|
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 | 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. |
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 ChlorideThe 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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| Parameter | Method | Limit |
|---|---|---|
| Assay (as anhydrous) | HPLC‑UV, 254 nm | ≥98.0 area‑% |
| Water | Karl Fischer, ASTM E203‑16 | ≤0.05 % |
| Residual Ethanol | HS‑GC‑FID, USP⟨467⟩ | ≤0.10 % |
| Chloride (ionic) | Ion chromatography, EPA 300.1 | ≤50 ppm |
| Heavy metals (Pb, Cd, Hg, As) | ICH Q3D Option 1 | ≤10 ppm each |
| Refractive index (nD20) | Abbé refractometer | 1.4765–1.4785 |
| Density (20 °C) | Oscillating U‑tube, DIN 51757 | 1.358–1.368 g cm⁻³ |