|
HS Code |
742265 |
| Chemical Formula | C4H3NO2S |
| Molar Mass | 129.14 g/mol |
| Appearance | White to off - white solid |
| Solubility In Water | Slightly soluble |
| Melting Point | 192 - 196 °C |
| Boiling Point | Decomposes before boiling |
| Pka Value | Around 3.95 |
| Odor | Odorless |
| Density | 1.51 g/cm³ |
| Stability | Stable under normal conditions |
As an accredited Thiazole-4-Caxboxylicacid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Thiazole - 4 - Carboxylic acid packaged in 1 - kg bags. |
| Shipping | Thiazole - 4 - Carboxylic acid is shipped in sealed, corrosion - resistant containers. Special handling procedures are followed due to its chemical nature. Shipment is via approved carriers, ensuring compliance with safety and regulatory requirements. |
| Storage | Thiazole - 4 - Carboxylic acid should be stored in a cool, dry place, away from direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and exposure to air, which could potentially lead to degradation. Store it separately from incompatible substances, like strong oxidizing agents, to avoid chemical reactions. This storage approach helps maintain its chemical integrity and stability. |
For β-lactam manufacturers operating under ICH Q7 and FDA 21 CFR 211 Current Good Manufacturing Practice for Active Pharmaceutical Ingredients, thiazole-4-carboxylic acid serves as the primary heterocyclic precursor routed toward 2-aminothiazole-4-carboxylic acid, the critical C-7 side-chain acid common to ceftazidime, cefodizime, and fourth-generation cephalosporins. In a production-scale 3,000 L glass-lined batch reactor equipped with a retreat-curve impeller and jacket cooling capable of removing –3.8 kcal/mol exotherm, nitration with mixed HNO₃/H₂SO₄ at a controlled mass ratio of 1:3.2 proceeds with a ΔT envelope not exceeding ±2 °C to suppress the generation of 5-nitro isomer; excursion beyond 7 °C has been documented to cause a 12–18% shift in para/ortho-nitration regioselectivity, leading to off-spec intermediate that fails the USP monograph HPLC purity threshold of ≥99.0% (USP 40-NF 35 related compounds method). The subsequent catalytic hydrogenation over 5% Pd/C (0.8–1.2 kg wet paste per 100 kg substrate) in anhydrous tetrahydrofuran under 3.5–4.0 bar H₂ at 60–65 °C converts the nitro group to the amine, with residual palladium stripped via activated carbon filtration to < 10 ppm per Ph. Eur. 2.4.8. Acylation of the resulting 2-aminothiazole-4-carboxylic acid with chloroacetyl chloride in dimethylacetamide at –5 to 0 °C yields the active side-chain block prior to condensation with 7-aminocephalosporanic acid (7-ACA). Molar addition ratios for the Schiff base formation are maintained at 1.02–1.05 equivalents relative to 7-ACA to drive conversion in the presence of triethylamine scavenger. Experience on isolator-contained product-contact surfaces has shown that residual moisture above 0.3 wt% by Karl Fischer titration during the final ester cleavage step promotes dimerization that can compromise sterility assurance in the finished sterile ceftazidime pentahydrate. Terminal products produced through this route include ceftazidime pentahydrate sterile powder (CAS 78439-06-2), cefodizime sodium (CAS 69712-56-7), and cefquinome sulfate for veterinary parenteral use, all required to meet the bacterial endotoxin limit of < 0.10 EU/mg under USP <85> when intended for injectable dosage forms.How Does Thiazole-4-Carboxylic Acid Mitigate Localized Corrosion in HCl-Based Oilfield Acidizing?When formulating 15% inhibited hydrochloric acid for matrix acidizing of carbonate formations, thiazole-4-carboxylic acid is introduced at 0.5–3.0 wt% of total fluid volume as a heterocyclic adsorption-type inhibitor, often in conjunction with an anionic surfactant intensifier and a cuprous iodide synergist to achieve a tight monolayer coverage on N-80 and L-80 tubing steel. Weight-loss coupon tests conducted per ASTM G31-72 under dynamic flow conditions (60 °C, 4-hour exposure, 1.0 m/s linear velocity on a rotating cylinder autoclave) demonstrate a corrosion rate reduction from 98.2 mm/year (uninhibited) to < 1.5 mm/year at 2.0 wt% loading, with no evidence of pitting when examined under 20× stereomicroscopy per NACE TM0169. A critical operational boundary exists: fluid temperatures exceeding 85 °C in the presence of H₂S partial pressures above 0.05 bar trigger a desorption onset detected via linear polarization resistance monitoring, where inhibitor film breakdown raises the anodic Tafel slope by 38–42 mV/decade within 25 minutes. Field blending at the suction header of a triplex pump skid introduces the inhibitor as a 10% active solution in isopropanol/water to ensure rapid dispersion; batch recirculation for 30 minutes prior to pumping downhole is standard to equilibrate the inhibitor film. Operators note that co-addition with propargyl alcohol-based inhibitors requires a mutual-solvent pre-flush of ethylene glycol monobutyl ether to prevent an immediate precipitation reaction that clogs high-pressure discharge lines downstream of the blender. The final product is a live acidizing fluid pumped at 15–20 bbl/min through 2-7/8-inch coiled tubing into the pay zone, with flowback fluids subject to disposal compliance under OGP Report 2.85/625 for aromatic carbon content. Published data for corrosion inhibition performance in spent acid conditions (pH > 4) remains limited, and separate compatibility testing with mutual solvents is advised when the treatment design stages an ammonium chloride overflush.Heterocyclic Diazo Component in High-Washfastness Disperse DyesDiazotization of thiazole-4-carboxylic acid at 0–5 °C in concentrated phosphoric acid furnishes a diazonium salt that couples with N,N-dialkylaniline derivatives to yield heterocyclic disperse dyes absorbing in the 450–520 nm region, specifically developed for polyester fiber dyeing at 130 °C under high-temperature exhaust methods. The dye synthesis vessel is a jacketed stainless-steel diazotizer with an anchor agitator; sodium nitrite (1.01 molar equivalent) is added below the liquid surface over 45 minutes to avoid nitrous oxide fume evolution. Coupling is conducted at pH 2.5–3.5 on a coupling component mill-base pre-dispersed in 1.5% lignosulfonate solution, resulting in a crude presscake that after reverse-osmosis dewatering achieves 35–40% solids before spray drying. The finished dry dye composition contains 92–95% active dyestuff, 4–6% naphthalene sulfonate dispersant, and 1–2% antifoam, meeting the permissible specific amine levels under REACH Annex XVII and the OEKO-TEX STANDARD 100 Appendix 4 limits for 4-chloroaniline (< 30 mg/kg). Exhaustion trials on a Mathis® laboratory dyeing unit with woven PET fabric at a 10:1 liquor ratio and 2.0% owf dye depth produce dyed samples achieving wash fastness grade 4–5 (ISO 105-C06), light fastness grade 6–7 (ISO 105-B02), and sublimation fastness at 210 °C for 30 seconds with < 10% staining onto adjacent multifiber (ISO 105-P01). The dyestuff is packed into 25 kg PE-lined fiberboard drums and is classified for transport under UN 3077 (Environmentally Hazardous Substance, Solid, N.O.S.) Class 9, PG III when the organic pigment loading exceeds the threshold for ecotoxicity.Bath formulations for architectural aluminum anodizing lines that employ thiazole-4-carboxylic acid-based metal complex dyes in the electrolytic coloring step generally operate at a concentration of 1–10 g/L of the pre-metallized dye complex in deionized water, with the dyestuff added as a 5% stock solution metered through a dosing pump into the 40–50 °C coloring bath. The Al-Mg-Si alloy extrusion (AA 6063-T5) is first anodized in 180 g/L sulfuric acid at 1.5 A/dm² to build a 10–15 µm oxide layer (ISO 7599:2018), then transferred within 60 seconds into the dye bath where the negatively charged thiazole-4-carboxylate ligand-cobalt/chromium complex precipitates electrophoretically within the porous anodic film under an applied AC voltage of 12–16 V (50 Hz). Fastness requirements enforced by EN 12373-14:2000 for UV resistance dictate that the colored anodized surface withstand 500 hours of accelerated weathering per ISO 11341 with a ΔE*ab shift of no more than 3.0 CIE units. Line audits on a 5-ton/day horizontal anodizing plant have identified that exceeding 12 g/L dye concentration without proportional increase of the buffer system (2.5 g/L ammonium acetate) leads to non-uniform dye uptake along the length of 6-meter profiles, manifested as a graduated color value variation of ΔC* > 1.2. The end products are bronze- to black-toned window frames, curtain wall mullions, and architectural cladding panels that must pass the admittance test of ISO 2143:2017 for sealing quality by nitric acid pre-immersion.When Latent Curing Acceleration Is Required in One-Component Epoxy AdhesivesThiazole-4-carboxylic acid incorporated at 0.2–1.0 phr into a dicyandiamide-cure epoxy resin formulation functions as a thermal-latent accelerant that substantially lowers the peak cure exotherm onset from the unaccelerated 188 °C to 142–158 °C when measured by differential scanning calorimetry under 10 K/min ramp (ISO 11357-2:2020). The accelerator is first dissolved in a minimal quantity of dimethylformamide or pre-milled with the liquid epoxy resin component on a three-roll mill to a grind fineness of < 15 µm (Hegman gauge, ASTM D1210), then metered into the resin-hardener-filler masterbatch in a planetary mixer under vacuum. Process engineers on full-scale adhesive dispensing lines for automotive hemming applications report that a loading exceeding 1.2 phr depresses the onset temperature below 135 °C, causing unintended partial cure inside the static mixer nozzle during > 45-second production pauses at 60 °C pre-heat, an effect confirmed by a measured viscosity increase from 45 Pa·s to over 300 Pa·s at 10 s⁻¹. Adhesive formulations designed for bonding galvanized steel to CFRP in body-in-white assembly are validated per ASTM D1002-10 for single-lap shear strength (substrate: 1.2 mm DX51D+Z, bondline 0.25 mm), with accelerated condition (40 °C/95% RH, 21-day) strength retention exceeding 85% of the initial 22 MPa value. Thermal analytical fingerprints confirm that the thiazole-4-carboxylic acid imidazole-like mechanism proceeds via adduct formation with dicyandiamide, releasing a substituted guanidine that initiates epoxy ring-opening at a calculated activation energy of 68–72 kJ/mol (Kissinger method). The operational constraint is absolute humidity during component storage: pre-drying of the accelerator at 50 °C for 8 hours under –0.09 MPa vacuum is mandatory when ambient RH exceeds 60%, as moisture accelerates the formation of free acid dimers that crystallize in the epoxy matrix and nucleate localized fracture zones visible under SEM as 1–3 µm crystalline domains. The end product is a one-component structural adhesive packaged in 310 mL coaxial cartridges or 200 L drum sets for high-volume meter-mix dispensing, supplied with a certificate of analysis referencing ISO 9001:2015 and the specific reactive peak temperature range from the batch DSC trace.Thermal Stabilization of Rigid PVC Profiles: Zinc-Soap SynergismIn rigid PVC extrusion for window main profiles and pipe, thiazole-4-carboxylic acid is applied as a secondary costabilizer within calcium-zinc stabilizer one-packs at a typical addition level of 0.1–0.3 phr, functioning primarily through scavenging of zinc chloride via complexation to delay catastrophic zinc burning that manifests as sudden blackening during the 8–12 minute dynamic heat stability test at 200 °C in a Brabender® Plastograph per DIN 53381-1. The compound is introduced as a 0.05 mm milled powder pre-blended with the Ca/Zn stearate primary stabilizer and calcium carbonate filler in a hot/cool mixer setup (heating to 120 °C, cooling to 45 °C) prior to counter-rotating twin-screw extrusion at a melt temperature of 190–195 °C through a L/D 26 conical screw. Prior plant-scale campaigns on a parallel twin-screw line with a throughput of 350 kg/h observed that omitting the thiazole-4-carboxylic acid component shortened the Congo red stability time from 85 minutes to 38 minutes at 200 °C (ISO 182-1:1990), with notable early pinking occurring within the first 15 minutes of static heat aging. The final extrudates must achieve color hold measured as ΔE < 5.0 against the RAL standard sheet after 30 minutes of thermal load, and the finished product is subject to heavy-metal limits under EU RoHS Directive 2011/65/EU and EN 15346:2014 for recycled content compliance. Commercially, the stabilizer one-pack is supplied in 25 kg PE-lined paper sacks and incorporated into white and woodgrain-foil-faced rigid PVC window profiles (EN 12608-1), soil-waste-vent pipes (EN 1329-1), and cellular foam board. Formulators should note incompatibility with amine-functional co-additives (hindered amine light stabilizers above 0.2 phr), which can complex with the acid functionality and precipitate as a waxy exudate on the die lip plate during runs longer than 4 hours. |
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| Parameter | Thiazole‑2‑carboxylic acid (CAS 141-91-6) |
Thiazole‑4‑carboxylic acid (CAS 1459-95-6) |
Thiazole‑5‑carboxylic acid (CAS 14527-41-4) |
|---|---|---|---|
| Melting point (°C) | 102–104 (no decomposition) | 195–198 (dec.) | 219–221 (dec.) |
| Decarboxylation onset by DSC (°C, 10 °C·min⁻¹, N₂) | ~165 | ~210 | ~230 |
| pKₐ (carboxylic acid, potentiometric, H₂O, 25 °C) | 2.0 ± 0.1 | 3.2 ± 0.1 | 2.8 ± 0.1 |
| Ring‑nitrogen pKₐₕ⁺ (conjugate acid) | ~0.5 | ~1.2 | ~0.8 |
| Water solubility at pH 1.0 (mg·mL⁻¹) | ~1.5 | < 0.5 | ~0.8 |
| Water solubility at pH 7.4 (mg·mL⁻¹) | > 75 | > 50 | > 60 |
| Typical purity range (HPLC, commercial) | 97–99% | 98–99% | 95–97% (less common) |