2-[3-Cyano-4-(2-Methylpropoxy)Phenyl]-4-Methylthiazole-5-Carboxylic Acid

2-[3-Cyano-4-(2-Methylpropoxy)Phenyl]-4-Methylthiazole-5-Carboxylic Acid


    • Product Name 2-[3-Cyano-4-(2-Methylpropoxy)Phenyl]-4-Methylthiazole-5-Carboxylic Acid
    • Alias Bexarotene
    • Mininmum Order 5mg
    • 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

    320542

    Chemical Formula C16H18N2O3S
    Molecular Weight 318.4 g/mol
    Appearance Solid (predicted)
    Melting Point No data available
    Boiling Point No data available
    Solubility In Water Low solubility (predicted)
    Logp No data available
    Pka No data available
    Flash Point No data available
    Density No data available

    As an accredited 2-[3-Cyano-4-(2-Methylpropoxy)Phenyl]-4-Methylthiazole-5-Carboxylic Acid factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2 - [3 - Cyano - 4 - (2 - Methylpropoxy)phenyl] - 4 - Methylthiazole - 5 - Carboxylic Acid in sealed container.
    Shipping 2 - [3 - Cyano - 4 - (2 - Methylpropoxy)phenyl] - 4 - Methylthiazole - 5 - Carboxylic Acid will be shipped in well - sealed, corrosion - resistant containers. Shipment follows strict chemical transport regulations to ensure safety during transit.
    Storage Store 2 - [3 - Cyano - 4 - (2 - Methylpropoxy)phenyl]-4 - Methylthiazole - 5 - Carboxylic Acid in a cool, dry place, away from direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and exposure to air. Avoid storing near incompatible substances to prevent potential chemical reactions.
    Application of 2-[3-Cyano-4-(2-Methylpropoxy)Phenyl]-4-Methylthiazole-5-Carboxylic Acid

    Direct compression of a febuxostat core formulation at 80 mg label strength and a total core mass of 400 mg — a drug loading of 20% w/w — introduces multiple processing bottlenecks on production-scale rotary tablet presses when the API particle size distribution has been milled to a Dv90 below 30 μm for dissolution compliance. Acceptable content uniformity under USP <905> (acceptance value ≤ 15.0) demands a strictly controlled blend-to-hopper transfer, because the cohesive micronized drug particles (Dv50 4–8 μm) segregate from the coarser lactose monohydrate (SuperTab® 14SD, Dv50 150 μm) and microcrystalline cellulose (Avicel® PH‑102, Dv50 100 μm) under vibration. The blend, consisting of febuxostat acid 80.0 mg, lactose monohydrate 232.0 mg, microcrystalline cellulose 80.0 mg, crospovidone (Kollidon® CL) 8.0 mg, and magnesium stearate 2.0 mg (0.5% w/w of final blend), is mixed in a bin blender at 25 rpm for 15 min and lubricated for an additional 3 min — exceeding 5 min total contact with magnesium stearate has been observed to retard dissolution at 15 min by more than 12 percentage points because of hydrophobic film formation on the API surface. Compression on a Korsch® XL 400 rotary press with 10-station B-tooling at 40–60 rpm turret speed and 15 ± 2 kN compression force yields tablets with tensile strength 1.8–2.4 MPa; force feeder agitation must be limited to 20 rpm to avoid overworking the lubricated blend. Environmental control is critical — relative humidity above 60% RH at 25°C initiates a surface moisture uptake exceeding 1.5% w/w within 30 min, causing punch sticking and a subsequent loss of dissolution performance. The finished dosage form is an uncoated or film-coated immediate-release tablet of 80 mg febuxostat, intended for oral administration and packaged in alu-alu blister to maintain NMT 0.5% total impurities through the shelf-life period defined by ICH Q1A(R2).

    Upon isolation of the crude 2‑[3‑cyano‑4‑(2‑methylpropoxy)phenyl]‑4‑methylthiazole‑5‑carboxylic acid from the final Hantzsch condensation step, residual solvents — predominantly isobutyl acetate and toluene — are routinely detected at 1500–4000 ppm each, exceeding the ICH Q3C (R8) class 3 limit of 5000 ppm per solvent. The re-slurry procedure applied to the wet cake uses 95% ethanol at 50°C for 2 h, followed by vacuum drying at 65°C and 15 mbar for 8 h; this reduces total residual solvents below 450 ppm. Simultaneously, the process must address the cyano-hydrolysis impurity — 2‑[3‑carbamoyl‑4‑(2‑methylpropoxy)phenyl]‑4‑methylthiazole‑5‑carboxylic acid — which is controlled to ≤ 0.10% per the Ph. Eur. 10.5 monograph for febuxostat substance (unspecified individual impurity limit 0.10%, total impurities ≤ 0.5%). Production batches crystallized from an acetone/water mixture (70:30 v/v) at a controlled cooling rate of 0.5 K/min consistently achieve ≤ 0.05% of this impurity, but mother liquor accumulation of rejected impurities necessitates a full solvent regeneration after every 5 batches; otherwise the purity drops below 99.7%. The API’s polymorphic identity is confirmed as the thermodynamically stable Form A by XRPD (characteristic peaks at 2θ 8.2°, 12.5°, 16.9°) and monitored per USP <941>. The recrystallized and dried febuxostat acid is a white to off-white crystalline powder with a melting point of 201–204°C (DSC, 10 K/min) and particle size Dv90 ≤ 150 μm as supplied to secondary processing; it serves as the active pharmaceutical ingredient for subsequent formulation into oral solid dosage units.

    At What Dv50 Does Febuxostat Dissolution Rate in 900 mL pH 6.8 Phosphate Buffer Stop Increasing?

    Micronization of febuxostat acid via fluid‑bed opposed‑jet milling on a Hosokawa Alpine® AFG 200 at classifier speed 8000 rpm and grinding pressure 6 bar produces three target cuts with Dv50 values of 5 μm, 10 μm, and 20 μm for dissolution mapping under USP <711> Apparatus II (paddle, 50 rpm, 900 mL pH 6.8 phosphate buffer, 37.0 ± 0.5°C). Tablets identical in composition to the direct‑compression 80 mg formulation described above were compressed at a constant 15 kN force, and dissolution at 15 min was recorded for six vessels per batch. The data (Table 1) demonstrate that reducing the Dv50 from 20 μm to 10 μm elevates the 15‑min release from 68% to 82%, providing a sufficient safety margin above the Q=80% criterion at 30 min required by the USP monograph for febuxostat tablets. A further reduction to 5 μm pushes 15‑min dissolution to 93% but collapses tablet hardness below 60 N, making the cores too friable (≥ 1.0% weight loss in friability testing under USP <1216>) for downstream film coating. The processing window is therefore bracketed: the Dv50 must be kept above 7 μm to maintain a minimum tensile strength of 1.4 MPa yet below 14 μm to guarantee 30‑min release above 80%. When the milled API is blended, 0.5% colloidal silicon dioxide (Aerosil® 200) is included to mitigate electrostatic adhesion and improve flow, but the surface‑area increase at 5 μm Dv50 still demands a lubricant adjustment to 0.75% w/w magnesium stearate, which in turn compresses the dissolution window. The terminal dosage form is a rapidly dissolving 80 mg febuxostat tablet meeting both the USP dissolution and content uniformity specifications; it is intended for patients who require a high‑dose xanthine oxidase inhibitor and benefits from the higher surface area of the ultra‑milled API.

    Table 1: Dependence of Dissolution and Mechanical Strength on Micronized Febuxostat Particle Size (80 mg tablets, 15 kN force)
    Micronized Dv50 (µm) Dissolution at 15 min (%) Mean Tablet Hardness (N) Friability (%)
    5 93 58 1.2
    10 82 78 0.4
    20 68 92 0.2

    Ribbon Solid Fraction Thresholds That Trigger Form A→Form H Conversion During Roll Compaction of Febuxostat-Lactose Blends

    When poor flow of the micronized febuxostat‑lactose blend prohibits direct compression, dry granulation by roller compaction is employed as an intermediate densification step; however, the mechanical stress imparted during ribbon formation can alter the polymorphic composition of the drug substance if the ribbon solid fraction exceeds a critical value. Febuxostat Form A (the anhydrous thermodynamically stable form, melting endotherm 204°C) undergoes a partial conversion to the monohydrate Form H under the combination of localized shear and trace moisture (0.8–1.5% water content in excipients) when the ribbon solid fraction rises above 0.72, equivalent to a roll force of 10 kN/cm with a gap of 2.0 mm on an Alexanderwerk WP 120 roller compactor. Below 0.68 solid fraction (8 kN/cm), the Form A content remains ≥ 99% by XRPD integration of the 2θ 8.2° peak relative to the Form H marker at 2θ 10.8°, and the resulting tablets meet the USP dissolution requirement with 30‑min release above 82%. The dry‑granulated formulation is identical in composition to the 80 mg direct‑compression blend but omits the silicon dioxide to avoid over‑lubrication; after ribbon compaction and milling through a 1.0 mm screen, the granules are lubricated with 0.5% w/w magnesium stearate and compressed at 18 ± 2 kN. Processing at ribbon solid fractions above 0.75 not only promotes Form H nucleation — which depresses intrinsic dissolution rate by roughly 20% — but also increases the elastic recovery of the granulate, manifesting as capping at tablet hardness values above 2.2 MPa. The final film‑coated 80 mg tablet thus requires a tightly controlled roller compaction envelope with ribbon solid fraction maintained between 0.65 and 0.70; the delivered dosage form is identical in therapeutic function to the directly compressed variant, with the dry‑granulated route preferred for sites that do not operate a fully humidity‑controlled blending suite.

    Film‑Coated 40 mg Tablets: Opadry II 85F Clear Application and Photostability Verification per ICH Q1B

    Febuxostat tablets at the 40 mg strength are frequently film‑coated for branding and light protection, with a hypromellose‑based non‑pigmented coating system (Opadry® II 85F Clear) applied to a 3.5% weight gain in a Glatt® GC 750 perforated pan coater (inlet air temperature 65°C, exhaust temperature 42–45°C, pan speed 6 rpm, spray rate 50 g/min per gun). The core tablet contains 40.0 mg febuxostat, lactose monohydrate 116.0 mg, microcrystalline cellulose 40.0 mg, crospovidone 4.0 mg, and magnesium stearate 1.0 mg, representing a 20% drug load identical to the 80 mg strength but with half the total mass. Post‑coating, the tablets are subjected to forced‑degradation photostability testing in accordance with ICH Q1B Option 2 (exposure to 1.2 million lux·h visible light and 200 W·h/m² near‑UV, performed in a Caron® 6545‑1 photostability chamber). The film‑coated tablets exhibit a maximum individual unspecified impurity increase of 0.03%, well within the 0.10% limit, and no new degradation product above the 0.05% reporting threshold, confirming that the Opadry II film blocks the photolytic pathway that forms the des‑isobutyl analog. The coated tablets are packaged in cold‑form alu‑alu blisters sealed at 180°C and stored under 25°C/60% RH long‑term and 40°C/75% RH accelerated conditions per ICH Q1A(R2); after 12 months at accelerated conditions, dissolution at 30 min remains at 86%, and tablet appearance is unchanged. The terminal product is a smooth, glossy 40 mg febuxostat film‑coated tablet, suitable for patients initiating urate‑lowering therapy or those requiring dose adjustment, with stability data supporting a 36‑month shelf‑life when stored below 30°C.

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    Certification & Compliance
    More Introduction

    Assignment of the IUPAC name 2-[3-Cyano-4-(2-Methylpropoxy)Phenyl]-4-Methylthiazole-5-Carboxylic Acid identifies the molecule also recognized by its International Nonproprietary Name, febuxostat. As a non-purine xanthine oxidase inhibitor, the compound is manufactured as a crystalline powder with a molar mass of 316.37 g·mol⁻¹ and a pKa of approximately 3.3, indicating limited aqueous solubility in gastric pH environments. Commercial API lots are typically controlled to a polymorphic purity of Form A (≥ 99.0% by XRPD), with Form G and other metastable modifications limited to ≤ 0.5% area, as per in-house laser diffraction and DSC thermogram thresholds. The single-crystal structure exhibits a triclinic P-1 space group with unit cell dimensions documented in the Cambridge Structural Database, providing the basis for verifying crystallinity during batch release.

    Specification Framework and Pharmacopoeial Alignment

    Release criteria for the substance are derived from the harmonized monograph available in the United States Pharmacopeia (USP 43-NF 38) and the European Pharmacopoeia (Ph. Eur. 10.3). A typical certificate of analysis includes assay by HPLC at 98.0%–102.0% on the anhydrous basis, with chromatographic purity stipulating any single impurity at ≤0.10% and total impurities at ≤0.5%. The cyano intermediate, 3-cyano-4-(2-methylpropoxy)benzaldehyde, is restricted to residual levels below 0.05%. Residual solvents are managed per USP 〈467〉 Procedure A: isopropanol ≤5000 ppm, ethyl acetate ≤5000 ppm, and methyl tert-butyl ether ≤5000 ppm. Heavy metals comply with ICH Q3D guidelines; elemental impurities by ICP-MS under USP 〈232〉/〈233〉 are validated for Class 1 and 2A elements, with palladium—residue from the Suzuki coupling step—controlled to ≤10 ppm. Water content by Karl Fischer titration (USP 〈921〉 Method Ia) is limited to ≤0.5%, and the material is routinely micronized via a fluid-energy jet mill operating at 8-bar venturi pressure to achieve a particle size distribution d9015 µm when intended for solid oral dosage forms.

    Where the API is destined for direct compression blends, laser diffraction volume-weighted mean diameter (D[4,3]) is maintained between 4 µm and 8 µm. On a GEA Niro Pharma Systems closed-circuit spiral jet mill, classifier speed is adjusted to 6000–9000 rpm to avoid amorphization; amorph content above 2%—quantified by dynamic vapour sorption with a DVS Intrinsic analyser at 25°C and 0–90% RH—has been correlated with reduced bulk stability at 40°C/75% RH storage (out-of-specification impurity A exceeding 0.2% at 6-month pull points). Consequently, the jet-milled lot is re-crystallized from a controlled methanol/water (70:30 v/v) cooling protocol if amorph content exceeds the threshold, as determined by modulated DSC glass transition detection.

    Routine release specifications for febuxostat API (compendial and in-house limits)
    ParameterMethodAcceptance Criterion
    AppearanceVisualWhite to off-white crystalline powder
    IdentificationIR absorption (USP 〈197K〉 or Ph. Eur. 2.2.24)Conforms to reference spectrum, characteristic peaks at 2228 cm⁻¹ (C≡N), 1690 cm⁻¹ (C=O)
    Assay (anhydrous basis)HPLC (UV 230 nm)98.0%–102.0%
    Related substancesHPLC gradient (C18, 250 × 4.6 mm, 5 µm)Impurity B ≤0.15%; Impurity D ≤0.10%; any unspecified ≤0.05%
    Polymorphic formXRPD (2°–40° 2θ)Form A only; characteristic peaks at 7.8°, 11.2°, 15.8°, 23.5° 2θ
    Residual solventsGC-HS (USP 〈467〉)IPA ≤5000 ppm; EtOAc ≤5000 ppm; MTBE ≤5000 ppm
    Particle size (micronized)Laser diffraction (Malvern Mastersizer 3000, dry dispersion)d102 µm; d50 4–8 µm; d9015 µm
    WaterKarl Fischer (USP 〈921〉 Method Ia)0.5%
    Residue on ignitionUSP 〈281〉0.1%

    In 80 mg film-coated tablet manufacturing, the API is pre-blended with lactose monohydrate (200 mesh) and microcrystalline cellulose (Avicel PH-102) in a high-shear mixer-granulator (Diosna P1-6, impeller speed 300 rpm, chopper 1500 rpm) before wet granulation with purified water. Drying in a fluid-bed dryer (Glatt GPCG 1.1) to LOD ≤1.5% at 50°C inlet air temperature is critical: deviation to 65°C has produced discoloration linked to Maillard-type reactions with lactose, elevating impurity E above ICH qualification thresholds. The granular blend is subsequently lubricated with 1.0% w/w magnesium stearate (vegetable source, specific surface area 4–8 m²/g) for 3 minutes in a bin blender; overlubrication beyond 5 minutes retards dissolution, with f2 similarity factor falling below 50 versus the reference product when paddle speed 50 rpm in 900 mL of pH 6.8 phosphate buffer is employed (USP Apparatus 2).

    When Bioavailability of a BCS Class II Acid Demands Dissolution Partitioning Control

    Febuxostat is categorized under the Biopharmaceutics Classification System as a Class II compound: low solubility (12.9 µg/mL in water at 37°C) and high permeability, with fraction absorbed exceeding 85% in mass balance studies using 14C-labeled drug. The dissolution rate therefore governs in vivo performance. Micronization alone reduces d50 to the 4–8 µm range, but even micronized lots can exhibit erratic dissolution in 0.1 N HCl media unless particle wetting is enhanced through sodium lauryl sulfate (SLS) inclusion in the tablet matrix at 0.5%–1.0% w/w. However, SLS concentrations outside the narrow window of 0.3%–1.2%—evaluated via stepwise dissolution media containing 0.1%, 0.3%, and 0.5% polysorbate 80—can mask true release differences in quality control testing, a known limitation when applying USP 〈711〉 to poorly wetted acids. Hence, the dissolution test for febuxostat tablets (USP monograph) specifies 0.05 M phosphate buffer pH 6.8 with 0.1% sodium lauryl sulfate, paddle speed 50 rpm, and a Q value of 75% dissolved in 45 minutes. In-house development lots must meet a more stringent Q threshold of 80% at 30 minutes to ensure bioequivalence robustness, given the steep inverse correlation between d90 > 20 µm and Cmax (observed drop of 18%–22% in fasted-state pilot studies, n=24).

    Avoidance of pH modifiers that push gastric pH permanently above 5.0 is essential when co-formulating; while febuxostat shows increased solubility above pH 6.0, premature neutralization causes burst release in the stomach and unpredictable absorption. Co-administration with proton-pump inhibitors (e.g., omeprazole 20 mg) does not clinically alter AUC, per literature, but concomitant use with aluminum/magnesium-containing antacids within 2 hours of dosing reduces Cmax by 32% per FDA-approved labeling, attributed to chelation and pH-mediated precipitation. The manufacturing process must avoid any residual aluminum from excipient sources, such as certain colloidal silicas; alternatives like hydrophilic fumed silica (Aerosil 200) with Al₂O₃ content <0.05% are specified.

    Contrasting the Xanthine Oxidase Engagement Profile with Allopurinol

    The most structurally and pharmacologically distinct comparator is allopurinol, a purine analogue that acts as a suicide substrate, requiring metabolic activation to oxypurinol. Febuxostat binds directly to the molybdenum-pterin cofactor within xanthine oxidase without entering the purine binding pocket, yielding a Ki value of 0.6 nM for the oxidized enzyme and 3.1 nM for the reduced form. This difference translates into a clinically relevant selectivity: febuxostat does not inhibit enzymes of the de novo purine synthesis pathway (IC50 > 100 µM for hypoxanthine-guanine phosphoribosyltransferase), whereas allopurinol interferes with multiple steps, causing feedback accumulation of hypoxanthine and xanthine. In patients with the HLA-B*5801 allele—prevalent at 5%–10% in Han Chinese and Southeast Asian populations—allopurinol-induced severe cutaneous adverse reactions (SCAR) are well-documented; febuxostat’s non-purine scaffold circumvents this recognition, making it the preferred agent in at-risk genotypes pending renal function considerations.

    From a formulation standpoint, allopurinol exhibits a higher aqueous solubility (>3 mg/mL at 25°C), falling into BCS Class I at doses up to 300 mg, and does not require particle-size engineering. Febuxostat’s dose-proportional exposure across 10–120 mg once-daily regimens has been established, but batch-to-batch variability in crystallinity and particle size can shift the dissolution profile outside design space, a problem not encountered with allopurinol tablets (which are highly soluble and typically formulated via direct compression without micronization). The challenge is exacerbated when febuxostat is formulated as a fixed-dose combination with aspirin or a proton-pump inhibitor, where differential particle adhesion in binary blends causes segregation during transfer from an IBC bin to the rotary tablet press (observed demixing potential > 20% RSD at hopper fill levels below 30% when d50 ratio between APIs exceeds 5:1).

    Topiroxostat, another non-purine inhibitor used in Japan, shares the carboxylic acid moiety and a cyano substituent, yet its thiazole core is replaced with a triazole-1-carboxamide. The difference manifests in a shorter half-life (1.5 hours vs. febuxostat’s 5–8 hours) and distinct metabolic route through CYP3A4/2D6, whereas febuxostat undergoes primarily glucuronidation (UGT1A1, UGT1A3) and oxidation to acyl-glucuronides that have been monitored for potential reactivity. Manufacturing of febuxostat APIs thus includes an IPC limit on conjugated glucuronide content in the final crystal slurry wash: residual ethyl acetate must be removed below 1000 ppm to avoid solvate formation during the critical crystallization step from methanol/water, preventing acetone-insoluble aggregates that resist micronization.

    When switching from allopurinol to febuxostat in continuous manufacturing lines employing a twin-screw wet granulator (Leistritz ZSE 18 HP, L/D 40:1), cleaning validation for the extruder barrel is complicated by febuxostat’s low solubility and adherence to stainless steel surfaces; the accepted cleaning procedure uses a warm (45°C) alkaline solution of 0.5% NaOH, followed by purified water flush until conductivity returns to <2 µS/cm. Allopurinol, being more polar, achieves acceptable swab limits (≤5 ppm) with water alone, so line changeover protocols must account for this divergence to avoid cross-contamination in shared facilities. Published data for alkaline degradation kinetics of febuxostat on 316L stainless steel at 60°C indicate a first-order rate constant of 0.003 h⁻¹, but for cold workover at ambient temperature, a static hold time of 4 hours is established as the maximum safe interval before rinse sampling.