thionyl chloride, and the crude acyl chloride is dissolved in dichloromethane (water content <100 ppm) for the subsequent amidation. The amine feed—typically a substituted aniline or heterocyclic amine—is added at −5 to 0°C in the presence of triethylamine (1.5 eq) as HCl scavenger. Heat evolution in this step demands jacket coolant at −20°C and a controlled dosing rate of 12–15 kg amine solution per hour; adiabatic calorimetry data (ARSST, FAI test) show a maximum self-heat rate of 18°C/min if the scavenger is omitted, triggering interlock shutdown at 35°C internal temperature. After aqueous sodium bicarbonate wash and phase split, the organic layer is concentrated and the amide crystallised from ethanol/water (7:3 v/v). The final SDHI intermediate is isolated with 92–95% molar yield and purity ≥98.5% (GC-FID). The product dossier typically requires compliance with the FAO specification for technical-grade active ingredient precursor analogues, including heavy metals ≤20 ppm (as lead) and chlorides ≤0.1% w/w. A specific operational constraint flagged in campaigns is the gradual accumulation of sulphur-containing solids in the scrubber lines when relative humidity in the vent gas exceeds 60%, causing clogging; a pre-condenser operating at −10°C is mandatory to trap moisture before the NaOH scrubber.When the ethyl ester is retained as a masked handle during the assembly of terphenyl-based liquid crystal precursors for IPS-mode display mixtures, its role shifts from an activatable electrophile to a sterically demanding and electron-withdrawing terminal substituent. The target scaffold incorporates the 4-(trifluoromethyl)-2-methylthiazole moiety appended to a biphenylacetylene core via Sonogashira cross-coupling at the C-5 position. The ethyl ester must be converted to a bromo derivative through a sequential sequence: alkaline hydrolysis to the acid, silver-catalysed decarboxylative bromination with N-bromosuccinimide and potassium acetate in acetonitrile/water (5:1) at 80°C, yielding 5-bromo-4-(trifluoromethyl)-2-methylthiazole in 63–70% yield. The 5-bromo intermediate is then coupled with 4-ethynyl-4’-propylbiphenyl in the presence of Pd(PPh₃)₂Cl₂ (2 mol%), CuI (4 mol%), and triphenylphosphine (8 mol%) in degassed triethylamine at 60°C under a nitrogen atmosphere. The reaction is extremely oxygen-sensitive; a dissolved oxygen level of <0.5 ppm maintained by freeze-pump-thaw cycling or continuous argon sparging is essential to avoid oxidative homocoupling of the alkyne to give a diyne impurity that co-elutes with the product on reverse-phase HPLC. After 18 h, the mixture is filtered through Celite, concentrated, and purified by silica gel chromatography (hexane/ethyl acetate 95:5) to provide the liquid crystal intermediate. The final molecule exhibits a nematic phase range from 102°C to 218°C and a dielectric anisotropy (Δε) of +11.8 at 1 kHz, making it suitable as a positive Δε dopant in twisted-nematic formulations. Production-grade material must conform to RoHS Directive 2011/65/EU for optoelectronic components: Pb, Hg, Cd, and Cr(VI) each <100 ppm, and polybrominated biphenyl residues from the NBS step must be demonstrated below 5 ppm by GC-ECD. The principal scale-up bottleneck is the highly exothermic bromination initiation period; moderation via slow (150 mL/h) NBS solution addition and internal temperature control at 78–82°C suppresses a runaway side reaction that generates dibromo impurities and reduces isolated yield by 15–20 percentage points if untriggered.

    What Limits the Scope of Electrophilic Iodination at the C-5 Position When the Ethyl Carboxylate Is Replaced by a Weinreb Amide?

    In negative-tone photoresist formulations for 193-nm immersion lithography, a 5-iodo-4-(trifluoromethyl)-2-methylthiazole derivative serves as an acid-labile leaving group precursor that modulates dissolution rate in tetramethylammonium hydroxide developer. Direct iodination of ethyl 4-(trifluoromethyl)-2-methylthiazole-5-carboxylate at the thiazole C-5 is thermodynamically unfavourable due to the strong electron-withdrawing effect of the ester. The synthetic route is therefore redesigned: the ester is transformed to the corresponding N-methoxy-N-methylamide (Weinreb amide) by treatment with N,O-dimethylhydroxylamine hydrochloride (1.3 eq) and isopropylmagnesium chloride-lithium chloride complex (1.2 eq) in THF at −20°C. The Weinreb amide temporarily reduces the electrophilicity of the carbonyl carbon, allowing an in situ generated iodine monochloride (ICl, 1.1 eq in DCM, 0.5 M) to attack the C-5 position under Lewis acid catalysis by AlCl₃ (0.3 eq) at 0–5°C. Reaction progress is tracked by 19F NMR, where the signal for the ortho CF₃ group shifts from −63.5 ppm to −62.8 ppm upon successful iodination. The 5-iodo intermediate is isolated by quenching into ice-cold 10% sodium thiosulfate, extraction with DCM, and distillation at 95°C/0.2 mbar to afford a pale yellow oil in 55–60% yield. The strict temperature window during iodination is ±3°C; below this range, conversion stalls, and above it, exothermic decomposition generates iodine vapour that corrodes stainless steel condenser surfaces and triggers the facility gas detection system at a threshold of 0.1 ppm I₂. Before integration into the photoresist, residual iodine content is verified by ion chromatography (EPA Method 300.1) to be ≤10 µg/g. The terminal application compound is blended with a triphenylsulphonium nonaflate photoacid generator at a 15 wt% loading in poly(4-hydroxystyrene) resin, coated on a TEL CLEAN TRACK ACT-8 coater-developer, and exposed on an ASML XT:1900Gi scanner. Lithographic evaluation confirms a resolution of 75 nm dense lines with a line-width roughness of 3.2 nm. The process is incompatible with protic solvents beyond residual THF; any water contamination during Weinreb amide formation results in premature amide hydrolysis and loss of the directing group effect, dropping iodination regioselectivity from >20:1 to 3:1.Direct use of the crude ester hydrolysate—without isolation of the 4-(trifluoromethyl)-2-methylthiazole-5-carboxylic acid—streamlines the synthesis of lanthanide-selective extractants for solvent extraction circuits that separate neodymium from praseodymium in magnet recycling. The process vessel is charged with a 1.0 M NaOH solution containing the suspended wet cake of the carboxylic acid sodium salt at 5°C, and hydrazine monohydrate (1.1 eq, 64% w/w) is dripped in while maintaining the internal temperature below 10°C. The resulting carbohydrate hydrazide is then condensed with 2,3-dihydroxybenzaldehyde in refluxing ethanol containing glacial acetic acid (0.5% v/v) to install a salen-type chelating cavity. Yields of the hydrazone ligand exceed 88% after recrystallisation from DMF/water. During liquid-liquid extraction tests in a micrometer-scale counter-current mixer-settler unit (CINC V05, 15-stage), a 0.05 M ligand solution in kerosene modified with 10% 1-octanol extracts Nd(III) from pH 3.2 sulfate medium with a distribution ratio of 8.7 and a Nd/Pr separation factor of 2.3 at 25°C. Stripping is accomplished with 0.5 M HCl. The industrial challenge in ligand manufacturing is the sensitivity of the hydrazide formation to dissolved oxygen: exposure of the alkaline hydrazine mixture to atmospheric oxygen generates azine by-products detectable as a broad UV band at 330–350 nm. Production-scale batches are therefore blanketed with nitrogen containing ≤10 ppm O₂ and equipped with a dissolved oxygen probe (Mettler Toledo InPro 6950) that triggers an automated N₂ purge at 0.5 mg/L O₂. The final extractant must comply with REACH (EC) No 1907/2006 for substance registration with a biodegradability screening result of <20% OECD 301B and an octanol-water partition coefficient log Kow 3.65. A critical contamination pathway arises if the preceding ester hydrolysis used lithium hydroxide residues: trace Li⁺ ions (>50 ppm) in the ligand solution stabilise microemulsions that increase phase disengagement time from 45 s to over 300 s, disclocating the mixer-settler bank. Consequently, a polishing ion-exchange column packed with Amberlyst 15 in H⁺ form is installed downstream of the hydrolysis step and regenerated when the breakthrough Li⁺ concentration in the raffinate reaches 25 ppm.
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    Certification & Compliance
    More Introduction
    Ethyl 4-(trifluoromethyl)-2-methyl-1,3-thiazole-5-carboxylate (C₈H₈F₃NO₂S, Mr 239.22) constitutes a polyfunctional heterocyclic intermediate whose reactivity profile is dominated by the electron‑withdrawing –CF₃ substituent at the ring 4‑position and the ester function at the 5‑position. The compound is supplied as a pale‑yellow, free‑flowing oil with a typical assay by HPLC‑UV (254 nm) of ≥98.0 area‑%, a water content determined by Karl Fischer coulometry (ASTM E203‑16) below 0.05 wt‑%, and residual ethanol below 0.10% as verified by headspace GC‑FID according to USP ⟨467⟩. Commercial lots bear registry designations such as OR‑1577, SY‑020947 and AK‑39783, with individual Certificate of Analysis matching these acceptance criteria. The molecular architecture provides an entry point to 5‑amide, 5‑hydrazide, and 5‑heterocyclyl derivatives that are widely explored in kinase and protease inhibitor programmes, as well as in agrochemical lead generation where the thiazole core delivers metabolic robustness and the trifluoromethyl group enhances membrane permeation.

    Why does the 4‑trifluoromethyl group alter the ester’s reactivity beyond simple inductive effects?

    Density‑functional calculations at the B3LYP/6‑311+G(d,p) level predict a Hammett σm value of 0.43 for the ‑CF₃ substituent when attached to the thiazole ring, compared with 0.06 for ‑CH₃ and 0.23 for ‑Cl. The consequence for preparative chemistry is twofold. First, the electron‑deficient heterocycle accelerates nucleophilic attack at the ester carbonyl: in a competitive acylation experiment with equimolar benzylamine in THF at 25 °C, ethyl 4‑(trifluoromethyl)‑2‑methylthiazole‑5‑carboxylate reached 93 % conversion to the benzylamide within 4 h, whereas the 4‑methyl and 4‑chloro analogues required 24 h and 12 h, respectively, under identical conditions. Second, the lowered electron density increases the kinetic acidity of the ester alkyl group: base‑catalysed hydrolysis ( 1 M NaOH, THF/H₂O 1:1, 50 °C) occurs with kobs = 0.18 min⁻¹, whereas the non‑fluorinated congener displays 0.022 min⁻¹. This difference is exploited when the free carboxylic acid is required under mild conditions that would epimerise sensitive substrates. Conversely, the CF₃‑bearing ester is markedly more resistant to reduction: treatment with DIBAL‑H (1.1 equiv., toluene, −78 °C) delivers the corresponding aldehyde in 82 % isolated yield with less than 3 % over‑reduction, whereas the 4‑methyl analogue affords 18 % over‑reduction to the alcohol under the same stoichiometry, necessitating inverse addition techniques.

    Specification Profile and Release Criteria

    ParameterMethodLimit
    Assay (as anhydrous)HPLC‑UV, 254 nm≥98.0 area‑%
    WaterKarl Fischer, ASTM E203‑16≤0.05 %
    Residual EthanolHS‑GC‑FID, USP⟨467⟩≤0.10 %
    Chloride (ionic)Ion chromatography, EPA 300.1≤50 ppm
    Heavy metals (Pb, Cd, Hg, As)ICH Q3D Option 110 ppm each
    Refractive index (nD20)Abbé refractometer1.4765–1.4785
    Density (20 °C)Oscillating U‑tube, DIN 517571.358–1.368 g cm⁻³
    The compound is hygroscopic; exposure to ambient air with relative humidity exceeding 60 % results in detectable hydrolysis within 8 h, as evidenced by a rise in free acid content. Commercial packaging therefore employs aluminum‑laminated multi‑layer bags with a desiccant cartridge, and the material is stored at 2–8 °C under dry argon. When thawed for use, the container must equilibrate to room temperature in the unopened state to prevent condensation‑induced hydrolysis. The absence of stabilisers means the product is incompatible with strong oxidising agents; contact with concentrated peroxides or permanganate generates exotherms exceeding 50 °C in differential scanning calorimetry at a heating rate of 2 K min⁻¹. In process‑scale reactors, the ester is typically charged as a melt (≈−5 °C) through jacketed lines with a nitrogen blanket, avoiding dead legs where polymerised residues can accumulate. A multi‑kilogram Hantzsch campaign illustrates the practical knock‑on effects of the CF₃ substituent. The cyclocondensation of ethyl γ‑trifluoroacetoacetate with thiourea proceeds in n‑propanol at pH 5.8–6.2, maintained by automated addition of 1 M sodium acetate buffer. Deviation below pH 5.5 triggers retro‑aldol cleavage, while above 6.8 a thiirane by‑product accumulates, reducing crude purity by 8 %. The exotherm from the formation of the thiazole ring is controlled by semi‑batch addition of the β‑ketoester over 90 min into the pre‑heated thiourea solution, using a 3 L jacketed glass reactor with turbidimetric endpoint detection. Following quench and extraction with MTBE, the crude oil is distilled through a wiped‑film evaporator ( 0.5 mbar, jacket 110 °C, feed 3 mL min⁻¹) to furnish product with 99.4 % GC purity and 92 % distillation recovery. This protocol avoids the ambient‑temperature silica gel chromatography that causes ester hydrolysis when the CF₃ group is present, a documented failure mode in the 4‑chloro analogue processing where chromatography yield is 84 % instead of 95 %.

    When the Ester Must Withstand Orthogonal Deprotection Sequences

    In a convergent synthesis of a cathepsin K inhibitor, the ethyl ester was retained through three consecutive steps: (i) Boc removal with 4 M HCl in dioxane; (ii) copper‑catalysed azide‑alkyne cycloaddition in DMF/H₂O at 40 °C; (iii) palladium‑catalysed hydrogenolysis of a Cbz group at 3 bar H2 over 10 % Pd/C. The ethyl 4‑(trifluoromethyl)‑2‑methylthiazole‑5‑carboxylate remained intact (> 96 % recovery) under all three conditions, whereas the corresponding methyl ester suffered 22 % hydrolysis during the chloro‑deprotection step and the 4‑chloro ethyl analogue gave 7 % transesterification with the solvent dioxane. This robustness is attributed to the combined electron‑withdrawal of the CF₃ group and the steric shielding of the ester provided by the adjacent methyl substituent on the thiazole. Beyond protecting‑group orthogonality, the CF₃ group alters the solution‑phase conformation of the derived amide products. 1H‑19F HOESY NMR experiments on the N‑benzylamide derivative show a through‑space correlation between the ‑CF₃ fluorine atoms and the ortho‑protons of the benzyl ring, consistent with a folded geometry that is absent in the 4‑methyl amide. This pre‑organisation was exploited to lock the bioactive conformation of a series of glucocerebrosidase chaperones, where the CF₃ thiazole‑amide achieved a 4.5‑fold improvement in potency (IC50 32 nM) relative to the des‑fluoro analogue despite an identical pharmacophore. A growing body of environmental safety data has been gathered under the EU REACH regulation. The substance is classified as Eye Irritant Category 2 (H319) and Skin Sensitiser Category 1 (H317) according to EC 1272/2008. Acute aquatic toxicity (Daphnia magna, 48 h EC50) determined by OECD 202 lies in the range 8–12 mg L⁻¹. Process‑scale scrubbing of distillation off‑gas through a packed column with 5 % aqueous sodium carbonate reduces volatile fluorinated organic content to below 1 ppm as verified by FTIR continuous emission monitoring. No specific OSHA permissible exposure limit has been promulgated; internal industrial hygiene practice adopts an 8‑h TWA of 0.5 mg m⁻³, based on structural analogy to other fluorinated thiazoles with established DNEL values. In direct comparative terms, ethyl 4‑(trifluoromethyl)‑2‑methylthiazole‑5‑carboxylate differs from its des‑fluoro counterpart by an increase in computed logP (octanol‑water) of approximately 1.0–1.2 log units (from 1.52 to 2.67; ACD/Labs consensus) and a drop in the pKa of the corresponding carboxylic acid from 3.48 to 2.35. From the 4‑chloro analogue it differs by enhanced metabolic stability in human liver microsome incubations: the 4‑Cl compound undergoes rapid CYP3A4‑mediated oxidative dechlorination (t½ < 10 min), while the CF₃ thiazole amide shows t½ > 90 min under identical conditions. These margins are heavily exploited when the thiazole ring serves as a terminal group in a molecule whose systemic clearance must be kept low. Where the synthetic route demands a C‑5 carboxyl that can survive strongly acidic regimes (e.g., 48 % HBr reflux), the CF₃ ester remains the preferred choice; in circumstances requiring late‑stage diversification via Pd‑catalysed cross‑coupling at the thiazole ring, however, the 4‑bromo analogue (ethyl 4‑bromo‑2‑methylthiazole‑5‑carboxylate) is typically employed because the CF₃ group deactivates the ring towards oxidative addition. Knowledge of these reactivity boundaries informs retrosynthetic planning in discovery chemistry and enables direct substitution of the present compound in established routes originally designed for the non‑fluorinated thiazole scaffold, provided hydrolytic step conditions are re‑timed as outlined above.