|
HS Code |
256041 |
| Chemical Formula | C7H10N2O3S |
| Molecular Weight | 202.23 g/mol |
| Appearance | Solid (usually) |
| Physical State At Room Temp | Solid |
| Solubility In Water | Low (usually) |
| Solubility In Organic Solvents | Soluble in some organic solvents |
| Melting Point | Data required |
| Boiling Point | Data required |
| Pka Value | Data required |
| Flash Point | Data required |
As an accredited 2-Isobutyrylaminothiazole-4-Carboxylic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 500g of 2 - Isobutyrylaminothiazole - 4 - Carboxylic Acid packaged in air - tight plastic bags. |
| Shipping | 2 - Isobutyrylaminothiazole - 4 - Carboxylic Acid is shipped in sealed, corrosion - resistant containers. Shipment follows strict chemical safety regulations, with temperature - controlled options if required, ensuring secure transport to destination. |
| Storage | 2 - Isobutyrylaminothiazole - 4 - 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 chemical degradation. Store it separately from incompatible substances, like strong oxidizers or bases, in a well - ventilated storage area. |
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2-Isobutyrylaminothiazole-4-carboxylic acid serves as the core heterocyclic fragment for constructing modern SDHI fungicides based on the pyrazole-4-carboxamide pharmacophore. The thiazole ring is retained in the final active ingredient to modulate lipophilicity and binding to the ubiquinone pocket of mitochondrial complex II. Production of the corresponding acyl chloride intermediate is carried out in 500 L glass-lined reactors using thionyl chloride at 1.3 eq in anhydrous toluene with 0.5% v/v pyridine as catalyst. Exotherm management is critical: dosing the chlorinating agent above 45°C leads to rapid gas evolution and batch losses exceeding 8% through foaming into the overhead condenser. Pre-distillation of the freshly generated acid chloride under reduced pressure (1.2 kPa, jacket temp 80°C) removes sulfur dioxide and excess reagent. The distillate is introduced dropwise into a precooled (-5°C) solution of the pyrazol-4-amine coupling partner in dichloromethane, with in-line FTIR monitoring the disappearance of the carbonyl chloride peak at 1790 cm⁻¹. The stoichiometric ratio is maintained at 1.02:1 (acid chloride to amine) to ensure consumption of the amine while avoiding diacylation. Post-reaction neutralization is performed with 8% aqueous sodium bicarbonate, and the organic layer is concentrated to incipient crystallization. The crude amide intermediate typically exhibits HPLC purity of 94–97%; recrystallization from isopropanol/water (3:1) elevates purity to 99.5% as required for the subsequent amination step. Regulatory compliance follows the FAO Specification Manual (2016) for technical-grade active ingredient synthesis intermediates. Batch homogeneity is verified under OECD 21 guidelines for physico-chemical properties. Residual thionyl chloride and its disproportionation products must be below 50 ppm total sulfur species as determined by ion chromatography with conductivity detection. Waste streams from the aqueous quench, containing sulfurous acid and pyridine hydrochloride, are neutralized with 30% NaOH to pH 8.5 before biotreatment in a dedicated MBBR system. The final SDHI fungicide product containing the thiazole fragment achieves field rates of 50–100 g ai/ha against Septoria tritici. Controlled Acylation in the Construction of HIV-1 Protease Inhibitor ScaffoldsThe compound is activated as its N-hydroxysuccinimide ester to assemble a hydroxyethylamine transition-state isostere under cGMP conditions. The carboxylic acid functionality is coupled with NHS using EDC·HCl in anhydrous dimethylformamide at 0–5°C. A molar ratio of acid:EDC:NHS of 1:1.05:1.2 is employed, with 0.05% w/v dibutylhydroxytoluene added to suppress radical side reactions. Activating the acid below -10°C is counterproductive; it slows O-acylisourea formation redundantly and extends processing beyond the permitted hold time under ICH Q7 interim stages. After 45 min of activation, the free amine of the hydroxyethylamine intermediate dissolved in precooled DMF is added via a calibrated metering pump at a rate ensuring internal temperature stays below 2°C. During the coupling, off-line IPCs track unreacted amine by a fluoran-based colorimetric stain, with a conversion threshold of >99.8% required before quench. The batch is then partitioned between ethyl acetate and 5% w/v citric acid at 10°C to remove N-hydroxysuccinimide and urea by-products. The organic extract is washed with 3% sodium bicarbonate and 20% brine sequentially, dried over magnesium sulfate, and concentrated in a wiped-film evaporator at 30°C and 0.5 kPa. The resulting foam solid is slurried in diisopropyl ether to yield the crystalline protected isostere with a typical purity of 99.0% by HPLC. All unit operations are conducted in 316L stainless steel portable vessels qualified under ASME BPE-2022 surface finish SF4. Solvent residues are controlled according to USP <467> procedure A: class 2 solvent DMF is limited to 880 ppm, while ethyl acetate must not exceed 5000 ppm. A documented in-process risk is O→N acyl transfer of the isobutyryl group when the crude reaction mixture is held for longer than 6 h without acidic workup, generating a structural isomer that co-elutes under standard reversed-phase conditions. The terminal product is registered in the US FDA DMF type II for a protease inhibitor active pharmaceutical ingredient used in combination antiretroviral therapy. What Determines the Coordination Geometry of Thiazole-4-Carboxylate-Based MOFs?The carboxylate and amide functionalities of 2-isobutyrylaminothiazole-4-carboxylic acid act as a ditopic linker capable of forming both hard carboxylate–oxophilic bonds and softer thiazole-N donor interactions. Solvothermal reactions between the ligand and transition-metal nitrates in N,N-dimethylacetamide at 120°C for 48 h in a 23 mL PTFE-lined autoclave (Parr 4748) give a crystalline framework with permanent porosity. The metal-to-ligand ratio is systematically screened between 1:1 and 1:3; a 2:1 ligand-to-metal stoichiometry consistently produces the highest crystallinity as confirmed by PXRD with a full width at half maximum below 0.12° 2θ at the 001 reflection. Cooling rate after isothermal heating is controlled at 0.3°C/min using a programmable oven; faster ramps lead to a mixture of phase-pure and an amorphous gel fraction that collapses upon activation. Supercritical CO₂ activation (using methanol as co-solvent, 80 bar, 40°C, 4 h exchange followed by dynamic flow) is mandatory for preserving pore architecture above 80% of the theoretical accessible volume. Thermal activation under vacuum at 150°C results in irreversible pore shrinkage of approximately 18% as measured by nitrogen adsorption isotherms. The framework shows directional flexibility of the isobutyryl moiety, mediating a gate-opening phenomenon at p/p₀ ~0.15 in CO₂ adsorption at 273 K. Table 1 summarizes comparative porosity data for three isostructural variants.
Purity of the ligand prior to MOF synthesis is validated by ¹H NMR (DMSO‑d₆, δ 12.80 s, COOH) and Karl Fischer titration (<0.05% H₂O). The chemical stability of the framework in aqueous media is limited: sustained crystallinity is retained only in deionized water at pH 5–8 for 24 h; below pH 4 the linker undergoes amide hydrolysis with an observed half-life of 6.5 h at 25°C. This operational boundary restricts its application to gas-phase separations and non-aqueous sensing rather than water treatment. When applied as a selective hydrocarbon adsorbent in a mixed-gas breakthrough column at 298 K, the Zn-based MOF exhibits 3.2 mmol/g of ethylene uptake under dynamic conditions, making it a candidate for olefin/paraffin screening in refining applications under ASTM D1946 gas analysis protocols. When Isobutyryl Group Retention Enhances Melt Processability in Semi-Aromatic PolyamidesMelt condensation of 2-isobutyrylaminothiazole-4-carboxylic acid with hexamethylenediamine and adipic acid produces a segmented copolyamide where the bulky thiazole-bearing unit acts as a chain extender and crystallinity disruptor. The thiazole-4-carboxylic acid does not require protection during nylon salt preparation; it is slurried in deionized water with a 5% molar excess of diamine to form a clear salt solution at 50°C. The salt is concentrated to 60% solids in a wiped-film evaporator at 90°C and transferred to an autoclave for prepolymerization at 230°C under a 1.7 MPa steam blanket. The isobutyryl substituent provides enough steric hindrance to suppress premature cyclization of the thiazole ring, a competing pathway that generates non-polymerizable 3-aminoisothiazole by-products. With end-capping using acetic acid at 0.8 mol% based on total monomers, the inherent viscosity η_inh reaches 1.4 dL/g as measured in 96% sulfuric acid at 25°C per ISO 307:2019. Solid-state polymerization (SSP) follows to raise molecular weight while avoiding thermal discoloration observed in the melt phase above 250°C. The prepolymer granules are predried in a tumble dryer with a dew point of -40°C (-15°C minimum for copolyamide handling) for 12 h at 100°C, then heated stepwise to 215°C under a vacuum of 30 Pa for 16 h. The resulting resin is injection-molded using a 30 mm L/D 25 reciprocating screw at a melt temperature of 245°C and a mold temperature of 80°C. Tensile properties per ASTM D638-14 type V specimens give a yield strength of 72 MPa and an elongation at break of 28%, compared to 55 MPa and 7% for the unmodified PA66 homopolymer. Notched Izod impact at 23°C (ASTM D256) improves to 95 J/m. Regulatory compliance for food-contact use is evaluated under EU 10/2011 and FDA 21 CFR 177.1500; the isobutyrylaminothiazole monomer is a new substance requiring specific migration testing with detection limits below 0.01 mg/kg in 3% acetic acid and 10% ethanol simulants. A notable limitation arises when the copolyamide is co-extruded with barrier layers containing free primary amines; the isobutyryl amide linkage undergoes slow interchain aminolysis at processing temperatures above 260°C, generating erratic melt viscosity fluctuations measured by online rheometers. Hence, the material is restricted to mono-resin injection-molded articles at a maximum processing window of 240–250°C. Cathodic Polarization Additives for Acid Copper Plating BathsA dilute additive incorporating 2-isobutyrylaminothiazole-4-carboxylic acid is introduced into acid copper sulfate electrolytes for printed circuit board through-hole plating. The compound is pre-dissolved as a 2.5% w/w stock solution in warm deionized water (45°C) with 0.1% v/v sulfuric acid to maintain solubility. The working concentration in the plating bath ranges from 0.2 to 0.8 g/L, depending on the carrier–brightener balance. In combination with sodium 3-mercapto-1-propanesulfonate (MPS) and a polyalkylene glycol suppressor of molecular weight 6000 g/mol, the thiazole carboxylic acid shifts the cathodic onset potential by approximately -45 mV at a current density of 2 A/dm², as determined by cyclic voltammetric stripping using a Pt rotating disk electrode at 2000 rpm. Hull cell tests (267 mL, 2 A, 10 min) demonstrate that the additive eliminates burn in high-current-density regions (> 4 A/dm²) and produces a fine-grained, semi-bright deposit across a range from 0.5 to 6 A/dm². The plating electrolyte is maintained at 25°C with vigorous air agitation and continuous carbon treatment at 0.5 g/L to remove organic decomposition products. Chloride ion concentration is held at 70 ppm via silver chloride monitor-controlled dosing; deviation below 40 ppm leads to loss of leveling, while above 110 ppm triggers surface pitting. Bath qualification follows IPC-4552A for electronics-grade electroplating. Metallic impurity limits for iron and nickel are 10 ppm and 5 ppm respectively, measured by ICP-OES. Thermal stress testing of plated through-holes per IPC-TM-650 2.6.8 shows no corner cracking after 10 s of solder float at 288°C when the additive is used within its replenishment regime of 12 mL/L per 1000 Ah. A persistent operational concern is the photochemical instability of the thiazole-amide additive under ambient light; exposed stock solutions develop a faint yellow tint within 72 h accompanied by 8% loss in suppressor performance. All transfer lines and storage tanks are therefore constructed from opaque HDPE with nitrogen blanketing. Incorporation of 2-isobutyrylaminothiazole-4-carboxylic acid into peptidomimetic oligomers via Fmoc-strategy solid-phase synthesis yields backbone-modified probes for studying aspartyl protease mechanisms. The compound is loaded onto 2-chlorotrityl chloride resin (1.6 mmol/g) in the presence of DIEA (4 eq) in dichloromethane, with a coupling density of 0.8 mmol/g targeted to preserve steric accessibility. Chain elongation employs HATU (3.8 eq) and DIEA (8 eq) in DMF at 45°C for double couplings of 3 h each. The steric hindrance imposed by the isobutyryl side arm necessitates extended activation compared to canonical Fmoc-amino acids; incomplete incorporation is detected by Kaiser test monitoring until the fourth resin wash, after which a negative result is mandatory. Cleavage from the resin is performed with a 95% TFA, 2.5% triisopropylsilane, 2.5% water cocktail over 3 h with continuous argon bubbling to avoid methionine oxidation in the peptide chain. Crude peptides are precipitated in cold diethyl ether at -20°C and purified by preparative reversed-phase HPLC using a C18 column and a 0.1% TFA water/acetonitrile gradient. Final product purity of >98% by HPLC at 215 nm is documented per Analytical Biochemistry guidance for in-vitro bioassay reagents. The structurally rigid thiazole linker reduces entropic penalties in enzyme binding studies, but exposes an incompatibility: prolonged exposure to 20% piperidine in DMF during iterative Fmoc removal beyond 20 min cycles partially cleaves the exocyclic isobutyryl amide, leading to an impurity with +18 Da mass shift detectable by ESI-MS. Synthesis protocols therefore limit cumulative piperidine treatment to 60 min for sequences containing this building block. |
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| Compound | Solubility in DMSO (mg/mL, 25 °C) | Solubility in DMF (mg/mL, 25 °C) | Aqueous solubility pH 7.4 buffer (µM) | LogD7.4 |
|---|---|---|---|---|
| 2-Aminothiazole-4-carboxylic acid | 18.5 | 12.1 | 980 | −2.1 |
| 2-Acetamidothiazole-4-carboxylic acid | 47.3 | 39.8 | 410 | −1.3 |
| 2-Isobutyrylaminothiazole-4-carboxylic acid | 52.0 | 44.6 | 175 | −0.4 |
| 2-Pivaloylamidothiazole-4-carboxylic acid | 38.2 | 31.7 | 64 | +0.6 |