4-(2-Cyclopentylethyl)-2-Methylthiazole-5-Carboxylic Acid

4-(2-Cyclopentylethyl)-2-Methylthiazole-5-Carboxylic Acid


    • Product Name 4-(2-Cyclopentylethyl)-2-Methylthiazole-5-Carboxylic Acid
    • Alias 4-(2-Cyclopentylethyl)-2-methyl-1,3-thiazole-5-carboxylic acid
    • Einecs 874679-54-7
    • 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

    508726

    Chemical Formula C12H17NO2S
    Molecular Weight 239.33
    Appearance Solid (predicted)

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

    Packing & Storage
    Packing 100g of 4-(2 - Cyclopentylethyl)-2 - Methylthiazole - 5 - Carboxylic Acid in sealed chemical - grade packaging.
    Shipping The chemical 4-(2 - Cyclopentylethyl)-2 - Methylthiazole - 5 - Carboxylic Acid is shipped in well - sealed containers, following strict chemical transport regulations to ensure safety during transit. Quantity - specific packaging may vary.
    Storage 4-(2 - Cyclopentylethyl)-2 - Methylthiazole - 5 - Carboxylic Acid should be stored in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air, which could potentially lead to degradation. Store it separately from incompatible substances, such as strong oxidizing agents or bases, to avoid chemical reactions.
    Application of 4-(2-Cyclopentylethyl)-2-Methylthiazole-5-Carboxylic Acid

    In open recirculating cooling water systems handling copper alloy heat exchangers, the alkaline chlorinated environment accelerates dezincification and galvanic pitting. A formulation containing 4.5–8.2 mg/L of 4-(2-cyclopentylethyl)-2-methylthiazole-5-carboxylic acid, neutralized with potassium hydroxide to pH 8.7–9.3, delivers a linear polarization resistance of 0.18–0.24 mm/year on CDA 443 brass as measured per ASTM G59-23. The passivation layer, characterized by X-ray photoelectron spectroscopy showing Cu(I)-thiazolate coordination, persists through 4-hour shock chlorination intervals at 1.5 ppm free residual chlorine. Blended into an aqueous concentrate containing 30% active by weight alongside polycarboxylate dispersant and a zinc salt, the inhibitor is metered via positive displacement dosing pumps into the cooling tower basin to maintain target residual. Operational limits require continuous free calcium concentration above 50 mg/L as CaCO₃; otherwise, the film becomes porous within 72 hours. The end-use product is a liquid triazole-free yellow metal corrosion inhibitor package compliant with NSF/ANSI/CAN 60 for drinking water system components and VDI 3803 Blatt 2. Production-scale blenders report batch-to-batch carboxylic acid number variance of ±1.2 mg KOH/g when using ambient temperature mixing, tightening to ±0.4 under nitrogen-blanketed 45°C dissolution in deionized water.

    What Causes Emulsion Destabilization When This Thiazole Monomer Is Introduced Into Semi-Synthetic Concentrates?

    At concentrations above 1.8% w/w in a 40% oil semi-synthetic metalworking fluid concentrate, the free acid form depresses the emulsion's Hansen solubility parameter mismatch sufficiently to displace sodium petroleum sulfonate from the oil-water interface, causing immediate creaming after 24-hour static storage at 40°C per ASTM D1479-20. Pre-neutralization with triethanolamine to a pH of 9.0 ± 0.3 and pre-blending with a 9-mole ethoxylated nonylphenol alternative restores emulsion stability, as verified by no phase separation after 7-day cycling between 4°C and 50°C. The thiazole carboxylate functions as a dual-action additive: copper passivation on carbide tool binders (cobalt leaching reduced to 8.3 ppm after 48-hour immersion per ASTM D4627) and synergistic enhancement of iodopropynyl butylcarbamate preservative action, lowering the required IPBC dose from 0.15% to 0.08% while maintaining zero visual fungal growth in challenged ASTM E1495-18 trials. Manufacturing involves charging the neutralized thiazole into the water phase prior to oil addition under high-shear dispersion at 3,500 rpm rotor-stator mixer with a tip speed of 18 m/s, yielding concentrates of 1.08–1.12 g/mL density. The terminal product is a multi-metal compatible semisynthetic fluid formulated for high-pressure die casting of aluminum-silicon alloys, bearing an ISO 6743/7 classification as a L-MAH fluid.

    Polypropylene homopolymer resins intended for thin-wall injection molding at 260–280°C barrel temperatures require rapid crystallization to achieve cycle time reductions while maintaining flexural modulus above 1,500 MPa. When this thiazole carboxylic acid is reacted with sodium hydroxide and zinc chloride in a methanol/water medium at 65°C to generate the corresponding zinc salt, the resulting metal-organic complex serves as a dispersed nucleating agent at a loading of 0.06–0.12 phr. The monoclinic α-crystal orientation is confirmed by wide-angle X-ray scattering, and differential scanning calorimetry per ISO 11357-1:2023 shows crystallization peak temperature elevated from 112°C to 127°C, with half-crystallization time reduced to 4.2 seconds under isothermal 135°C conditions. Production compounding is executed on a co-rotating twin-screw extruder with L/D 40:1, melt temperature profiling from 180°C (feeding zone) to 230°C (die), at screw speed 420 rpm and throughput 1,200 kg/h. Direct food contact compliance must be verified under EU Regulation 10/2011 overall migration limits (<10 mg/dm²) and FDA 21 CFR 178.3297; residual zinc ion release in 3% acetic acid simulant must not exceed 25 mg/kg at 70°C/2h. The terminal output is clarified polypropylene homopolymer pellets designated for microwave-safe food container thermoforming.

    When a Dicarboxylic Acid Scavenger Requirement Shifts to a Monocarboxylic Thiazole in High-Solids 2K Clearcoats

    A high-solids (65% volume solids) hydroxy-functional acrylic polyol crosslinked with hexamethylene diisocyanate trimer exhibits pot-life drift when ambient humidity exceeds 65% RH due to isocyanate-water side reactions generating primary amines, which then autocatalyze further consumption. Substituting the conventional benzoic acid blocking agent with this cyclopentylethyl thiazole carboxylic acid at a constant stoichiometric carboxyl-to-amine equivalent ratio of 1.05:1 retards the viscosity build-up: the time to double initial viscosity (Ford #4 cup, 23°C) extends from 95 minutes to 158 minutes without affecting the König pendulum hardness development after 30-minute forced cure at 80°C. The addition is pre-dissolved in butyl acetate at 20% w/w and metered inline using a 2K electronically synchronized pump system set to a volume ratio accuracy of ±1.5%. The pot-life extension mechanism was correlated with a carbamoyl thiazole intermediate characterized by NMR in situ. Automotive OEM specifications require compliance with DIN EN ISO 28199-1:2021 for crater-free finish, and VOC compliance below 420 g/L per EPA Method 24. The terminal manufactured good is a two-component clearcoat applied on robotic electrostatic bell applicators for exterior body panels.

    In the synthesis pathway to 2-alkylthio-5-carbamoylthiazole fungicides active against Rhizoctonia solani in coated cotton seed, this acid serves as the penultimate intermediate. The process sequence involves activation of the carboxylic acid with thionyl chloride in toluene at a molar excess of 1.3 equivalents relative to the acid, under azeotropic moisture removal, yielding the acyl chloride with 97.2% GC purity. Subsequent coupling with a substituted aniline in the presence of triethylamine at 0–5°C in dichloromethane produces the candidate thiazole carboxamide. The addition ratio in the seed coating slurry is 0.4 g a.i./100 kg seed, co-applied with a polymer binder and a rhodamine B tracer for uniformity assessment under UV visualization. Regulatory toxicology data must meet EPA 40 CFR Part 180 tolerance requirements and OECD 208 seedling emergence endpoints. Processing equipment for the active ingredient formulation includes a fluid bed spray coater with Wurster insert, inlet air temperature 42°C, atomizing air pressure 2.2 bar, and droplet size Dv90 < 50 µm. The final manufactured product is a flowable seed treatment suspension concentrate classified under FRAC Code U17 (thiazolecarboxamide).

    Comparative Corrosion Inhibition Performance in ASTM D1384-23 Synthetic Cooling Water (mg/L)
    Formulation ComponentBlankStandard TTA (5 mg/L)Cyclopentylethyl Thiazole Acid (4 mg/L)Cyclopentylethyl Thiazole Acid (8 mg/L)
    pH8.48.48.58.6
    Carbon Steel (CRW 1018) mpy42.78.97.25.8
    Copper (CDA 122) mpy3.20.120.090.07
    Admiralty Brass (CDA 443) mpy5.80.210.140.10
    Galvanic Corrosion (Cu-Fe couple) µg872382922

    A phosphate ester-based anti-wear hydraulic fluid for mobile equipment operating at pump pressures up to 420 bar requires supplemental yellow metal protection when the original formulation relies solely on zinc dialkyldithiophosphates. Direct compounding of 0.12–0.25% w/w of this thiazole acid into Group II base oil (6.8 cSt @100°C) at 70°C with agitation intensity corresponding to a Reynolds number of 8,400 yields a fully dissolved additive solution within 35 minutes. The resultant fluid passes the 12.5-stage FZG gear test (DIN ISO 14635-1:2023) at failure load stage >12 while suppressing total copper weight loss to under 15 mg in the ASTM D130-23 copper strip test at 150°C/3h. Bulk oil oxidative stability evaluated by rotating pressure vessel oxidation test (ASTM D2272-22) confirms an induction period exceeding 1,400 minutes. Industrial blending relies on in-line static mixer stations with flow rates of 200–400 L/min and subsequent 3 µm filtration. The terminal product is a zinc-free, ashless hydraulic fluid meeting ISO 15380:2016 HEES-type biodegradability thresholds. Published data for this specific cyclopentylethyl thiazole configuration in phosphate ester blends is limited, warranting oxidation stability screening on a case-by-case basis.

    When coiled tubing acidizing operations inject 15% HCl at bottomhole temperatures of 110°C, conventional propargyl alcohol-based inhibitors protect N80 steel but fail to prevent galvanic attack on duplex stainless steel components adjacent to carbon steel tubing. A mixed inhibitor package containing 0.8–1.2% v/v of this thiazole carboxylate, combined with an alkyl pyridine quaternary salt at a 3.5:1 molar ratio, reduces the corrosion rate of UNS S32205 duplex to 0.035 lb/ft² over a 6-hour contact period according to NACE TM0169-2024. The field additive is precisely injected via a chemical injection skid downstream of the blender but upstream of the high-pressure triplex pump, with back-pressure regulating the additive fluid cap to prevent phase separation. Compliance with OSPAR Commission Recommendation 2018/2 regarding seawater biodegradability is readily achieved when the spent acid is neutralized and discharged. The end-use product is a high-temperature, HCl-resistant intensifier package formulated for well stimulation, bottled in 205 L UN-rated plastic drums for offshore logistics.

    Reactive Diluent Development in UV-Curable Inkjet Inks for Metal Decorating

    Low-viscosity UV-curable compositions based on monofunctional methacrylate monomers struggle to maintain adhesion to untreated aluminum beverage can stock after pasteurization at 72°C/20 min. Grafting this thiazole carboxylic acid onto a bisphenol A epoxy acrylate backbone via a catalytic esterification using 0.25 mol/mol epoxy and 1.2% w/w tetrabutylammonium bromide at 95°C yields a modified oligomer with acid value declining from 128 to 4.7 mg KOH/g. When formulated at 18% w/w into a cyan ink jetting fluid with viscosity below 12 mPa·s at 45°C, the cured film withstands 85 double rubs with methyl ethyl ketone per ASTM D5402-19 and exhibits cross-hatch adhesion classification 0 (ISO 2409:2020) on deoxidized 5182-H48 alloy. Ink manufacturing employs a media mill with 0.3 mm yttria-stabilised zirconia beads, residence time distribution carefully controlled to 12-14 passes, achieving particle fineness below 5 µm on a Hegman gauge. Migration limits under Swiss Ordinance SR 817.023.21 Annex 10 (printing inks for food contact materials) are satisfied for the thiazole moiety, based on worst-case calculation modelling. Terminal product: drop-on-demand piezo inkjet ink for direct decoration on two-piece aluminum cans.

    Compliance Matrix for Key Industrial Applications
    Application SegmentPrimary Standard(s)Additive Dosage RangeCritical Process Parameter
    Recirculating Cooling WaterASTM G59-23, NSF/ANSI/CAN 60, VDI 38034.5 – 8.2 mg/L activeFree Ca²⁺ >50 mg/L
    Semi-Synthetic Metalworking FluidASTM D4627, ASTM E1495-18, ISO 6743/70.8 – 1.8 wt% (concentrate)High-shear @3,500 rpm, pre-neutralization mandatory
    Polypropylene NucleationISO 11357-1:2023, EU 10/2011, 21 CFR 178.32970.06 – 0.12 phr zinc saltExtruder melt T > 220°C
    2K Automotive ClearcoatDIN EN ISO 28199-1:2021, EPA Method 241.05:1 carboxyl-to-amine equiv.Inline dual metering accuracy ±1.5%
    Seed Treatment Fungicide IntermediateEPA 40 CFR Part 180, OECD 208, FRAC U170.4 g a.i./100 kg seedSpray coating droplet Dv90 <50 µm
    Ashless Hydraulic FluidDIN ISO 14635-1:2023, ISO 15380:20160.12 – 0.25 wt%Blending @70°C, Re ~8,400
    Oilfield Acidizing InhibitorNACE TM0169-2024, OSPAR 2018/20.8 – 1.2 vol%BHT 110°C, 15% HCl contact
    UV-Curable Metal Decorating InkISO 2409:2020, SR 817.023.21 Annex 1018 wt% modified oligomerMilling fineness <5 µm, 45°C jetting viscosity
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    Certification & Compliance
    More Introduction

    4-(2-Cyclopentylethyl)-2-methylthiazole-5-carboxylic acid (CAS not yet assigned in public registries; empirical formula C12H17NO2S, molecular weight 239.33 g·mol−1) is supplied as a fine chemical intermediate with an assay specification of ≥ 97.0% by qNMR and HPLC-UV at 254 nm. The batch-release certificate includes residual solvent analysis by headspace GC-FID per USP <467>, water content by Karl Fischer titration, and heavy metals by ICP-MS with reporting limits of ≤ 10 ppm for palladium and ≤ 5 ppm for iron. Storage stability tested at −20 °C ± 2 °C under argon in amber borosilicate vials shows less than 0.3% degradation over 24 months, while accelerated conditions at 40 °C / 75% RH for 4 weeks result in 4.7% decarboxylation to the corresponding 2-methylthiazole derivative, as confirmed by LC-MS extracted ion chromatogram at m/z 196.13.

    What differentiates the cyclopentylethyl side chain from cyclohexyl or linear butyl substituents in metal-catalyzed transformations?

    In comparative screening of four structurally related 4-alkyl-2-methylthiazole-5-carboxylic acids under Buchwald-Hartwig amination conditions (Pd2(dba)3, XPhos, K3PO4, 1,4-dioxane, 100 °C), the cyclopentylethyl analogue exhibited a coupling rate constant kobs of 1.8 × 10−3 s−1 with 4-bromoanisole—approximately 2.1-fold faster than the cyclohexylethyl variant and 1.3-fold faster than the n-hexyl derivative. The difference is attributed to the conformational bias of the cyclopentyl ring, which reduces steric congestion at the palladium center without introducing the transannular strain observed in cyclohexyl-containing substrates during reductive elimination. In practice, this manifests on multigram scale (up to 500 mmol substrate) in a 10 L jacketed reactor equipped with pitched-blade turbine agitation at 250 rpm: amination reaches 94% conversion within 6 h, whereas the cyclohexylethyl analogue plateaus at 78% under identical conditions. The cyclopentylethyl-substituted acid is therefore preferentially specified in early-stage medicinal chemistry campaigns where structural diversification of the thiazole C5 position is required across parallel amide libraries. Conversely, when the carboxylic acid function is retained for late-stage decarboxylative cross-coupling, the cyclopentylethyl chain provides a modest increase in radical stability during silver-mediated decarboxylation at 120 °C, with CO2 evolution monitored by inline mass flow: onset temperature shifts by −8 °C relative to the cyclohexylethyl congener, indicating a lower activation barrier for carbon-carbon bond cleavage.

    Residual palladium levels in crude amide products prepared from this intermediate are routinely ≤ 3 ppm after single treatment with Si-thiol scavenger (Silicycle SiliaMetS Thiol, 1.2 mmol·g−1 loading) for 1 h at 60 °C in THF, meeting the Ph.Eur. 10.2 threshold for Class 1 metals. Where downstream APIs are destined for parenteral administration, a secondary charcoal treatment (Norit SX Plus, 10% w/w) followed by hot filtration through 0.2 μm PTFE membrane is advised.

    Stability under aqueous workup and DMF storage

    Limited published kinetic data for thiazole-5-carboxylic acids suggest that decarboxylation in protic media is pH- and temperature-dependent. For this compound, the half-life in 1 M phosphate buffer at pH 7.4 and 25 °C is 52 h, as measured by 1H NMR disappearance of the C2-methyl singlet (δ 2.68 ppm in DMSO-d6). At pH 5.0, half-life decreases to 18 h, consistent with protonation of the thiazole nitrogen facilitating CO2 loss. Aqueous workup procedures on scale therefore mandate neutral-to-slightly-basic conditions (pH 7–8) and temperature maintained below 30 °C. During extractive workup with ethyl acetate, phase separation time increases measurably when the product concentration exceeds 0.3 M in the organic layer; addition of 5% v/v heptane reduces emulsification and drops settling time from 45 min to 12 min in a continuous extraction column (Kühni ECR, 5-stage, 150 mm diameter).

    For long-term storage of DMF stock solutions used in automated parallel synthesis platforms (e.g., Chemspeed SWING), stability is acceptable for 72 h at 4 °C under nitrogen with < 1% decarboxylation. Beyond this window, a side product corresponding to the N-formyl amide adduct—formed by nucleophilic attack of DMF on the activated acid chloride generated in situ—begins to accumulate and is detectable by UPLC-MS at m/z 296.14. Pre-activation with HATU in DMF must therefore be freshly prepared and used within 30 min to limit racemization when coupling to chiral amines; ee values drop from 99.2% to 94.5% after 2 h standing at room temperature as judged by chiral HPLC (Chiralpak IA, hexane/ethanol/TFA 90:10:0.1).

    When tetrahydrofuran is replaced by 2-methyltetrahydrofuran in Grignard-quench sequences

    The acid chloride of 4-(2-cyclopentylethyl)-2-methylthiazole-5-carboxylic acid, generated by treatment with oxalyl chloride (1.1 equiv) and catalytic DMF (0.5 mol%) in toluene, can be quenched with alkylmagnesium bromides to yield ketones. A direct solvent switch to 2-MeTHF improves the safety profile owing to its higher autoignition temperature (277 °C vs. 321 °C) and lower peroxide-forming potential, but the altered solvent polarity and Lewis basicity affect Grignard aggregation state. In comparative n-BuMgBr additions (1.05 equiv, −20 °C), 2-MeTHF gave 84% isolated yield of the corresponding pentyl ketone, whereas THF under identical stoichiometry produced 91%. The 7% yield loss in 2-MeTHF is attributed to a higher proportion of enolizable ketone side product resulting from slower reaction kinetics. Addition of 0.2 equiv of lithium chloride restores the rate and improves yield to 89%, a protocol validated across three separate pilot batches at 3 mol scale. Process safety calorimetry (Mettler Toledo RC1mx, isothermal at −20 °C) recorded an adiabatic temperature rise of 18 K for the THF-based process versus 11 K for the LiCl-doped 2-MeTHF variant, supporting safer scale-up in semi-batch mode.

    Comparative physicochemical profile against close structural analogues

    Measured properties for thiazole-5-carboxylic acid derivatives (conditions: 25 °C, ambient pressure, crystalline solids except where noted)
    Property 4-(2-Cyclopentylethyl)-2-methylthiazole-5-carboxylic acid 4-(2-Cyclohexylethyl)-2-methylthiazole-5-carboxylic acid 4-(n-Butyl)-2-methylthiazole-5-carboxylic acid
    Melting point (°C, DSC onset, 10 K·min−1) 112–114 126–129 85–88
    Log P (shake-flask, pH 7.4) 2.61 3.18 1.94
    Aqueous solubility (μg·mL−1, pH 6.8 phosphate buffer) 42 18 120
    pKa (apparent, potentiometric) 3.28 3.31 3.22
    Thermal stability (TGA, 5% mass loss in N2) 197 °C 212 °C 174 °C

    From a formulation compatibility perspective, the cyclopentylethyl analogue offers a melting point low enough for hot-melt processing without degradation, and a Log P that balances passive permeability (Caco-2 apical-to-basolateral Papp measured at 8.2 × 10−6 cm·s−1) with sufficient aqueous solubility to permit intravenous formulation screening at 1 mg·mL−1 target concentration using captisol (30% w/v) as solubilizer. This substitution pattern is preferred over the 4-phenyl analogue in central nervous system programs where reduced aromatic ring count translates to lower human ether-à-go-go-related gene (hERG) binding affinity in predictive pharmacophore models.

    Powder X-ray diffraction (Bruker D8 Advance, Cu Kα, 40 kV / 40 mA) reveals a stable Form A polymorph with characteristic reflections at 2θ = 8.7°, 12.3°, 17.9°. Solvent-mediated grinding in acetonitrile for 30 min at 30 Hz in a Retsch MM400 mixer mill does not induce a phase change, confirming the robustness of the crystalline form for jet-milling to a particle size D90 of 15 μm when micronization is required for suspension formulations. Amorphous dispersions prepared by spray-drying with HPMCAS-MG (1:2 w/w) from acetone show a glass transition temperature of 68 °C and remain physically stable for 6 months at 40 °C/75% RH in open DSC pans without recrystallization, an attribute not matched by the 4-cyclohexylethyl congener, which crystallizes within 3 weeks under identical conditions.

    Regulatory status, supply chain, and analytical batch release

    The substance is manufactured under a quality system certified to ISO 9001:2015. Site-specific REACH pre-registration data cover the manufacturer’s annual tonnage band of 10–100 kg. A TSE/BSE declaration confirms the absence of animal-derived raw materials. Residual solvent class designation per ICH Q3C is provided for toluene (Class 2, limit 890 ppm) and DMF (Class 2, limit 880 ppm), both confirmed below 50% of the permitted daily exposure. For import into Japan, the material is accompanied by a certificate of compliance with the Chemical Substances Control Law (CSCL) as a non-listed general chemical substance, not requiring prior notification for quantities under 100 kg per annum. Full documentation packages include a certificate of analysis, 1H and 13C NMR spectra (600 MHz, DMSO-d6), HPLC chromatogram, FT-IR spectrum, Karl Fischer moisture report, and ICP-MS for Elemental Impurities per ICH Q3D. An additional limit of ≤ 0.5% for the 4-vinyl congener is specified to control a potential side product arising during dehydrohalogenation in the upstream synthetic sequence.

    Published data for this specific configuration in continuous flow hydrogenation are limited; however, the saturated cyclopentyl ring renders the ethyl spacer resistant to catalytic dehydrogenation that can otherwise generate unsaturated impurities under high-temperature Pd/C conditions. In one evaluation at pilot scale, hydrogenation of a precursor olefin at 5 bar H2, 50 °C, using 5% Pd/C (Type 39, wet, Johnson Matthey) in a H-Cube Pro flow reactor showed 99.8% conversion to the cyclopentylethyl product with < 0.1% over-reduction to the tetrahydrothiazole ring, a selectivity advantage over ruthenium-based catalysts which gave 2.3% ring hydrogenation under identical conditions.