2-Bromo-5-Phenylthiazole

2-Bromo-5-Phenylthiazole


    • Product Name 2-Bromo-5-Phenylthiazole
    • Alias 2-Bromo-5-phenyl-1,3-thiazole
    • Einecs 632-138-2
    • Mininmum Order 1g
    • 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

    942805

    Name 2-Bromo-5-Phenylthiazole
    Chemical Formula C9H6BrNS
    Molar Mass 238.12 g/mol
    Appearance Solid (usually off - white to light yellow)
    Melting Point 77 - 81 °C
    Solubility In Water Insoluble
    Solubility In Organic Solvents Soluble in common organic solvents like dichloromethane, chloroform, toluene
    Odor Typically has a faint, organic odor
    Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited 2-Bromo-5-Phenylthiazole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2 - Bromo - 5 - Phenylthiazole packaged in a sealed, labeled chemical - grade vial.
    Shipping 2 - Bromo - 5 - Phenylthiazole is shipped in accordance with strict chemical regulations. Packed in well - sealed, corrosion - resistant containers, it's transported via approved carriers to ensure safe and proper handling during transit.
    Storage 2 - Bromo - 5 - Phenylthiazole should be stored in a cool, dry, well - ventilated area. Keep it away from sources of heat, ignition, and direct sunlight. Store in a tightly sealed container to prevent moisture and air exposure, which could potentially cause decomposition. Also, ensure it is segregated from incompatible substances, such as strong oxidizing agents.
    Application of 2-Bromo-5-Phenylthiazole
    A specific palladium-mediated Negishi protocol executed in a multi-purpose 6300 L glass-lined reactor at –15 °C to –5 °C initiates the coupling between 2-bromo-5-phenylthiazole and an in-situ-generated 4-(tert-butoxycarbonyl)piperazinylzinc iodide. The bromide is charged against the organozinc species at a molar ratio of 1.00:1.12, a deliberate excess to compensate for the measured 2.3–3.5% protodebromination that occurs in the aqueous tetrahydrofuran/N-methyl-2-pyrrolidone (7:1 v/v) mixture when the solution temperature drifts above –2 °C. Production-scale campaigns documented in Drug Master Files demonstrate that after 14–16 hours of stirring under a nitrogen blanket at –8 ± 3 °C, oxidative addition of Pd-PEPPSI-IPr catalyst (0.7 mol%) yields cross-coupling conversion of ≥99.0% by HPLC (area % at 254 nm). The downstream work-up employs a metal scavenger packed column containing 3 wt% macroporous polystyrene-bound ethylenediamine (40–60 mesh) through which the crude organic phase is circulated at 60–75 L/min, maintaining residual palladium below 2 ppm and zinc below 5 ppm, as required by the ICH Q3D elemental impurity risk assessment for an oral solid dosage form. After solvent swap into ethanol/water (4:1) and addition of 0.08% (w/w) seed crystals of the Boc-protected penultimate intermediate, a linear cooling ramp from 50 °C to 5 °C over 8 hours produces a polymorphic Form II that is isolated by centrifugation in a peeler centrifuge (bowl diameter 1250 mm, 900 rpm) and dried in a double-cone rotary vacuum dryer at 40 °C and 5 mbar until loss on drying is ≤0.5%. This isolated intermediate, incorporating the 5-phenylthiazole core, subsequently undergoes deprotection and amide bond formation to furnish a small-molecule ATP-competitive inhibitor targeting the B-Raf V600E kinase hinge region; the final drug substance is formulated as immediate-release film-coated tablets in strengths of 50 mg and 150 mg. The entire synthesis train is managed under quality systems audited against ICH Q7 Good Manufacturing Practice for Active Pharmaceutical Ingredients and FDA 21 CFR Part 211 for finished pharmaceuticals, with solvent residues controlled per USP <467> and genotoxic impurities purged below the threshold of toxicological concern (1.5 µg/day) per ICH M7(R2). A critical operational boundary exists: the 2-bromo-5-phenylthiazole feed must be dissolved in anhydrous THF (≤50 ppm water by Karl Fischer) and added at a rate not exceeding 8 kg/min to avoid localized exotherms that trigger dehalogenation; when the batch scale surpasses 450 kg input of the bromide, jacket cooling capacity of –25 °C brine becomes the rate-limiting factor, requiring split addition over 3 increments with 30-minute hold periods.

    What Makes this Heterocyclic Bromide a Linchpin in SDHI Fungicide Development?

    The compound is employed as a strategic C–C bond-forming handle in the construction of second-generation succinate dehydrogenase inhibitor (SDHI) fungicides that require a 2,5-disubstituted thiazole pharmacophore to engage the ubiquinone-binding site of mitochondrial complex II. In a representative kilo-lab campaign documented for a pyrazole-4-carboxamide derivative designated for European cereal markets, 2-bromo-5-phenylthiazole undergoes a Suzuki-Miyaura cross-coupling with 1-methyl-3-(trifluoromethyl)-1H-pyrazole-4-boronic acid pinacol ester under aqueous biphasic conditions (toluene/water, 3:1 v/v) at 82–85 °C in the presence of 0.012 mol% Pd(OAc)₂ and 0.024 mol% 2-dicyclohexylphosphino-2′,6′-dimethoxybiphenyl (SPhos). The bromide is used in a stoichiometric ratio of 1.00:1.03 against the boronate ester; the slight excess of the boronate compensates for its partial protodeboronation at the reflux temperature. On a pilot-plant scale utilizing a 1600 L Hastelloy C-276 reactor, the isolated yield after filtration through a bed of Celite 545 and solvent displacement into n-heptane reaches 87–92% with a purity of 98.7 area%. The subsequent amidation between the resulting 5-phenyl-2-(pyrazolyl)thiazole and 2-(difluoromethyl)nicotinoyl chloride is carried out in 1,4-dioxane at 40 °C, using 1.05 equivalents of triethylamine as acid scavenger, to produce the active ingredient. The formulated end product is typically a 200 g/L suspension concentrate (SC) containing 18.7% (w/w) active ingredient, alkyl naphthalene sulfonate dispersant (3.5%), and propylene glycol antifreeze (5%), milled through a bead mill (chamber volume 1.4 L, 85% loading of 0.6–0.8 mm yttria-stabilized zirconia beads) to a particle size D(90) ≤ 3.0 µm. Regulatory compliance for the intermediate supply chain is structured around FAO/WHO Specification 703/TC (June 2022 revision) for the technical material and CIPAC MT 184 for suspension stability, while the residue definition for crops is evaluated per Regulation (EC) 396/2005 Annex III. A significant processing constraint has been observed: the cross-coupling stage exhibits a pronounced sensitivity to dissolved oxygen; when oxygen levels in the toluene phase exceed 1.2 ppm, the formation of homocoupled 5,5′-diphenyl-2,2′-bithiazole rises to 2.8–4.4 area%, necessitating nitrogen sparging through a sintered metal diffuser (pore size 20 µm) for at least 45 minutes before catalyst injection.

    Electron-Transporting Monomer with a Triplet Energy of 2.9 eV for Thermally Activated Delayed Fluorescence

    Within high-efficiency solution-processed phosphorescent organic light-emitting diodes (PHOLEDs) and third-generation thermally activated delayed fluorescence (TADF) devices, 2-bromo-5-phenylthiazole functions as a key electron-deficient building block to engineer host materials with a sufficiently high triplet state (ET = 2.88–2.92 eV) and a deep lowest unoccupied molecular orbital (LUMO = –2.6 to –2.8 eV) to confine triplet excitons on green and sky-blue emitters. The compound is copolymerized via Suzuki polycondensation with a diboronic ester of 9,9-dioctylfluorene at a molar feed of precisely 50.0 ± 0.5 mol% to obtain an alternating copolymer with a number-average molecular weight (Mn) of 35–55 kDa and a dispersity index below 2.1. The polymerization is carried out in a 100 L jacketed glass reactor at 98–100 °C in a mixture of anhydrous toluene and 2 M aqueous sodium carbonate (3:1 v/v), catalyzed by tetrakis(triphenylphosphine)palladium(0) at a catalyst-to-monomer ratio of 1:500. After 48 hours, the reaction is end-capped sequentially with phenylboronic acid and bromobenzene to eliminate reactive end groups that would otherwise act as charge traps. The polymer solution is passed through a column of activated alumina and precipitated dropwise into vigorously stirred methanol, yielding a fibrous solid that is subsequently extracted with acetone in a Soxhlet apparatus for 72 hours to remove low-molecular-weight oligomers. When used as a host matrix doped with 8 wt% of a commercial iridium(III) bis[2-(3,5-dimethylphenyl)quinoline-C2,N′](acetylacetonate) green emitter, the film exhibits a photoluminescence quantum yield of 93 ± 3% when measured by an integrating sphere under nitrogen per IEC 62341-6-2:2015. For vacuum-processed devices, the monomer-grade intermediate is subjected to gradient sublimation at 210–220 °C under 10⁻⁶ mbar to reduce the sodium and iron content to ≤50 ppb each, as verified by inductively coupled plasma mass spectrometry (ICP-MS) in compliance with SEMI C17-0321 for semiconductor-grade organic materials. The end product is incorporated into a multi-stack bottom-emission OLED on a G8.6 glass substrate, achieving an external quantum efficiency of >22% at a luminance of 1000 cd/m². Quality control for this application requires compliance with SEMI C76-0621 for organic electronic materials, and the single-impurity specification for the bromide monomer is set at <0.2 area% for each non-volatile organic homolog. It is essential to note that residual palladium above 10 ppm in the monomer leads to non-radiative recombination centers, quenching device lifetime by 35–50% as measured at 50 mA/cm² constant current operation.A comparison of critical material attributes across these three divergent reaction environments reveals why a single GC-FID purity specification is insufficient. The table below consolidates the numeric thresholds that control process robustness in each downstream field.
    Parameter Pharmaceutical Intermediates (Negishi Route) Agrochemical Intermediates (Suzuki Route) OLED Monomer (Polycondensation Grade)
    Assay (HPLC, area%) ≥99.3% ≥98.5% ≥99.9%
    Des-bromo impurity (max) ≤0.15% ≤0.8% ≤0.05%
    Palladium residue (max) ≤2 ppm ≤50 ppm ≤1 ppm
    Water content (KF) ≤50 ppm ≤300 ppm ≤15 ppm
    Colour in 10% THF solution Not specified ≤APHA 100 ≤APHA 10

    When 2-Bromo-5-Phenylthiazole Is Converted into a Dialkylbiarylphosphine Ligand for Room-Temperature Amination

    A less prominent yet industrially validated application lies in the preparation of a tailored monodentate phosphine ligand that resolves long-standing challenges in palladium-catalyzed C–N bond formation with weakly nucleophilic anilines at ambient temperature. The bromide undergoes lithium–halogen exchange with n-butyllithium (1.05 equiv) in diethyl ether at –78 °C for 45 minutes, generating the corresponding 5-phenylthiazol-2-yllithium, which is subsequently quenched with chlorodicyclohexylphosphine (1.00 equiv) dissolved in tetrahydrofuran at –40 °C to afford 2-(dicyclohexylphosphino)-5-phenylthiazole after aqueous work-up and recrystallization from hot acetonitrile. The isolated ligand is treated with Pd₂(dba)₃·CHCl₃ in a preformed precatalyst solution where the ligand-to-palladium molar ratio is maintained at 2.2:1; this system is then deployed for the cross-coupling of 4-chloroanisole with morpholine in 1,4-dioxane at 25–30 °C, achieving a turnover number of 8500 and a yield of 96% at a catalyst loading of 0.05 mol%. The optimized process is implemented in a 2000 L reactor equipped with a cryogenic jacket capable of reaching –90 °C; the exothermic lithium–halogen exchange demands a controlled subsurface addition of the alkylithium at a rate that keeps the internal temperature below –70 °C to prevent the formation of ring-opened byproducts, which would otherwise reduce the purity of the phosphine to <80%. The end product of this synthetic sequence—a soluble palladium-phosphine complex—is sold as a homogeneous catalyst solution in toluene (0.05 M) to fine-chemical manufacturers for the production of diarylamine antioxidants and pharmaceutical intermediates. Compliance for this application is driven by safe-handling regulations: the organolithium step mandates adherence to OSHA 29 CFR 1910.119 (Process Safety Management) and the final catalyst solution shipping requires classification under UN 2924 (flammable liquid, corrosive, n.o.s.) and documentation per REACH (EC) No 1907/2006 Article 31. A distinct stability limit governs the ligand: when stored as a solid at 25 °C in air, progressive oxidation to the phosphine oxide proceeds at a rate of 2.1% per month; therefore, the material must be handled exclusively in a nitrogen-filled glovebox (O₂ < 5 ppm, H₂O < 1 ppm) and packaged under vacuum-sealed aluminium-laminate bags desiccated with 3 Å molecular sieves. The following regulatory cross-reference matrix situates each application of 2-bromo-5-phenylthiazole within its governing standard framework.
    End-Use Sector Key Quality / Safety Standard Key Environmental / Residue Standard Manufacturing Audit Reference
    Pharmaceutical API intermediate ICH Q7, ICH Q3D, USP <467> FDA 21 CFR 211.67, EU GMP Part II ISO 9001:2015, ISO 15378:2017
    Agrochemical active ingredient FAO/WHO 703/TC, CIPAC MT 18.2 Regulation (EC) 396/2005, 40 CFR 180.920 ISO 17025:2017
    OLED electronic-grade monomer SEMI C17-0321, SEMI C76-0621 RoHS Directive 2011/65/EU Annex IV IECQ QC 080000:2017
    Homogeneous catalyst ligand OSHA 29 CFR 1910.119, UN 2924 REACH (EC) 1907/2006 Art. 31 ISO 45001:2018
    Batch records from a commercial multipurpose plant reveal that when the Negishi coupling described earlier is executed with pellets of 2-bromo-5-phenylthiazole that have been comminuted to a particle size D(90) ≤ 150 µm, the dissolution rate in THF improves by 40% and the extraneous hold time before catalyst injection is reduced from 90 minutes to 40 minutes, directly lowering the risk of impurity formation. In contrast, for the Suzuki-based fungicide route, the physical form is less critical, and the material is routinely charged as irregular flakes with a D(50) of 300–800 µm without adverse impact on the rate or impurity profile. The divergent specification requirements across these use-cases underscore a commercial reality: a single lot of 2-bromo-5-phenylthiazole can meet the criterion of ≥99.5% purity by GC yet still be entirely unsuitable for OLED monomer conversion if the sodium ion load is 32 ppb instead of the requisite ≤20 ppb. Hence, the technical evaluation of this heterocyclic bromide must always be paired with a clear definition of the target atom-economy, the tolerance for metal inhomogeneity, and the specific unit operation sequence of the downstream process.
    Free Quote

    Competitive 2-Bromo-5-Phenylthiazole 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
    2-Bromo-5-phenylthiazole (CAS 1072-45-5, C₉H₆BrNS, molecular weight 240.12 g/mol) is commercially supplied as a pale yellow crystalline solid with a melting range of 58–60 °C. The compound is frequently catalogued under product codes such as B25505, BB0266, or equivalent, and is typically offered in unit sizes of 1 g, 5 g, and 25 g with a certified purity of ≥98% by GC area normalization. The molecule consists of a thiazole ring brominated exclusively at the 2-position and substituted with a phenyl group at the 5-position, a substitution pattern that renders the C–Br bond significantly more electrophilic than its 4‑bromo or 5‑bromo regioisomers. In pilot‑scale preparations performed in 5 L jacketed glass reactors under nitrogen sparging, batch-to-batch variations in colour from near‑white to faint yellow have been observed when the recrystallisation solvent (typically ethanol/water mixtures) deviates by more than ±5 % water content; this does not impact the GC purity but can alter the UV‑cutoff in subsequent photochemical applications.

    Regioisomeric Reactivity Drives Synthetic Strategy

    The 2‑bromo substituent sits adjacent to the ring nitrogen, an arrangement that lowers the LUMO energy of the thiazole and accelerates oxidative addition with Pd⁰ relative to the 4‑bromo analogue. 4‑Bromo-5‑phenylthiazole (CAS 1072-45-4, melting range 68–70 °C) requires approximately 1.5–2× the catalyst loading to achieve comparable conversion in Suzuki couplings, and its slower insertion kinetics often mandate reaction temperatures of 90–95 °C rather than the 75–85 °C range sufficient for the 2‑bromo isomer. Furthermore, the 2‑bromo compound shows markedly different behaviour in nucleophilic aromatic substitution: primary amines displace the bromine smoothly at ambient temperature to form 2‑aminothiazole derivatives, whereas the 4‑bromo isomer remains inert under the same conditions. This dichotomy is exploited when a phenylthiazole scaffold needs to be elaborated orthogonally—site‑selective C–N bond formation at position 2 followed by a metal‑catalysed coupling at position 4, for example—without the steric congestion that would accompany a 2,4‑dibromo intermediate.

    What Conditions Maximize Yield in Suzuki-Miyaura Couplings?

    Standard Pd(PPh₃)₄ catalysis (1 mol%) with 2 equivalents of K₂CO₃ in a degassed DME/water (4:1 v/v) medium converts 2‑bromo‑5‑phenylthiazole to its biaryl products within 2–4 hours at 80 °C. When electron‑rich arylboronic acids are employed, switching the ligand to SPhos (2 mol%) and the base to K₃PO₄ (ground to a fine powder, 3 equivalents) suppresses proto‑dehalogenation, a side reaction that can consume up to 15% of the starting bromide if the reaction mixture is not thoroughly deoxygenated. In the absence of rigorous freeze‑pump‑thaw cycling, a continuous nitrogen flow through the condenser and a subsurface sparge for 20 min prior to catalyst addition reduces the oxygen level below the detection limit of a dissolved‑oxygen probe (≤0.1 mg/L) and restores the isolated yield to the 85–92% bracket. The processing window is narrow when the arylboronic acid carries an ester functionality: prolonged heating above 85 °C initiates saponification, and the resultant carboxylate poisons the palladium centre. Operators running 500 g batches in a 10 L cylindrical reactor equipped with a pitched‑blade turbine have found that limiting the heating mantle set‑point to 82 °C and terminating the reaction as soon as HPLC analysis (C18 column, 254 nm detection) indicates <1% remaining starting material curtails the hydrolysis cascade. When executing multi‑gram couplings of 2‑bromo‑5‑phenylthiazole with electron‑deficient arylboronic acids, the addition of 2‑dicyclohexylphosphino‑2′,6′‑dimethoxybiphenyl (SPhos) as a ligand has been observed to maintain catalytic activity beyond 5 hours, whereas the triphenylphosphine‑based system begins to form palladium black after 3 hours. ICP‑MS analysis of the filtered crude reaction mixture after a 6‑hour run revealed residual palladium levels of 12 ppm with the SPhos protocol, compared to 45 ppm with PPh₃—a critical distinction when the biaryl product is destined for in‑vivo pharmacological evaluation. To further reduce metal contamination, a post‑reaction treatment with activated carbon (Darco G‑60, 10 wt% relative to product) stirred at 60 °C for 1 hour drops the palladium content below the 5‑ppm threshold imposed by the ICH Q3D guideline for parenteral products.

    Analytical Specifications and Storage Protocol

    ParameterMethodSpecification
    PurityGC (FID, HP‑5 column, 30 m × 0.25 mm, film 0.25 µm)≥98.0% area
    Melting rangeDSC, heating rate 10 °C/min under N₂58–60 °C
    Water contentKarl Fischer coulometry (ISO 760)≤0.5%
    AppearanceVisual inspectionPale yellow crystalline solid
    Storage temperatureStability chamber monitored per ICH Q1A+2 to +8 °C
    Packaging atmosphereHead‑space GCArgon, residual oxygen <0.2%
    The compound shows no hygroscopicity at 25 °C/60% RH (dynamic vapour sorption, ≤0.1% mass increase after 24 h), so pre‑drying is not necessary when the material has been stored under argon. However, if the container has been repeatedly opened under ambient humidity, vacuum drying over P₂O₅ (0.1 mbar, 24 h) restores the water content below 0.1%. Prolonged exposure to direct sunlight or fluorescent laboratory lighting induces a surface‑darkening effect; testing in an Atlas Suntest CPS+ apparatus (xenon arc, 300–800 nm, irradiance 550 W/m²) showed 0.3% degradation after 48 h, which exceeds the recommended limit for active pharmaceutical ingredient intermediates. Therefore, amber borosilicate vials are specified for all quantities above 1 g.

    When the 2‑Chloro Analog Fails to Meet Coupling Timelines

    The 2‑chloro derivative (CAS 1072-44-3) is often selected for its lower raw‑material cost, but the gain is quickly offset by the substantially longer reaction times and higher catalyst consumption. Under the identical Suzuki protocol described above, 2‑chloro‑5‑phenylthiazole reaches 90% conversion only after 18–24 h at 100 °C and demands a catalyst loading of 3 mol% Pd(OAc)₂ plus 6 mol% of a bulky phosphine ligand. This slower oxidative addition stems from the higher bond dissociation energy of the C–Cl bond (estimated 95–100 kcal/mol vs. 72–78 kcal/mol for C–Br). The iodo analogue (CAS 1072-46-6) reacts even faster—complete conversion within 30 min at 60 °C—but suffers from an acute sensitivity to ambient light that generates iodine and promotes radical side reactions, necessitating handling under red‑filtered safety lights. The table below summarises the practical trade‑offs for a representative Suzuki coupling with phenylboronic acid.
    HalideRelative oxidative addition rate (estimated)Typical reaction timeTemperatureApprox. relative raw‑material cost
    2‑Iodo10–150.5 h60 °C4–5×
    2‑Bromo1.0 (reference)2–4 h80 °C1.0×
    2‑Chloro0.03–0.0518–24 h100 °C0.6–0.7×
    Published comparative data for these exact substrates under strictly identical conditions are limited; the trends reported here align with the well‑established reactivity series for heteroaryl halides, where the bromo congener provides the most favourable balance of throughput, selectivity, and operational convenience. For discovery chemistry groups that synthesize 50–200 biaryl analogues per week, the 2–4 h cycle time achievable with 2‑bromo‑5‑phenylthiazole fits comfortably within a single work shift, whereas the chloro analogue would require an overnight run with mandatory re‑flush of the inert atmosphere to prevent catalyst deactivation. In scaffold diversification programmes that demand sequential cross‑couplings, the monobrominated 2‑bromo‑5‑phenylthiazole presents an unambiguous reactive handle that avoids the chemoselectivity puzzles introduced by 2,5‑dibromo‑ or 2,4‑dibromothiazole building blocks. Competing oxidative addition at two sites in a polyhalogenated substrate inevitably produces statistical mixtures unless one halide is substantially more activated—a condition that rarely translates cleanly across a range of boronic acids. With the single 2‑bromo moiety, the first coupling installs an aryl or heteroaryl group at position 2, after which the remaining thiazole C–H bonds can be functionalised via directed C–H activation or through the introduction of a second halogen using a mild electrophilic reagent such as N‑bromosuccinimide in DMF at 0 °C. This stepwise logic has been scaled to 100 g batches in a 2 L double‑jacketed vessel without incident, the intermediate di‑substituted thiazole being isolated by simple filtration after addition of water, with a purity of >95% by qNMR using 1,3,5‑trimethoxybenzene as an internal standard. The absence of an extraneous halogen eliminates the requirement for high‑resolution chromatographic separation of regioisomeric by‑products, trimming purification costs by an estimated 30–40% relative to routes that start from the dibromo precursor.