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2'-Fluoro-2'-deoxyuridine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    • Product Name: 2'-Fluoro-2'-deoxyuridine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 966992
    Product Name 2'-Fluoro-2'-deoxyuridine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable
    Synonyms 2'-FdU; 2'-Deoxy-2'-fluorouridine; 2'-Fluoro-2'-deoxyuridine
    Cas Registry Number 784-71-4
    Molecular Formula C9H11FN2O5
    Molecular Weight 246.19 g/mol
    Grade Pharma Grade / API
    Dosage Forms Tablet; Capsule; Granule; Injection
    Routes Of Administration Oral; Injectable
    Appearance White to off-white crystalline powder
    Assay Purity ≥98.0% (HPLC)
    Solubility Soluble in water and methanol; slightly soluble in ethanol
    Storage Conditions Store at 2-8°C, protected from light and moisture
    Melting Point 147-149°C
    Pka 9.3 (estimated)
    Logp -1.5 (estimated)
    Pharmacological Class Nucleoside analog / antimetabolite
    Therapeutic Category Antiviral / antineoplastic (investigational)
    Handling Precautions Use personal protective equipment; avoid inhalation and contact

    As an accredited 2'-Fluoro-2'-deoxyuridine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

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    Application of 2'-Fluoro-2'-deoxyuridine Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable

    In oral solid dose manufacturing for fluoropyrimidine antimetabolite products, 2'-fluoro-2'-deoxyuridine pharma grade is weighed and dispensed within a negative-pressure isolator; the containment system is operated to maintain a performance target of 0.01–0.1 µg/m³ 8-hour TWA because the compound is handled as a cytotoxic antimetabolite. The API is a synthetic fluoropyrimidine nucleoside analogue; after intracellular phosphorylation, the 5'-monophosphate metabolite inhibits thymidylate synthase and reduces deoxythymidine triphosphate pools, which justifies containment and cleaning protocols consistent with hazardous drug handling. Direct compression is selected when the milled API has a laser diffraction D90 below 100 µm under ISO 13320:2020 and bulk density above 0.40 g/mL; if these thresholds are not met, dry granulation is introduced. Tablet core API loadings in development formulations typically range from 5% w/w to 25% w/w for label claims between 20 mg and 200 mg. The blend is prepared by geometric dilution in a bin blender operating at 10 rpm for 15 min, with croscarmellose sodium as intragranular disintegrant and lactose monohydrate as filler. Magnesium stearate is added at 0.5% w/w and blended for 3 min; over-lubrication beyond 5 min produces tablet hardness loss and delayed disintegration. Compression runs use a rotary tablet press with 8–18 kN compression force and a target tablet breaking force of 60–120 N under USP <1217>. Tablet weight variation exceeding 3% RSD indicates insufficient glidant; colloidal silicon dioxide at 0.5–1.0% w/w is added before final lubrication. Finished tablets are tested under USP <905> for uniformity of dosage units, USP <711> for dissolution using Apparatus II at 50 rpm in 900 mL of 0.1 M HCl, and FDA 21 CFR 211.166 for batch release. Terminal finished product is an immediate-release film-coated tablet in PVC/PVDC-aluminium blisters with light protection.

    What changes when direct compression is replaced by roller compaction in capsule-based oral dosage forms?

    When 2'-fluoro-2'-deoxyuridine pharma grade is filled into hard gelatin or hypromellose capsules, direct compression blends with high API loading often segregate during transfer to the dosator; roller compaction is introduced to improve flow, increase bulk density, and reduce dust generation in the containment isolator. API addition ratio in capsule fill powder commonly ranges from 10% w/w to 40% w/w, with the higher limit reserved for high-dose capsules up to 150 mg; microcrystalline cellulose and pregelatinised starch are used as compressible fillers. Roller compaction is performed on a roller compactor with roll pressure 6–12 kN/cm, roll speed 2–5 rpm, and screen size 0.8–1.6 mm. The resulting granules are blended with crospovidone and magnesium stearate, then filled on an automatic capsule filler at 60,000 capsules/h with a target weight variation of ±3%. A process failure mode observed on production lines is granule overcompaction, which reduces dissolution below 80% at 30 min because intragranular porosity falls below 15%; roll pressure is therefore monitored as a critical process parameter. Capsules are tested by USP <905> and USP <711>; where gelatin shell cross-linking is suspected, dissolution media containing pepsin are used under USP <711> to distinguish shell-related delay from API release failure. Compliance is anchored to ICH Q3D for elemental impurities, ICH Q3C for residual solvents, and FDA 21 CFR 211.165 for testing of finished product. Terminal finished product is a hard gelatin or hypromellose capsule for oral cytotoxic administration.

    Thermal degradation pathways in lyophilised 2'-fluoro-2'-deoxyuridine injection manufacturing

    Lyophilisation cycle design for 2'-fluoro-2'-deoxyuridine injection starts with dissolution of the API in Water for Injection at a concentration of 2.5–25 mg/mL; mannitol is added as the bulking agent at an API-to-mannitol ratio between 1:1 and 1:5 to provide a crystalline cake structure with acceptable reconstitution time. The solution pH is adjusted with dilute hydrochloric acid or sodium hydroxide to pH 5.0–7.0; the uracil chromophore undergoes photolytic degradation, so manufacturing is conducted under sodium vapour lighting or amber glass protection. The solution is sterile-filtered through a 0.22 µm PVDF membrane and filled into Type I borosilicate glass vials with bromobutyl rubber stoppers. Lyophilisation includes freezing at -40 °C for 2 h, primary drying at -20 °C and chamber pressure 50–100 mTorr for 20–30 h, and secondary drying at 25 °C for 6–8 h until residual moisture is below 1.0% w/w by Karl Fischer under USP <921> Method Ia. A critical processing window exists during primary drying: product temperature must remain below the collapse temperature; exceeding -15 °C causes cake meltback or shrinkage, yielding a poorly soluble residue with reconstitution time beyond 2 min. Published data for this specific lyophilised configuration is limited; therefore, cycle robustness is verified by freeze-drying microscopy and differential scanning calorimetry before scale-up. Compliance is anchored to EU GMP Annex 1, FDA 21 CFR 211.167, USP <797>, ICH Q3D, and bacterial endotoxin limits under USP <85> at <0.5 EU/mg. Terminal finished product is a sterile lyophilised powder for solution for injection or intravenous infusion.

    Dosage form / stepCritical quality attributeStandard / test methodAcceptance criterion
    Oral immediate-release tabletContent uniformityUSP <905>Acceptance value ≤ 15.0
    Oral capsuleDissolutionUSP <711>Q = 80% at 30 min
    Lyophilised injectionBacterial endotoxinUSP <85><0.5 EU/mg
    Granules for suspensionLoss on dryingUSP <731>NMT 1.0% w/w
    Hospital compounded infusionSterilityUSP <71>No growth at 14 days

    Sachet-based granules for extemporaneous oral suspension impose particle-size constraints because 2'-fluoro-2'-deoxyuridine is administered through nasogastric or gastrostomy tubes when patients cannot swallow intact tablets or capsules; the granule blend must pass through an 8 French tube without clogging. Wet granulation is performed in a high-shear mixer with impeller speed 300–500 rpm and chopper speed 1500–2000 rpm; the API is loaded at 2–8% w/w of the total sachet fill, with lactose monohydrate and mannitol as diluents and HPMC E5 as binder at 5% w/w solution concentration. Granules are dried in a fluid bed dryer at an inlet air temperature of 60 °C and product temperature of 35–40 °C until loss on drying is not more than 1.0% w/w under USP <731>, then sieved through a 1.0 mm screen. Suspension is prepared with 20 mL purified water per sachet; the mixture is stirred for 30 s and administered within 4 h because published data for long-term suspension stability in this specific configuration is limited. Compliance is anchored to USP <711> for suspension dissolution, Ph. Eur. 2.9.1 for particle size, and FDA 21 CFR 211.165 for finished-product testing. Terminal finished product is a single-dose granule sachet for extemporaneous oral suspension.

    Closed-system transfer devices and hospital compounding of cytotoxic ready-to-administer infusion bags

    Within hospital pharmacies that prepare cytotoxic infusions, the closed-system transfer device is mandatory for reconstituting 2'-fluoro-2'-deoxyuridine lyophilised vials because aerosol generation during needle withdrawal exposes operators to genotoxic nucleoside analogues. The lyophilised cake is reconstituted with 0.9% sodium chloride or 5% dextrose to a concentration of 5 mg/mL; this solution is further diluted into polyolefin infusion bags to a final concentration of 0.5–5 mg/mL for intravenous infusion. The final infusion bag is labelled for light-protected administration and assigned a beyond-use date not exceeding 24 h at controlled room temperature or 48 h refrigerated at 2–8 °C, based on USP <797> compounding risk levels and limited stability data for the specific admixture. Sterile preparation areas operate under ISO 14644-1 Class 5 conditions; containment is governed by NIOSH hazardous drug handling recommendations, OSHA 29 CFR 1910.1200, and EU Directive 2004/37/EC for carcinogenic or mutagenic agents at work. Terminal finished product is a ready-to-administer cytotoxic infusion bag for hospital-based intravenous administration.

    Blinded clinical supply of oral cytotoxic candidates frequently uses overencapsulation of 2'-fluoro-2'-deoxyuridine pharma grade into opaque hard gelatin capsules; the API is filled at dose-cohort strengths from 20 mg to 150 mg per capsule, with microcrystalline cellulose as backfill and a riboflavin-based visual marker in the placebo to preserve blinding. Semiautomatic capsule fillers operating in a negative-pressure isolator are used, with a filling speed below 5,000 capsules/h to maintain ±5% dose accuracy; in-process control includes weight sorting and near-infrared identity confirmation of the active capsule. Compliance is anchored to ICH E6(R2), FDA 21 CFR Part 312, EU Clinical Trials Regulation 536/2014, and Annex 13 of EU GMP for investigational medicinal products. Terminal finished product is an investigational blinded capsule for oral administration in clinical trial settings.

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    Certification & Compliance
    More Introduction

    2′-Fluoro-2′-deoxyuridine, CAS 784-71-4, molecular formula C9H11FN2O5, relative molecular mass 246.19, is released under the model designation 2FdUrd-Ph-API for tablet, capsule, granule, and injectable manufacture. The material is a white to off-white crystalline powder. Identity is verified by infrared absorption spectrophotometry and HPLC retention time concordance against a qualified reference standard. The release specification includes assay by HPLC of 98.0% to 102.0% on the anhydrous basis, total related substances ≤ 1.0%, water content ≤ 0.5% w/w by Karl Fischer titration, residue on ignition ≤ 0.1%, and residual solvents controlled per ICH Q3C. Elemental impurities are controlled per ICH Q3D for oral and parenteral routes; ICP-MS is used after microwave-assisted acid digestion.

    The compound is a positional isomer of 5-fluoro-2′-deoxyuridine; both share the molecular formula C9H11FN2O5 but differ in the attachment position of the fluorine atom. In the present material, the fluorine is located at the 2′ position of the deoxyribose ring, whereas in floxuridine the fluorine is located at the 5 position of the uracil base. This distinction changes the infrared C–F stretching region, the reversed-phase HPLC retention time, and the acid-hydrolysis profile. The solid is packaged in double low-density polyethylene bags inside aluminum-laminated drums and stored at 2–8 °C with desiccant.

    For oral solid-dose processing, the API is blended with microcrystalline cellulose and lactose monohydrate meeting current Ph. Eur. excipient monographs. Wet granulation is avoided unless a non-aqueous binder system is used, because the glycosidic bond is susceptible to acid-catalyzed hydrolysis. For injectable presentations, the API is dissolved in Water for Injections and lyophilized; the bulk solution is filtered through a 0.22 µm polyvinylidene fluoride membrane before filling. Published data for this specific configuration in finished oral dosage forms is limited; therefore, dissolution and bioavailability must be established by the finished-product manufacturer.

    What limits direct compression of this API in low-dose oral solid dosage forms?

    The direct compression window is governed by particle size distribution, moisture content, and powder flow. Laser diffraction data are generated according to ISO 13320:2020; the release specification requires D90 ≤ 150 µm for tableting grade and D90 ≤ 45 µm for injectable-grade micronized material. Bulk density and tapped density are measured per USP 616; the Carr index and Hausner ratio are calculated from those values. A batch with Carr index > 25 or Hausner ratio > 1.25 is not released for direct compression without dry granulation.

    On a 10-station rotary tablet press operated at 15–25 rpm and compression force 8–15 kN, capping and lamination are observed when residual moisture exceeds 1.0% w/w and the granulate contains more than 20% fines below 75 µm. Pre-drying at 40 °C under vacuum until loss on drying ≤ 0.5% w/w is required when the processing area exceeds RH 60%. The API is blended in a V-shell blender at 25 rpm for 15 min; extended blending beyond 30 min increases electrostatic charge and reduces content uniformity.

    When dry granulation is used, a roller compactor with roll pressure 20–40 bar and a 1.0 mm screen is operated. The resulting ribbons are milled and the granulate is compressed into tablets with hardness 5–8 kp; disintegration is tested per USP 701. Tablet dissolution is evaluated using USP Apparatus II at 50 rpm in 900 mL of 0.1 M hydrochloric acid.

    When the API is designated for injectable lyophilization, endotoxin and subvisible particulate thresholds become release-limiting

    Injectable grade requires bacterial endotoxin ≤ 0.5 EU/mg by Ph. Eur. 2.6.14. Subvisible particulate matter is tested per USP 788 after reconstitution of the lyophilized product; the limits are ≤ 6000 particles per container at ≥ 10 µm and ≤ 600 particles per container at ≥ 25 µm. The bulk solution is filtered through a 0.22 µm polyethersulfone membrane filter before lyophilization. Filter compatibility is confirmed by extractables and leachables profiling according to current regulatory guidance.

    The lyophilization cycle uses a primary drying shelf temperature of −25 °C to −20 °C and chamber pressure 100–150 mTorr. The API is dissolved in Water for Injections at 20–25 °C; if the solution is held for more than 4 h before filtration, the parent peak area should be rechecked by HPLC because of potential glycosidic hydrolysis. The sterile grade is tested for sterility per Ph. Eur. 2.6.1; terminal steam sterilization is not used because heat and moisture accelerate degradation. The injectable grade is released only after lyophilizate cake appearance is confirmed as intact and the reconstituted solution meets clarity and pH specifications of 4.0–7.0.

    Compendial release criteria and elemental impurity mapping

    TestAcceptance criterionAnalytical procedure
    AppearanceWhite to off-white crystalline powderVisual inspection
    IdentificationIR spectrum concordant with reference; HPLC retention time concordantPh. Eur. 2.2.24; Ph. Eur. 2.2.29
    Assay98.0%102.0% anhydrous basisHPLC
    Related substancesTotal impurities ≤ 1.0%; any unspecified impurity ≤ 0.10%HPLC area normalization
    Water content0.5% w/wKarl Fischer titration, Ph. Eur. 2.5.12
    Residual solventsClass 3 solvents per ICH Q3C; methanol ≤ 3000 ppm; ethanol ≤ 5000 ppmHeadspace GC, USP 467
    Elemental impuritiesPer ICH Q3D for oral and parenteral routesICP-MS after microwave-assisted acid digestion
    Residue on ignition0.1%Ph. Eur. 2.4.14
    Polymorphic formXRPD pattern concordant with referenceX-ray powder diffractometer
    Particle size distributionD90 ≤ 150 µm for oral grade; D90 ≤ 45 µm for injectable gradeLaser diffraction, ISO 13320:2020
    Microbial limitsTotal aerobic microbial count ≤ 100 CFU/g; total combined molds and yeasts ≤ 10 CFU/g for non-sterile oral gradePh. Eur. 2.6.12
    Bacterial endotoxins0.5 EU/mg for injectable gradePh. Eur. 2.6.14
    SterilityNo growth after 14 days for injectable gradePh. Eur. 2.6.1

    Chromatographic purity is determined using a reversed-phase C18 column with UV detection at 260 nm. The quantitation limit for specified impurities is 0.05% relative to the API peak. The XRPD measurement is performed over the 2θ range 3–40°; the three principal reflections must match the reference within ± 0.2° 2θ.

    For granule-filled sachets, the API is dry-granulated with mannitol and crospovidone; the granulate is filled at a target weight of 500 mg per sachet with fill weight variation ≤ 5% RSD. The moisture barrier of the sachet laminate is specified at water vapour transmission rate ≤ 0.1 g/m²/day at 38 °C/90% RH per ASTM F1249. The finished granule is tested for dissolution using USP Apparatus II at 50 rpm in 900 mL of 0.1 M hydrochloric acid; acceptance is Q = 80% in 30 min for immediate release. Capsule formulations use size 3 hard gelatin capsules with lactose monohydrate and sodium starch glycolate; the blend is filled on a dosator-type capsule machine. The blend is not lubricated with magnesium stearate above 0.5% w/w because hydrophobic lubricant films reduce dissolution at low dose. The empty capsules meet the requirements of USP 711 and the finished capsules are stored in PVC/PVDC/aluminum blisters to limit moisture ingress.

    The 2′-fluoro substitution is not analytically interchangeable with 5-fluorouracil or floxuridine

    In 5-fluorouracil the fluorine atom is bonded to the uracil base at the 5 position; in floxuridine the same base modification is present with a 2′-deoxyribose sugar. The material described here carries fluorine at the 2′ position of the deoxyribose ring while the uracil base remains unsubstituted. This difference changes the infrared C–F stretching fingerprint, the reversed-phase HPLC retention time, and the susceptibility of the glycosidic bond to acid hydrolysis. The API should not be substituted by weight into a floxuridine or 5-fluorouracil formulation without re-development of the analytical method and process.

    Attribute2′-Fluoro-2′-deoxyuridine5-FluorouracilFloxuridine
    CAS784-71-451-21-850-91-9
    Molecular formulaC9H11FN2O5C4H3FN2O2C9H11FN2O5
    Substitution position2′ position of deoxyribose5 position of uracil base5 position of uracil base
    Product presentation routeOral and injectable API under defined specificationsInjectable; oral absorption is variable due to dihydropyrimidine dehydrogenaseInjectable; often hepatic arterial infusion
    Key degradation pathwayAcid-catalyzed glycosidic hydrolysisBase hydrolysis and photodegradationGlycosidic and base modifications
    Analytical differentiationIR C–F sugar region; HPLC retention time distinctIR C–F base region; different relative retention timeIR C–F base region; same molecular formula but distinct retention time

    The API supplier does not establish therapeutic equivalence or bioequivalence. Substitution of this API into a marketed floxuridine or 5-fluorouracil drug product should not occur without appropriate regulatory variation, finished-product stability data, and comparative dissolution testing. The manufacturer is responsible for confirming that the final dosage form meets the finished-product monograph and the approved marketing authorization specification.

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