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HS Code |
809780 |
| Chemical Formula | C4H7ClN2S |
| Molecular Weight | 152.63 |
| Appearance | Typically a solid (powder or crystal form) |
| Solubility In Water | Soluble to some extent |
| Melting Point | Specific value would need further literature research |
| Odor | May have a characteristic, likely pungent odor |
| Density | Value requires specific experimental determination |
| Ph In Solution | Acidic due to hydrochloride part |
| Stability | Stable under normal storage conditions away from strong oxidants |
As an accredited 5-Amino-3-Methylisothiazole Hydrochloride factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 5 - Amino - 3 - Methylisothiazole Hydrochloride: 100g in sealed, chemical - resistant packaging. |
| Shipping | 5 - Amino - 3 - Methylisothiazole Hydrochloride is shipped in well - sealed, corrosion - resistant containers. Compliance with chemical transportation regulations is ensured, with proper labeling indicating its nature for safe and smooth transit. |
| Storage | 5 - Amino - 3 - Methylisothiazole 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 exposure to air, which could potentially lead to degradation. Store it separately from incompatible substances, and ensure the storage area is well - ventilated to minimize the risk of hazardous fumes. |
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Among the heterocyclic diazo components employed for the production of alkali-stable, high-washfastness disperse dyes on polyester, 5-amino-3-methylisothiazole hydrochloride has been adopted where the isothiazole sulfur atom contributes to the polarized chromophoric system, shifting the absorption maximum to 450–480 nm in the coupled state. The manufacturing route proceeds via diazotization in 96% sulfuric acid with nitrosylsulfuric acid at a temperature strictly maintained between −3 °C and +2 °C, as the diazonium salt decomposes with a half-life of less than 15 minutes at 5 °C. This thermolability constitutes a key process bottleneck, requiring jacketed glass-lined reactors (Pfaudler WB series, 4000 L) equipped with cascade temperature control and online Raman spectroscopy to monitor diazonium concentration in real time. Coupling is effected onto N-ethyl-3-cyano-4-methyl-6-hydroxypyridone-2 at pH 0.8–1.1, a narrow window where the pyridone exists in its reactive enol form but the diazonium species is not yet hydroxylated; exceeding pH 1.3 results in tar formation rates exceeding 12% w/w of reactor contents. After drowning in ice water and filtration, the press cake is washed with deionized water to conductivity <50 μS/cm, then dried in a vacuum paddle dryer at 60 °C. The crude dye is subsequently formulated into commercial liquid brands using a bead mill (NETZSCH MiniFer) charged with 0.8–1.0 mm yttria-stabilized zirconia beads, and a dispersant blend of sodium lignosulfonate and a naphthalene sulfonate condensate, achieving a primary particle size D90 <2.0 µm for high-temperature exhaust dyeing on polyester at 130 °C in a Thies iMaster H2O jet dyeing machine. The addition ratio in the dye synthesis is nearly stoichiometric: 1.00 mole of 5-amino-3-methylisothiazole hydrochloride (molar mass 150.63 g/mol) yields 1.00 mole of crude dye, translating to approximately 48 kg of the salt per 100 kg final formulated powder dye. Relevant compliance standards for the finished dye include ISO 105-B02 for light fastness (rating >7 for 1/1 standard depth), ISO 105-C06 for washing fastness at 60 °C, and Oeko-Tex Standard 100 (Annex 4) for restricted aromatic amine content, with the heterocyclic amine being non-carcinogenic according to REACH Annex XVII entry 43. The end product is commercialized as a high-energy disperse dye for polyester sportswear and automotive upholstery, often appearing under generic classifications analogous to C.I. Disperse Yellow 114. How is 5-Amino-3-Methylisothiazole Hydrochloride Incorporated into Modern Carboxamide Fungicides?The agrochemical synthesis route to thiazolecarboxamide fungicides, which act through inhibition of mitochondrial respiration complex II, frequently begins with the acylation of the 5-amino group to install the key carboxamide pharmacophore. In a representative sequence, the hydrochloride salt is suspended in anhydrous dichloromethane (water content <200 ppm) and neutralized with 1.2 equivalents of triethylamine at 0–5 °C, followed by dropwise addition of 1.05 equivalents of 2,6-dichlorobenzoyl chloride dissolved in the same solvent over 30 minutes. The reaction mass is maintained under a nitrogen blanket to exclude atmospheric moisture, which would hydrolyze the acid chloride and generate corrosive HCl that can deactivate the catalyst—a risk mitigated by using a Hastelloy C-22 reactor with a scrubbing system. After 2 hours at 10 °C, the batch is washed with chilled deionized water, and the organic phase is subjected to solvent swap from dichloromethane to methanol under vacuum (200 mbar, jacket temperature 45 °C) for the crystallization step. Seed crystals (0.5 wt% based on expected yield) are added when the temperature reaches 40 °C, then cooled linearly at 0.3 °C/min to −5 °C, yielding the amide intermediate as colorless needles with a melting point of 148–150 °C and HPLC purity >98.5 area% (method per CIPAC MT 179, column C18, detection UV 254 nm). The intermediate is a technical grade active ingredient precursor that aligns with FAO Specification 1/TC for technical material, and all analytical procedures are validated according to CIPAC Handbook H. Its subsequent conversion to the final fungicide active substance involves coupling with an aminopyrazole derivative through amide bond formation, liberating HCl that is scavenged by the basic pyrazole, thus requiring no additional base. The end product—a formulated suspension concentrate (SC) containing 200 g/L active ingredient—is sold in global markets for the control of Oomycete diseases in vineyards and potato crops, registered under local regulations such as EU Regulation (EC) No 1107/2009. In continuous wire rod pickling lines operating at HCl concentrations of 15–18 wt% and temperatures of 60–70 °C, 5-amino-3-methylisothiazole hydrochloride acts as a mixed-type corrosion inhibitor via chemisorption at the steel surface. The protonated amino group in acidic media adsorbs onto the cathodic sites, while the isothiazole ring provides π-electron density for anodic inhibition. Typical dosage is 100–200 mg/L in the acid bath, which reduces corrosion rate by 85–92% as per ASTM G31-72 immersion testing on SAE 1010 carbon steel. Industry compliance requires evaluation of inhibitor efficiency via Tafel extrapolation (ASTM G59) and corrosion product cleaning in accordance with ASTM G1-03. The downstream production process involves premixing the hydrochloride salt with a non-ionic surfactant (alkyl polyglucoside) in a metered dosing skid to ensure wetting, then injecting the mixture into the recirculation loop of the pickling bath where inline conductivity probes maintain constant inhibitor depletion rates. End product is clean wire rod with surface roughness Ra <2.5 µm, suitable for subsequent hot-dip galvanizing or cold wire drawing operations. Published inhibitor efficiency values for this specific hydrochloride derivative remain limited in open literature, but experimental data on structurally analogous isothiazole compounds confirm mixed-type inhibition consistent with the Langmuir adsorption isotherm on mild steel. Thiazolo[5,4-b]pyridine Scaffold Preparation: A Key Starting Material under ICH Q7In medicinal chemistry programs targeting bromodomain and extra-terminal (BET) protein inhibitors, the 5-amino group of the raw material is exploited to construct a fused thiazolo[5,4-b]pyridine core through a Friedländer-type annulation with 1,3-diketones. The hydrochloride salt must first be neutralized in situ: it is dissolved in anhydrous DMF and treated with 1.0 equivalent of sodium bicarbonate at 25 °C, allowed to effervesce, and then combined with 1.1 equivalents of pentane-2,4-dione premixed with 0.5 wt% acetic acid as catalyst. The mixture is heated to 80 °C under a nitrogen atmosphere for 8 hours, with conversion monitored by HPLC (C18, acetonitrile/water gradient, UV 254 nm). At this point, the addition ratio of raw material to diketone is critical: excess diketone beyond 1.1 eq leads to formation of the bis-condensed byproduct, while sub-stoichiometric amounts leave unreacted amine that complicates purification. Post-reaction, the crude product is quenched into 10 volumes of deionized water, extracted with ethyl acetate (3 × 500 mL for a 1 kg scale input), dried over sodium sulfate, and concentrated to a slurry that is triturated with cold heptane/ethyl acetate (4:1 v/v) to afford the thiazolopyridine derivative as an off-white solid with a purity of >97 area% by HPLC. All processing steps are executed according to ICH Q7 good manufacturing practice for active pharmaceutical ingredient starting materials, and residual solvent levels are validated against ICH Q3C (R8) limits, particularly for DMF (≤880 ppm) and ethyl acetate (≤5000 ppm) as determined by headspace GC. The end product is a key starting material (KSM) supplied to contract development and manufacturing organizations (CDMOs) under a drug master file (DMF)-ready certificate of analysis, ultimately enabling phase I clinical candidates in oncology indications. When High-Solubility Solvent Dyes Demand Non-Migrating Chromophores for Coil CoatingsIndustrial coil coating lines running polyester-melamine baking enamels on aluminum strip benefit from solvent dyes that combine full solubility in ketonic solvents with migration fastness under cure cycles reaching 250 °C peak metal temperature. 5-Amino-3-methylisothiazole hydrochloride is converted into a 1:2 cobalt complex dye through diazotization of the amine, coupling onto 1-(2-chlorophenyl)-3-methyl-5-pyrazolone, and subsequent metallization. The coupling step employs a molar ratio of diazonium salt to pyrazolone of 1:1.02, maintaining a slight excess of the coupling component to prevent unreacted diazonium accumulation, which can generate gassing during complexation. The wet press cake of the monoazo dye is reslurried in methanol, treated with 0.55 equivalents of cobalt(II) acetate tetrahydrate at 60 °C for 3 hours to achieve full 2:1 ligand-to-metal complexation, monitored by UV-vis spectroscopy for the disappearance of the free ligand band at 430 nm. The resulting metal-complex dye is precipitated by slow addition of water, filtered, washed to conductivity <100 μS/cm, and dried in a vacuum tray dryer at 60 °C to yield a powder that shows solubility exceeding 100 g/L in methyl ethyl ketone and butyl acetate. Color strength and shade consistency are measured against ASTM D2244, and light fastness on coil-coated panels attains a rating of 7–8 according to ISO 105-B02 at 1/1 standard depth. The downstream production process formulates the powder into a 35% liquid concentrate by dissolution in a ketone/ester mixture and filtration through a 1 µm absolute cartridge filter before packaging under nitrogen. REACH Annex XVII restriction entry 72 is not triggered because the cobalt content in the dye concentrate falls below the chronic aquatic toxicity classification threshold, though a full safety data sheet with disclosure of cobalt content is mandatory for downstream users. The final product serves as a transparent yellow-orange colorant for two-coat coil finishes, aluminum cladding panels, and architectural curtain wall systems. |
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5-Amino-3-methylisothiazole hydrochloride (molecular formula C4H7ClN2S, MW 150.63 g/mol) is supplied as a white to off-white crystalline powder with a minimum HPLC assay of 98.0% (area %). The salt form circumvents the oxidative instability inherent to the free amine, enabling long-term storage under inert gas at −20 °C without significant discoloration or dimer formation. This heterocyclic building block serves as a key intermediate in the construction of 1,2-thiazole-containing pharmacophores, particularly in kinase inhibitor programs where the 5-amino group directs electrophilic substitution and metal-catalyzed cross-coupling reactions.
| Parameter | Specification | Test Method |
|---|---|---|
| Appearance | White to off-white crystalline powder | Visual / USP <695> |
| Assay (HPLC, area %) | ≥ 98.0% | EP 2.2.29 (C18, 210 nm) |
| Water (Karl Fischer) | ≤ 0.5% (w/w) | USP <921> Method Ia |
| Residue on Ignition | ≤ 0.1% | USP <281> |
| Heavy Metals (as Pb) | ≤ 10 ppm | USP <231> / ICP-MS |
| Regioisomeric Purity | ≥ 99.5% (5-amino vs. 4-amino) | 1H NMR (δ 6.85 vs 6.92 ppm, DMSO-d6) |
Each lot is accompanied by a certificate of analysis documenting these values. For pharmaceutical intermediate supply chains operating under ICH Q7, residual solvent profiles are also controlled; typical residual solvents (GC headspace) show acetone ≤ 0.5%, ethyl acetate ≤ 0.1%, and dichloromethane ≤ 60 ppm, aligning with USP <467> Option 1 limits.
Trace 4-amino regioisomer contamination, detectable only by high-field 1H NMR or a dedicated gradient HPLC method, drastically alters downstream catalytic behavior. During Buchwald-Hartwig amination using Pd2(dba)3/XPhos, the 4-amino isomer—bearing the primary amine adjacent to the ring sulfur—forms a stable, catalytically inactive palladacycle that arrests turnover at loadings as low as 0.5 mol% contaminant relative to substrate. Process development groups at pilot-plant scale therefore enforce a minimum regioisomeric purity of 99.5% as an incoming raw-material gate, verified by 1H NMR integration of the clearly resolved aromatic singlets. This specification is absent from typical catalogue-grade material and must be expressly requested from custom synthesis providers when the end application involves late-stage functionalization of advanced intermediates.
A condensed comparison of the hydrochloride salt and its free amine clarifies the operational advantages driving formulation choice:
| Property | 5-Amino-3-methylisothiazole HCl | 5-Amino-3-methylisothiazole (free base) |
|---|---|---|
| Physical state at 25 °C | Crystalline solid | Low-melting solid / oil |
| Melting point | 165–168 °C (decomposition) | 35–40 °C |
| Solubility in water | >500 mg/mL (freely soluble) | <10 mg/mL (slightly soluble) |
| Hygroscopicity | Hygroscopic (requires desiccated storage) | Non-hygroscopic |
| Oxidative stability (ambient air) | Stable >6 months at −20 °C under argon | Discolors within 72 h; dimerization observed by LC-MS |
| Typical commercial form | Free-flowing powder, 98–99% assay | Often supplied as a technical-grade oil requiring distillation |
The solid hydrochloride can be stored at room temperature in a well-sealed desiccator for short-term use (≤7 days), but for inventory exceeding one month, 2–8 °C refrigerated storage under argon is mandated. Differential scanning calorimetry (DSC) reveals an exothermic decomposition onset at 180 °C (heating rate 10 K/min, closed pan), which drives the recommended upper handling limit of 80 °C during drying or reaction setup.
In HATU-mediated amidation sequences conducted in anhydrous DMF, water has a disproportionate impact on kinetic partitioning. When residual moisture in the reaction mixture exceeds 0.3% (w/w relative to the aminoisothiazole substrate), the activated uronium ester undergoes hydrolysis at a rate competitive with aminolysis, slashing isolated yields from 85% to below 40%. This sensitivity is compounded by the hygroscopicity of the hydrochloride salt, which can absorb atmospheric moisture within 15 minutes of bench-top exposure at relative humidity above 60%. Kilogram-scale protocols therefore enforce a strict pre-drying regimen: the powder is spread in a 2 cm layer in a vacuum oven and held at 40 °C/<10 mbar for 4 h, then transferred under counter-flow argon into a Schlenk flask charged with freshly activated 3 Å molecular sieves. On a pilot-plant line equipped with a 50 L glass-lined reactor, the dried salt is dissolved in DMF that has been sparged with argon for 45 min and verified to contain ≤ 50 ppm water by in-line NIR spectroscopy. Failure to implement this dehydration sequence has been documented as the primary root cause of batch failures during technology transfer from medicinal chemistry to kilo-lab production, with the characteristic signature of hydrolyzed acid by-product appearing at RRT 0.72 in the in-process HPLC control.
Adiabatic calorimetry (Phi-TEC II) demonstrates that the dry hydrochloride salt can sustain a self-accelerating decomposition if a thermal runaway event is initiated above 60 °C in the presence of strong bases. Contact with sodium hydride or potassium tert-butoxide triggers immediate gas evolution and a pressure rise exceeding 10 bar/s in closed-cell testing; hence, neutralization of the hydrochloride with hindered amine bases such as N,N-diisopropylethylamine is preferred for in-situ free-amine liberation. Incompatibility extends to strong oxidizing agents—chlorine, bromine, and concentrated nitric acid cause rapid exothermic degradation with charring. For this reason, the product must never be dried or handled in proximity to floor-level oxidizer storage within a warehouse configured to NFPA 400 hazard classifications. Secondary containment in high-density polyethylene trays is standard for all stored containers.
The salt is typically packaged in 25 g, 100 g, and 1 kg amber borosilicate glass bottles with PTFE-faced silicone septa under a positive argon pressure of 0.2 bar. For shipments exceeding 5 kg, double-bagged liner-in-fiber drums with desiccant sachets between the inner and outer bags are employed, and each container undergoes a helium leak test prior to dispatch to guarantee seal integrity over a 24-month shelf-life from the date of manufacture when stored at −20 °C.