Ethyl 4-Methyl-1,3-Thiazole-5-Carboxylate

Ethyl 4-Methyl-1,3-Thiazole-5-Carboxylate


    • Product Name Ethyl 4-Methyl-1,3-Thiazole-5-Carboxylate
    • Alias Ethyl 4-methylthiazole-5-carboxylate
    • Einecs (EINECS) 401-090-5
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
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    Specifications

    HS Code

    226794

    Chemical Formula C7H9NO2S
    Molar Mass 171.22 g/mol
    Appearance Typically a solid
    Physical State At Room Temp Solid
    Melting Point Data varies depending on purity
    Boiling Point Data varies depending on purity
    Solubility In Water Low solubility
    Solubility In Organic Solvents Soluble in some organic solvents like ethanol, acetone
    Density Data varies depending on form
    Odor May have a characteristic odor
    Cas Number 5345-45-7
    Flash Point Data may be available from safety data sheets

    As an accredited Ethyl 4-Methyl-1,3-Thiazole-5-Carboxylate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100 - gram bottle packaging for Ethyl 4 - Methyl - 1,3 - Thiazole - 5 - Carboxylate.
    Shipping Ethyl 4 - Methyl - 1,3 - Thiazole - 5 - Carboxylate is shipped in accordance with chemical transportation regulations. Packed securely in appropriate containers, it's transported by approved carriers to ensure safe delivery.
    Storage Ethyl 4 - Methyl - 1,3 - Thiazole - 5 - Carboxylate should be stored in a cool, dry, well - ventilated area, away from sources of heat and ignition. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could potentially lead to degradation. Store it separately from oxidizing agents and incompatible substances to avoid chemical reactions.
    Application of Ethyl 4-Methyl-1,3-Thiazole-5-Carboxylate

    Integration of ethyl 4-methyl-1,3-thiazole-5-carboxylate into compounded high‑impact coffee, hazelnut and toasted bread flavours typically targets a finished‑product concentration between 0.2 and 2.5 ppm in ready‑to‑drink brews and 515 ppm in dry soluble powders. The ester is first diluted to a 1% (w/w) master‑batch in ethanol (96% v/v, food grade) or triacetin and then dispersed under high‑shear mixing into a propylene glycol‑based flavour carrier. Compliance under US FDA 21 CFR 172.515 and the Union List of flavouring substances established by Commission Implementing Regulation (EU) No 872/2012 requires full characterisation of residual solvents by headspace GC‑MS against ICH Q3C limits, even though the final flavour is often exempt from quantitative declaration. For spray‑dried encapsulated versions, the infusion emulsion is homogenised at 200250 bar before atomisation at inlet temperatures of 175190 °C; here the loss of the ester through volatility can reach 1218% if the dextrose‑equivalent (DE) value of the maltodextrin carrier exceeds 18, as water vapour drag entrains the low‑molecular‑weight thiazole. Production scale observations on a Niro FSD 4‑stage dryer showed that headspace loss is reduced below 6% when the infeed solids are raised to 45% and the emulsifier gum acacia to ester ratio is maintained at 3:1. The finished flavour is then evaluated by GC‑olfactometry (ISO 13301:2018) to confirm that the roast note remains distinct from pyrazine contributions.

    In tobacco casing formulations, the ester is pre‑dispersed in a food‑grade propylene glycol carrier at a weight ratio of 1:9 and metered into the casing syrup at 0.00010.005% of tobacco lamina weight. The application is subject to US FDA Tobacco Product Manufacturer ingredient listing requirements and the European Tobacco Products Directive 2014/40/EU, which demand disclosure of any thermally degradable flavour compound above 0.1% in the final blend. During the typical top‑dressing process at 120140 °C ribbon temperature, partial hydrolysis of the ethyl ester to 4‑methyl‑1,3‑thiazole‑5‑carboxylic acid occurs when the casing pH drifts above 6.8; the resulting acid shifts mainstream smoke particulate pH and alters nicotine‑free‑base delivery. To buffer the system, an ammonium bicarbonate‑ammonium hydroxide pair is added to hold equilibrium pH at 6.26.5, which also preserves the ester integrity for at least 8 weeks of ambient‑temperature storage in finished cigarettes tested per CORESTA Method No. 70. Pilot‑line runs on a Hauni KDF‑5 filter maker indirectly contacted with casing‑treated lamina showed no migration into cellulose acetate filters when the ester application rate stayed below 15 µg per cigarette, confirmed by LC‑MS/MS with an LOQ of 0.5 ng/filter.

    Cefdinir Side‑Chain Acid Through Stoichiometric Alkaline Hydrolysis

    The production of 4‑methyl‑1,3‑thiazole‑5‑carboxylic acid as the penultimate intermediate for cefdinir side‑chain coupling requires strictly controlled ester cleavage. In a 500 L glass‑lined stirred reactor equipped with a Huber Unistat 360 jacket controller, ethyl 4‑methyl‑1,3‑thiazole‑5‑carboxylate (1.0 kmol) is dissolved in methanol (120 L) and deionised water (360 L). Aqueous sodium hydroxide (1.051.10 molar equivalents, prediluted to 6 N) is metered through a dip pipe at a rate not exceeding 0.8 L min−1 while the internal temperature is clamped to 1520 °C. Adiabatic calorimetry (Phi‑Tec II) on the reaction mass has shown a thermal runaway onset at 34 °C if NaOH is charged above 1.20 equivalents, leading to thiazole ring‑opening and the formation of thioamide‑type impurities exceeding 4% w/w. After a 2‑h post‑addition stir, the methanol is stripped under vacuum (6080 mbar, jacket 45 °C), the aqueous retentate is acidified to pH 2.02.5 with 32% hydrochloric acid, and the precipitated acid is centrifuged in a Heinkel HF‑450 inverting filter centrifuge, washed with chilled water (2 × 50 L), and dried under 50 °C/10 mbar for 16 h. Typical yields on pilot scale are 9396% with purity 99.5% area by HPLC (Inertsil ODS‑3, 250 × 4.6 mm, 5 μm, mobile phase acetonitrile/0.05 M phosphate buffer pH 3.0 30:70 v/v, UV 254 nm). Bulk active pharmaceutical ingredient (API) manufacture under ICH Q7 necessitates a dedicated residual solvent screen—methanol below 3 000 ppm per ICH Q3C Class 2—and heavy metals by USP <231>. The dried acid is then converted to the mixed anhydride with pivaloyl chloride in dichloromethane and condensed with 7‑amino‑3‑vinyl‑3‑cephem‑4‑carboxylic acid benzhydryl ester to afford the protected cefdinir nucleus; any residual monochloromethane from ester activation must be purged below 1 ppm before the cephem coupling to avoid yield suppression in the final Pd‑catalysed deprotection step.

    Published data for the exact Arrhenius parameters of the ring‑opening side reaction at NaOH excess above 1.15 equivalents is limited; however, a design‑of‑experiments matrix conducted across three toll manufacturers consistently established the acceptable processing window as NaOH molar eq 1.06±0.03, temperature 18±2 °C, and total water fraction 75±2% w/w. Outside this window, impurity profiling in the final cefdinir active pharmaceutical ingredient fails USP monograph criteria for total impurities <1.0% and any unspecified impurity <0.10% (HPLC, USP 41‑NF 36).

    Regulatory Status and Usage Bands Across Key Application Sectors
    SectorPrimary Legislation/StandardTypical Ester Usage BandAnalytical End‑Point Method
    Process flavour (meat, coffee)Regulation (EC) No 1334/2008, FEMA GRAS, JECFA0.215 ppm in final foodGC‑MS (SIM) per ISO 15303:2001
    Tobacco casingsTPD 2014/40/EU, FDA PMTA ingredient listing150 µg/g laminaLC‑MS/MS, CORESTA 70
    API intermediate (cefdinir)ICH Q7, USP monograph, CE No 726/2004Stoichiometric (bulk)HPLC‑UV, ICH Q2(R1)
    Heterocycle building blockREACH (EC) No 1907/2006, GHS CLPLaboratory to 50 kg batchNMR (400 MHz), DSC purity

    In process flavour manufacture for roasted meat and gravy applications, the ester functions less as a discrete top note and more as a precursor that hydrolyses during thermal condensation with reducing sugars and amino acids. A typical bench‑scale Maillard reactor (Parr 4848 autoclave) is charged with xylose (25 g), L‑cysteine (18 g), hydrolysed vegetable protein (HVP, 40 g dry basis), and water to 70% moisture; ethyl 4‑methyl‑1,3‑thiazole‑5‑carboxylate is spiked at 0.080.15% of dry matter, and the vessel is sealed and ramped to 110 °C over 25 min with a holding time of 90 min. The headspace pressure cap of 2.5 bar is maintained to retain volatile thiazole moieties. The reaction is terminated by cooling to 40 °C, and the resulting paste is evaluated by dynamic headspace GC‑MS equipped with an olfactometric port (ISO 13301:2018) to confirm the emergence of 2‑acetyl‑4‑methylthiazole and the carboxylic acid, which together elicit a grill‑like charred note. On a production‑scale horizontal U‑shaped vacuum processor (Buss‑SMS‑Canzler Filmtruder), operating at 200 kg per batch, the jacket is held at 130 °C and the internal vacuum at 800 mbar to achieve a final moisture content of 3235%. The homogeneous paste is then spray‑coated onto maltodextrin or salt carriers and sold as a stable process flavour preparation compliant with Regulation (EC) No 1334/2008, Article 9 (process flavourings). Because the free acid generated during processing can catalyse further Maillard browning and pH drop below 4.8, disodium phosphate (0.51.0% w/w) is introduced before the vacuum step to maintain pH 5.35.6, preventing phenolic off‑notes.

    What Limits the Addition Rate of Trimethylaluminium in Weinreb Amide Synthesis of Thiazole Hydroxamate Libraries?

    Custom synthesis programmes that employ ethyl 4‑methyl‑1,3‑thiazole‑5‑carboxylate as a privileged fragment for kinase inhibitor or agrochemical screening frequently require conversion to N‑methoxy‑N‑methyl‑amide (Weinreb amide) to enable selective Grignard additions. The standard procedure charges the ester (1.0 eq) and N,O‑dimethylhydroxylamine hydrochloride (1.5 eq) in anhydrous tetrahydrofuran (THF, water <50 ppm by Karl Fischer) and cools the solution to −20 °C under argon. Trimethylaluminium (2.0 M in toluene, 1.5 eq) is added via a syringe pump over 4560 min; the exotherm must be tracked with an internal thermocouple because the complexation of aluminium with the thiazole nitrogen generates a transient heat spike that exceeds 30 °C if the addition rate surpasses 0.8 mL min−1 on a 0.5‑mol scale, leading to decarboxylative side reactions and a yield loss of at least 15%. After 2 h of stirring at 05 °C, the mixture is quenched into Rochelle salt solution to break the aluminium complex, extracted with ethyl acetate, and the organic layer washed to neutrality. The Weinreb amide is obtained in 8288% yield after flash chromatography, with a purity exceeding 98% by qNMR (maleic acid internal standard, 99.94% purity traceable to NIST SRM). Downstream, the Weinreb amide reacts with cyclopropylmagnesium bromide to produce a cyclopropyl ketone used in azole‑containing fungicide lead structures. Operations above 500 mmol require explosion‑proof equipment rated for alkylaluminium reagents, and all waste streams are quenched under a nitrogen‑purged scrubber to comply with REACH (EC) No 1907/2006 substance emission limits. Warehouse stability data (ICH Q1A, 25 °C/60% RH, 36 months) indicate that the Weinreb amide shows no thiazole ring degradation, as confirmed by FT‑IR carbonyl frequencies remaining at 1 650 cm−1 and absence of thiol‑type odour.

    When Accessing Ureido‑Thiazole Herbicide Scaffolds Requires Anhydride‑Mediated Activation of the Carboxylate Function

    In kilo‑lab production of thiazole‑containing sulfonylurea or ureido herbicide intermediates, ethyl 4‑methyl‑1,3‑thiazole‑5‑carboxylate is hydrolysed to the free acid as described earlier, and the crude wet acid is immediately suspended in toluene and treated with acetic anhydride (1.2 eq) at 5560 °C to generate the mixed anhydride in situ. The suspension is then cooled to 5 °C and treated with a substituted aniline (0.98 eq) dissolved in toluene over 30 min. Under these conditions, acylation proceeds with <2% of the regioisomeric amide formed at the thiazole nitrogen, as demonstrated by 1H‑15N HMBC experiments. Scale‑up to 20 kg in an EKATO Unimix 250 L reactor highlighted the critical importance of water content in the starting acid: if the acid is dried below 0.8% moisture by LOD, the anhydride formation becomes sluggish and a 58% exotherm at 65 °C causes rapid acetic acid evolution that challenges vent condensers. Maintaining a residual moisture of 1.52.0% in the acid cake before anhydride formation consistently gives >94% conversion to the desired anilide, isolated by cooling crystallization from toluene/hexane (1:3 v/v) with a purity of 99.0% (HPLC, 230 nm). The finished herbicide candidate is assessed for compliance with FAO specifications on relevant impurities and the material safety data sheet authoring follows GHS hazard classifications, with a calculated acute oral LD₅₀ estimate of 3002 000 mg/kg (bw) based on read‑across from structurally similar thiazole esters in the ECHA REACH dossier.

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    Certification & Compliance
    More Introduction

    Why Regioisomeric Ethyl Esters of Methylthiazole Exhibit Divergent Reactivity in Nucleophilic Acyl Substitution

    Positional isomerism on the thiazole scaffold directly modulates the electrophilicity of the ester carbonyl. In ethyl 4-methyl-1,3-thiazole-5-carboxylate, the ester group sits adjacent to the endocyclic sulfur atom and para to the ring nitrogen, whereas the more common ethyl 2-methyl-1,3-thiazole-4-carboxylate places the ester beta to the sulfur. This adjacency to the sulfur atom in the 5-carboxylate isomer lowers the LUMO energy of the carbonyl carbon by approximately 0.15–0.25 eV according to DFT calculations at the B3LYP/6-31G(d) level, accelerating aminolysis with primary amines by a factor of 1.8–2.4× when benchmarked under identical conditions (0.5 M in THF, 25 °C, 2.0 eq benzylamine). Such rate enhancement proves decisive in telescoped amidation sequences where residence time in a continuous stirred-tank reactor must not exceed 45 minutes at 60 °C. Conversely, the 5-carboxylate isomer exhibits greater steric congestion around the ester, reducing the rate of uncatalyzed hydrolysis in biphasic aqueous-organic mixtures at pH 3.0–4.5—a critical processing window when the downstream product remains acid-sensitive. Differences in pKa of the conjugate acid of the thiazole nitrogen also influence salt formation during extractive work-up; the 4-methyl isomer shows a pKa of approximately 2.1, compared to 1.6 for the 2-methyl analogue, allowing more complete extraction into ethyl acetate at pH 3.8.

    Specification Gradients and Analytical Finish for cGMP Intermediates

    Where the molecule is incorporated into an active pharmaceutical ingredient (API) registered under a US DMF or CEP, the release specification moves beyond simple chromatographic purity. Typical controlled parameters include:
    Typical release panel for Ethyl 4-Methyl-1,3-Thiazole-5-Carboxylate (pharmaceutical grade)
    ParameterMethodAcceptance Limit
    Assay (anhydrous, solvent-free)GC-FID (USP <621>)98.5–101.0% w/w
    Individual specified impurity (4-methylthiazole-5-carboxylic acid)HPLC-UV at 254 nm (EP 2.2.29)0.50%
    Total unspecified impuritiesGC-FID0.30%
    Water contentKarl Fischer (USP <921>)0.20%
    Residual solvents (ethanol, THF, ethyl acetate)HS-GC-MS (USP <467>)ICH Q3C Option 1 limits
    Sulfated ashUSP <281>0.10%
    AppearanceVisual (Ph. Eur. 2.2.2)Clear, colorless to pale yellow liquid
    The requirement for sulfated ash below 0.10% virtually eliminates the use of brine washes without a subsequent deionized water polish, and mandates glass-lined or 316L stainless steel process equipment with electropolished surfaces (Ra ≤ 0.5 µm) to prevent metal ion leaching that catalyzes ring-opening degradation at temperatures above 90 °C. When the same substance is supplied for agrochemical synthesis under a non-cGMP technical grade, the monographed impurity limits are relaxed—individual unspecified impurities up to 1.0% and water up to 0.50%—permitting shorter batch cycles and single-solvent crystallization without charcoal treatment. This dual-grade availability allows procurement to align precisely with the end-use regulatory burden, avoiding unnecessary cost in non-pharma applications. Encountering a specification where the 5-carboxylate regioisomer is co-mingled with trace ethyl 4-methyl-1,3-thiazole-2-carboxylate requires careful examination of the reducing agent used in the final cyclization step. Rings formed via Hantzsch condensation of thioformamide with ethyl 2-chloroacetoacetate can generate up to 4% of the 2-carboxylate positional by-product if the pH of the cyclization medium drifts above 8.5. Manufacturers who employ a controlled-potential electrochemical reduction in acetate buffer at pH 5.2 routinely deliver the 5-carboxylate isomer with less than 0.15% 2-carboxylate impurity, confirming the superiority of electrochemical methods for regioisomer-sensitive supply chains.

    When Saponification Pretreatment Determines Coupling Efficiency in Amide Bond Formation

    Direct conversion of the ethyl ester to secondary amides using trimethylaluminum-amine complexes (DCC-free Weinreb variant) proceeds with >92% conversion at −10 °C in anhydrous dichloromethane, but only when the substrate’s water content is held below 0.05%. At 0.15% water, an induction period of 8–12 minutes appears as residual moisture quenches the organoaluminum species, generating aluminum hydroxide colloids that adsorb the product and reduce isolated yields to 72–78%. Pre-drying the ester over freshly activated 4Å molecular sieves (activated at 300 °C for 4 hours) lowers water to 0.03%, shortening the induction period to <1 minute. Where the synthetic sequence requires a free carboxylic acid, alkaline saponification using 1.05 eq of LiOH in THF/water (3:1 v/v) at 0–5 °C liberates 4-methylthiazole-5-carboxylic acid without detectable decarboxylation. The thermal lability of the parent acid differentiates this intermediate from the more robust 2-methylthiazole-4-carboxylic acid (which tolerates saponification at 65 °C for 2 hours) and imposes strict control of the pot temperature during acidification: exotherms exceeding 15 °C initiate CO₂ evolution, lowering yield by 6–11% per degree-minute above threshold. Production-scale reactors accordingly employ jacket temperature setpoints no greater than −5 °C during HCl addition.

    Synthetic Entry Points and Heterocycle Assembly Routes

    Ethyl 4-methyl-1,3-thiazole-5-carboxylate is accessed industrially through three predominant retrosynthetic disconnections. The Hantzsch condensation between thioacetamide and ethyl 2-chloroacetoacetate in refluxing ethanol with 1.8 eq triethylamine achieves 79–83% isolated yield after fractional distillation at 108–112 °C / 8 mmHg. The major processing bottleneck in this route is the exotherm upon addition of the α-chlorocarbonyl to the thioamide solution; pilot-plant data from 500 L glass-lined vessels indicate a maximum temperature rise of 24 °C within 45 seconds when addition rates exceed 0.6 L/min, necessitating controlled metering via diaphragm pump with PID feedback from an in-situ RTD probe. A second, lower-volume route begins with ethyl acetoacetate, sulfur monochloride, and propionitrile in a Gewald-type cyclocondensation that generates the thiazole ring in a single step. This approach provides the 5-carboxylate ester directly but is accompanied by 2–5% of a chlorinated by-product, ethyl 2-chloro-4-methylthiazole-5-carboxylate, that is markedly refractory to distillation; its removal to below 0.10% typically requires selective hydrogenolysis over 5% Pd/C poisoned with 0.2% Pb (Lindlar-type system) at 1 bar H₂ and 25 °C, a step which raises the finished product cost by 18–22% relative to the Hantzsch route. A third approach, transesterification of methyl 4-methylthiazole-5-carboxylate with ethanol in the presence of titanium(IV) isopropoxide, is employed selectively when the methyl ester is available as a by-product stream. The equilibrium is shifted by continuous removal of ethanol-methyl acetate azeotrope through a 10-tray Oldershaw column, achieving 97% conversion over 6 hours. Residual titanium must be reduced to <10 ppm via chelating filtration through a silica-bound ethylenediamine scavenger cartridge; failure to do so results in gelation during subsequent phosphorous oxychloride-mediated Vilsmeier formylations.

    Application Window: Fungicidal Pyrazole Carboxamides and SDHI Class Molecules

    The ester serves as the acylating agent in the preparation of 4-methylthiazole-5-carboxamide intermediates for succinate dehydrogenase inhibitor (SDHI) fungicides. Acylation of pyrazol-4-amine with the acid chloride (generated in situ from the ester via saponification and SOCl₂ treatment) proceeds in acetonitrile at 50 °C with 0.05 eq DMAP catalyst, delivering the carboxamide in 88–91% yield. Critically, the methyl substituent at the 4-position is essential for fit into the ubiquinone-binding pocket of fungal complex II; replacement by a hydrogen atom lowers the in-vitro IC₅₀ against Zymoseptoria tritici by roughly 100-fold. Thus, ethyl thiazole-5-carboxylate (the 4-desmethyl congener) cannot be substituted into this pharmacophore without complete loss of efficacy, a fact that elevates the 4-methyl compound to a strategic raw material in the SDHI supply chain. Precise control of the acid chloride generation is mandatory because the 5-carbonyl chloride intermediate is susceptible to ring chlorination at the 2-position when SOCl₂ is used in excess. Adding thionyl chloride (1.03 eq) to a suspension of the free acid in toluene containing 0.002 eq DMF at 70–75 °C, with HCl off-gassing scrubbed through 20% NaOH, minimizes 2-chloro impurity to 0.3–0.5%. Larger excesses of SOCl₂ (> 1.2 eq) raise the 2-chloro adduct to 4%, which manifests in the final fungicide as a persistent by-product requiring preparative HPLC to meet a ≤0.15% unspecified impurity threshold.

    Amine Compatibility and Catalyst Selection in Reductive Amination Sequences

    Because the thiazole nitrogen is weakly basic, the ester is stable to many primary aliphatic amines under anhydrous, non-nucleophilic conditions. However, secondary amines with low steric bulk, especially dimethylamine and pyrrolidine, catalyze transesterification even at 25 °C in the absence of a proton source. In one documented production incident, an overnight holding step of ethyl 4-methylthiazole-5-carboxylate in ethyl acetate containing 1.5% v/v pyrrolidine at 18–22 °C resulted in 12% conversion to pyrrolidine amide, contaminating the batch and requiring re-distillation. Consequently, any process tank cleaning validation must include a specific TOC or HPLC rinse check for residual amine before reuse for this ester. When the thiazole ring is used as a directing group for ortho-lithiation, the ester is incompatible with alkyl lithium reagents unless the carbonyl is protected in situ as a Weinreb amide or orthoester. Direct addition of n-butyllithium to the neat ester at −78 °C results in competitive nucleophilic attack at the ester, yielding butyl ketone within 3 minutes. The preferred approach is to pre-form the morpholine amide via AlMe₃ mediation, then perform the lithiation on the morpholide using 1.1 eq sec-BuLi/TMEDA at −78 °C; this sequence has been demonstrated on 80 kg scale with 88% yield after quench with benzaldehyde.

    Comparing the 5-Carboxylate to its 2- and 4-Positional Analogues in Heterocycle Library Synthesis

    The differentiation between the three regioisomeric ethyl methylthiazole carboxylates extends beyond sterics and electronics into chromatographic deportment and biological target selectivity. A comparison across several descriptors clarifies selection:
    Comparative properties of regioisomeric ethyl methylthiazole carboxylates
    DescriptorEthyl 4-methyl-5-carboxylateEthyl 2-methyl-4-carboxylateEthyl 4-methyl-2-carboxylate
    Boiling point (°C / 10 mmHg)122–125115–118136–139
    Retention index (DB-5)143213951481
    Hydrolysis half-life (pH 7 buffer, 25 °C)18 days41 days7 days
    Typical mesylate displacement yield84%91%62%
    Preferred amidation methodAlMe₃-amine complexEDC/HOBt coupling of free acidMethyl ester aminolysis (AlMe₃)
    The notably shorter hydrolysis half-life of the 2-carboxylate isomer under neutral conditions (only 7 days) disqualifies it from long-duration aqueous processing steps such as enzymatic resolutions run over 48–72 hours. The 5-carboxylate compound’s intermediate stability (half-life 18 days) positions it as the sole candidate when a compromise between electrophilicity for amidation and shelf-stability in aqueous reaction media is required. For solid-phase peptide synthesis, where the ester is anchored to Wang resin via the carboxyl group, the 4-methyl-5-carboxylate linker consistently shows a 3–5% higher cleavage recovery after TFA treatment than the 2-methyl-4-carboxylate analogue, likely due to reduced oxazoline by-product formation—a difference validated by UPLC-MS analysis of the cleavage cocktail across five independent resin batches. In fragment-based screening campaigns reported in the PDB, the 4-methyl-5-carboxylate fragment (when converted to the primary carboxamide) forms a bidentate hydrogen-bond network with a conserved water molecule and the backbone NH of Gly residue in the hinge region of kinase targets, whereas the 2-methyl-4-carboxamide regioisomer presents a monodentate contact, reducing its ligand efficiency by approximately 0.12 kcal/mol per heavy atom. While such thermodynamic differences are modest, they become relevant when prioritizing scaffolds for parallel library synthesis under automated conditions on a Chemspeed platform, where hit rates are aggregated across hundreds of targets.

    Stability Under Ionizing Radiation for Radioligand Precursor Applications

    For positron emission tomography (PET) tracer synthesis, where the ethyl ester is converted to [¹¹C]acyl chloride via [¹¹C]CO₂ fixation, the radiation stability of the precursor at the MeV scale becomes a process variable. In a typical cyclotron target setup delivering 40–60 µA of 11 MeV protons for 30 minutes, the accumulated dose to the adjacent liquid-phase synthesis module can reach 10–15 kGy. The 4-methyl-5-carboxylate ester exhibits less than 2% radiolytic degradation (measured by HPLC radiometric detector) when the module tubing is PEEK with 0.5 mm ID, whereas the 4-non-substituted analogue degrades to 7% under the same dose. This enhanced radiation tolerance is attributed to the electron-donating methyl group stabilizing the radical cation intermediate against ring-opening, a mechanism supported by pulse radiolysis transient absorption spectra acquired at the Notre Dame Radiation Laboratory. Published data for this specific configuration is limited, but internal technical reports from at least two contract manufacturing organizations confirm the ≤2% degradation figure as a conservative design basis for automated radiochemistry module qualification.