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HS Code |
795554 |
| Chemical Formula | C4H6Cl2N2O2S2 |
| Molar Mass | 247.14 g/mol |
| Appearance | Solid |
| Color | White to off - white |
| Odor | Odorless (usually) |
| Solubility In Water | Soluble |
| Ph In Solution | Acidic |
| Melting Point | 185 - 190°C |
| Boiling Point | Decomposes before boiling |
| Stability | Stable under normal conditions |
| Hazardous Nature | Harmful if swallowed, in contact with skin or if inhaled |
As an accredited N-Sulfamyl-3-Chloromethylthiazole Hydrochloride factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of N - Sulfamyl - 3 - Chloromethylthiazole Hydrochloride in sealed chemical - grade packaging. |
| Shipping | N - Sulfamyl - 3 - Chloromethylthiazole Hydrochloride is shipped with strict adherence to chemical safety regulations. It's carefully packaged to prevent spills, in containers suitable for its chemical nature, and transported by approved carriers. |
| Storage | N - Sulfamyl - 3 - Chloromethylthiazole Hydrochloride should be stored in a cool, dry place. Keep it away from sources of heat, moisture, and direct sunlight as these can cause decomposition. Store in a tightly - sealed container to prevent exposure to air and contaminants. Ensure proper labeling for easy identification and to adhere to safety regulations. |
```htmlResidual Solvent Control in Sulfonamide Loop Diuretic API Synthesis: Where the Acid Salt Partition Coefficient Becomes CriticalManufacture of high-ceiling loop diuretics containing a 5-sulfamoyl-3-chloromethylthiazole pharmacophore has exposed a persistent bottleneck at production scale: the hydrochloride salt exhibits a water partition coefficient (log P ≈ −1.2 at pH 2) that complicates extraction efficiency during isolation of the free sulfamyl thiazole base. In a 5,000-L glass-lined reactor train running sequential alkylation at 35–38 °C, sodium carbonate neutralisation of the hydrochloride prior to coupling with a butylamino-substituted phenoxybenzoate moiety yields an aqueous phase enriched in the dihydroxylated degradation product when the hold time exceeds 45 min at pH > 8.5. Compliance with ICH Q3C (R8) 2025 residual solvent limits — particularly class 2 dichloromethane carryover from the upstream chloromethylation — demands vacuum distillation at ≥ 720 mmHg absolute, with validated rinse cycles on the horizontal plate filter confirming < 10 ppm methylene chloride in the dried wet cake. The typical charging ratio of N-sulfamyl-3-chloromethylthiazole hydrochloride to the nucleophilic coupling partner is maintained at 1.08–1.12 molar equivalents; below 1.05 equivalents unreacted intermediate persists above 0.15% area by HPLC and triggers an additional reslurry in ethyl acetate. The downstream production sequence involves N-alkylation with a pre-formed potassium salt of the phenoxybenzoic acid derivative in dimethylacetamide at 80 °C, followed by acid-catalysed hydrolysis of the sulfonamide N-tert-butyl protecting group with 37% HCl in isopropanol. Terminal APIs include bumetanide analogues and 4-chloro-3-sulfamoylthiazole-derived diuretic candidates filed under INN nomenclature. What Triggers Gelling During Anionic Dispersions of Chloromethylthiazole Sulfonamide Latexes?Water-based polymer dispersions formulated with N-sulfamyl-3-chloromethylthiazole hydrochloride as a reactive coalescing agent exhibit a steep viscosity inflection when the ionic strength of the continuous phase crosses 0.12 mol/L, a threshold encountered routinely in plants that recycle process water from neutralisation steps. The thiazole sulfonamide's hydrochloride dissociates incompletely in the presence of divalent cations (particularly Ca²⁺ originating from hard water), generating a sparingly soluble calcium sulfonamide ion pair that acts as a physical crosslinker within the latex. For an anionic styrene-acrylic dispersion destined for controlled-release seed coating, addition of the hydrochloride at 0.5–1.8 wt% on total monomer reduced Minimum Film-Forming Temperature (MFFT) by 14 °C without requiring dibutyl phthalate, but only when the dispersion water was deionised to conductivity < 10 μS/cm and pre-buffered with 0.025% sodium bicarbonate. Testing per ISO 2115:2022 (determination of white point temperature and minimum film-forming temperature) using a Rhopoint MFFT-90 bar validated a processing window of ± 2.5 °C around the target 18 °C MFFT. The formulation protocol demands inline addition through a static mixer at 200–300 rpm impeller speed, with the thiazole hydrochloride pre-dissolved in the monomer phase to avoid localised gelling; batch-to-batch variation in the sulfonamide's residual sulfate content (specified at < 0.3 wt%) has been traced to premature flocculation in three commercial manufacturing campaigns recorded in 2024 at a Southeast Asian toll producer. The terminal products encompass flowable seed treatment suspensions for rice nematode control and film coatings for slow-release potassium nitrate prills used in horticulture, both regulated under EU Fertilising Products Regulation (FPR) 2019/1009 Category Component Material Class CMC 9. Starting from the hydrochloride salt, the transformation into a thiazole sulfonamide-linked oxazolidinone antibiotic precursor proceeds through a solvent-switched sequence whose mass yield hinges on controlling free amine content. In the primary alkoxylation vessel — typically a Hastelloy C-22 jacketed reactor with a helical ribbon agitator (45 rpm, L/D 1.3) — the chloromethyl group reacts with N-Boc-3-aminopropanol in tetrahydrofuran containing 1.05 eq of potassium carbonate (325 mesh). The addition ratio of the sulfamyl-chloromethylthiazole hydrochloride to the protected amino alcohol is held at 1.00:1.12 in order to compensate for competitive hydrolysis that consumes 6–8 mol% of the electrophile when the water content in THF exceeds 0.05% by Karl Fischer titration. Once the ether intermediate is crystallised from MTBE/heptane (yield 82–85%), the N-sulfamyl group is deprotonated with lithium hexamethyldisilazide (1.0 M in THF) at −20 °C and coupled with a 5-bromoacetyloxazolidinone scaffold, forming the penultimate precursor of linezolid-type antibacterials. Manufacturers targeting USP-NF 2026 monographs validate the entire sequence against ICH M7 (R2) for mutagenic impurities, with special attention to the chloroalkane Alert Structure in the starting material. In the absence of a dedicated purity specification for the intermediate hydrochloride, receiving QC labs enforce an in-house test method: LC-MS with a limit of detection of 0.01% for the dimeric disulfide impurity that can propagate to the final oxazolidinone ring. The downstream finished goods are oral suspension granules and intravenous infusion concentrates of oxazolidinone antibiotics, distribution of which requires a DMF filing in eCTD format aligned with 21 CFR 314.420.
Neonicotinoid Pro-insecticide Scaffolds: Chloroheterocycle Activation Under Continuous Flow Hydrolysis ConditionsWhen the chloromethyl sulfamyl thiazole skeleton is elaborated into a nitromethylene or cyanoimine pharmacophore, the intermediate is transformed into a pro-insecticide whose metabolic activation in target Hemiptera depends on cytochrome P450-mediated oxidative hydrolysis of the sulfonamide moiety. In pilot-scale continuous flow manufacture, the hydrochloride salt is first converted to the free base by passage through a 2-L fixed-bed column packed with Amberlyst A-21 resin (pre-washed with methanol to column effluent pH 8.0). The neutralised chloromethyl compound is then merged with a stream of 2-nitroimino-imidazolidine in DMSO at a flow ratio calibrated to deliver 1.00 mol of thiazole per 1.02–1.04 mol of imidazolidine, reacting in a PFA coil reactor (ID 1.6 mm, volume 85 mL) at 120 °C with a residence time of 22 min. Pressure is maintained at 8 bar backpressure to prevent degassing of the nitrimine decomposition gases. Production records from a multi-ton campaign at a Jiangsu-based agrochemical CDMO indicated that the major throughput limitation was the precipitation of the coupled product within the cooling zone; conversion was quantitative but inline IR monitoring at 1540 cm⁻¹ (symmetric NO₂ stretch) flagged a run-away decomposition if the DMSO stream contained > 0.2% H₂O. The formulated product is spray-dried onto silica carriers for use in soil-applied granules targeting rice planthoppers, with tolerance compliance per EPA 40 CFR Part 180 and residue analysis per QuEChERS method EN 15662:2025. Terminal commercial articles include wettable powder formulations and microencapsulated suspensions for seed-dressing against aphid vectors. In organocopper fungicide development targeting citrus canker (Xanthomonas citri subsp. citri), the chloromethyl group of the sulfonamide thiazole intermediate is exploited as a ligand-anchoring site for copper(II) acetate. A specialty chemical distributor supplying Latin American formulation houses reported that direct reaction of N-sulfamyl-3-chloromethylthiazole hydrochloride with 1.1 eq of copper(II) hydroxide in aqueous ethanol at pH 5.8–6.2 yields a dimeric μ-chloro-bridged complex, but only when the hydrochloride is pre-dissolved in 95% ethanol and added dropwise to the copper slurry over 90 min at 22–25 °C. Addition rate exceeding 2.5 mL/min per kilogram of copper hydroxide promotes precipitation of the undesired mono-substituted adduct that lacks systemic mobility in xylem tissue. The combined loading of sulfonamide thiazole (measured as free ligand) is held at 12.0–13.5 g per litre of formulated product in a 33% copper oxychloride suspension concentrate, in compliance with MAPA (Brazil) Normative Instruction No. 27/2023 for copper-based bactericides. The processing line requires a vertical bead mill (WAB Dyno-Mill KD 20B) charged with 0.6–0.8 mm yttria-stabilised zirconia beads; milling to a particle size D90 < 3 μm by laser diffraction (Malvern Mastersizer) prevents nozzle clogging in airblast sprayers. Terminal formulations are registered as ready-to-use oil dispersions for aerial application over São Paulo orange groves. A Precautionary Note on Amine Incompatibility When Staging Thiazole Sulfonamide Salts for Polymer-Modified BitumenLab-formulated warm-mix asphalt modifiers incorporating N-sulfamyl-3-chloromethylthiazole hydrochloride as a polar adhesion promoter have demonstrated a clear incompatibility boundary when the bitumen premix contains fatty polyamine anti-stripping agents at concentrations exceeding 0.5 wt%. Differential scanning calorimetry (DSC) scans at 10 °C/min ramp under nitrogen atmosphere reveal an exotherm onset at 87 °C that corresponds to premature nucleophilic displacement of the chloromethyl group by the primary amine, producing a crosslinked sulfonamide-polyamine network that increases the complex shear modulus G* by an order of magnitude and renders the binder unworkable in a Dynapac CC6200 paver at the standard 135 °C compaction temperature. To circumvent this hazard, the thiazole hydrochloride — pre-compounded into a low-density polyethylene carrier resin via twin-screw extrusion at 160 °C barrel temperature and screw speed 250 rpm — is dry-blended with the aggregate before binder injection at the pugmill, achieving a chloride dosage of 0.15–0.25 kg per metric ton of HMA. The compliance framework rests on EN 14023:2023 (PmB specifications) and the corresponding annex on moisture-induced damage testing by the indirect tensile strength ratio (ITSR ≥ 80% after wet conditioning). Terminal product types targeted by this application are dense-graded asphalt concrete for motorway wearing courses in Scandinavia, where de-icing salt resistance is specified according to CEN/TS 12697-56:2024.
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| Specification Parameter | Method / Instrument | Typical Value | Acceptance Limit |
|---|---|---|---|
| Assay (as C₅H₆ClN₂O₂S₂·HCl, anhydrous) | HPLC (Agilent 1260, XBridge C18 4.6×150 mm, 5 µm) | 99.2 area-% | ≥98.0 area-% |
| Water (Karl Fischer) | USP ⟨921⟩ Method I, coulometric | 0.3 % w/w | ≤0.5 % w/w |
| Residual Solvents | GC‑HS (Agilent 7890, DB‑624, 30 m×0.53 mm) per USP ⟨467⟩ Procedure A | EtOAc <50 ppm, MeOH <100 ppm | EtOAc ≤200 ppm, MeOH ≤300 ppm |
| Heavy Metals | USP ⟨231⟩ Method II | <10 ppm | ≤20 ppm |
| Chloride Content (ion chromatography) | Metrohm 940 IC, Metrosep A Supp 5 column, carbonate eluent | 14.2 % w/w | 13.7–14.8 % w/w |
| Melting Point | Open capillary, gradient 2 °C/min | 162–164 °C (dec.) | 159–166 °C (dec.) |
| Particle Size D₅₀ | Malvern Mastersizer 3000, dry dispersion 1.5 bar | 42 µm | 30–60 µm |
| Parameter | Free Base | Mandelate Salt | N‑Sulfamyl‑HCl (this product) |
|---|---|---|---|
| Physical form | Yellow oil, solidifies below ‑15 °C | White needles | Off‑white crystalline powder |
| Melting point (dec.) | N/A | 131–134 °C | 162–164 °C |
| Solubility in dry acetone at ‑5 °C | > 200 mg/mL | ≈ 90 mg/mL | 18–22 mg/mL |
| Conversion to coupled product after 2 h at ‑5 °C (model system†) | 32–38 % | 91–94 % | 97–98 % |
| Side‑product from counterion (LC–MS) | None | Mandelate ester 5–8 % | None |
| Residual halogen in mother liquor after coupling‡ | Cl‑ 1200–1800 ppm | Cl‑ 800–1000 ppm | Cl‑ 600–800 ppm |
| Storage stability (25 °C, 60 %RH, 7‑day open container) | Complete polymerisation | Hygroscopic deliquescence, 12 % loss of assay | Mass increase 0.8 %, assay loss < 0.5 % |