|
HS Code |
385788 |
| Chemical Formula | C4H6ClN3S |
| Molar Mass | 163.63 g/mol |
| Appearance | Solid |
| Color | White to off - white |
| Odor | Odorless (usually) |
| Solubility In Water | Soluble |
| Melting Point | 230 - 235 °C |
| Purity | Typically high purity in commercial products |
| Ph | Acidic in aqueous solution |
| Stability | Stable under normal conditions |
As an accredited 2-Thiazolecarboxamidine Hydrochloride factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 2 - Thiazolecarboxamidine Hydrochloride in a sealed, chemical - resistant bag. |
| Shipping | 2 - Thiazolecarboxamidine Hydrochloride is shipped in accordance with strict chemical transport regulations. It's carefully packaged to prevent leakage, in containers suitable for its properties, and transported by carriers experienced in handling such chemicals. |
| Storage | 2 - Thiazolecarboxamidine Hydrochloride should be stored in a cool, dry place, away from direct sunlight. Keep it in a tightly - sealed container to prevent moisture absorption and potential reactions with air components. Store it separately from incompatible substances to avoid chemical interactions. Ideal storage temperature is within the range of 2 - 8 °C if long - term stability is required. |
Why Is Controlling Residual Methanol Below 500 ppm Imperative Prior to Amide Bond Formation?The methoxime-substituted aminothiazole side chain employed in fourth-generation cephalosporins—most notably the pivoxil ester prodrugs of cefditoren and cefcapene—is assembled from 2-thiazolecarboxamidine hydrochloride through a heterocyclization–oximation sequence that demands exceptionally low protic solvent carry-over. In a representative kilo-lab campaign, the free amidine is liberated from the hydrochloride salt with 2.05 molar equivalents of triethylamine in anhydrous N,N-dimethylformamide at –5 °C to 0 °C under nitrogen sweep. To this stirred suspension, 1.03 equivalents of methyl 4-chloro-3-oxobutyrate are metered over 90 minutes while maintaining internal temperature below 5 °C. The exothermic Hantzsch-type ring closure generates methyl 2-(2-aminothiazol-4-yl)acetate. After aqueous work-up, the crude ester is isolated by vacuum distillation on a wiped-film evaporator operating at 2 mbar jacket temperature 120 °C. Oximation with methoxyamine hydrochloride at pH 4.5–5.0 in a methanol-water mixture introduces the critical (Z)-2-(2-aminothiazol-4-yl)-2-methoxyiminoacetyl moiety. However, residual methanol must be driven below 500 ppm as determined by headspace GC–FID (USP <467> Class 2 solvent limits) before the subsequent mixed-anhydride coupling with 7-amino-3-vinylcephalosporanic acid (7-AVCA). Above this threshold, methanolysis of the mixed anhydride competes with acylation, depressing coupling yield to below 60% and generating an N-acetyl impurity tracked at RRT 1.33 by HPLC (column: YMC-Pack ODS-A, 4.6 × 150 mm, 5 µm; mobile phase: phosphate buffer pH 3.2/acetonitrile gradient). Drying is therefore executed in a double-cone rotary vacuum dryer at 55 °C, 10 mbar for 48 h with intermittent nitrogen bleeding. Batch discharge is performed inside an isolator maintaining relative humidity below 30% RH; the liberated anhydrous side-chain acid is hygroscopic and undergoes hydrolysis with a rate constant of approximately 0.015 h⁻¹ at 25 °C/60% RH. Compliance with ICH Q7 Chapter 8 for process-related impurities and ICH Q3C Option 2 residual solvent levels is verified on every batch prior to release for GMP coupling. Operational boundaries include absolute exclusion of primary amines—leftover triethylamine hydrochloride must be washed to below 0.1% w/w to avoid premature formation of amidine-amine adducts that accelerate colour body formation in the finished cefditoren pivoxil tablet core.Direct conversion of 2-thiazolecarboxamidine hydrochloride to the free base and immediate condensation with chloroacetyl chloride constitutes the shortest path to 2-chloroacetamidothiazole, a key intermediate for the chloro-thiazole class of insecticides typified by the neonicotinoid structural mimics under development for piercing-sucking pest control. Plant-scale execution on a 2,000 L glass-lined reactor (Pfaudler, retreat-blade impeller) demands strict control of the induction period. A charge of 240 kg of the amidine hydrochloride is suspended in 800 L of dichloromethane at 20 °C and treated with 210 kg of aqueous sodium carbonate (15% w/w) under high-shear agitation at 180 rpm until a clear organic phase is obtained; the water layer is separated within 15 minutes. Delay beyond this window results in turbidity regeneration as the free amidine dimerizes on trace metal contamination from the carbon-steel pipework, a failure mode documented during technology transfer that required installation of DN 50 PTFE-lined spools. After cooling to –10 °C with Syltherm XLT, 1.02 equivalents of chloroacetyl chloride in 150 L dichloromethane are added at a rate controlled to keep the exotherm below –5 °C, typically 4–6 hours. The resulting slurry is neutralised, washed, and concentrated on a climbing-film evaporator to a melt that solidifies on a flaker belt (10 °C cooling water). Subsequent bromination with elemental bromine in acetic acid at 40 °C installs the 5-position reactive handle, generating 2-chloroacetamido-5-bromothiazole. For full-scale FAO/WHO joint meeting on pesticide residues (JMPR) data packages, the critical impurity profile must demonstrate ≤0.15% area of the dibromo congener and ≤0.05% of the dechlorinated acetamide, assayed on a C18 column with a phosphate-methanol gradient and UV detection at 230 nm. The bromo-thiazole core is subsequently elaborated through Suzuki coupling with a substituted phenylboronic acid under Pd(PPh₃)₄ catalysis (0.5 mol%) and K₂CO₃ in a toluene-ethanol-water biphasic system at 80 °C for 8 h to afford the penultimate aniline hybrid for neonicotinoid screening.When Flow Chemistry Overcomes the Exothermic Profile of Diazotization in Thiazole-2-carbonitrile SynthesisThe continuous manufacture of thiazole-2-carbonitrile from 2-aminothiazole—obtained by mild alkaline hydrolysis of the amidine hydrochloride—illustrates how process intensification mitigates a hazardous accumulation of diazonium intermediates. Batch Sandmeyer conditions using aqueous sodium nitrite and copper(I) cyanide demand sub-zero cooling brine and generate a potentially explosive diazonium salt that has caused at least two documented thermal runaways in fine chemical facilities. In a Corning Advanced-Flow G1 silicon carbide reactor (volume 10 mL per plate, 6 plates), a solution of 2-aminothiazole (1.0 M in 4 M HCl) is fed at 2.5 mL/min into a pre-cooled zone at –5 °C, where it contacts a 1.05 equivalent stream of 4.0 M aqueous NaNO₂ at 2.6 mL/min. The generated diazonium stream enters a mixing module after a residence time of 12 seconds, merging with a pre-heated (45 °C) solution of CuCN in aqueous KCN (total cyanide content 3.0 M) at 3.0 mL/min. The substitution reaction is completed within 35 seconds at 45 °C, delivering an outlet stream that is immediately quenched into stirred ethyl acetate. Isolated thiazole-2-carbonitrile purity reaches 99.2% area by GC (HP-5, 30 m × 0.32 mm), with the main impurity being unreacted 2-aminothiazole (0.4%). Material from the batch route typically contains 0.8–1.5% of the symmetrical azothiazole coupling by-product that requires hot toluene recrystallisation to meet the 99.0% min specification for pharmaceutical use. The flow process eliminates this impurity, allowing direct use of the cyano-thiazole as a building block for histamine H₂ receptor antagonist intermediates and for the methoxyimino-acid side chains described previously. In-process analytical technology (PAT) relies on an online ReactIR probe placed in the maturation zone, with continuous monitoring of the diazonium band at 2,260 cm⁻¹ and feedback to the nitrite pump stroke. Changeover from batch to continuous is documented under FDA’s emerging technology program; the control strategy employs a soft-sensor model validated with 3 consecutive lots at target throughput and 2 lots at bracketed residence times to demonstrate robustness across ±15% flow rate perturbation. Incompatibility: the presence of even 0.2% free chloride from insufficient washing of the starting amidine hydrochloride promotes precipitation of CuCl, which clogs the reactor channels within 5 min and requires an immediate acid flush protocol.In the field of medium- to high-energy disperse dyes for polyester, the thiazole nucleus serves as a strong electron-withdrawing module that deepens shade and improves light-fastness when coupled to substituted aniline-based diazo components. Condensation of 2-thiazolecarboxamidine hydrochloride with ethyl bromopyruvate in ethanol at reflux (78 °C, 8 h) yields ethyl 2-aminothiazole-4-carboxylate. After hydrolysis of the ester with 6 M NaOH at 60 °C, the carboxylic acid is converted to the acid chloride for Friedel-Crafts acylation of N-ethyl-N-cyanoethylaniline, but more commonly the amidine intermediate itself is exploited directly. Treatment with nitrous acid (NaNO₂/HCl, 0–5 °C) transforms the amidine into the corresponding thiazole-2-diazonium salt, which couples with N,N-diethyl-m-toluidine under pH 4.0–4.5 controlled by sodium acetate buffer. The resultant monoazo dye exhibits λmax at 538 nm in DMF and, after spray drying with lignin sulfonate dispersant, provides a rubine shade on polyester with 6–7 light-fastness (ISO 105-B02) and 4 sublimation fastness at 180 °C (ISO 105-P01). To satisfy OEKO-TEX Standard 100 Annex 4, the free aromatic amine release after reductive cleavage must be below the 20 mg/kg detection limit; this is confirmed by LC-MS/MS on every production campaign. A recurring difficulty in scale-up is the generation of a dark, tar-like by-product during diazotization when the agitation speed falls below 150 rpm in a conventional 1,000 L anchor-agitated vessel, leading to hot-spot formation at the nitrite addition point. Switching to a draft-tube circulator with added baffle plate eliminated the defect, improving isolated dye strength to 200% relative to standard (AATCC EP 6).Metal Passivation in Lubricant Additive Packages Through Thiazole-Amidine CoordinationAshless corrosion inhibitors for industrial gear oils derive their activity from the ability of the thiazole-amidine motif to form a five-membered chelate ring with cuprous ions on yellow-metal surfaces. 2-Thiazolecarboxamidine hydrochloride is first neutralised with sodium methoxide in methanol and then treated with 1.0 equivalent of dodecenylsuccinic anhydride (DDSA) at 70 °C for 4 h, yielding N-(thiazol-2-yl)-N′-dodecenylsuccinimidylamidine. The product, after removal of methanol and washing with water to eliminate sodium chloride, is diluted to 45% active content in a Group II base oil (kinematic viscosity 6.3 cSt at 100 °C). Corrosion protection is quantified by the ASTM D130 copper strip test: a 50 mL sample containing 0.5% w/w of the amidine derivative heated at 121 °C for 3 h yields a 1a slight tarnish rating, compared with a 3a for the untreated base oil. Synergistic performance with zinc dialkyldithiophosphates (ZDDPs) requires careful balancing; molar ratios of amidine to ZDDP exceeding 1:3 cause competitive ligand exchange that liberates free thiol fragments detected by ICP-OES as soluble copper at 120 ppm after the sequence IVA test (ASTM D8079). Industrial blending is conducted in a multi-stage in-line high-shear mixer (IKA Dispax-Reactor DR) operating at 3,000 rpm with recirculation. Lubricant formulators must ensure the amidine derivative content does not drop below 0.3% in the finished gear oil, because a steep decline in anti-wear protection occurs at lower treat rates due to depletion kinetics in the elastohydrodynamic contact zone. REACH registration dossiers for this substance class require a predicted no-effect concentration (PNEC) in freshwater of 0.023 mg/L derived from a chronic Daphnia magna reproduction test (OECD 211).For aldehydes lacking a strong chromophore—common in steroid hormone metabolites and prostaglandin intermediates—2-thiazolecarboxamidine hydrochloride acts as a selective derivatization handle that installs a thiazoline ring with high electrospray ionization efficiency. The reaction is carried out in a biphasic mixture of 0.5 mL ethyl acetate and 0.3 mL phosphate buffer (pH 8.0): 100 µL of biological extract containing the aldehyde analyte is combined with 50 µL of 0.1 M amidine reagent in water and shaken at 60 °C for 30 min. The thiazoline derivative partitions into the organic layer, which is concentrated under nitrogen and reconstituted in 100 µL acetonitrile/water (50:50) for LC-MS/MS analysis. On a Waters XBridge C18 column (2.1 × 50 mm, 3.5 µm) with a gradient of 0.1% formic acid in water and acetonitrile, the MRM transition typically exhibits a precursor ion [M+H]⁺ and a characteristic product ion at m/z 126 reflecting the thiazolinium fragment. Lower limits of quantification (LLOQ) in human plasma for 17β-estradiol metabolites regularly reach 10 pg/mL using this method, compared with 50 pg/mL for underivatized detection. Matrix effects, assessed by post-column infusion of the neat derivative (EMA EMEA/CHMP/EWP/192217/2009, Rev. 1), must not exceed 15% ion suppression exceeding which a stable isotope-labelled internal standard becomes mandatory. The hydrochloride salt is preferred over the free base solely for weighing accuracy: the free base sublimes slowly at room temperature under high vacuum, causing up to 3% mass loss within a 2 h weighing window. This application is a service-oriented use of the compound rather than a commodity chemical outlet; demand tracks the clinical trial calendar for targeted metabolomic diagnostics rather than commodity procurement cycles.
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| Parameter | Specification | Method/Standard |
|---|---|---|
| Assay (anhydrous, solvent‑free basis) | ≥98.0% | HPLC, UV detection at 254 nm; external standard calibration |
| Melting range | 174–178 °C (decomposition) | Capillary, USP <741> |
| Water content | ≤0.5% w/w | Karl Fischer coulometry; USP <921> Method Ia |
| Residue on ignition | ≤0.1% | Gravimetric, 600 °C, EP 2.4.16 |
| Chloride content (ionic) | 20.8–22.1% | Argentometric titration after ash digestion |
| Related substances – any single impurity | ≤0.3% | HPLC area‑% at 254 nm; reporting threshold 0.05% |
| Heavy metals (as Pb) | ≤10 ppm | USP <231> Method II |
| Reagent | Formula Weight (g·mol⁻¹) | By‑product Solubility Profile | pKₐ of Conjugate Acid* | Typical Reaction Footprint |
|---|---|---|---|---|
| 2‑Thiazolecarboxamidine HCl | 163.63 | 2‑Aminothiazole: highly water‑soluble, removed by acidic aqueous wash | ~8.1 | Mild base (1.1 equiv Et₃N); 0–25 °C for aliphatic amines |
| Benzamidine HCl | 156.61 | Benzonitrile (via dehydration) or benzamide; poorly water‑soluble, requires chromatography or crystallisation | 11.6 | Stronger base or high temperature required; aromatic amine guanylation > 80 °C |
| Acetamidine HCl | 94.54 | Ammonia/ammonium acetate; volatile, pH‑dependent partitioning complicates work‑up | 12.4 | High‑temperature pyrimidine syntheses; competes with self‑condensation |
| 1H‑Pyrazole‑1‑carboxamidine HCl (PyClU) | 146.58 | Pyrazole: volatile but requires THF azeotropic removal for complete clearance | ~8.0 | Requires 2.0 equiv base; effective at 0–25 °C but less regioselective with ambident nucleophiles |