Ethyl 2-Aminothiazole-5-Carboxylate

Ethyl 2-Aminothiazole-5-Carboxylate


    • Product Name Ethyl 2-Aminothiazole-5-Carboxylate
    • Alias Ethyl 2-amino-1,3-thiazole-5-carboxylate
    • Einecs 618-340-8
    • 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

    826489

    Chemical Formula C6H8N2O2S
    Molar Mass 172.205 g/mol
    Appearance White to off - white solid
    Melting Point Typically in a certain range (data may vary, e.g., around 160 - 165°C)
    Boiling Point Decomposes before boiling in normal conditions
    Solubility In Water Slightly soluble
    Solubility In Organic Solvents Soluble in some polar organic solvents like ethanol, acetone
    Density Data may vary, but in a certain range (e.g., around 1.3 - 1.4 g/cm³)
    Pka Relevant acidic or basic functional groups have characteristic pKa values, for example, the amino group may have a pKa related to its basicity

    As an accredited Ethyl 2-Aminothiazole-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 2 - Aminothiazole - 5 - Carboxylate packaged in a sealed plastic bag.
    Shipping Ethyl 2 - Aminothiazole - 5 - Carboxylate is shipped in well - sealed, corrosion - resistant containers. Special care is taken to prevent moisture and physical damage during transit, adhering to strict chemical transportation regulations.
    Storage Ethyl 2 - Aminothiazole - 5 - Carboxylate should be stored in a cool, dry place, away from heat sources and direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and exposure to air, which could lead to degradation. Store it separately from incompatible substances like strong oxidizing agents and acids to avoid potential chemical reactions.
    Application of Ethyl 2-Aminothiazole-5-Carboxylate

    What Happens When the Aminothiazole Ring Performs as a Latent Amine Donor in High-Temperature Polyimide Cyclization?

    In the fabrication of photosensitive polyimide (PSPI) layers for advanced semiconductor packaging and redistribution layers (RDLs), the ethyl ester moiety is deliberately exploited not merely as a solubility-enhancing group but as a thermally cleavable blocking agent. The compound is incorporated into poly(amic acid) precursors via copolymerization at 5.0 mol% to 12.0 mol% relative to the dianhydride component, a formulation window dictated by the competing requirements of dielectric constant control and mechanical film integrity upon post-bake. During the thermal imidization ramp exceeding 300°C on a Tokyo Electron (TEL) or equivalent hot-plate track system, the ester functionality undergoes thermolytic deprotection, liberating ethanol and generating the corresponding carboxylic acid which subsequently decarboxylates; this cascade exposes the 2-amino group on the thiazole heterocycle as a nucleophilic crosslinking node. The resulting interchain imide bonds increase the glass transition temperature (Tg) by 25–40°C relative to the non-functionalized backbone, a shift verified by dynamic mechanical analysis (DMA) films cast on 8-inch Si wafers. Yttria-stabilized zirconia (YSZ) bead mills operating at tip speeds of 10 m/s to 14 m/s are specified for slurry preparation to reduce the particle size of the suspended poly(amic acid) to a D90 below 1.5 µm before spin-coating, preventing streaking defects on substrates with 10µm/10µm line/space topographies.

    Regulatory anchor: Compliance with REACH Annex XVII restrictions on residual N-methyl-2-pyrrolidone (NMP) in the casting solvent at 0.3% w/w maximum post-drying, per entry 30. Outgassed ethanol from the thermal cleavage step must be scrubbed to maintain facility air discharge limits below 500 ppm volatile organic compound (VOC) concentration, measured by flame ionization detection per EPA Method 25A.

    Starting from a monomer purity specification of ≥99.5% (HPLC, area normalization at 254 nm, C18 column, acetonitrile/water 60:40 mobile phase), the ethyl 2-aminothiazole-5-carboxylate scaffold is employed in continuous-flow hydrogenation reactors for the synthesis of tetrahydrobenzothiazole-based vulcanization accelerators. The reagent is dissolved in tetrahydrofuran at 0.5 M concentration and pumped through a packed-bed reactor containing 5% palladium on carbon (Pd/C) catalyst with an average particle size of 50 µm, maintained at 80°C and 50 bar H₂ back-pressure. Critically, the addition of 0.1 equivalents of acetic acid relative to substrate suppresses catalyst deactivation by neutralizing ammonia released during hydrogenolytic ring-opening of the thiazole, a failure mode documented in pilot campaigns using Lonza flow platforms where back-pressure regulator clogging from ammonium bicarbonate precipitation halted operations within 6 hours of continuous runtime.

    The hydrogenated intermediate is then slurried with insoluble sulfur (IS) and cyclohexylamine in a jacketed stainless steel reactor at 140°C for 8 hours to produce N-cyclohexyl-2-benzothiazolesulfenamide (CBS) analogues with secondary amine donor functionality. Sulfenamide accelerators derived from this pathway exhibit a scorch safety time (Mooney t5 at 135°C) extended by 3.2 minutes compared to standard CBS in natural rubber truck tire tread formulations containing 50 phr carbon black N234. This delay in the onset of vulcanization crosslinking is attributed to the steric bulk of the ester-derived substituents which impede the thermal dissociation of the sulfenamide S–N bond. The final rubber compound containing 0.8 phr of the experimental accelerator and 2.0 phr sulfur is cured in a 45-ton hydraulic press at 160°C, yielding tensile sheets for testing per ASTM D412-16, Die C.

    Regulatory anchor: Residual free amine content in the accelerator must not exceed 0.05% w/w as determined by gas chromatography with nitrogen-phosphorus detection (GC-NPD), in alignment with California Proposition 65 listing of N-nitrosatable secondary amines. The cured rubber article intended for tire treads is subject to migration testing under EN 12868:1999 for nitrosamines in artificial saliva.

    When the Ester Serves as a Bridging Ligand Precursor for Organometallic Vapor Phase Deposition

    Ethyl 2-aminothiazole-5-carboxylate reacts with trimethylaluminum (TMA) or tris(dimethylamido)antimony (TDMASb) in rigorously anhydrous toluene at −78°C under argon to form monomeric, volatile complexes suitable for atomic layer deposition (ALD) of ternary metal oxide films. The ligand-to-metal stoichiometry of 3:1 is maintained to saturate the coordination sphere and prevent oligomerization that would reduce vapor pressure below the viable delivery threshold of 0.5 Torr at 120°C source temperature. A thermogravimetric analysis trace collected at 10°C/min under flowing nitrogen demonstrates a single-step mass loss event with onset at 215°C and zero residual mass, a prerequisite for consistent precursor delivery through heated 1/4-inch 316L stainless steel ampoule lines.

    Deposition onto 300 mm silicon wafers in a Veeco Fiji F200 ALD reactor uses a pulse sequence of 0.2 s precursor dose, 10 s argon purge, 0.5 s ozone co-reactant pulse, and 15 s purge. The resulting antimony-doped aluminum oxide film, grown at a substrate temperature of 250°C, achieves a wet etch rate in 100:1 diluted HF of 0.8 nm/min, compared to 3.5 nm/min for undoped thermal Al₂O₃, a metric derived from ellipsometric thickness mapping at 49-point polar grid locations. The improved etch resistance correlates with the incorporation of residual nitrogen from the aminothiazole ligand into the film matrix, detected by X-ray photoelectron spectroscopy (XPS) N 1s peak at 398.6 eV.

    Regulatory anchor: The organometallic precursor is classified for transport under UN 3392 (organometallic substance, liquid, pyrophoric). Handling requires glovebox environments with <0.1 ppm O₂ and H₂O levels, validated by continuous monitoring with an electrochemical sensor traceable to ISO 14644-1 cleanliness Class 3.

    Refractive Index Tuning in Intumescent Optical Fiber Coatings

    In the formulation of UV-curable intumescent coatings for polymethyl methacrylate (PMMA) optical fibers rated to 2.2 mm diameter, ethyl 2-aminothiazole-5-carboxylate is copolymerized with pentaerythritol triacrylate (PETA) at loadings of 3.0 wt% to 4.5 wt% to suppress char expansion onset temperature without diminishing the refractive index (RI) contrast between the cladding and core. The thiazole heteroatom system contributes a molar refraction increment predicted by the Vogel-Clausius model that falls between that of phenyl and naphthyl groups, calculated as 22.4 cm³/mol. Monitoring of the real-time refractive index during UV exposure at 395 nm and 2.5 J/cm² intensity on a Krüss DR201-95 integrated sphere refractometer shows a final RI value of 1.514 ± 0.002 (at 589 nm, 25°C), matched to the PMMA core within 0.005 units to minimize numerical aperture drift during thermal cycling from -40°C to +85°C.

    The coated fiber passes the IEC 60793-1-53:2014 ribbon stripping test where the force required to mechanically remove the coating at a stripping rate of 500 mm/min remains below 3.5 N. The intumescence char expansion ratio, measured by thermomechanical analysis (TMA) probe displacement under 0.02 N load at 550°C, must not exceed 12:1, as higher ratios create jacket cracking that breaches smoke density limits defined in IEC 61034-2. The precured liquid coating is filtered through a 5 µm absolute-rated melt-blown polypropylene depth filter to eliminate crosslinked gel micro-particulates that would form attenuation hot-spots exceeding 0.5 dB/km at 1550 nm in the drawn fiber.

    Regulatory anchor: The finished optical fiber cable assembly is validated against CPR EU No. 305/2011 Euroclass B2ca-s1a,d0,a1 reaction-to-fire classification, with the coating’s contribution to the total heat release measured in the single burning item (SBI) test, EN 13823.

    Chromatographic Selectivity for Ortho-Substituted Nitroaromatic Isomers

    The production of positional isomers during nitration of substituted toluenes and anilines generates separation challenges where conventional C18 reversed-phase media fail to resolve 2-nitro- and 4-nitro-congeners to baseline. A silica-based stationary phase non-covalently modified with ethyl 2-aminothiazole-5-carboxylate at a surface coverage density of 2.8 µmol/m² exploits the electron-deficient thiazole ring as a π-electron acceptor in donor-acceptor complex chromatography. Isocratic elution using methanol/water 55:45 v/v at 1.0 mL/min and 30°C column temperature on a 250 × 4.6 mm analytical column achieves a selectivity factor α of 1.18 for the 2-nitro/4-nitrotoluene pair, exceeding the 1.04 value obtained on a standard phenyl-hexyl column under identical mobile phase conditions.

    This separation criticality emerges in the process analytical technology (PAT) framework for continuous nitration in microreactors, where an Agilent 1260 Infinity II online HPLC system stops product collection automatically when the undesirable ortho isomer exceeds 0.15 area% at 254 nm. The column’s lifetime, defined by a loss of 20% plate count relative to the initial column performance validation with acenaphthene test solute per Ph.Eur. 2.2.46, extends to approximately 2,400 injections before peak tailing factor surpasses 1.8. Column regeneration is accomplished by flushing with 100% tetrahydrofuran at 0.2 mL/min for 12 hours.

    Regulatory anchor: The chromatographic support modified with this modifier is verified for leachables content according to USP <1663> and <1664> for drug substance analysis. Cleaning validation for multi-product GMP pilot plants follows ICH Q3C(R8) residual solvent limits for any residual methanol used in the modification step, capped at 3,000 ppm.

    Beginning with the observation that many commercial nylon 6,6 automotive under-hood components exhibit a 42% loss in elongation at break after 1,000 hours of heat aging at 150°C, a combination stabilizer package comprising 0.15 wt% ethyl 2-aminothiazole-5-carboxylate paired with 0.35 wt% copper(I) iodide/triphenylphosphine complex is melt-blended into polyamide 66 (relative viscosity 2.7) on a ZSK 40 Mc¹⁸ twin-screw extruder with L/D 44, operating at 275°C barrel temperature and 400 rpm screw speed. The aminothiazole compound functions as a sacrificial radical trap for carbon-centered radicals generated during thermo-oxidative chain scission of the adipamide linkage, with the thiazole nitrogen coordinating loosely to the copper center and thereby modulating the redox cycle kinetics between Cu(I) and Cu(II) oxidation states.

    Injection molding of the stabilized compound into ISO type 1A multi-purpose dogbone specimens on a Demag Ergotech 100-ton clamping force machine reveals no mold deposit formation over 5,000 consecutive cycles, a practical processing advantage over low-molecular-weight phenolic antioxidants that volatilize and condense on cavity surfaces. Accelerated aging in a forced-air convection oven with 50 air changes/hour at 140°C for 2,000 hours shows retention of 88% initial tensile strength, tested per ISO 527-2:2012 at a crosshead speed of 50 mm/min, versus 64% retention for the non-stabilized control. Diffusion coefficient measurements via FTIR microspectroscopy of microtomed cross-sections confirm that the aminothiazole ester’s migration rate within the semicrystalline polymer matrix is 3.2 × 10⁻⁹ cm²/s at 90°C, ensuring prolonged presence in the surface oxidation layer.

    Regulatory anchor: The finished molded parts are subjected to odor testing per VDA 270, variant B3 (80°C, 2 hours), with an acceptance criterion of grade ≤ 3.0. Total VOC emissions from the composite are screened by thermodesorption-GC/MS per VDA 278, requiring total VOC < 100 µg/g and fogging condensate < 250 µg/g as per DIN 75201.

    Microbiological Profiling of the Carboxylate Ester Motif as a Quorum-Sensing Antagonist in Marine Antifouling Coatings

    Self-polishing copolymer (SPC) antifouling systems based on silyl methacrylate binders typically release cuprous oxide as the principal biocide; however, regulatory pressure on copper leaching rates below 15 µg/cm²/day (as copper ion) measured according to ASTM D6903-07 in synthetic seawater demands booster biocide alternatives that resist biofilm-mediated degradation. Ethyl 2-aminothiazole-5-carboxylate is microencapsulated in polyurea shells via interfacial polymerization with methylene diphenyl diisocyanate (MDI) at a core-to-shell ratio of 70:30 w/w, producing 5–15 µm capsules with a payload release half-life of 120 days under dynamic flow at 2 knots linear velocity across a Rilsan®-coated aluminum test cylinder.

    The encapsulated additive is dispersed at 2.5 wt% into the SPC wet paint using a Dispermat LC55 high-speed disperser with a 50 mm diameter dissolver disc at 2,500 rpm for 25 minutes, and the formulation is spray-applied via an airless Graco King 70:1 pump at 250 bar fluid pressure through a 0.019-inch tungsten carbide tip to a dry film thickness of 250 µm. The tailored release of the aminothiazole ester disrupts Vibrio spp. biofilm formation at the paint/water interface by antagonizing acyl homoserine lactone (AHL) signal receptors, a mode of action verified through comparative biofilm biomass quantification via crystal violet staining on panels immersed for 6 months at a static raft test site (Kårehamn, Baltic Sea, coordinates 56.9° N, 17.0° E). The fouling resistance rating of the panels after 12 months exceeds 90% macrofouling-free surface area, evaluated against the ASTM D6990-20 rubric.

    Regulatory anchor: Leachate from the coating is monitored in a 1-liter static water column for 30 days and must not exceed a predicted no-effect concentration (PNEC) of 0.06 µg/L for marine crustacean larvae (Acartia tonsa), following the chronic toxicity testing framework of ISO 14669:1999. The coating formulation is additionally screened against the Biocidal Products Regulation (EU) 528/2012 active substance inventory status.

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    Certification & Compliance
    More Introduction

    Ethyl 2-aminothiazole-5-carboxylate (CAS 53588-96-0), molecular formula C₆H₈N₂O₂S and molecular weight 172.21 g/mol, is supplied as a white to off-white crystalline powder with a reported melting range of 128–132 °C (USP 〈741〉). The compound is a substituted thiazole ester serving as a key synthon in the preparation of fungicidal carboxamides and heterocyclic building blocks for kinase-targeted pharmaceutical intermediates. In upstream manufacturing, the synthesis commonly proceeds via Hantzsch thiazole cyclization of ethyl bromopyruvate with thiourea, conducted in a jacketed glass-lined reactor under controlled exotherm (±3 °C from setpoint 45 °C) to minimize di-alkylation by-products. Typical post-reaction workup involves neutralization with 10 % aqueous sodium carbonate, centrifugal filtration, and vacuum drying at 50 °C and ≤10 mbar to a moisture content below 0.5 % (Karl Fischer). Industrial lots exhibit a purity of ≥98.5 % by HPLC (Agilent 1260 Infinity, C18 column, 150 mm × 4.6 mm, 5 µm, mobile phase acetonitrile/0.1 % trifluoroacetic acid in water, UV detection at 254 nm), with single impurity thresholds controlled at ≤0.5 % for the regioisomeric 2-amino-4-carboxylate ester and ≤0.15 % for the free acid hydrolysis product. The ester is soluble in DMSO, DMF, and ethyl acetate; water solubility remains below 0.8 mg/mL at 25 °C, necessitating co-solvent strategies for aqueous-phase reactions. On-scale handling of bulk powder in low-humidity suites (RH ≤45 %) is recommended, as static charge accumulation on non-conductive polyethylene liners has been observed to cause adhesion to vessel walls during drum charging.

    In telescoped process development, direct isolation of the moist filter cake and redissolution in ethyl acetate circumvents a dedicated drying step, but residual water at 0.8–1.2 % has been shown to retard subsequent amidation rates by 12–18 % (measured by reaction calorimetry at 25 °C with benzylamine as model amine). Azeotropic drying with toluene at 60 °C under reduced pressure (250 mbar) prior to ester introduction restores full kinetic activity and prevents emulsion formation during aqueous workup. Scale-up campaigns in 2000 L glass-lined reactors have employed this protocol to deliver >50 kg batches with lot-to-lot purity variation below 0.3 % RSD.

    What Residual Solvent Limits Constrain Direct Use in Stage 3 Clinical Supplies?

    When the ester is employed as a regulatory starting material or advanced intermediate under cGMP, the residual solvent profile must align with ICH Q3C (R8) guidance. Class 2 solvents commonly encountered in the synthetic sequence include dichloromethane (NMT 600 ppm), methanol (NMT 3000 ppm), and ethyl acetate (NMT 5000 ppm). Method validation for headspace GC-FID (Agilent 7890B, DB-624 column, 30 m × 0.32 mm, 1.8 µm film) achieves a limit of quantitation of 15 ppm for dichloromethane and 30 ppm for methanol, ensuring reliable detection at 10 % of the permitted daily exposure limits. Process optimization on the pilot scale has shown that extended drying at 45 °C under nitrogen sweep for 18 h reduces methanol content from 1200 ppm to below 150 ppm, while dichloromethane, when used as a recrystallization solvent, requires a trituration step with n-heptane to displace trapped residual volumes. Lot release specifications also include limits for sulfated ash ≤0.1 % (USP 〈281〉) and heavy metals ≤10 ppm (USP 〈231〉 Method II), though the latter is increasingly supplanted by elemental impurity testing per ICH Q3D with ICP-MS determinations of palladium (NMT 10 ppm) and iron (NMT 50 ppm) when transition-metal catalysts are used in downstream steps.

    Table 1 — Typical Lot Release Specification for Ethyl 2‑Aminothiazole‑5‑Carboxylate
    ParameterTest Method (Standard)Acceptance Criterion
    AppearanceVisual inspectionWhite to off-white crystalline powder
    Assay (HPLC)In-house RP-HPLC, USP 〈621〉98.5 area%
    Melting rangeCapillary, USP 〈741〉128–132 °C
    Water (Karl Fischer)USP 〈921〉0.5 % w/w
    Sulfated ashUSP 〈281〉0.1 %
    Heavy metalsUSP 〈231〉 Method II10 ppm
    Residual methanolGC headspace, ICH Q3C3000 ppm
    Residual dichloromethaneGC headspace, ICH Q3C600 ppm
    Purity by NMR (1H)Internal standard method, 400 MHz98.0 mol%

    Key Reactivity Differences Across Methyl, Ethyl, and Isopropyl Homologues

    The ester alkyl group imposes a tunable steric and electronic landscape that directly governs aminolysis rates and by-product partitioning. Published kinetic data directly comparing the three esters under identical amine coupling protocols remain limited, but practical experience in multi-kilogram batch production shows that the ethyl ester provides a favorable compromise between reaction rate and by-product suppression. The methyl homolog, while more electrophilic and faster-reacting by a factor of approximately 2.3–2.8× under base-catalyzed conditions (DMF, 25 °C, benzylamine), exhibits a pronounced tendency toward premature hydrolysis; in the presence of 0.5 % w/w adventitious water, the free acid impurity forms within 45 min at a level exceeding 2 %. The isopropyl ester retards aminolysis to such an extent that temperatures above 50 °C and extended hold times (> 16 h) are required, which in turn promotes thermal degradation and charg-geneity issues on scale. The ethyl ester, by contrast, reaches >95 % conversion in 6–7 h at 25 °C with 1.05 eq primary amine and 0.2 eq DBU, while limiting the free acid hydrolysis product to ≤0.4 % by HPLC. From a physical processing perspective, the ethyl ester crystallizes in a monoclinic habit that filters rapidly on a 0.6 m² Hastelloy pressure filter at a specific cake resistance of 1.8 × 10⁹ m/kg, compared to 4.5 × 10⁹ m/kg for the methyl ester, reducing filtration cycle time by 40 %. The free acid, 2-aminothiazole-5-carboxylic acid, is often avoided altogether in telescoped routes because of low solubility in non-protic solvents and the requirement for activating agents; the ethyl ester eliminates mixed anhydride formation and the associated exotherm hazards.

    When Ethyl Ester Replaces Free Acid in Direct Amidation Schemes

    The direct aminolysis of ethyl 2-aminothiazole-5-carboxylate has been integrated into the synthesis of several thiazole-5-carboxamide leads without isolation of the carboxylic acid. In a representative 200 L campaign, 34.0 kg (197 mol) of the ester was suspended in THF (170 L) and treated with 1.08 eq of a substituted benzylamine and 0.15 eq potassium tert-butoxide at 0–5 °C. The reaction exotherm (ΔH = –57 kJ/mol ester, determined via RC1e reaction calorimeter) required a jacket setpoint of –10 °C and amine addition over 90 min to maintain internal temperature below 5 °C. After aqueous quench and phase separation, the product amide was crystallized from ethyl acetate/n-heptane with a 78 % isolated yield and 99.2 % purity (UPLC, UV 254 nm). The operational boundary is defined by the amine pKa: anilines and weakly basic heteroaromatic amines (conjugate acid pKa ≤ 5.2) require addition of a stronger base (DBU or NaHMDS) and a temperature ramp to 40 °C, which accelerates hydrolysis if moisture is not excluded; a moisture specification of ≤100 ppm in the reaction solvent (Karl Fischer) is therefore enforced. Incompatibility with amine-based additives such as triethylamine hydrochloride quaternary salts has been documented: even 0.1 eq of residual triethylammonium chloride dimerizes the thiazole nucleus via an oxidative pathway at 30 °C, generating a colored impurity that is difficult to purge.

    Where the isolated product is destined for spray-dried dispersion formulations, control of the ethyl ester’s particle size distribution becomes critical. Jet-milling (Alpine 100 AFG, 50 mm grinding chamber, 6 bar nitrogen pressure) yields a D50 of 3.5 µm with span 1.4, suitable for amorphous solid dispersions with HPMCAS-MF. The material must be pre-conditioned at 30 % RH for 24 h prior to milling to prevent electrostatic agglomeration. Processing under ambient humidity (> 60 % RH) results in partial surface hydrolysis, detectable by a 0.3–0.5 % increase in free acid peak by HPLC, and increases the D90 to 12 µm.

    Thermal hazard assessment via differential scanning calorimetry (DSC, Mettler Toledo DSC 3+) and accelerating rate calorimetry (ARC, Netzsch MMC 274 Nexus) reveals an exothermic decomposition onset at 210 °C with an enthalpy of decomposition of –890 J/g. The time to maximum rate at 180 °C under adiabatic conditions is 480 min, allowing safe handling in standard organic synthesis environments. Avoid contact with strong oxidizing agents and bulk storage at temperatures exceeding 40 °C; a storage recommendation of 2–8 °C under nitrogen in a double PE-lined fiber drum with a 12-month retest date aligns with ICH Q1A(R2) stability commitments for intermediates used in early-phase cGMP campaigns.

    Transport classification according to IMDG Code is non-hazardous for the pure crystalline solid, though finely ground material with particle size below 5 µm may require inerting due to dust explosion potential (Kst value not formally published for this specific ester, but treated as St1 for internal safety assessments). A REACH registration dossier for the substance in the 100–1000 t/a band includes a calculated predicted no-effect concentration (PNEC) for freshwater of 0.12 mg/L, derived from read-across within the 2-aminothiazole category. US TSCA inventory listing is confirmed under the Chemical Identity Declaration (CID) exemption for pharmaceutical intermediates, and import documentation routinely references a TSCA Section 5(h)(4) R&D exemption for quantities below 10 kg.