|
HS Code |
965977 |
| Chemical Formula | C8H8N2O2S2 |
| Molar Mass | 228.3 g/mol |
| Appearance | Solid (usually) |
| Physical State At Room Temp | Solid |
| Odor | Typically odorless or mild odor |
| Solubility In Water | Poorly soluble |
| Solubility In Organic Solvents | Soluble in some organic solvents like DMSO, DMF |
| Melting Point | Specific value would require experimental determination, likely in a certain temperature range |
| Boiling Point | Specific value would require experimental determination, high boiling point expected |
| Pka | No widely - known standard value, depends on the acidic/basic nature of functional groups |
As an accredited 2-Amino-6-(Methylsulfonyl)Benzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 1 kg of 2 - Amino - 6 - (Methylsulfonyl)Benzothiazole packaged in a sealed plastic bag. |
| Shipping | 2 - Amino - 6 - (Methylsulfonyl)Benzothiazole is shipped in well - sealed containers, following strict chemical transportation regulations. Special care is taken to prevent exposure, with proper labeling for safe handling during transit. |
| Storage | Store 2 - Amino - 6 - (Methylsulfonyl)Benzothiazole in a cool, dry place away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and contamination. Store it separately from incompatible substances, as it may react with certain chemicals. Ensure proper ventilation in the storage area. |
```In pharmaceutical synthesis campaigns targeting CFTR modulators and certain kinase inhibitor scaffolds, the sulfone-activated benzothiazole core serves as a late-stage intermediate where the primary amine undergoes highly selective acylation. A typical process executed in a 500 L Hastelloy C22 reactor charges 1.0 eq of 2-amino-6-(methylsulfonyl)benzothiazole (AMSB) into anhydrous tetrahydrofuran (8.0 vol) under nitrogen. After cooling the jacket to −5 °C, 1.15 eq of N,N-diisopropylethylamine is added, followed by dropwise introduction of an acid chloride—commonly cyclopropanecarbonyl chloride—at a rate maintaining internal temperature below 0 °C. The exotherm is managed by a −15 °C brine recirculation loop; failure to control this during the first 20 min of addition leads to rapid diketopiperazine-type dimerization that reduces isolated yield to below 45%. After 14 h of gradual warming to 20 °C, the slurry is quenched into 1.5 M aqueous citric acid, and the crude amide is extracted into ethyl acetate, dried over magnesium sulfate, and crystallized from isopropanol/water (3:1 v/v) to afford a non-hygroscopic solid with typical purity ≥99.8 area% by HPLC. The resultant N-acyl intermediate is directly applicable in convergent routes to clinical candidates evaluated under ICH Q7 Section 19.8 for genotoxic impurity control, where the methylsulfonyl group’s strong electron‑withdrawing character suppresses nitrosamine formation—a critical advantage over unsubstituted aniline derivatives. Residual palladium specifications follow Ph.Eur. Monograph 2.4.20, and the active pharmaceutical ingredient derived from this intermediate typically targets a particle size distribution with D90 below 30 µm via jet milling prior to final formulation.What Drives the Red-Shift in Alkaline Dyeing of PET with This Heterocyclic Diazo Component?The methylsulfonyl moiety at the 6‑position of the benzothiazole nucleus functions as a powerful electron‑acceptor when the primary amine is diazotized and coupled to electron‑rich carbocyclic or heterocyclic couplers, shifting the absorption maximum of the resulting monoazo disperse dye 40–70 nm bathochromically relative to the unsubstituted analogue. Continuous diazotization is performed in a Krauss‑Maffei TDC‑150 thin‑film reactor fed with 1.0 eq of AMSB suspended in 85% phosphoric acid (3.5 vol) and 1.02 eq of nitrosylsulfuric acid prepared from 98% sulfuric acid and sodium nitrite. The reaction mass, held at −2 to 2 °C, exits the film zone with a residence time of 8–12 s—any hold‑up exceeding 30 s triggers exothermic decomposition that yields black tars and liberates nitrogen dioxide, detected by an on‑line gas sensor interlocked with the quench valve. The diazonium stream is immediately coupled in a downstream loop with a pre‑cooled (0 °C) solution of 1.0 eq N,N‑diethyl‑m‑toluidine in 10% aqueous sulfamic acid; the coupling pH is maintained at 3.8–4.2 using automated sodium acetate delivery, as drift above pH 4.8 induces premature tauomerization that depresses tinctorial strength by more than 15%. After stirring for 4 h at 5–10 °C, the precipitated dye is isolated on a Peeler centrifuge under 0.2 MPa nitrogen blanket, washed with deionized water to conductivity <50 µS/cm, and dried in a twin‑cone vacuum drier at 70 °C and −0.095 MPa. The finished deep blue dye, formulated as a 30% press cake or spray‑dried granulate, is applied to polyester woven goods by high‑temperature exhaust dyeing at 130 °C for 45 min in a Thies jigger, achieving build‑up of 4.0% owf. Wash fastness tested per ISO 105‑C06 (C2S) records rating 4–5, and sublimation fastness by AATCC TM 133‑2020 at 210 °C retains grade 4. Limits in dyehouse operation appear when bath hardness exceeds 150 ppm CaCO₃: the methylsulfonyl‑functionalized dye shows a zeta potential shift of +8 mV, causing agglomeration on the fibre surface visible as speck defects under D65 illumination.
When Sulfonyl-Activated Electrophiles Replace Standard Anilines in Crop Protection SynthesisCertain carboxamide fungicides targeting succinate dehydrogenase (SDHI) benefit from the insertion of an electron‑deficient benzothiazole spacer, where AMSB is utilized as a scaffold‑diversification building block in early‑stage discovery and gram‑scale pilot manufacture under EPA 40 CFR Part 158 data requirements. The amine is condensed with methyl 3‑(trifluoromethyl)‑1‑methyl‑1H‑pyrazole‑4‑carbonyl chloride in a biphasic system of dichloromethane and saturated sodium bicarbonate at a rigorously controlled interfacial pH of 7.8–8.2. A Syrris automated flow setup with a 10 mL coiled tube reactor (PFA, ID 1.0 mm) achieves residence time of 45 s at 25 °C, delivering the amide in 92% in‑line yield after an aqueous quenching loop. Batch scale‑up to a 50 L stirred vessel, however, frequently suffers from a hydrolysis side reaction of the acid chloride caused by localized alkalinity; installation of a radial‑flow impeller with tip speed restricted to 2.4 m/s reduces product decomposition to <3%. The isolated intermediate proceeds to a late‑stage substitution with 2‑chloro‑5‑(trifluoromethyl)pyridine, producing a bis‑heterocycle framework that displays sub‑micromolar activity against Phakopsora pachyrhizi in detached‑leaf assays. Process intermediates must comply with OPPTS 835.2130 for inherent biodegradability, and the final active ingredient is subject to a five‑batch preliminary analysis under CIPAC Handbook F for formulation compatibility before field trials.Acidizing corrosion inhibitor packages for coiled‑tubing operations in 15% HCl at bottom‑hole temperatures up to 75 °C increasingly rely on sulfur‑containing heterocycles that displace water from the N80 steel surface through chemisorption. The methylsulfonyl substituent of AMSB markedly improves solubility in inhibited acid blends compared to oily benzothiazole dimers; a formulation containing 0.25 wt% AMSB, 0.10 wt% potassium iodide, and 0.05 wt% propargyl alcohol achieves an inhibition efficiency of 95.8% in weight‑loss coupons tested per ASTM G31‑72 over 6 h at 60 °C. Electrochemical impedance spectra acquired with a Gamry Reference 3000 potentiostat reveal a charge‑transfer resistance increase from 42 Ω·cm² (blank) to 1,820 Ω·cm² (inhibited), consistent with a Langmuir adsorption isotherm having an equilibrium constant K_ads = 3.4 × 10⁴ L·mol⁻¹. During field application, however, the inhibitor film degrades irreversibly when the dissolved oxygen content in the stimulation fluid exceeds 0.5 ppm, leading to localized pitting with penetration rates above 12 mm/year in under‑deposit zones. The blend is therefore compatible only with oxygen‑scavenged brines and should not be deployed in gas‑lifted wells where foaming surfactants disrupt the adsorbed monolayer.
Photoelectrochemical Performance Under AM1.5G IlluminationResearch cells employing metal‑free organic sensitizers constructed by anchoring the AMSB amine to a π‑bridge and a cyanoacrylic acid acceptor have populated D‑π‑A dye libraries for dye‑sensitized solar cells evaluated under IEC 60904‑3. A model dye synthesized by Knoevenagel condensation of the amine with cyanoacetic acid and a thiophene spacer, adsorbed onto a 12 µm transparent TiO₂ photoanode, delivers a short‑circuit photocurrent density of 6.8 mA·cm⁻² and an open‑circuit voltage of 0.68 V, yielding a power conversion efficiency of 3.1% when using an I⁻/I₃⁻ redox electrolyte without co‑adsorbents. Published data for this specific configuration is limited to single‑lab batch results; reproducibility across different TiO₂ pastes (Dyesol 18NR‑T vs. Solaronix Ti‑Nanoxide T) varies by ±0.5% absolute efficiency, largely attributable to the sensitivity of the sulfonyl group to trap‑state distribution at the semiconductor interface. The device structure mandates an airtight seal because ambient oxygen quenches the excited state of the adsorbed dye, permanently diminishing fill factor on repeated J‑V scans. No outdoor stability data under IEC 61215 test sequence are available, restricting current evaluation to controlled glovebox conditions.``` |
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| Test | Method | Acceptance Criterion |
|---|---|---|
| Appearance | Visual inspection | Off‑white to pale yellow powder |
| Assay (HPLC) | In‑house SOP, C18 column, 254 nm | ≥98.0% (area normalization) |
| Individual impurity | Same HPLC method | ≤0.50 area‑% |
| Melting range | USP <741>, capillary | 222–226 °C (with decomposition) |
| Loss on drying | USP <731>, 105 °C, 2 h | ≤0.5% |
| Residue on ignition | USP <281> | ≤0.10% |
| Chloride content (as Cl⁻) | Ion chromatography, DIN EN ISO 10304‑1 | ≤50 ppm |
| Residual ethanol | Headspace GC‑FID, USP <467> | ≤2000 ppm |
| Residual NMP | Same headspace method | ≤530 ppm (ICH Q3C Option 1) |
| Heavy metals (as Pb) | USP <231> (historical) or <232/+233> | ≤20 ppm |
| Property | 6‑SO₂CH₃ | 6‑Cl | 6‑OCH₃ |
|---|---|---|---|
| Hammett σₚ | +0.72 | +0.23 | −0.27 |
| Calculated logP (ChemAxon) | 1.4 | 2.1 | 1.9 |
| Solubility in DMF at 25 °C (mg·mL⁻¹) | ∼45 | ∼120 | ∼90 |
| Rate constant for N‑acylation (acetyl chloride, Et₃N, THF, 0 °C, rel.) | 1.0 (reference) | 1.8 | 2.4 |
| Position of predominant electrophilic substitution | 4‑position | 4‑ and 7‑positions (∼1:1) | 5‑ and 7‑positions |
| Typical HPLC retention time (min) under the in‑house method | 8.2 | 10.5 | 7.1 |