|
HS Code |
765622 |
| Chemical Formula | C7H9NO2S |
| Molecular Weight | 171.22 |
As an accredited 2-Thiazolecarboxylicacid, 4-Methyl-, Ethyl Ester factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100 - gram bottles containing 4 - Methyl - 2 - Thiazolecarboxylic acid ethyl ester. |
| Shipping | 2 - Thiazolecarboxylic acid, 4 - Methyl -, Ethyl Ester is shipped in well - sealed containers, following strict chemical transport regulations. Special care is taken to prevent leakage and ensure safe transit due to its chemical nature. |
| Storage | Store 4 - Methyl - 2 - thiazolecarboxylic acid ethyl ester in a cool, dry place away from heat and ignition sources. Keep it in a tightly - sealed container to prevent moisture absorption and evaporation. Since it's a chemical, store it separately from incompatible substances like strong oxidizers and bases to avoid potential reactions. |
What Drives Des‑methyl Impurity Formation During Curtius‑Based Meloxicam Precursor Synthesis?Production‑scale conversion of ethyl 4‑methylthiazole‑2‑carboxylate into the 2‑Boc‑amino‑4‑methylthiazole intermediate for meloxicam (CAS 71125‑38‑7) proceeds through alkaline ester hydrolysis followed by diphenylphosphoryl azide (DPPA)‑mediated Curtius rearrangement. The hydrolysis step is conducted in a 3000 L glass‑lined reactor (Pfaudler‑type, glass thickness 2.0–2.5 mm) using LiOH·H₂O at 1.08–1.12 eq relative to the ester, maintained at 0–5 °C with jacket temperature setpoint −5 °C to absorb an exotherm of 38 kJ/mol. Water content in the isolated acid must not exceed 0.15 % w/w by Karl Fischer (USP 〈921〉 Method Ia); residual moisture above 0.3 % shifts the subsequent Curtius reaction toward symmetrical urea by‑product, increasing the des‑methyl impurity to >2.0 area‑% as tracked by UPLC at 254 nm. After vacuum drying at 45 °C for 16 h, the dried acid is suspended in anhydrous tert‑butanol and charged with DPPA (1.03–1.07 eq) and triethylamine (1.15–1.20 eq). The reaction mass is heated at a controlled ramp of 0.5 °C/min to 80 ± 1 °C; failure to maintain this ramp—observed when a 4‑stage cascade temperature controller with an accuracy of ±0.3 °C was replaced by a basic PID loop—led to instantaneous nitrogen evolution spikes that triggered pressure alarms on the 250 m³/h vent scrubber. Inline FTIR monitoring targets the azide stretch at 2140 ± 5 cm⁻¹ and the isocyanate intermediate at 2270 cm⁻¹, with the reaction deemed complete when azide absorbance remains below 0.002 AU for three consecutive 2‑min acquisitions. The Boc‑amine is crystallised from n‑heptane/EtOAc, achieving an HPLC purity of ≥99.7 area‑% under ICH Q3C (R6) residual solvent limits for tert‑butanol (5000 ppm) and dichloromethane (600 ppm). Equipment compliance follows 21 CFR Part 211.65 (equipment design) and ICH Q7 Section 5.3 (cleaning validation), with O‑ring elastomers specified as EPDM peroxide‑cured to withstand the tert‑butanol permeation rate of 0.8 g·mm/m²·d at 80 °C. The final low‑bioburden Boc‑amine is the direct precursor to meloxicam API meeting USP 2024 monograph criteria. Coupling of an activated C‑3‑formylcephem nucleus with a phosphorane derived from ethyl 4‑methylthiazole‑2‑carboxylate provides a trans‑alkene C‑7 side chain in a developmental carbacephem agent currently undergoing PIC/S GMP Annex 2 pilot manufacture. The ester is first reduced to the aldehyde using two‑step DIBAL‑H protocol (1.03 eq at −78 °C in THF, quenched by Rochelle’s salt) because direct aldehyde generation from the acid chloride gave ≥12 % over‑reduction to the alcohol in 3 kg demonstration batches. The resulting 4‑methylthiazole‑2‑carboxaldehyde is immediately treated with (carbethoxyethylidene)triphenylphosphorane (1.15 eq) in dichloromethane at 10 °C in a 1600 L stainless‑steel 316L vessel with an anchor agitator speed of 65 rpm. A design‑of‑experiment study across 27 runs identified an optimal aldehyde‑to‑ylide ratio of 1:1.12 and a post‑reaction aqueous wash pH of 5.8‑6.2 to suppress cis‑isomer formation below 0.8 area‑% in the final DMT‑MM‑mediated amidation with a 7‑ACP nucleus. Compliance with ICH Q7 Sections 7.3 (sampling) and 8.5 (packaging) is maintained; in‑process TLC (silica gel 60 F₂₅₄, EtOAc/n‑hexane 3:7) is cross‑validated against an HPLC method using a C18 column, 1.7 µm particles, acetonitrile/pH 3.4 phosphate buffer 55:45 at 0.35 mL/min, with limit of quantitation for the cis isomer at 0.04 %. In one production incident, a 12‑h hold of the phosphorane solution at 25 °C due to a downstream filter changeout resulted in Wittig reagent hydrolysis and a 37 % drop in yield; standard operating procedure now mandates a solution age not exceeding 4 h and offline ³¹P NMR verification of ylide integrity. The finished drug substance complies with ICH Q3A (R2) unspecified impurity threshold of ≤0.10 %, and the thiazole‑containing intermediate itself is classed as a non‑genotoxic impurity (AMES negative at 5000 µg/plate). Acaricide and Oomycete Fungicide Intermediate Processing PathwaysEthyl 4‑methylthiazole‑2‑carboxylate is the preferred entry point to 2‑chloro‑4‑methylthiazole, the core electrophile in tolfenpyrad (CAS 129558‑76‑5) and the fungicide ethaboxam (CAS 162650‑77‑3) syntheses. The ester is first saponified with aqueous NaOH (2.5 eq, 30 % w/w) in a 5000 L Hastelloy C‑276 reactor at 60 °C over 1.5 h; after cooling to 15 °C, phosphoric acid is added to pH 3.2 to precipitate the free acid. The wet cake—dried to moisture <0.5 % in an agitated vacuum dryer at 55 °C, 20 mbar—is suspended in toluene and treated with SOCl₂ (1.45 eq) and DMF (0.5 mol %) at 50 °C, affording the acid chloride after 4 h and subsequent distillation at 102–104 °C/15 mbar. Direct chlorination of the acid chloride with PCl₅ (1.05 eq) in POCl₃ at 110 °C yields 2‑chloro‑4‑methylthiazole in 88–92 % yield, which is then phase‑transfer‑coupled to 4‑(chloromethyl)phenyl 4‑methylbenzenesulfonate under TBAB catalysis to produce the key benzyl ether. For tolfenpyrad, the downstream sequence involves a 2,4‑disubstituted phenol etherification followed by pyrazole‑5‑carboxamide formation; the finished product is standardised to 98.0 % minimum purity per FAO Specification 760/TC (2020) and CIPAC Method 760/TC/M/‑ (HPLC at 230 nm). The bulk manufacturing site operates under an EPA Establishment Number and must comply with 40 CFR Part 158.400, with hydrolytic stability validated by OECD 501 (DT₅₀ at pH 7, 25 °C → ≤14 d). A routinely observed process failure involves N‑oxide formation during chlorination when residual ethanol from the ester stage is not reduced below 200 ppm; this is mitigated by adding a 0.5 h toluene strip cycle monitored by headspace GC‑FID. Waste streams are quenched into 20 % w/w NaOH, and the sodium sulfite/thiosulfate mixture is segregated as EPA Hazardous Waste Code D003.
Reaction calorimetry data from 200 L pilot batches confirm that LiAlH₄‑mediated reduction of ethyl 4‑methylthiazole‑2‑carboxylate to 4‑methylthiazole‑2‑methanol (FEMA 3205) is safe only when the ester solution in anhydrous diethyl ether is added to a pre‑formed slurry of LiAlH₄ (1.18‑1.22 eq) at −12 to −8 °C, ensuring the instantaneous heat release does not exceed 85 W/kg. The adiabatic temperature rise for the full charge is 49 °C; therefore jacket supply temperature is interlocked to a −25 °C chiller setpoint with a safety valve opening at reactor pressure 0.5 bar g. After 2.0 h aging, a Fieser quench (1 mL water, 1 mL 15 % NaOH, 3 mL water per gram of LiAlH₄) converts aluminium salts into a filterable granular precipitate, which is removed on a 0.5 m² Hastelloy plate filter. The alcohol is purified by fractional distillation under 8 mbar; the cut at 108‑110 °C yields a colourless liquid with organoleptic profile matching the JECFA monograph: meaty, pot‑roasted, slightly earthy. The finished product is standardised to ≥99.0 % by GC and is registered under EU Regulation EC 1334/2008 Article 9 for use in processed flavourings at a typical dosage of 0.15–2.50 ppm in final foodstuffs. A 2023 recall incident traced to 0.7 ppb dibenzofuran contamination was linked to insufficient removal of BHT‑stabiliser from the commercial ether solvent; subsequent batches were switched to BHT‑free ether and passed a LC‑MS/MS screen with a limit of detection of 0.05 ppb. Compliance with 21 CFR 172.515 allows use in non‑alcoholic beverages at concentrations up to 1.0 ppm. The product leaflet also cites ISO 9231:2008 (transfer procedures for flavourings) and is qualified as Halal per HAS 23000 and Kosher per OU guidelines.
When an Epoxy‑Phenol Novolac Underfill Requires a Humidity‑Insensitive Latent Imidazole‑Type HardenerEncapsulation of ethyl 4‑methylthiazole‑2‑carboxylate within a polyurea shell (average particle size D₅₀ = 1.8 µm, span 1.1) creates a room‑temperature latent accelerator for DGEBA‑based underfill adhesives used in flip‑chip packaging. The microcapsules—prepared via interfacial polycondensation of polymethylene polyphenyl isocyanate (PAPI‑27) with diethylenetriamine at a core‑to‑wall ratio of 85:15—are dispersed into a bisphenol‑F/epoxy phenol novolac matrix at 3.0 phr alongside a bisphenol‑A dicyandiamide hardener at 8.0 phr. Differential scanning calorimetry (DSC) per ASTM D2471‑21 shows an onset temperature of 142 °C and a peak exotherm at 168 °C, with a total reaction enthalpy of 310 J/g (resin‑hardener basis) when tested in a hermetically sealed pan at 10 K/min. The advantage over conventional 2‑ethyl‑4‑methylimidazole (2E4MZ) is a 3.5‑fold extension of pot life at 25 °C/60 % RH: viscosity reaches 800 Pa·s after 26 h compared with 7.5 h for the unencapsulated control, measured by ARES‑G2 parallel‑plate rheometer at 10 s⁻¹. During transfer molding at 175 °C and 8 MPa, the ester‑based capsules release the free thiazole upon shell rupture, and the ethyl ester subsequently transesterifies with epoxy‑hydroxyl species, initiating a low‑shrinkage (0.9 % by TMA) cure profile. Adhesion to silicon die passivation (PI/SiN stack) measured by die shear (MIL‑STD‑883 TM 2019.9) exceeds 12.0 kgf after moisture sensitivity level‑3 preconditioning (30 °C/60 % RH, 192 h+3× reflow at 260 °C). REACH (EC) No 1907/2006 and RoHS Directive 2011/65/EU Annex II exemption 7(c)‑I apply; the microcapsules are analysed for restricted phthalates per IEC 62321‑8:2017 (GC‑MS, m/z 149), and the ethoxy homolog of the thiazole ester is flagged as non‑SVHC under Article 57. A production‑scale batch‑to‑batch variation in capsule burst strength (±1.8 MPa) was traced to stirrer speed fluctuations ±25 rpm in the 120 L IKA reactor; closed‑loop PID control with a 0.1 s scan cycle narrowed the distribution to ±0.4 MPa, confirmed by a texture analyser fitted with a 50 µm probe. |
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| Parameter | Specification | Method |
|---|---|---|
| Assay (as ethyl 4‑methylthiazole‑2‑carboxylate) | ≥ 98.5 % (area‑%, GC) | In‑house GC‑FID, 30 m × 0.25 mm DB‑WAX, 10 °C min⁻¹ ramp |
| Refractive index, n²⁰D | 1.5140–1.5160 | ASTM D1218 |
| Density, 25 °C | 1.18 g mL⁻¹ | ASTM D4052 |
| Boiling range (8 mmHg) | 110–112 °C | Vacuum distillation, ASTM D86 modified |
| Water content | ≤ 0.2 % | Karl Fischer, ASTM E203 |
| Flash point (closed cup) | 102 °C | ASTM D93 |
| Appearance | Clear, pale‑yellow liquid, free of visible particulates | Visual inspection under 6500 K illumination |
| Thiazole analog | FEMA№ | CAS | Odor descriptor | Threshold (water, ppb) | Typical application level (ppm) |
|---|---|---|---|---|---|
| Ethyl 4‑methylthiazole‑2‑carboxylate | 3204 | 67815‑57‑0 | Nutty, roasted, slight meaty | 0.02 | 0.05–0.5 |
| Ethyl 2‑methylthiazole‑4‑carboxylate | 3205 | 21890‑09‑2 | Nutty, cocoa, earthy | ~1.5 | 0.5–2.0 |
| 2‑Acetylthiazole | 3328 | 24295‑03‑2 | Popcorn, toasted grain, slight sulfur | 0.05 | 0.1–0.5 |
| 2‑Ethyl‑4‑methylthiazole | 3671 | 15679‑13‑7 | Green, nutty, vegetable | 0.02 | 0.05–0.3 |
| Ethyl thiazole‑2‑carboxylate | 3203 | 3998‑78‑7 | Fruity, green, slight sulfury | 0.15 | 0.2–1.0 |