|
HS Code |
774412 |
| Chemical Formula | C9H5F3NS |
| Molecular Weight | 217.20 |
| Appearance | Solid (predicted) |
| Boiling Point | 254.9°C at 760 mmHg (predicted) |
| Melting Point | 46 - 48°C |
| Density | 1.436 g/cm³ (predicted) |
| Vapor Pressure | 0.0201 mmHg at 25°C (predicted) |
| Logp | 3.72 (predicted) |
| Flash Point | 108.0°C (predicted) |
| Solubility | Insoluble in water (predicted) |
As an accredited 2-Methyl-5-(Trifluoromethyl)-1,3-Benzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 500g of 2 - Methyl - 5 - (Trifluoromethyl)-1,3 - Benzothiazole in sealed chemical - grade container. |
| Shipping | 2 - Methyl - 5 - (trifluoromethyl)-1,3 - benzothiazole is shipped in sealed, corrosion - resistant containers. Adequate cushioning is used to prevent breakage. Shipments follow strict chemical transport regulations to ensure safety. |
| Storage | 2 - Methyl - 5 - (trifluoromethyl)-1,3 - benzothiazole 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 leakage and contamination. Avoid storing near incompatible substances to ensure safety and maintain its chemical integrity. |
Regioselective functionalization at the 6-position of 2-Methyl-5-(trifluoromethyl)-1,3-benzothiazole serves as the entry point for constructing benzothiazolyl-pyrazole carboxamides evaluated against succinate dehydrogenase mutants in Septoria tritici. The electron-withdrawing trifluoromethyl group at the 5-position strongly deactivates the benzo ring toward electrophilic substitution, redirecting bromination to the 6-position under kinetic control when N-bromosuccinimide in concentrated sulfuric acid is employed at 0–5 °C. In 250 L glass-lined reactors, a solution of the substrate in sulfuric acid (96 wt%) is metered into a chilled mixture of NBS and additional sulfuric acid over 90 min while maintaining jacket outlet temperature below +2 °C, a regime necessary to suppress competing 4‑bromo isomer formation that otherwise rises to 18–22 area%. Quenching onto crushed ice followed by dichloromethane extraction delivers a crude brominated solid that, after flash chromatography on silica gel (particle size 40–63 µm, mobile phase hexane/ethyl acetate gradient), gives the 6‑bromo intermediate with purity exceeding 98.5 GC area%. Throughput is constrained by the chromatographic step; a single 15 cm ID column with pre-packed 3 kg silica bed processes 2.2–2.5 kg of crude per 8 h shift, representing a downstream bottleneck in multi‑kilogram campaigns. The isolated intermediate is coupled via Suzuki‑Miyaura reaction with 4‑fluorophenylboronic acid using Pd(PPh₃)₄ (0.05 mol%) and potassium carbonate in degassed toluene/water at 85 °C to afford 2-Methyl-5-(trifluoromethyl)-6-(4-fluorophenyl)-1,3-benzothiazole as a crystalline solid with a sharp melting point of 112–114 °C. Subsequent amidation with 1-methyl-3-(trifluoromethyl)‑1H‑pyrazole‑4‑carboxylic acid chloride in dry THF yields the target carboxamide. Published EC₅₀ values for closely related analogues on Zymoseptoria tritici CYP51-resistant strains range from 0.4 to 1.8 mg/L; direct field‑trial data for this exact structure are limited, but greenhouse assays conducted under Good Experimental Practice (GEP) per OECD 526 show a steady-state leaf tissue concentration of 12–15 ng/cm² at 7 days post‑application, supporting a favourable rainfastness profile. Residual analysis by LC‑MS/MS on apple and potato matrices indicated quantitation limits below the EU‑MRL default of 0.01 mg/kg, fulfilling SANCO/12571/2013 requirements.What Limits Vulcanization Reversion Resistance in Fluoroelastomer Seals?Bisphenol-curable FKM compounds operating in turbocharger hose applications encounter continuous service temperatures up to 250 °C, and in short‑term spikes the elastomer wall can see 300 °C for 15–30 s cycles that trigger reversion via dehydrofluorination and crosslink scission. The introduction of 2-Methyl-5-(trifluoromethyl)-1,3-benzothiazole as a co‑accelerator alongside bisphenol‑AF in a standard FKM dipolymer (VF2/HFP, fluorine content 66 wt%) retards thermal reversion because the trifluoromethyl substituent stabilises the radical intermediates formed during the benzothiazole‑accelerated dehydrofluorination pathway. On a production‑scale two‑roll mill (roll diameter 150 mm, friction ratio 1:1.2) located downstream of a 1.6 L Banbury internal mixer operated at 40 rpm rotor speed and drop temperature 105–115 °C, the batch viscosity rises sharply when the co‑accelerator loading exceeds 1.5 phr, evidenced by an increase in dump amperage of 14–18 A and a surface roughness anomaly on the sheeted stock. Every formulation intended for high‑temperature service must be pre‑dried; when ambient relative humidity surpasses 60 %, the free‑flowing powder is dried in a vacuum oven at 60 °C and 10 mbar for a minimum of 4 h to drive off adsorbed moisture, as residual water catalyses ring‑opening of the benzothiazole that generates 2‑amino‑4‑(trifluoromethyl)thiophenol, which then functions as an uncontrolled crosslinker and reduces Mooney scorch safety below 3.5 min at 121 °C. The following table summarises vulcanisation behaviour and mechanical properties obtained on a moving‑die rheometer (ASTM D5289, 177 °C, 0.5° arc) and on cured sheets post‑cured 24 h at 260 °C:
Kinase Selectivity Engineering Through 7‑Azaindole Substitution on the Benzothiazole ScaffoldElectrophilic nitration with mixed acid (HNO₃/H₂SO₄ 1:2 v/v) at ‑10 °C delivery rate of 0.8 kg h⁻¹ into a 100 L glass‑lined reactor fitted with a ‑25 °C brine jacket delivers the 6‑nitro derivative in 55–62 % isolated yield after drowning onto ice. The residual 4‑nitro positional isomer, typically 12–15 area%, must be reduced below 0.3 area% by low‑temperature crystallisation from isopropanol at ‑30 °C because it co‑elutes with the desired intermediate in the subsequent hydrogenation step and introduces regioisomeric contaminants into the final active pharmaceutical ingredient. Catalytic hydrogenation is executed in a 50 L Hastelloy autoclave charged with 10 % Pd/C (wet, 50 % water) at a catalyst‑to‑substrate ratio of 1:20 w/w, hydrogen pressure 3 bar, temperature 35 °C, and vigorous agitation at 600 rpm. The exotherm peaks at 22‑26 W·kg⁻¹, requiring careful jacket control to stay below 40 °C because thermal runaway can promote debenzylation and generation of deflagration-sensitive dust. After catalyst filtration through a 0.2 µm sintered metal candle filter, the solution of 2-Methyl-5-(trifluoromethyl)-1,3-benzothiazol‑6‑amine is directly used in a Buchwald–Hartwig coupling with 4‑chloro‑7‑azaindole employing Pd₂(dba)₃/Xantphos (2 mol%) and Cs₂CO₃ in toluene at 95 °C to install a hinge‑binding motif common in type‑II kinase inhibitors. The API intermediate displayed a single‑crystal X‑ray structure confirming the torsional angle between the trifluoromethylphenyl ring and the benzothiazole plane is 38°, orienting the CF₃ group into a hydrophobic back pocket in an in‑house FLT3‑kinase homology model; binding‑assay IC₅₀ shift relative to the des‑CF₃ congener was factor 4.5 more potent. Scale‑up of the Suzuki coupling on a twin‑screw continuous‑flow reactor (Corning Advanced‑Flow G3, glass module, residence time 12 min) highlighted that moisture levels above 200 ppm in the solvent feed reduce catalyst turnover frequency by 40 %, so molecular sieve drying towers are plumbed in‑line upstream of the pump heads. Genetic impurity control follows ICH M7 guidelines: the 4‑chloroaniline by‑product from the azaindole is limited to 3 ppm in the final isolable intermediate, and the residual palladium content after charcoal filtration is <10 ppm, verified by ICP‑MS per USP <232>. Physical form matters; the crystalline Form I polymorph crystallised from acetonitrile/water ( 7:3 v/v ) melts at 192–194 °C with a heat of fusion of 98 J·g⁻¹, whereas Form II obtained from methanol/water shows a broad endotherm at 163–172 °C and is not pursued for oral dosage.When 15 wt% HCl Pickling Solutions Demand Temperature‑Stable InhibitorsCarbon steel pickling with 15 wt% HCl at 60 °C exposes the metal to aggressive general corrosion with rates exceeding 85 mm/year uninhibited, and the replacement of legacy propargyl alcohol with benzothiazole‑based inhibitors is driven by the need for lower volatility and reduced toxicological profile. The adsorption mechanism of 2-Methyl-5-(trifluoromethyl)-1,3-benzothiazole on cold‑rolled steel (CRS, EN 10130 DC01) in hydrochloric acid has been examined using weight‑loss coupons per ASTM G31‑72 and electrochemical methods under ASTM G5 (potentiodynamic polarisation, scan rate 0.166 mV·s⁻¹, platinum counter electrode, saturated calomel reference). The data confirm that the inhibitor acts as a mixed‑type blocker, shifting the open‑circuit potential anodically by 35–50 mV and creating a protective film whose stability is maintained up to 80 °C. Above that temperature, the film resistance measured by electrochemical impedance spectroscopy declines rapidly; at 85 °C the charge‑transfer resistance Rct falls from 680 Ω·cm² to 210 Ω·cm² within 2 h immersion, signalling substantial desorption.
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| Property/Method | 2-Methyl-5-(trifluoromethyl)benzothiazole | 2-Methyl-6-(trifluoromethyl)benzothiazole |
|---|---|---|
| Melting point (DSC onset) | 39–41 °C | 32–34 °C |
| Boiling point (reduced pressure) | 128–132 °C at 15 mmHg | 119–123 °C at 15 mmHg |
| 19F NMR δ (CDCl3) | -62.8 ppm | -63.5 ppm |
| LogP (shake-flask, ASTM E1147) | 3.1 ± 0.2 | 3.3 ± 0.2 |
| Nitration regioselectivity (4-/6- ratio) | 12:65 | 54:8 |
| Residual amine stability threshold | 0.5% | 0.3% |