Likely soluble in common organic solvents like ethanol, dichloromethane
As an accredited 2-((2-Hydroxy-4,5-Dimethoxybenzoyl)Amino)-1,3-Thiazole-4-Carboxylic Acid Methyl Ester factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
Ship the chemical "2-((2 - Hydroxy - 4,5 - Dimethoxybenzoyl)Amino)-1,3 - Thiazole - 4 - Carboxylic Acid Methyl Ester" in properly sealed, corrosion - resistant containers. Ensure compliance with hazardous chemical shipping regulations during transit.
Storage
Store 2-((2 - Hydroxy - 4,5 - Dimethoxybenzoyl)Amino)-1,3 - Thiazole - 4 - Carboxylic Acid Methyl Ester in a cool, dry place away from direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and contamination. Avoid storing near heat sources or reactive chemicals to maintain its chemical integrity.
Free Quote
Competitive 2-((2-Hydroxy-4,5-Dimethoxybenzoyl)Amino)-1,3-Thiazole-4-Carboxylic Acid Methyl Ester prices that fit your budget—flexible terms and customized quotes for every order.
2-((2-Hydroxy-4,5-Dimethoxybenzoyl)Amino)-1,3-Thiazole-4-Carboxylic Acid Methyl Ester is manufactured under an ISO 9001 quality system and complies with relevant regulatory requirements.
COA, SDS/MSDS, and related certificates are available upon request.
For certificate requests or inquiries, contact: sales9@bouling-chem.com.
More Introduction
Why does the 2-hydroxy substituent influence coupling efficiency?
During amide bond formation between 2-amino-1,3-thiazole-4-carboxylic acid methyl ester hydrochloride and 2-hydroxy-4,5-dimethoxybenzoic acid under standard carbodiimide conditions, the free phenolic group competes for the activated ester intermediate. When 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide (EDC) is deployed with 1-hydroxybenzotriazole (HOBt) in anhydrous dimethylformamide at 0–5 °C, HPLC monitoring (USP <621>, Column L1, 254 nm) shows a transient intermediate eluting at relative retention time 1.34 that consumes approximately 12–18% of the acylating species. This byproduct, isolated and characterized as an O-acylated oxybenzotriazole adduct, is not observed when the phenolic hydroxyl is protected as a tert-butyldimethylsilyl ether prior to coupling, confirming competitive acylation at oxygen. Consequently, unprotected coupling yields plateau at 71–74% after 16 h regardless of excess acid, whereas the protected-intermediate route followed by tetra-n-butylammonium fluoride deprotection achieves isolated yields of 88–91% (three validation batches, 500 g scale). The difference becomes analytically significant when residual starting thiazole levels must remain below 0.10 area% for downstream biological testing panels.
A practical workaround that bypasses protecting-group manipulations involves the use of the symmetrical anhydride of 2-hydroxy-4,5-dimethoxybenzoic acid, generated in situ with pivaloyl chloride and triethylamine in tetrahydrofuran at −15 °C. This method, validated on a 20 L jacketed glass reactor with retreat-blade impeller at 180 rpm, suppresses O-acylation competition and delivers crude purity exceeding 96 area% prior to recrystallization. The anhydride approach is preferred when the target compound is destined for further derivatization that requires the free phenol, as it avoids trace silicon residues that can poison palladium-catalyzed cross-coupling steps later in the sequence.
Specification Profile and Batch Release Criteria
Each production batch is released against a panel of compendial and internally validated methods. The compound is hygroscopic; equilibrium moisture content exceeds 0.5 wt% within 30 min of exposure to ambient air at 50% RH, necessitating handling under a dry nitrogen blanket during subdivision. The specification table below reflects data pooled from 12 consecutive cGMP campaigns.
Table 1: Release specifications and typical batch data for BCS-THZ-0421
Batch-to-batch variability in the melting endotherm has been correlated with residual THF content above 300 ppm, which depresses the onset temperature by approximately 1.5 K. Routine drying in a vacuum oven (40 °C, ≤ 10 mbar, 12 h) is therefore stipulated when the compound is intended for melt-phase processing or solid-state formulation.
The unprotected phenol introduces a liability during long-term storage. Forced degradation studies at 40 °C/75% RH open-dish over 4 weeks (ICH Q1A(R2) conditions) revealed 2.8% degradation, primarily through ester hydrolysis to the free acid and subsequent decarboxylation of the thiazole ring, confirmed by LC-MS (ESI⁺, m/z 281.1 corresponds to the decarboxylated amide). Consequently, storage recommendations specify sealed amber vials under argon at −20 °C ± 5 °C, with retest dating of 24 months from manufacture when held under these conditions.
If methyl ester hydrolysis is required post-coupling
Several exploratory medicinal chemistry programs utilizing this intermediate demand the free carboxylic acid at C-4 for subsequent amide library generation. Alkaline hydrolysis with lithium hydroxide monohydrate (2.5 equiv) in tetrahydrofuran/water (3:1 v/v) at 0 °C is selective for the methyl ester over the benzamide linkage, provided the reaction is quenched before internal temperatures exceed 5 °C. At 10 °C and above, competitive cleavage of the exocyclic amide bond accelerates; Arrhenius analysis of the competing hydrolytic pathways indicated a steeper temperature dependence for amide hydrolysis (Eₐ ≈ 72 kJ·mol⁻¹) compared to ester hydrolysis (Eₐ ≈ 48 kJ·mol⁻¹), narrowing the selectivity window as temperature rises. Accordingly, pilot-scale saponifications are executed in jacketed vessels with a ±1 °C control band, and quenched with 1 M hydrochloric acid to pH 2.8–3.2 within 45 min of base addition. The resultant acid precipitates as a microcrystalline solid that is filtered, washed with chilled water, and dried. Typical recovery: 84–89%, with residual starting ester below 0.3 area%.
Direct transesterification to a more hindered ester (e.g., isopropyl, tert-butyl) cannot be performed on this substrate because the phenolic hydroxyl undergoes competitive alkoxide exchange. Published data for this specific configuration is limited, but model studies on 2-hydroxybenzamides suggest that titanium(IV) isopropoxide-mediated transesterification leads to at least 40% O-acylation unless the phenol is masked.
What truly differentiates this building block from the widely available 2-(benzoylamino)thiazole-4-carboxylates is the interplay between the ortho-hydroxyl and the methoxy substituents on the pendant phenyl ring. In standard 2-benzamido derivatives, the amide NH is a solitary hydrogen-bond donor; here, the 2-hydroxy group creates an intramolecular six-membered ring that preorganizes the amide into a conformation where the thiazole sulfur and the amide carbonyl are coplanar. Solid-state packing diagrams show that this preorganization reduces the dihedral angle between the thiazole and phenyl planes from an average of 34° (unsubstituted benzamide) to 8.5°, which has measurable consequences on π-stacking interactions with kinase hinge regions when the fragment is elaborated into ATP-competitive inhibitors. Further, the 4,5-dimethoxy motif enhances solubility in common reaction media (dichloromethane, ethyl acetate) by approximately 1.5-fold relative to the 4-methoxy or unsubstituted analogs, as determined by gravimetric solubility measurement in ethyl acetate at 23 °C: 52 mg/mL for the dimethoxy derivative versus 34 mg/mL for 4-methoxy and 19 mg/mL for the unsubstituted phenyl congener.
Table 2: Comparative solution behavior of thiazole C-4 methyl ester analogs in ethyl acetate at 23 °C
Benzoyl Substituent
Solubility (mg/mL) ± SD
Crystallization propensity (evaporative)
4,5-Dimethoxy-2-hydroxy (BCS-THZ-0421)
52 ± 3
Moderate; forms gels in > 70 mg/mL solutions
4-Methoxy
34 ± 2
High; rapid nucleation
2-Hydroxy (no methoxy)
28 ± 2
Low; requires seeding
Unsubstituted benzoyl
19 ± 1
Very high; precipitates during coupling
These differences become operationally significant during parallel synthesis campaigns: the dimethoxy derivative maintains homogeneous reaction mixtures at concentrations up to 0.25 M in ethyl acetate during acylation chemistries, whereas the unsubstituted analog requires dichloromethane co-solvent to avoid premature precipitation, which can clog multi-needle liquid handler tips in automated library production.
Processing on a twin-screw extruder (Coperion ZSK 18 MEGAlab, L/D 40) for hot-melt extrusion feasibility studies highlighted another behavioral contrast. The dimethoxy-substituted compound, blended with vinylpyrrolidone-vinyl acetate copolymer (Kollidon VA 64) at 15 wt% drug load, exhibited a melt viscosity at 140 °C and 100 s⁻¹ of 420 Pa·s, within the acceptable window for strand pelletization. The 4-methoxy analog under identical conditions produced 580 Pa·s, and the unsubstituted benzoyl derivative generated a phase-separated extrudate with surface roughness Ra exceeding 12 µm, necessitating a processing temperature increase to 160 °C where partial degradation (brown discoloration) initiated.
Storage incompatibility with primary and secondary amines must be observed: even in solid state, co-milling with benzylamine in a Retsch MM 400 mixer mill (30 Hz, 10 min) caused 7.3% conversion to the corresponding benzylamide via transamidation, as quantified by HPLC. This pathway is accelerated in the presence of catalytic imidazole, which forms a reactive acyl imidazolium intermediate with the methyl ester. Users are advised to avoid amine-containing excipients during solid-form screening unless prior compatibility data are generated by DSC (ISO 11357-3) and isothermal microcalorimetry.
When transitioning from gram-scale research quantities to multi-kilogram campaigns, the filterability of the final recrystallized product merits attention. The platelet morphology obtained from ethyl acetate/n-heptane (1:2 v/v) crystallization exhibits a specific cake resistance (α) of 3.8 × 10¹¹ m/kg in a pilot-scale Nutsche filter (Porcelain, 0.25 m² filter area, 10 µm polyethylene frit) at a filtration pressure of 0.5 bar. Adding a slow cooling ramp (−0.1 K/min) between 45–35 °C enlarges the mean particle size (d₅₀) from 38 µm to 72 µm, reducing α to 1.1 × 10¹¹ m/kg and cutting filtration cycle time from 47 min to 16 min. This adjustment is incorporated into the standard operating procedure for all campaigns exceeding 2 kg.