2-(4-Methylphenyl)-1,3-Benzothiazole

2-(4-Methylphenyl)-1,3-Benzothiazole


    • Product Name 2-(4-Methylphenyl)-1,3-Benzothiazole
    • Alias 4-Methylphenylbenzothiazole
    • Einecs 629-457-6
    • Mininmum Order 1mg
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
    VTB
    Specifications

    HS Code

    544575

    Chemical Formula C14H11NS
    Molecular Weight 225.31
    Appearance Solid
    Melting Point Data needed
    Boiling Point Data needed
    Solubility In Water Low solubility
    Solubility In Organic Solvents Soluble in some organic solvents
    Density Data needed
    Flash Point Data needed
    Stability Stable under normal conditions

    As an accredited 2-(4-Methylphenyl)-1,3-Benzothiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2-(4 - Methylphenyl)-1,3-Benzothiazole packaged in a sealed plastic bag.
    Shipping 2 - (4 - Methylphenyl)-1,3 - benzothiazole is shipped in accordance with strict chemical transportation regulations. Packaged securely in suitable containers, it's transported by approved carriers to ensure safety during transit.
    Storage Store "2-(4 - Methylphenyl)-1,3 - Benzothiazole" in a cool, dry place away from heat sources and open flames. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could potentially degrade the chemical. Ensure storage areas are well - ventilated and separated from incompatible substances like oxidizing agents and strong acids.
    Application of 2-(4-Methylphenyl)-1,3-Benzothiazole
    An injection-grade polyethylene terephthalate (PET) preform manufacturing line operating with a throughput exceeding 800 kg/h and a barrel residence time of less than 180 s at melt temperatures between 275°C and 290°C typically introduces 2-(4-methylphenyl)-1,3-benzothiazole not as a direct additive but as the conjugated stilbene-benzothiazole derivative synthesized from it. The derivative functions as an optical brightener that counteracts the intrinsic yellow shift attributed to antimony- or titanium-based polycondensation catalysts. The synthesis pathway involves a base-catalyzed condensation of the parent tolylbenzothiazole with 4,4′-dichlorostilbene under phase-transfer conditions; the resulting crude brightener is then micronized via a fluidized-bed opposed-jet mill to a median particle size (D₅₀) below 4 µm to ensure dispersibility in the polyester melt. The brightener masterbatch, typically formulated at a concentration of 10 wt% in a PET carrier resin with a melt volume-flow rate of 20 cm³/10 min (ISO 1133-1:2022), is let down to a final optical brightener concentration of 0.015–0.035 wt% in the finished preform. Dosing into the main feed throat of a twin-screw injection molding machine with a L/D 24:1 barrier screw must synchronize with the gravimetric blender to avoid deviation exceeding ±0.5% by mass; excursions beyond this window produce visible “optics drift” — a batch-to-batch whiteness variation measurable as a ΔE*₀₀ shift greater than 0.8 under a D65 illuminant per ISO 11664-6:2014. Compliance anchors: the finished preform must satisfy EU Reg. 10/2011 for food-contact PET, specifically the overall migration limit of 10 mg/dm², while the brightener itself must be listed on the positive list of Commission Regulation (EU) No. 10/2011 Annex I with an SML if applicable. Residual free amine from condensation must remain below 5 ppm by HPLC-UV as per in-house specification aligned with GMP EC 2023/2006 for food-contact material manufacture.

    What governs the kinetic stability of dithiocarbamate-free vulcanization reversion inhibitors derived from tolyl-benzothiazole?

    In sulfur-vulcanized natural rubber (NR) truck tire tread compounds processed on a two-wing rotor internal mixer with a fill factor of 0.75 and a dump temperature setpoint of 155°C, 2-(4-methylphenyl)-1,3-benzothiazole acts as a reversion inhibitor precursor. The mechanism does not rely on sulfenamide cleavage; instead, the methylphenyl substituent stabilizes the benzothiazole radical formed during overcure, quenching conjugated diene radicals that would otherwise accelerate main-chain scission in the polysulfidic network. The compound is pre-dispersed in a binder (e.g., an ethylene-propylene-diene monomer binder with a Mooney viscosity ML 1+4 at 125°C of 40 MU) to form a 70% active pelletized masterbatch. Typical addition levels range from 0.4 phr to 1.2 phr as a direct partial replacement for conventional antioxidant 6PPD (N‑(1,3-dimethylbutyl)-N′-phenyl-p-phenylenediamine); higher loadings above 1.5 phr induce a pronounced bloom on the uncured sheet within 48 h at 40% RH, confirmed by FTIR‑ATR surface spectroscopy. The downstream process is a sequential three-stage mixing procedure: masterbatch incorporation in Stage 1 at 50 rpm rotor speed, curative addition in Stage 2 at 35 rpm and 105°C maximum batch temperature to prevent premature reversion-inhibitor decomposition, and a final refining stage on a two-roll mill with a friction ratio of 1:1.2 and nip gap of 1.5 mm. Finished tire treads cured to a T₉₅ rheometer state exhibit an extended plateau torque retention of >92% after 120 min at 160°C (ISO 3417:2011, large rotor). Regulatory conformity demands EU Directive 2005/69/EC limits on polycyclic aromatic hydrocarbons (PAHs) — the benzothiazole congener must not release benzo[a]pyrene above 1 mg/kg extract, tested by GC‑MS after a 24‑h Soxhlet extraction with toluene. The cured rubber article is classified under FDA 21 CFR §177.2600 for repeated-use rubber articles, requiring total extractives below 15 mg/in² in water and hexane extracts.

    Charge Transport Layer Dopants in Organic Photoconductor Drum Coating Formulations

    Laser printer organic photoconductor (OPC) drum manufacturing relies on a charge transport layer (CTL) solution cast onto an anodized aluminum substrate; the CTL formulation comprises a bisphenol‑A polycarbonate binder (Makrolon® Rx2435 or equivalent), a hole-transport N,N′-diphenyl-N,N′-bis(3-methylphenyl)-1,1′-biphenyl-4,4′-diamine (TPD), and an electron-transport molecule. 2-(4-Methylphenyl)-1,3-benzothiazole functions as an electron deficient dopant that forms a charge-transfer complex with TPD, lowering the ionization potential offset and reducing residual potential after repeated charge-discharge cycles. A production-scale coating line at a web speed of 60 m/min deposits a CTL film with a dry thickness of 22–26 µm via immersion dip coating, followed by forced-air drying at 120°C for 45 min in a Class‑1000 cleanroom. The dopant is dissolved in a THF:toluene 1:1 v/v solvent blend together with the binder; its solid fraction in the dried CTL is held between 7 wt% and 15 wt%. At loadings exceeding 18 wt%, the amorphous film undergoes phase separation detectable by AFM phase imaging as islands >200 nm in diameter, which manifest as print ghosting artifacts at cycle counts above 50,000 impressions. The finished OPC drum must meet electrostatic discharge decay specifications per IEC 62899‑201‑1:2021 parameters: dark decay below 8 V/s and residual potential below 60 V after 10,000 cycles. Hazardous substance compliance requires each dopant batch to be certified RoHS 2.0 (Directive 2011/65/EU Annex II) with total bromine <900 ppm by combustion ion chromatography, due to fire-retardant contamination carryover from upstream bromination processes.When an amine-cured bisphenol‑A‑diglycidyl ether (DGEBA) epoxy floor topping is specified for a sour crude oil tank farm, the formulation must integrate an acid-gas barrier synergist to prevent blistering under constant exposure to H₂S partial pressures exceeding 0.5 bar. 2-(4-Methylphenyl)-1,3-benzothiazole is incorporated as a liquid corrosion inhibitor adduct — pre-reacted with a stoichiometric deficit of a low-viscosity cycloaliphatic epoxy diluent to create an oxirane-functionalized inhibitor that chemically bonds into the network. The inhibitor-adduct, added at 1.0–2.5 wt% on total resin weight, is blended into the Part‑A component using a toothed-disc high-speed disperser at 1,200 rpm for 15 min under nitrogen blanket to avoid moisture ingress; excessive shear above 1,800 rpm generates local hot spots above 50°C that trigger premature oxirane ring opening and raise the mixed viscosity by ≥30% within the 45‑min pot life window. The flooring is applied at a nominal wet film thickness of 2 mm by a two-component airless plural-component spray rig fitted with a static mixer with 24 elements. After a 7‑day ambient cure at 23°C and 50% RH, the system undergoes adhesion testing per ASTM D4541‑22 (pull‑off >12 MPa on grit‑blasted steel with profile 90–110 µm) and a 3,000‑h salt spray exposure per ISO 9227:2022 with scribe creep limited to <3 mm. The cured topping qualifies as a high-performance protective coating under ISO 12944‑6:2018 category C5‑M for offshore and chemical plant floors and enters service as the primary hydrocarbon-resistance barrier in crude oil secondary containment bunds.

    When Tolylbenzothiazole Replaces Benzothiazole Disulfide in Regenerated Cellulose Film Bleaching — Process Window Constraints

    Regenerated cellulose film (cellophane) production for twist‑wrap confectionery packaging demands an optical brightener that withstands the acidic coagulation bath and the alkaline desulfuration stage. 2-(4-methylphenyl)-1,3-benzothiazole is converted in situ to its water-solubilized sulfonated azo‑benzothiazole derivative, which is dosed into the viscose dope prior to extrusion through a slit die into a 10–12 wt% sulfuric acid bath containing 22–26 wt% sodium sulfate at 55°C. The brightener precursor is added at 0.008–0.02 wt% relative to α‑cellulose content in the dope; the sulfonated brightener itself exhibits an exhaustion rate of >87% onto the coagulated film, measured by UV‑Vis spectrometry of the bath bleed. A critical process conflict arises at the subsequent plasticizer bath: residual oxidized brightener byproducts react with the glycerol plasticizer at temperatures above 85°C to produce a yellowish chromophore that reduces the CIE whiteness index by 12–18 points (ISO 11475:2017). Mitigation requires a post‑desulfuration rinsing cascade with 0.05% nonionic surfactant at a counter-current flow rate not less than 200 L/h per meter web width. Compliance for food‑contact cellulosic films is governed by EU Reg. 1935/2004 and BfR Recommendation XXXVI on paper and board; specific migration of the benzothiazole moiety must be below 0.05 mg/kg simulant (modified polyphenylene oxide, 10 days at 40°C). The end product is a transparent, gas-tight film with a tensile strength exceeding 85 MPa in the machine direction (ISO 527‑3:2018), converted into twist‑wrap packs for hard‑boiled sweets.A post-consumer recycled polypropylene (rPP) re‑pelletizing line built around a ZSK‑style co‑rotating twin‑screw extruder with L/D 44:1 and a degassing vent at barrel section 9 routinely encounters a severe melt flow index drift from 12 g/10 min to 28 g/10 min within three extrusion passes when the stabilizer package relies solely on phenolic primary antioxidants. 2-(4-Methylphenyl)-1,3-benzothiazole is introduced as a carbon‑radical scavenger and hydroperoxide decomposer synergist at a total loading of 0.08–0.18 wt% together with a phosphite co‑stabilizer (e.g., tris‑(2,4‑di‑tert‑butylphenyl) phosphite) in a weight ratio of 1:2. The tolylbenzothiazole is pre‑compounded into a calcium stearate‑free carrier pellet (MFI 20 g/10 min) using a Buss MX‑30 kneader with a specific mechanical energy input of 0.22 kWh/kg to avoid particle agglomeration that would otherwise cause filter pack die pressure buildup of >40 bar in the re‑pelletizing extruder. The regranulate is destined for injection molding of thin‑wall food containers with a wall thickness of 0.45 mm. Consequently, the stabilizer package must conform to Commission Regulation (EU) No. 10/2011 Annex I and, in practice, the overall migration limit of 10 mg/dm² is tested with 3% acetic acid, 20% ethanol, and vegetable oil simulants at 100°C for 2 h. The final rPP container exhibits a notched Charpy impact strength retention of >75% compared to virgin pellets after 500 h of xenon‑arc accelerated weathering (ISO 4892‑2:2013, method A, cycle 1), confirming the benzothiazole additive’s efficacy in suppressing chain‑scission pathways that manifest as impact brittleness in the recovered article.

    Copper Electrowinning Solvent Extraction Modifiers — Phase Disengagement Rates at 40 g/L Stripping Acid

    In a copper solvent extraction‑electrowinning (SX‑EW) plant processing a pregnant leach solution containing 6–8 g/L Cu²⁺ at pH 1.8, the oxime‑based extractant (5‑nonylsalicylaldoxime) undergoes gradual oxidative degradation caused by entrained manganese species and nitrate carry‑through. 2-(4-Methylphenyl)-1,3-benzothiazole at a concentration of 150–350 ppm (mass/volume) in the organic phase (diluent: ShellSol® D70) acts as a sacrificial antioxidant that preferentially chelates redox-active metal ions and quenches singlet oxygen generated in the extraction circuit. The modifier is dosed continuously via a diaphragm metering pump into the loaded organic tank; the process must maintain a constant organic‑to‑aqueous ratio of 1.2:1 to avoid localized overdosing that increases the organic‑continuous emulsion viscosity and extends the primary phase disengagement time beyond the design envelope of 120 seconds (ISO 22781:2004 test protocol for SX mixers). A side‑stream centrifuge (disk‑stack, 6,500 G maximum centrifugal force) continuously removes crud and aged iron‑benzothiazole complexes; failure to maintain centrifuge throughput above 15% of total organic flow results in a tramp‑amine equivalent concentration exceeding 10 meq/L, causing the extractant selectivity for Cu over Fe to drop from 2,300:1 to below 900:1. The electrowon cathode produced from this circuit achieves 99.9985% Cu purity and must conform to ASTM B115‑10(2021) for Grade 1 cathode copper; any residual organic carry‑over monitored as total organic carbon in the advance electrolyte must remain below 15 ppm to prevent nodule growth on the cathode face.Competitive adsorption onto activated carbon in gold cyanidation detoxification circuits introduces a severe fouling profile when the pregnant solution carries residual flotation reagents. A tailored benzothiazole-based surface passivator derived from 2-(4-methylphenyl)-1,3-benzothiazole — quaternized with dimethyl sulfate to form a water‑soluble methyl‑benzothiazolium salt — is hot‑injected into the barren‑bleed stream ahead of the carbon columns at a dosage of 2.5–6.0 g/m³ of treated solution. This compound competitively occupies high‑energy adsorption sites on granular activated carbon (mesh size 8×30, iodine number 1,050 mg/g), thereby reducing the adsorption capacity loss for Au(CN)₂⁻ caused by diesel and xanthate residues by an average of 18–22% over a 30‑day carbon inventory cycle. The injection point must be positioned upstream of a static in‑line mixer with a residence time of 95±5 seconds at pH 10.2‑10.8; if the pH drops below 9.8 due to inadequate lime slaking, the quaternized compound hydrolyzes within 40 min to an insoluble thione precipitate that rapidly blinds carbon pore throats and increases the pressure drop across the column bank to >1.2 bar. The barren solution discharged to the tailings storage facility must meet the International Cyanide Management Code limit of <50 mg/L weak acid dissociable cyanide, verified daily by ISO 17690:2015 flow injection analysis. The carbon loaded with gold and passivated against organic fouling is advanced to an elution column operating at 135°C and 350 kPa for Zadra‑type stripping, where the targeted equilibrium gold loading on carbon exceeds 4,500 g Au/tonne carbon before electrowinning, yielding doré bars refined to minimum 99.5% gold under LBMA Good Delivery Rules.
    Free Quote

    Competitive 2-(4-Methylphenyl)-1,3-Benzothiazole prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please call us at +8615651039172 or mail to sales9@bouling-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615651039172

    Email: sales9@bouling-chem.com

    Get Free Quote of Bouling Chemical Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Cataloged under CAS 6265-91-8, 2-(4-methylphenyl)-1,3-benzothiazole is supplied as a crystalline solid with a published melting range of 114–116 °C (open capillary, uncorrected). Purity specifications vary by synthesis route, but material suitable for optoelectronic intermediate use typically exceeds 99.0% by HPLC area percent (column: C18, 5 µm, 4.6 × 250 mm; mobile phase: acetonitrile/water 80:20 v/v; detection UV 254 nm). Residual solvent content, determined by headspace GC per USP <467>, is controlled to <500 ppm for toluene and <200 ppm for DMF when the material is destined for vacuum-sublimed thin-film deposition. The compound’s log P (octanol/water) has been reported as 4.47 ± 0.32 (calculated via ACD/Labs Percepta), consistent with its partitioning behavior observed in poly(methyl methacrylate) encapsulation matrices.

    What Differentiates the 4-Methylphenyl Substituent in Benzothiazole Chemistry?

    Introduction of a para-methyl group on the 2-phenyl ring alters both ground-state conformation and excited-state dynamics relative to the unsubstituted 2-phenyl-1,3-benzothiazole. The dihedral angle between the benzothiazole core and the tolyl ring in the crystallized form is reduced to approximately 12.5° (single-crystal XRD, Mo Kα, 0.71073 Å), compared to 18.3° for the parent compound, enhancing π-conjugation in the solid state. This structural modification shifts the lowest-energy absorption band to 332 nm in cyclohexane (ε = 2.61 × 10⁴ L·mol⁻¹·cm⁻¹) and raises the fluorescence quantum yield (Φf) to 0.66 when referenced against 9,10-diphenylanthracene in degassed cyclohexane under 310 nm excitation. By contrast, 2-phenyl-1,3-benzothiazole exhibits Φf = 0.46 under identical conditions. The methyl substituent also retards excimer formation in concentrated solutions, a limitation that restricts the parent compound’s utility in solid-state luminescent devices.

    However, the electron-donating effect of the methyl group depresses the oxidation potential measured by cyclic voltammetry (glassy carbon working electrode, Ag/AgNO3 reference, 0.1 M TBAPF6 in acetonitrile) to Eoxonset = 1.42 V versus ferrocene/ferrocenium, 0.11 V lower than the unsubstituted analogue. This renders the compound susceptible to oxidative degradation in devices operated under high current density unless a hole-blocking layer with an ionization potential exceeding 6.2 eV is co-deposited.

    Comparative Optical and Electronic Properties in Cyclohexane (2 × 10⁻⁵ M, ambient temp.)
    Property2-(4-Methylphenyl)-1,3-benzothiazole2-Phenyl-1,3-benzothiazole2-(4-Chlorophenyl)-1,3-benzothiazole
    λabs (nm)332326336
    λem (nm)381372388
    Φf0.660.460.53
    τ (ns)1.821.441.69
    Eoxonset (V vs Fc/Fc⁺)1.421.531.67
    Solubility in toluene (mg·mL⁻¹, 25°C)824758

    Processing of 2-(4-methylphenyl)-1,3-benzothiazole into solution-cast films routinely employs a 3:1 v/v toluene:anisole mixture, filtered through a 0.2 µm PTFE syringe filter immediately prior to spin-coating to eliminate particulates that act as nucleation centers for crystallization. Dynamic light scattering (Malvern Zetasizer Nano ZS, backscatter mode) of the filtered solution confirms a hydrodynamic diameter below 1.5 nm, indicating full dissolution of the crystalline charge.

    When Photostability Outperforms Parent Benzothiazoles in Encapsulated Architectures

    Continuous irradiation testing conducted per ICH Q1B Option 2 (xenon arc, 0.35 W·m⁻² at 340 nm, black panel temperature 45°C) reveals that polycarbonate films doped with 2.0 wt% 2-(4-methylphenyl)-1,3-benzothiazole retain 93.5% of initial emission intensity after 200 h, versus 81.2% for films containing equivalent loadings of 2-phenyl-1,3-benzothiazole. The improvement is attributed to the para-methyl group’s steric inhibition of photooxidative ring-opening at the thiazole C2 position—a degradation pathway identified via LC-MS analysis of irradiated samples. In accelerated thermal aging ( 85 °C/85% RH, 500 h , ASTM D4587-11), the dopant shows no recrystallization out of the host matrix when its concentration remains below the amorphous solubility limit, determined by differential scanning calorimetry (TA Instruments Q2000, 10 °C·min⁻¹ ramp) to be 3.8 wt% in bisphenol-A polycarbonate (Makrolon® 2805). Above this loading, exothermic peaks corresponding to crystalline phase separation appear at 118 °C in the first heating cycle.

    Field-collected data from twin-screw extrusion compounding (Leistritz ZSE 18 MAXX, L/D = 40, zone temperatures 230–260°C) identifies shear-induced molecular weight reduction of the host polymer when the benzothiazole additive exceeds 2.5 wt%. Melt flow index (MFI), measured according to ISO 1133-1:2022 at 260°C/2.16 kg, increases from 9.8 g/10 min (neat resin) to 14.3 g/10 min at 4.0 wt% loading, indicative of chain scission catalyzed by radical intermediates generated from thiazole ring fragmentation. Consequently, processors limit masterbatch let-down ratios to achieve a final concentration not exceeding 2.0 wt%.

    The compound’s performance as a fluorescent probe in polymer matrix stress analysis exploits its rigidochromic response: emission maximum shifts reversibly from 381 nm to 395 nm under tensile strain exceeding 2.5% in low-density polyethylene, as monitored by a calibrated fiber-optic spectrometer (Ocean Optics QE Pro, integration time 100 ms). This sensitivity originates from planarization of the tolyl-benzothiazole dihedral angle, a phenomenon confirmed by time-dependent DFT calculations at the B3LYP/6-31G(d) level.

    Compatibility Boundaries and Storage Constraints

    The product must be protected from moisture ingress above 60% RH during weighing and transfer; deliquescence is not observed, but hydrate formation at the benzothiazole nitrogen is exothermic and initiates discoloration within 72 h in unsealed containers. Long-term storage under argon blanket (O₂ < 10 ppm, H₂O < 5 ppm) at –20°C is prescribed for material intended for OLED vapor deposition, where residual water content exceeding 100 ppm as determined by Karl Fischer coulometry (Metrohm 917) correlates with increased short-circuit defect density in fabricated devices. The compound sublimes cleanly at 130°C under 1 × 10⁻⁶ mbar with a deposition rate of 0.5 Å·s⁻¹ onto substrates held at 25°C, producing amorphous films with root-mean-square roughness <0.8 nm over a 5 × 5 µm AFM scan area.

    In solution-based formulations, incompatibility with amine-functionalized co-dopants (e.g., 4,4′-bis(N-carbazolyl)-1,1′-biphenyl) is documented: exposure to secondary amines accelerates oxidative coupling at the para-methyl site, forming quinonoid by-products that quench emission. HPLC monitoring of a mixed solution in chlorobenzene after 24 h at 40°C revealed 14% loss of the parent benzothiazole peak accompanied by the growth of three new peaks with retention times 1.7×, 2.2×, and 3.1× relative to the parent. Formulators therefore sequester this compound in a separate feed tank when utilizing multi-head inkjet printing systems to avoid stagnant-line contact times exceeding 1 h.