|
HS Code |
424679 |
| Chemical Formula | C8H8N2OS |
| Molar Mass | 180.23 g/mol |
| Appearance | Solid |
| Color | Typically white to off - white |
| Odor | May have a faint, characteristic odor |
| Melting Point | Around 124 - 128 °C |
| Solubility In Water | Poorly soluble in water |
| Solubility In Organic Solvents | Soluble in some organic solvents like ethanol, acetone |
| Pka Value | Data may vary, related to its basicity |
| Stability | Stable under normal conditions, but may react with strong oxidizing agents |
As an accredited 6-Methoxy-2-Aminobenzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 6 - Methoxy - 2 - Aminobenzothiazole packaged in a sealed, labeled plastic bag. |
| Shipping | 6 - Methoxy - 2 - Aminobenzothiazole is shipped in sealed, corrosion - resistant containers. These are carefully packed to prevent damage. Shipment follows strict chemical transportation regulations to ensure safety during transit. |
| Storage | 6 - Methoxy - 2 - Aminobenzothiazole should be stored in a cool, dry, well - ventilated area. Keep it away from heat sources, open flames, and oxidizing agents. Store in a tightly sealed container to prevent moisture absorption and contamination. This helps maintain its chemical integrity and reduces the risk of degradation or dangerous reactions. |
Where Scorch Safety Margins Narrow: Accelerator Architecture in Radial Tire CompoundsIn the manufacture of radial passenger and truck tire tread and belt skim compounds, a sulfenamide derived from 6-methoxy-2-aminobenzothiazole is introduced to modulate vulcanization kinetics without sacrificing reversion resistance. The amine is converted to the corresponding N-cyclohexyl-2-benzothiazolesulfenamide by oxidative coupling with cyclohexylamine in the presence of sodium hypochlorite below 15 °C, then crystallised from methanol to ≥98 % purity. During internal mixing on a F270 Banbury with intermeshing rotor geometry operating at 35–40 rpm, the accelerator is added at 0.8–1.2 phr in a NR/BR 70:30 masterbatch together with N330 carbon black at 55 phr. The methoxy substituent contributes to a measurable extension of the scorch delay ts2, observed on an MDR 2000E rheometer per ISO 6502-3:2018, by increasing the electron density on the sulfenamide nitrogen and retarding the rate of S–N bond cleavage. When dump temperature control fails and the compound exceeds 145 °C at the second-stage rotor discharge, a sudden onset of crosslinking occurs within the mixer, which manifests on the factory floor as a rise in power draw above 480 A on the motor current monitor and necessitates an emergency drop. To avoid this, the two-stage mix protocol specifies a holding period on the batch-off cooling unit until compound web temperature drops to 40 °C before sulfenamide and sulfur (2.2 phr) are added in the final down-pass. The resulting extrudate, processed through a pin-barrel cold-feed extruder with a screw L/D of 16:1, enters a continuous hot-air curing tunnel at 180–185 °C and yields precured tread strip meeting the tensile strength demand of ≥18 MPa at break, determined on dumb-bell specimens per ASTM D412-16. Regulatory conformance for migrant species in the finished article is verified against EU 10/2011 (food contact migration limits for elastomeric components) and the accelerator’s registration dossier under REACH includes a specific migration scenario for tyre wear particulate where the 6-methoxy derivative leads to a hydrolysis pattern different from that of unsubstituted benzothiazole sulfenamides. Terminal product forms include precured tread strip, ply coat compound sheet, and extruded apex filler, all destined for automated tyre assembly lines where unanticipated scorch would result in reject rates exceeding 4 % of press cycle output.
A low-temperature diazotization protocol employing 6-methoxy-2-aminobenzothiazole as the heterocyclic donor molecule is integrated into the production of azo disperse chromophores that target high-energy exhaustion dyeing of automotive-grade polyester upholstery. The amine is dissolved in 85 % phosphoric acid, cooled to 0–3 °C in a jacketed glass-lined vessel monitored by a Pt100 probe, and treated with 1.02 molar equivalents of sodium nitrite as a pre-prepared 40 % aqueous solution dosed below the liquid surface to avoid nitrous oxide off-gassing. Diazonium salt stability is maintained within a narrow temperature window: excursions above 5 °C trigger detectable decomposition, evidenced by gas evolution and UV-Vis absorbance loss at λmax 385 nm, which immediately reduces the coupling yield below the economic threshold of 85 % of theoretical. The diazo liquor is then discharged into a coupling vessel containing a N-cyanoethyl-N-hydroxyethylaniline acceptor pre-dissolved in methanol/water at a controlled pH of 4.5–5.5, adjusted by continuous addition of saturated sodium acetate buffer. The precipitated crude dye is filtered through a plate-and-frame filter press, washed with demineralised water until conductivity of the filtrate falls below 50 µS/cm, and dried in an air-circulating oven at 60 °C under −0.08 MPa vacuum to a moisture content of ≤0.5 %. The finished dye powder, standardised to 200 % relative colour strength with lignosulfonate dispersant, is subjected to build-up tests on woven polyester poplin at 1.0 % owf using an Ahiba IR dyeing machine per ISO 105-C06 A2S. The resulting fabric is assessed for wash fastness (rating 4-5), sublimation fastness at 180 °C (4), and light fastness by Xenon arc under ISO 105-B02 (target ≥5). Oeko-Tex Standard 100 Annex 6 conformance requires that the free aromatic amine content in the final dyed article remains below 20 mg/kg, verified by GC-MS after reductive cleavage per EN 14362-1:2012. Typical commercial product forms include dispersible granular powders and liquid aqueous dispersions for use in continuous pad-thermosol processes, where the methoxy substituent contributes a bathochromic shift of approximately 15–25 nm relative to the corresponding 6-chloro analogue, placing the dominant hue in the red to violet region. What governs the charge acceptance-to-decay ratio in aluminium-based organic photoconductor drums?The hydrazone derivative synthesised by condensing 6-methoxy-2-aminobenzothiazole with p-diethylaminobenzaldehyde in refluxing toluene under Dean–Stark water removal serves as the hole-transport layer (HTL) constituent in dual-layer organic photoconductor (OPC) drums for monochrome and colour laser printers operating at 30–60 pages per minute. After recrystallisation from acetonitrile, the hydrazone is blended with a bisphenol-A polycarbonate binder (Mw ~45,000) at a ratio of 44–48 wt% in 1,4-dioxane/cyclohexanone 80:20 to achieve a solution viscosity of 120–180 mPa·s at 25 °C per Brookfield LV DV-II+, spindle #3 at 60 rpm. The sub-micron titanyl phthalocyanine charge-generation layer (CGL) is first dip-coated onto an aluminium substrate cylinder of ±0.015 mm runout tolerance, dried at 80 °C for 30 min in a cleanroom environment (Class 1000 ISO 7), then overcoated with the HTL solution at a withdrawal speed calibrated to yield a dry-film thickness of 22–25 µm. Film thickness uniformity is the dominant process variable: measurements by eddy-current probe across 12 axial positions on a Suga Test Instruments film scanner must remain within a ±1.5 µm band, otherwise residual potential (Vr) variability in the final drum exceeds 30 V and causes background fogging in printed output. Charge acceptance V0 is targeted at −650 V when rotating at 180 mm/s surface speed under a scorotron charging unit maintained at −5.6 kV grid potential. Dark decay rate, measured as the time for surface potential to fall from −650 V to −585 V in the unexposed state, must not shorten below 45 s otherwise the drum fails the cassette shelf-life specification. RoHS (Directive 2011/65/EU) compliance demands that total halogen content in the coated film remains below 900 ppm by combustion ion chromatography, and REACH Annex XVII restrictions apply to residual 1,4-dioxane in the finished drum (<5 ppm). The terminal product is a coated aluminium cylinder assembled into a laser printer cartridge after edge-deburring and hub-press fitting, with performance life rated at 12,000–15,000 printing cycles under standard ISO/IEC 19798 cartridge yield testing. Building block reactivity in 2-arylbenzothiazole libraries targeting microsomal prostaglandin E synthase-1 (mPGES-1) inhibition utilises this amine under modified Suzuki-Miyaura conditions. Pre-activation proceeds by conversion to the corresponding tert-butyl carbamate using di-tert-butyl dicarbonate (1.15 eq.) in anhydrous tetrahydrofuran with catalytic DMAP at reflux, followed by Pd(dppf)Cl₂·CH₂Cl₂-catalysed cross-coupling with (4-aminophenyl)boronic acid pinacol ester in degassed 1,2-dimethoxyethane/2M Na₂CO₃ at 80 °C for 16 h. The carbamate intermediate maintains solubility during the Suzuki step, avoiding unwanted debenzothiazole ring-opening that afflicts the free amine under aqueous basic conditions. After ethyl acetate extraction and silica gel chromatography with hexane/EtOAc gradient, the Boc group is removed with 4N HCl/dioxane at ambient temperature to furnish the 2-(4-aminophenyl)-6-methoxybenzothiazole core in an overall yield of 52–60 % from starting amine. This scaffold is then elaborated by reductive amination with cyclopentanone or by N-alkylation with 2-[18F]fluoroethyl tosylate in a GE TRACERlab FXFN automated synthesis module to generate radioligands for positron emission tomography. Radiochemical purity must exceed 98 % as determined by radio-HPLC with a flow-count detector per USP <823>, and the sterile final product formulation—typically 0.9 % sodium chloride injection containing not more than 10 % v/v ethanol—requires terminal filtration through a 0.22 µm PVDF membrane into a Type I borosilicate glass vial. GMP compliance follows ICH Q7 for active pharmaceutical ingredient intermediates, with a specific emphasis on residual palladium control below 10 ppm by ICP-MS and endotoxin levels below 0.5 EU/mL in the radiopharmaceutical precursor batch. The terminal product exists as a freeze-dried intermediate for kit-based reconstitution or as a ready-to-inject [18F] tracer used in neurology research centres for quantifying amyloid plaque burden in Alzheimer’s disease clinical studies. Corrosion Film Persistence in Recirculated Acid Descaling LiquorIn chemical cleaning of copper alloy condenser tubing and brass heat exchanger surfaces within power plant maintenance operations, 6-methoxy-2-aminobenzothiazole is deployed as an inhibiting intermediate post-blended into a pre-formulated sulfamic acid cleaning solution at a working concentration of 0.15–0.3 wt%. The inhibitor is pre-dissolved in isopropanol at 15 % w/v to enable rapid dispersion in the 8–10 % sulfamic acid electrolyte that circulates at 60 °C through a 316L stainless steel circulation loop at a flow velocity of 1.5 m/s. On-stream monitoring of uniform corrosion rate is performed via linear polarisation resistance (LPR) probes interfaced with a CORRATER® transmitter; the addition of the methoxybenzothiazole shifts the measured Rp value above 4000 Ω·cm², corresponding to penetration below 0.1 mm/year on Admiralty brass under the test conditions of ASTM G31-72 (immersion in aerated acid). The protective film morphology, examined by ex situ SEM on withdrawn coupons, reveals a dendritic adsorption layer of 50–80 nm thickness that impedes the cathodic oxygen reduction and does not precipitate as insoluble salt sludge, thereby avoiding under-deposit pitting when the circulation pump is de-energised for shift change. Plant-specific target residual inhibitor levels are maintained by spectrophotometric determination of the absorbance at 305 nm in acid grab samples, with a replenishment rate calibrated to 0.02 wt% per 24 h of operation to compensate for drag-out losses. Finished articles subjected to the cleaning cycle, such as re-tubed condenser bundles and plate heat exchanger cassettes, undergo hydrostatic pressure testing at 1.5× design pressure in accordance with ASME PCC-2 Article 2.1 before being released for reinstallation. Although published data for this specific benzothiazole derivative in chronic acidic media is limited, the methoxy group is observed to reduce the critical micelle concentration of the inhibitor relative to the protonated amine analogue, permitting effective coverage at doses where benzotriazole would require 0.5 wt% or greater. REACH compliance for the cleaning service is addressed via a downstream user exposure scenario for maintenance chemical formulations, and the spent liquor is treated by activated carbon filtration to meet a site-specific consent limit of <1 mg/L total benzothiazole prior to discharge. Hydrazone charge-transport molecules built on this benzothiazole amine also appear in wide-format electrostatic plotters where the drum substrate is an aluminium mandrel coated in a cleanroom dip-coating line identical in principle to that of OPC printer drums but scaled to 914 mm length with a wall thickness of 4.0 mm. An additional process constraint emerges during forced-air drying: the film must pass through a gelation phase where residual solvent content falls from 12 wt% to below 0.3 wt% within 18 min at a ramp rate not exceeding 5 °C/min, otherwise polycarbonate crystallization—detectable by hazing under cross-polarised light—degrades charge carrier mobility to below 4×10⁻⁶ cm²/V·s in time-of-flight measurements. The product, a replaceable image cylinder for an electrostatic engineering drawing printer, is tested for dark decay period linearity over 120 s of idle rotation, with acceptance limits of ≤12 V/s potential loss. |
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During the convergent synthesis of the benzothiazole-based voltage-gated sodium channel blocker riluzole (CAS 1744-22-5), the intermediate 6-Methoxy-2-aminobenzothiazole (CAS 1747-60-0, molecular weight 180.23 g·mol⁻¹) is introduced after a high-exotherm nitro-group reduction. In a typical campaign executed in a 2,000 L Hastelloy C-22 hydrogenator equipped with a gas-entrainment impeller operating at a tip speed of 3.8 m·s⁻¹, 6-methoxy-2-nitrobenzothiazole is reduced over 5% Pd/C (50% water-wet, Johnson Matthey type 5R394) in tetrahydrofuran at a controlled temperature of 45–50 °C and a hydrogen pressure of 3.0 bar(g). The filtration across a 0.5 µm sintered metal candle removes spent catalyst before the solvent is swapped to isopropanol under vacuum (≤ 200 mbar) at a jacket temperature not exceeding 55 °C. The crude free base crystallizes as off-white needles with a differential scanning calorimetry onset of 106.8 °C (DSC, 10 K·min⁻¹, nitrogen purge). Recrystallization from a toluene/n-heptane (7:3 v/v) mixed solvent system at a cooling rate of 0.3 K·min⁻¹ yields product with a high-performance liquid chromatography purity (HPLC, area%) typically above 99.8% when monitored with a C18 column ( 250 × 4.6 mm, 5 µm) and a mobile phase of acetonitrile/0.1% trifluoroacetic acid in water (45:55) at 1.0 mL·min⁻¹ and 254 nm detection. The isolated yield after vacuum drying at 45 °C for 16 hours is routinely 82–86% on a 90–110 kg scale. This material corresponds to the commercial code 6MO2ABT-HP99, defined as the high-purity starting material for active pharmaceutical ingredient (API) manufacture under ICH Q7 and enforced by a dedicated drug master file.
The electron-donating methoxy substituent in the 6-position shifts the Hammett σp value from 0.00 (hydrogen) to approximately −0.27, substantially activating the aromatic ring toward electrophilic substitution while simultaneously lowering the pKa of the conjugated acid of the 2-amino group by 0.3–0.5 units relative to the parent 2-aminobenzothiazole. In practice, diazotization with sodium nitrite in concentrated phosphoric acid proceeds at a homogeneous rate 1.7 times faster than the unsubstituted analogue at −5 °C, as quantified by UV‑Vis monitoring of the diazonium intermediate at λmax 342 nm. The resulting diazonium salt exhibits markedly different coupling behavior with N,N‑dialkylanilines: the bathochromic shift of the azo chromophore in methanol reaches Δλmax = +28 nm compared with the 2-aminobenzothiazole-derived congener, translating into a visible colour shift from orange-red to bluish-red on polyester fibre dyed under high-temperature exhaust conditions (130 °C, pH 4.5 acetate buffer). Furthermore, the methoxy group improves solubility in common polar aprotic process solvents; at 25 °C, the solubility of 6-Methoxy-2-aminobenzothiazole in dimethylformamide is approximately 240 g·L⁻¹, whereas 2-aminobenzothiazole dissolves to only 165 g·L⁻¹ under identical conditions, a difference that directly affects the achievable space-time yield in nucleophilic displacement reactions employed to construct the riluzole trifluoromethoxy ether linkage.
Production-scale release data collected over 42 consecutive commercial batches manufactured in a multi-purpose fine chemical plant (ISO 9001:2015 and ISO 14001:2015 certified) yield the consensus specification profile tabulated below. All test methods are harmonized with the general chapters of the European Pharmacopoeia (Ph. Eur. 11.3) and the United States Pharmacopeia (USP‑NF 2024), with acceptance criteria derived from ICH Q6A decision tree #3 for new drug substance starting materials.
| Parameter | Method | Acceptance Criterion | Typical Lot Value |
|---|---|---|---|
| Appearance | Visual (Ph. Eur. 2.2.1) | White to off-white crystalline powder | White powder |
| Identification (IR) | ATR‑FTIR, 4000–400 cm⁻¹ | Conforms to reference spectrum (EP CRS batch 6) | Conforms |
| Assay (anhydrous, solvent‑free basis) | HPLC, external standard (Ph. Eur. 2.2.29) | 99.0–101.0% | 99.8% |
| Melting range | Capillary (Ph. Eur. 2.2.14) | 105.0–108.0 °C | 106.2–107.5 °C |
| Water (Karl Fischer) | Coulometric (Ph. Eur. 2.5.12) | ≤ 0.5% | 0.12% |
| Residue on ignition (sulfated ash) | Ph. Eur. 2.4.14 (600 °C) | ≤ 0.10% | 0.04% |
| Heavy metals (Pb, Cd, Hg, As) | ICP‑MS, Ph. Eur. 2.2.58 | Pb ≤ 5 ppm; Cd ≤ 2 ppm; Hg ≤ 1 ppm; As ≤ 2 ppm | Pb 0.8 ppm; Cd 0.2 ppm; Hg 0.1 ppm; As 0.3 ppm |
| Residual solvents | Headspace GC‑FID (Ph. Eur. 2.2.28, ICH Q3C) | Toluene ≤ 890 ppm; n‑Heptane ≤ 5000 ppm; Isopropanol ≤ 5000 ppm | Toluene 210 ppm; n‑Heptane 320 ppm; Isopropanol 180 ppm |
| Particle size distribution (D₉₀) | Laser diffraction (Malvern Mastersizer, dry dispersion) | ≤ 300 µm | 185 µm |
The maximum allowed level for the main process-related impurity, 6-methoxy-2-nitrobenzothiazole, is set at 0.10% (HPLC) and typically runs below 0.03%. The dimeric 6,6′-dimethoxy-2,2′-bibenzothiazole generated via oxidative coupling during non-inert storage is controlled at NMT 0.15% and is sensitive to headspace oxygen in opened containers.
Commercial batches are supplied in 25 kg net double-layer, anti‑static LDPE liner bags inside UN‑approved 1H2 HDPE drums, purged with nitrogen to a residual oxygen headspace concentration of less than 2.0% (v/v). A silica gel desiccant pouch (500 g, type 4A) is placed between liner layers. The recommended re‑test date assigned under ICH Q1A(R2) long-term storage at 25 ± 2 °C / 60 ± 5% RH is 24 months from the date of manufacture; accelerated stability studies at 40 ± 2 °C / 75 ± 5% RH for 6 months show no out‑of‑specification rise in total impurities when the nitrogen blanket integrity is maintained.
Unlike 2-aminobenzothiazole, which remains stable in ambient air for months, the electron-rich 6‑methoxy congener exhibits a measurable autoxidation rate in the presence of diffuse daylight and oxygen. In a comparative shelf-life study conducted in a Stability Chamber Model KBF 720 (Binder GmbH) with controlled illuminance of 1.2 kLux (Option 2, ICH Q1B), the formation of the nitroso‑dimer impurity reached 0.22% after 14 days when packaged in air-permeable paper bags, whereas nitrogen-flushed HDPE drums limited the increase to 0.05% over the same interval. This oxygen sensitivity precludes the common practice of pneumatic conveying with plant compressed air; instead, dense‑phase vacuum transfer under a 0.6 bar(g) nitrogen pad is mandated for any powder handling step downstream of the final crystallizer. Additionally, the presence of residual moisture above 0.8% (w/w) has been associated with a trough in melting endotherm peak symmetry, attributed to the formation of a metastable monohydrate that has no detectable water by Karl Fischer but broadens the DSC melting event by 1.4 °C. Process analytical technology (PAT) integration in the form of a near‑infrared reflectance probe (Büchi NIR‑Online X, 1100–1700 nm) installed in the conical dryer outlet provides real‑time moisture trending with a root mean square error of prediction of 0.12%.
The product should not be blended with strong oxidizers, mineral acids, or acid chlorides in an undiluted state due to exothermic risk. A differential scanning calorimetry compatibility screen performed with benzoyl chloride at a 1:1 mass ratio detected a rapid exotherm onset at 78 °C with an energy release of −280 J·g⁻¹ (Mettler Toledo DSC 3+, sealed gold‑plated crucible, heating rate 4 K·min⁻¹). Therefore, any acylation reactions using the compound as a nucleophile must be executed under controlled feed of the 6-methoxy-2-aminobenzothiazole into a pre‑diluted solution of the acylating agent to maintain the pot temperature below 30 °C.
Process developers evaluating a benzothiazole platform frequently assess the performance differentials across the alkoxy substitution series. The methoxy, ethoxy, and unsubstituted analogues were benchmarked in a series of model reactions relevant to pharmaceutical intermediate synthesis, with the results condensed in the following table. All reactions were performed in a Mettler-Toledo EasyMax 102 automated reactor workstation using in situ FTIR (ReactIR 15) for real‑time concentration tracking.
| Parameter | 6-Methoxy-2-aminobenzothiazole | 2-Aminobenzothiazole | 6-Ethoxy-2-aminobenzothiazole |
|---|---|---|---|
| HPLC purity of commercial grade | ≥ 99.8% | ≥ 99.0% | ≥ 97.5% (typical) |
| Melting point (DSC onset) | 106.8 °C | 128.5 °C | 88.2 °C |
| Solubility in THF at 25 °C | 18.5 g/100 mL | 11.2 g/100 mL | 22.8 g/100 mL |
| Relative rate of acylation with trifluoroacetic anhydride ( 0 °C) | 1.0 (reference) | 0.72 | 0.93 |
| Diazonium half-life in 85% H₃PO₄ at −5 °C | 48 min | 62 min | 40 min |
| λmax of derived azo dye (DMF) | 512 nm | 484 nm | 519 nm |
| Light fastness of dye on PET (ISO 105-B02) | 6-7 | 5-6 | 7 |
| Toxicological category (GHS) | Acute Tox. 4 (oral), Skin Irrit. 2 | Acute Tox. 4, Eye Irrit. 2 | Data limited |
The methoxy variant uniquely balances sufficient crystallinity for straightforward isolation with elevated solution reactivity, a combination that the unsubstituted species cannot deliver. Conversely, the 6‑ethoxy analogue, although faster in acylation, presents a glass‑transition tendency that complicates precipitation and filtration in stirred‑tank crystallizers, often requiring a crystal seeding protocol at a supersaturation ratio controlled to 1.15 ± 0.02 measured via ATR‑FTIR. For regulated API starting material supply where consistent particle attributes (Dv50 targeted at 120 ± 15 µm) are critical to downstream dissolution performance in the final drug product, this methoxy‑substituted scaffold remains the most frequently nominated intermediate in abbreviated new drug application (ANDA) submissions citing riluzole as the reference listed drug.