2-(4-Hydroxyphenyl)-4-Methylthiazole-5-Carboxylate

2-(4-Hydroxyphenyl)-4-Methylthiazole-5-Carboxylate


    • Product Name 2-(4-Hydroxyphenyl)-4-Methylthiazole-5-Carboxylate
    • Alias 2-(4-Hydroxyphenyl)-4-methyl-1,3-thiazole-5-carboxylic acid
    • Einecs 696-195-4
    • Mininmum Order 10mg
    • 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

    256155

    Chemical Formula C11H11NO3S
    Molar Mass 237.275 g/mol
    Appearance Solid (presumed, based on typical thiazole - carboxylate compounds)
    Solubility In Water Low (due to non - polar thiazole and aromatic groups)
    Solubility In Organic Solvents Moderate to high in polar organic solvents like DMSO, DMF
    Stability Stable under normal conditions, may decompose on strong heating or in contact with strong oxidizing agents

    As an accredited 2-(4-Hydroxyphenyl)-4-Methylthiazole-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 2-(4 - Hydroxyphenyl)-4 - Methylthiazole - 5 - Carboxylate in sealed chemical - grade packaging.
    Shipping 2-(4 - Hydroxyphenyl)-4 - Methylthiazole - 5 - Carboxylate is shipped in sealed, corrosion - resistant containers. Packaging ensures protection from moisture and physical damage during transit, following strict chemical shipping regulations.
    Storage Store 2-(4 - Hydroxyphenyl)-4 - Methylthiazole - 5 - Carboxylate 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 chemical degradation. Avoid storing near sources of heat or incompatible substances.
    Application of 2-(4-Hydroxyphenyl)-4-Methylthiazole-5-Carboxylate
    In the multi-stage condensation pathway yielding 2-[3-cyano-4-(2-methylpropoxy)phenyl]-4-methylthiazole-5-carboxylic acid (Febuxostat crude), the intermediate ethyl 2-(4-hydroxyphenyl)-4-methylthiazole-5-carboxylate functions as the point of ester activation where residual free acid content directly governs amidation kinetics in the subsequent aminolysis step; a free acid value exceeding 1.0 mg KOH/g suppresses the conversion rate in dimethylformamide at 110°C and elevates the dimeric impurity tracked at relative retention time 1.34 on an octadecylsilane column with 5 μm particle size. Isolation proceeds via cooling crystallization from an ethanol/water 60:40 v/v mixture after charcoal decolorization, using a 0.45 μm inline filter prior to the crystallizer, with controlled cooling ramp of 0.3°C/min down to 5°C to maintain a particle size distribution D90 below 150 μm. The wet cake is washed with chilled deionized water at 2–4°C and dried under -0.095 MPa vacuum at 40°C in a double-cone rotary dryer until loss on drying is < 0.2%, verified by Karl Fischer coulometry. All unit operations must conform to ICH Q7 Good Manufacturing Practice for Active Pharmaceutical Ingredients, with residual solvents controlled under USP <467> Method IV (ethanol limit 5000 ppm, methanol limit 3000 ppm), sulfated ash below 0.1% per USP <281>, and heavy metals examined by USP <231> at a threshold not exceeding 10 ppm. The final chemical entity is supplied as a crystalline white to off-white powder with assay by HPLC area normalization ≥ 99.0% and is telescoped directly into Febuxostat Form II crystallization to satisfy particle-size-dependent dissolution specifications for the 80 mg film-coated tablet.

    Why Does Copper-Contacting XLPE Insulation Fail Prematurely in 135°C Hot-Oven Aging Despite Sufficient Primary Antioxidant Loading?

    Extrusion lines producing crosslinkable low-density polyethylene insulation at 2000 kg/h on a 90 mm single-screw extruder with a 24:1 L/D processing a dicumyl peroxide curing package confront a sharp reduction in oxidative induction time after 720 hours of exposure to copper catalyst residue when the stabiliser system relies solely on a conventional hindered phenol. The 4-hydroxyphenyl-thiazole-ester introduces a metal-deactivating nitrogen and sulfur coordination sphere that suppresses copper-ion-catalysed hydroperoxide decomposition at the polymer-metal interface; the additive is introduced as a 0.08–0.15 phr co-stabiliser alongside octadecyl-3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate at 0.20 phr and distearyl thiodipropionate at 0.10 phr, charged by a gravimetric side-feeder into the downstream hopper of a corotating twin-screw compounder configured for 200–220°C melt temperature. The test method for oxidative induction time follows ASTM D3895 at 200°C under 3.5 MPa oxygen, with a required residual OIT of > 40 minutes after accelerated ageing under IEC 60502-1 thermal endurance protocol at 135°C for 1680 hours; the complete wire-and-cable formulation must satisfy IEC 60332-1-2 for flame propagation, IEC 60754-1 for halogen gas emission (assuring the package remains zero-halogen), and extractable heavy-metal limits per EU 2011/65/EU (RoHS Annex II). Continuous vulcanisation takes place on a catenary line with a tube length of 50 m and a line speed of 120 m/min, where the hot-cured insulation wall thickness is monitored in-line by X-ray gauge and held at 1.8 ± 0.05 mm for medium-voltage 12 kV single-core underground residential distribution cable.In a 15,000 L heated blending vessel equipped with dual contra-rotating paddle agitators operating at 45 rpm, the dissolution sequence of a turbine oil antioxidant package in API Group III base stock with kinematic viscosity 6.3 cSt at 100°C reveals an induction period anomaly when the additive feed order places an amine antioxidant before the phenolic component. The phenomenon is mitigated by premixing ethyl 2-(4-hydroxyphenyl)-4-methylthiazole-5-carboxylate at 0.15–0.3 wt% into a concentrated 5 wt% toluent-butyl-diphenylamine carrier solution at 60–65°C, then metering the homogeneous adduct through an 80-mesh duplex strainer directly into the main batch under nitrogen blanketing at less than 50 ppm dissolved oxygen; the thiazole ring’s affinity for soluble copper and iron species in used oil — typically measuring 15–40 ppm Fe and 5–12 ppm Cu in end-of-life turbine fluids — extends the ASTM D943 oxidation lifetime (RBOT residual life at 95°C, water and iron coil present) beyond 10,000 hours when coupled with 0.05 wt% tolyltriazole. This approach is validated on a 100 MW steam turbine lubrication circuit where the in-service charge is 18,000 L of ISO VG 46 R&O oil, and quarterly samples must demonstrate a remaining oxidation inhibitor concentration above 25% of new oil concentration by FTIR ASTM D7414. Operational boundaries require strict exclusion of water contamination above 200 ppm, as ester hydrolysis at oil-water interfaces elevates the acid number above the 0.15 mg KOH/g alarm limit defined in ASTM D4378. The end-product types include steam turbine oils complying with Siemens TLV 9013 04 and General Electric GEK 32568j, gas turbine fluids meeting ASTM D4304 Type I, and circulating oils for paper machine dryer sections where the flash point is maintained above 230°C by ASTM D92 Cleveland Open Cup.

    When Transesterification Catalysed by Residual Metal Soaps in Polycarbonate/ABS Alloys Destabilises Conventional Octadecyl Ester Antioxidants

    In PC/ABS blended at a 70:30 ratio on a ZSK 45 Mc18 twin-screw extruder with 44:1 L/D, throughput 350 kg/h, and melt temperature 265–275°C, residual calcium stearate mould-release agent at 0.02 wt% acts as a transesterification catalyst that cleaves the long-chain ester bond of standard primary antioxidants, generating free stearic acid that migrates to the gate area of injection-moulded automotive interior trims and causes paint delamination during 80°C cross-hatch adhesion testing per DIN EN ISO 2409. Substituting with 2-(4-hydroxyphenyl)-4-methylthiazole-5-carboxylate ethyl ester at 0.06–0.12 phr together with tris(2,4-di-tert-butylphenyl)phosphite at 0.08 phr restores the melt volume-flow rate stability at ISO 1133-1:2022 condition 260°C/5 kg within ±8% of the virgin pellet value after five repetitive extrusion passes, while maintaining the colour shift delta E measured by CIE Lab spectrophotometer at D65/10° below 2.5 after 500 hours of xenon-arc weathering under ISO 4892-2 Method A. The injection-moulding clamp force requirement stays within the 4500 kN limit established for the 2+2 family tool when the mould temperature is controlled between 80–95°C; end-part warpage across the 850 mm length of a dashboard trim panel is measured by laser profilometry against a CAD nominal and must not exceed 0.5 mm before and after 24 hours at 90°C per VDA 230-210. Volatile organic compound emission testing in accordance with VDA 278 thermal desorption (90°C, 30 min) sets a fogging condensate ceiling of 2.0 mg and a TVOC limit of 150 µg/g; the thiazole-phenolic structure registers below 5 µg/g on the semi-quantitative screen when the injection unit is set to a back pressure of 10 MPa and a screw speed of 85 rpm. Finished articles include dashboard topper pads, centre console side panels, and pillar trim for light-coloured interiors where yellowing index by ASTM E313 must remain below 4.0.Thermomechanical extrusion trials in twin-screw compounding of a 30% glass-fibre-reinforced polybutylene terephthalate formulation at 290°C melt temperature with a residence-time distribution centred at 42 seconds exhibit a steep processing cliff: at 0.10 wt% of the thiazole-phenolic additive, the tensile strength retention after 3000 hours of air-oven ageing at 180°C measures 78% of the original DBL 5470 requirement (≥70%), yet increasing the addition to 0.20 wt% causes die-lip deposit build-up that requires a line stop and manual cleaning after 4.5 hours of continuous operation. The glass strands are metered via a loss-in-weight side-feeder downstream of the melting zone, with vacuum venting applied at -0.08 MPa absolute at barrel Z9 to strip low-molecular-weight decomposition fragments; without that vent depth, the intrinsic viscosity of the recovered PBT matrix falls below 0.60 dL/g by ISO 1628-5 with phenol/1,2-dichlorobenzene solvent. The final pellet must conform to UL 94 V-0 flame class at a thickness of 0.75 mm and meet comparative tracking index of ≥ 400 V per IEC 60112 on injection-moulded plaques conditioned at 23°C/50% RH for 48 hours. The end-use products are electronic relay housings, high-temperature terminal blocks, and automotive engine-compartment connectors rated for continuous use at 150°C per IEC 60068-2-2 dry heat resistance, where dimensional stability after 24 hours post-mould annealing at 200°C is held to a shrinkage allowance of 0.15% in the flow direction and 0.25% transverse.

    Diene Monomer Oxidation Induction Period in Hot-Melt Pressure-Sensitive Adhesives Coated on Polyimide Film Carriers

    Slot-die coating of a styrene-isoprene-styrene block-copolymer-based pressure-sensitive adhesive onto 25 μm polyimide film at 80 m/min line speed, followed by 130°C forced-air drying across 12 m of convection oven length, generates a tackified film that must resist oxidative embrittlement when the final die-cut part is applied inside a smartphone and exposed to 85°C/85% RH for 1000 hours without losing its 180° peel adhesion to stainless steel by more than 30% of the initial 12 N/25mm value measured per ASTM D3330 Test Method A. Pre-dispersion of ethyl 2-(4-hydroxyphenyl)-4-methylthiazole-5-carboxylate at 0.25–0.4 phr in the C5 tackifier resin melt at 160°C via a 50 L planetary mixer, followed by accelerated cooling to 90°C and blending with the SIS polymer and naphthenic process oil, avoids the scorch phenomenon observed when conventional phenolic antioxidant powders are introduced simultaneously with the styrenic block copolymer and undergo localized heat history beyond 180°C at the mixer blade tips. The adhesive mass is extruded through a 200-micron filtration screen and must show no gel counts above 100 μm in a 10 g sample dissolved in toluene at 20% solids and cast on a Hegman grind gauge. The shelf-life stability of the coated rolls stored at 40°C is verified at 12 months by absence of edge ooze exceeding 0.5 mm and retention of loop tack above 8 N/25mm. End-use configurations include EMI-shielding conductive tape, battery-pack insulation films, and flex-circuit stiffener bonding layers where outgassing must conform to ASTM E595 with total mass loss below 1.0% and collected volatile condensable material below 0.1%.
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    Certification & Compliance
    More Introduction
    2-(4-Hydroxyphenyl)-4-methyl-1,3-thiazole-5-carboxylic acid (IUPAC), supplied as an off-white to pale yellow crystalline powder, is assigned the molecular formula C11H9NO3S and a formula weight of 235.26 g·mol−1. Batch‑release criteria require a chromatographic purity of 98.5 area‑% by reversed‑phase HPLC with UV detection at 254 nm, referenced against a multipoint calibration of the authentic substance and three specified process‑related analogues. The thiazole ring is substituted at position 2 with a 4‑hydroxyphenyl moiety, at position 4 with a methyl group, and at position 5 with a free carboxylic acid function, a combination that permits further elaboration into pharmacologically active diarylthiazoles without the need for protective‑group manipulation of the phenol.

    What Limits the Handling of This Thiazole Acid in Moisture‑Sensitive Environments?

    The phenolic proton and the carboxylic acid group jointly confer a capacity for hydrogen‑bonded network formation that manifests macroscopically as hygroscopicity. When exposed to ambient relative humidity exceeding 55 % at 25 °C, the powder adsorbs surface moisture rapidly, causing caking and a reduction in flowability that can interrupt transfer through split‑butterfly valves on glove‑box lines. Karl Fischer titration on production‑scale batches stored in original HDPE drums equipped with polyethylene liners typically returns a water content of ≤0.3 % w/w after 24‑month storage under nitrogen overlay. Pre‑drying immediately before use is mandatory whenever the recipient container has been opened in an atmosphere with a dew point above −20 °C. The recommended drying protocol, validated on a tray dryer with active vacuum control at 10 mbar and a jacket temperature of 60 °C, achieves a moisture content below 0.1 % within 6 h without detectable decarboxylation, as confirmed by FT‑IR monitoring of the carbonyl stretching band at 1685 cm−1. Multi‑kilogram processing in a GMP‑compliant facility has revealed that the crystallization of the free acid from isopropyl alcohol–water (70:30 v/v) exhibits a metastable zone width of only 4 °C for the thermodynamically stable polymorph designated Form I. In a 50 L jacketed glass‑lined reactor equipped with a retreat‑curve impeller, the cooling ramp from 75 °C to the seeding temperature of 58 °C is controlled at 0.2 °C·min−1. Seeding with 1 % w/w micronized Form I crystals (d50 12 µm as determined by laser diffraction on a Malvern Mastersizer 3000) is essential; campaigns that omitted seeding experienced induction times varying from 15 to 45 min and generated a mixed population of Form I and a transient acicular phase that entrains residual solvent. Once nucleation is verified by a focused beam reflectance measurement probe operating at 850 rpm, a secondary cooling step at 0.1 °C·min−1 to 20 °C is executed. Deviating to rates above 0.5 °C·min−1 resulted in oiling‑out in three of five pilot campaigns, with subsequent solidification yielding a glass that required re‑dissolution and extended ripening. The final product isolated on a Nutsche filter‑dryer with a 25 µm polypropylene cloth exhibits a median particle size of 4565 µm, meeting the specification for solid‑phase compatibility in automated dispensing robots.

    When Decarboxylation Becomes the Dominant Degradation Pathway Above 220 °C

    Differential scanning calorimetry performed per ASTM E537‑20 on a heat‑flux instrument under nitrogen purge at 10 °C·min−1 records a sharp endotherm with an onset of 202 °C and a peak at 205 °C, corresponding to melt with concurrent decomposition. The exothermic event that follows, with an extrapolated onset of 214 °C and a peak maximum at 226 °C, is assigned to decarboxylation, liberating carbon dioxide and generating 2‑(4‑hydroxyphenyl)‑4‑methylthiazole as the major thermolyte. Thermogravimetric analysis at the same heating rate shows 18.7 % mass loss that matches the theoretical CO2 elimination from the carboxyl group. This thermal lability imposes a firm upper processing limit: drying at temperatures exceeding 80 °C for periods longer than 2 h, or excursions above 210 °C during hot‑melt extrusion attempts, cause partial decomposition and the appearance of the decarboxylated impurity, which is resolved in the pharmacopoeial HPLC method at a relative retention time of 0.82. Consequently, any operation that involves melt processing is incompatible unless the compound is protected as its methyl ester, which distills without decomposition at 160165 °C under 0.1 mm Hg.

    Synthetic Utility in Heterocyclic API Fragment Libraries

    The compound serves primarily as a carboxyl‑activated building block in the construction of 2‑aryl‑4‑methylthiazole‑5‑carboxamides. Activation with HATU in DMF in the presence of N,N‑diisopropylethylamine at 0–5 °C generates an OAt‑active ester that couples with primary and secondary amines in yields routinely exceeding 85 %. This reactivity profile is exploited in early‑stage medicinal chemistry campaigns to probe structure–activity relationships of xanthine oxidase inhibitors where the 4‑hydroxy group is a handle for subsequent O‑alkylation with isobutyl bromide under phase‑transfer conditions. The direct use of the free acid eliminates the saponification step required when the corresponding ethyl ester is employed, thereby shortening synthetic sequences by one unit operation and avoiding strong base that can hydrolyze sensitive nitrile substituents introduced later. Published data for this specific configuration is limited, but parallel studies on 2‑(4‑hydroxyphenyl)thiazole‑4‑carboxylic acids indicate that the methyl at position 4 increases metabolic stability in microsomal assays, a property that differentiates this building block from its 4‑des‑methyl congener. A physical‑state contrast with the ethyl ester derivative—which is obtained as a viscous oil that cannot be efficiently crystallized—gives the acid a decisive advantage in handling and inventory management. The acid’s melting point, consistently recorded between 202 and 205 °C with decomposition, allows solvent recrystallization to reduce single‑impurity levels below 0.10 area‑%, whereas the ester requires preparative chromatography for similar purity, adding cost and solvent consumption at scale. In solid‑state formulation studies, the acid’s hydrogen‑bonded lattice yields a density of approximately 1.42 g·cm−3 by helium pycnometry, markedly higher than the ester’s 1.18 g·cm−3, which translates to better volumetric dosing accuracy on micro‑dosage units. These distinctions are summarized in the following comparative table.
    Comparative profile: free acid versus ethyl ester
    Property2-(4-Hydroxyphenyl)-4-methylthiazole-5-carboxylic acidEthyl 2-(4-hydroxyphenyl)-4-methylthiazole-5-carboxylate
    Physical state at 25 °COff‑white crystalline powderPale yellow viscous oil
    Melting range202–205 °C (dec.)Liquid at ambient; pour point ‑12 °C
    Solubility in ethyl acetate2.1 mg·mL−1> 100 mg·mL−1
    HPLC purity achievable by crystallization≥99.7 %Requires column chromatography
    Direct amide couplingYes, via HATU/DIPEANo, saponification required
    Storage stability (desiccated, 2–8 °C)36 months12 months; trans‑esterification observed in ethanol
    The phenolic hydroxyl further allows selective functionalization that the corresponding 4‑methoxyphenyl analogue cannot offer without demethylation. Regioselective Mitsunobu reactions with allyl or propargyl alcohols proceed at 0 °C in THF without affecting the carboxylic acid, delivering ethers that maintain the acid handle for downstream diversification. This orthogonal reactivity has been utilized in fragment‑based screening cascades where simultaneous modification of the phenol and the carboxylate is scored against a target enzyme.
    Release specifications and reference methods
    ParameterSpecificationTest method
    AppearanceWhite to off‑white powderVisual inspection
    Assay (HPLC)98.0–102.0 % (anhydrous basis)USP <621>, C18 column, 254 nm
    Melting point200–205 °C (decomposition)ASTM E324‑16, capillary method
    Loss on drying≤0.5 % (105 °C, 2 h)USC <731>
    Residue on ignition (sulfated ash)≤0.10 %USP <281>
    Heavy metals (as Pb)≤20 ppmUSP <231> Method II
    Residual solvents (isopropanol)≤5000 ppmUSP <467>, GC‑HS
    Water content (Karl Fischer)≤0.3 %USP <921> Method Ia
    Reactor‑scale experience indicates that the free acid is incompatible with strong oxidizing agents and with primary amines under melt conditions, where salt formation accelerates decarboxylation. During campaign closure, equipment is rinsed with dilute sodium bicarbonate solution to prevent build‑up of insoluble metal carboxylate residues on heat‑exchange surfaces. Storage recommendations derived from accelerated stability studies at 40 °C/75 % RH per ICH Q1A(R2) support a retest interval of 36 months when the material is kept in tight, light‑resistant containers under inert gas.