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Florfenicol Uterine Infusion Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    • Product Name: Florfenicol Uterine Infusion Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions
    • 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 563336
    Product Name Florfenicol Uterine Infusion Veterinary Grade API
    Cas Number 73231-34-2
    Molecular Formula C12H14Cl2FNO4S
    Molecular Weight 358.21 g/mol
    Appearance White or almost white crystalline powder
    Solubility Slightly soluble in water; soluble in methanol, ethanol, and acetone
    Mechanism Of Action Inhibits bacterial protein synthesis by binding to the 50S ribosomal subunit
    Pharmacological Class Amphenicol antibiotic
    Target Species Cattle, pigs, poultry, sheep, goats, and aquatic animals
    Indications Treatment of uterine infections and systemic bacterial infections caused by susceptible gram-positive and gram-negative organisms
    Compatible Dosage Forms Tablets, injections, capsules, powders, granules, premix, and solutions
    Veterinary Grade High-purity API suitable for veterinary pharmaceutical formulation
    Purity ≥99.0%
    Storage Conditions Store in a cool, dry, well-ventilated area away from light and moisture
    Shelf Life 24 to 36 months when stored under recommended conditions

    As an accredited Florfenicol Uterine Infusion Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in sealed, moisture-proof 25 kg drums with tamper-evident closures, suitable for veterinary pharmaceutical formulations including tablets, injections, powders, and solutions.
    Container Loading (20′ FCL) One 20-foot container loaded with Florfenicol veterinary API, securely packed for use in tablets, injections, capsules, powders, granules, premixes, and solutions.
    Shipping All shipments are securely packed in moisture-proof, sealed containers to maintain product integrity. Transport is performed under controlled temperature conditions, away from direct sunlight. Full documentation, including certificates of analysis and compliance with international shipping regulations, accompanies each consignment to ensure safe, traceable, and on-time delivery worldwide.
    Storage Store Florfenicol veterinary-grade API in a cool, dry, well-ventilated area at controlled room temperature (20–25°C). Keep containers tightly sealed, protected from light, moisture, and heat. Avoid exposure to strong oxidizers and incompatible materials. Use clean, dry utensils when handling. With proper storage, material remains stable for the manufacturer-specified shelf life.
    Shelf Life Shelf life is typically 24 months from manufacture date when stored in original sealed packaging under cool, dry, shaded conditions.
    Application of Florfenicol Uterine Infusion Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions

    In postpartum dairy cows, compounded florfenicol uterine infusions are prepared at 20 mg/mL nominal concentration because aqueous solubility of the unesterified API is limited to approximately 1.32 mg/mL at 25 °C. A 316L stainless steel jacketed vessel with bottom-sweep agitation is charged with water for injection, and a suspending carrier is hydrated—hypromellose 0.5% w/v plus poloxamer 188 0.1% w/v—before the API is dispersed under a rotor-stator homogenizer at 3,000 rpm for 10 min. pH adjustment with phosphate buffer to 6.5–7.0 reduces mucosal irritation, but moving pH toward 7.4 further depresses the already low solubility. Terminal moist-heat sterilization at 121 °C for 15 min is acceptable only if the polymer system does not undergo thermal gelation; otherwise the preparation is filtered through a 5 μm capsule filter as a non-sterile uterine suspension under veterinary direction. Documentation for extemporaneous compounding follows USP <795>, and if sterile filtration is claimed, USP <797> engineering controls apply. VICH GL18 residual-solvent limits apply when organic cosolvents are introduced. Published large-scale clinical outcome data for this specific compounded configuration are limited, so batch records must capture particle size, sedimentation behavior, and osmolality at release.

    The dominant source of batch-to-batch variance is API particle size, not mixing time. A milled D90 exceeding 25 μm commonly produces visible settling within 1 h, while a D90 below 10 μm can maintain redispersibility for up to 6 h under intermittent agitation. The suspension is filled into 100 mL amber type II glass vials with butyl rubber closures. In-use stability after first opening is assigned under VICH GL3 at 25 °C/<60% RH and 5 °C for 7 days; beyond this period, resuspendability and microbiological quality may decline. Moisture content of the dried API prior to dispersion is controlled below 0.5% by USP <921>. Oxidizing agents and strong alkaline buffers are avoided because the methylsulfonyl and dichloroacetamide groups may degrade under oxidative or strongly alkaline conditions.

    What Solvent System Prevents Florfenicol Precipitation in Injectable Concentrates?

    For injectable concentrates at 300 mg/mL, florfenicol is formulated in non-aqueous aprotic solvent blends because the aqueous solubility of the base is 1.32 mg/mL at 25 °C. A binary solvent system of 2-pyrrolidone and propylene glycol is typical; when 2-pyrrolidone falls below 20% v/v, recrystallization can occur after 48 h at 4 °C. In a 200 L glass-lined vessel, the solvents are heated to 35 °C before micronized florfenicol is added under 500 rpm agitation. Tip speed is maintained above 1.5 m/s; lower tip speed can create unmixed solvent pockets and promote crystal growth. The finished solution is cooled to 25 °C and filtered through a 0.22 μm PVDF cartridge. Viscosity at 25 °C is typically 25–45 mPa·s; readings above this range reduce filter throughput and complicate filling-line nozzle drip control. The approved injectable reference for bovine respiratory disease associated with Mannheimia haemolytica, Pasteurella multocida, and Histophilus somni is 21 CFR 522.955. USP <788> particulate-matter limits apply to the filtered solution.

    Cold-chain logistics are not normally required, but the ternary solvent system can undergo phase separation when propylene glycol exceeds 45% v/v and the product is held at 2 °C for more than 48 h. Water uptake is controlled below 0.1% by Karl Fischer titration; residual water above 0.3% w/w causes turbidity and supports hydrolytic degradation. Filling under nitrogen overlay reduces dissolved oxygen below 1 mg/L. In-use stability is validated according to VICH GL3 at 25 °C and 4 °C; the 4 °C condition is significant because product is frequently stored in farm refrigerators. The injectable solution is administered undiluted because aqueous dilution at the point of administration can cause immediate precipitation. Needle size is determined by injection site and animal size, commonly 18-gauge or larger for subcutaneous or intramuscular administration in adult cattle.

    When Florfenicol Premix Granulation Exceeds 60 °C

    During high-shear wet granulation of swine feed premixes, dry blending alone may fail USP <905> blend uniformity because raw florfenicol API has poor flow and tends to segregate in low-dose premixes. The API is first milled to D90 below 75 μm and dry-blended with lactose monohydrate and microcrystalline cellulose in a 500 L high-shear granulator. Water is sprayed at 8–12% w/w over 3–5 min while impeller speed is kept at 250 rpm and chopper speed at 3,000 rpm. Wet massing is limited to 3 min; extended massing densifies the granule and can retard subsequent drug release. The wet granules are dried in a fluid-bed dryer with inlet air temperature not exceeding 60 °C, because case hardening above this temperature can trap residual moisture inside granules and generate assay variability in the finished premix. Final moisture is controlled below 2.0% using USP <921>.

    Dried granules are milled through a 1.0 mm screen, blended with colloidal silicon dioxide 0.5% w/w and magnesium stearate 0.25% w/w, and packed into 25 kg multi-wall paper bags with polyethylene liners. At the feed mill, the premix is diluted in a ribbon blender with 10 min mixing at 70% nominal capacity. Overfilling above 80% capacity reduces mixing uniformity; underfilling below 40% may create dead zones. The following release criteria are applied to the granulated premix before feed dilution:

    ParameterMethod/StandardAcceptance Limit
    AssayPh. Eur. 2.2.29 HPLC95.0–105.0% of label claim
    MoistureUSP <921> Karl Fischer≤2.0%
    Blend uniformity AVUSP <905>≤15.0 for 10 sampling points
    Particle size D90ISO 13320:2020 laser diffraction≤75 μm
    Related substances, totalPh. Eur. 2.2.29 HPLC≤2.0%
    Residual solventsVICH GL18Class 2 limits for ethanol, isopropanol, or methylene chloride if used
    Loss on drying, APIPh. Eur. 2.2.32≤0.5%

    Stability of the granulated premix is evaluated under VICH GL3 accelerated storage at 40 °C/75% RH for 6 months; assay loss greater than 5% triggers long-term confirmatory testing. Where feed-grade regulatory approval exists, final medicated feed must comply with 21 CFR Part 558 or corresponding local medicated feed rules.

    When drinking-water powders are prepared for broilers and turkeys, the finished powder is not a true solution at label doses; the base API dissolves at approximately 1.32 mg/mL in water at 25 °C, so line distribution depends on dispersed low-micron particles. The dry powder is manufactured by blending florfenicol with maltodextrin and sodium lauryl sulfate 0.2% w/w as a wetting agent, then wet granulating or compacting with an isopropanol-based binder. Residual isopropanol is limited by VICH GL18 and measured by headspace gas chromatography. The granulate is milled through a 0.5 mm screen; D90 after dispersion is specified below 50 μm to prevent nipple-drinker occlusion. Field water hardness above 250 mg/L calcium carbonate can reduce dispersability because anionic wetting agents complex with divalent cations; in such water, nonionic wetting systems are preferable to anionic surfactants.

    The diluted stock solution is metered into drinking lines at 1:1000 proportioning to deliver 20 mg/kg body weight per day over the required treatment period. The final dispersion should be consumed within 24 h after mixing; beyond 24 h, settling and biofilm growth in header tanks can lower the delivered dose below target. In-use stability is validated under VICH GL3 at 25 °C and 60% RH for 24 h with assay loss not more than 5% and redispersibility after 10 inversions. Free chlorine at 2–4 ppm in municipal drinking water is not known to immediately inactivate florfenicol, but published data on all water matrices are limited; verification in the specific farm water source is required before release of the in-use protocol.

    Aquaculture Premix Dispersibility and Gastric Retention in Freshwater Species

    After extrusion and vacuum coating, florfenicol premixes for farmed finfish are applied at 10 mg/kg biomass per day for 10 consecutive days where authorized. The medication is incorporated after wet extrusion rather than before, because aqueous extrusion and barrel temperatures above 105 °C can reduce recovery, and post-extrusion vacuum coating preserves surface-associated drug from wash-off. A vacuum coater operating at −0.8 bar coats pellets with fish oil containing suspended florfenicol; the oil phase is sprayed at 0.5 bar to achieve 2% w/w oil uptake. Fine particle control is significant because fines smaller than 0.5 mm sink or remain suspended and are not consumed by fish, reducing actual dose. Sieve analysis after coating should show not more than 2% w/w fines passing a 0.5 mm screen.

    Leaching from finished pellets is evaluated by static immersion in water at 25 °C for 30 min; a design target of ≥90% label claim retention in the pellet after immersion is used. Pellet hardness is balanced against water stability; excessively hard pellets reduce gastric retention in species such as tilapia, while soft pellets disintegrate and release the drug into the water column. Premix assay is verified by HPLC per Ph. Eur. 2.2.29, and blend uniformity is verified by USP <905>. Where fish feed applications are regulated, 21 CFR Part 558 or equivalent national medicated feed rules apply. Solvent residues from coating oils are limited by VICH GL18. Uncoated mash use is associated with substantial wash-off losses, and aqueous medication of pond water is not a reliable route.

    Tablet Hardness above 10 kp Delays Disintegration in Small Ruminant Doses

    If tablet hardness exceeds 10 kp, disintegration can extend beyond 30 min in compounded small-ruminant formulations. Raw florfenicol is roll-compacted rather than directly compressed because bulk density is below 0.4 g/mL and powder flow is erratic on rotary tablet presses. Roller compaction with microcrystalline cellulose PH102 and croscarmellose sodium 2.0% w/w at 12 kN/cm roll force, followed by milling through a 1.0 mm screen, raises bulk density to approximately 0.6 g/mL. Tablets compressed to 5–8 kp hardness disintegrate within 15 min in water at 37 °C using USP <701>. If hardness is raised above 10 kp to reduce friability, the resulting delay in disintegration slows dissolution in 900 mL of 0.1 N HCl at 50 rpm using USP <711> Apparatus 2.

    Capsule filling avoids the hardness-disintegration conflict but requires tight control of D90 below 150 μm and magnesium stearate below 0.5% w/w, because hydrophobic lubricant overlubrication retards wetting. Fill weight variation is monitored by USP <905>; dissolution method transfer uses USP <711> with 900 mL of 0.1 N HCl at 37 °C ± 0.5 °C. Published dissolution specifications for florfenicol tablets and capsules of veterinary origin are not harmonized; each batch release is therefore based on site-specific validated methods. Compounded use in small ruminants is outside approved label in many jurisdictions, and published residue depletion data for this configuration are limited. These tablets should not be combined with antacids containing magnesium trisilicate, which raises gastric pH and can alter the dissolution rate.

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    Certification & Compliance
    More Introduction

    Florfenicol Uterine Infusion Veterinary Grade API is a non-sterile, crystalline active pharmaceutical ingredient identified by CAS 73231-34-2, molecular formula C12H14Cl2FNO4S, and molecular mass 358.21 g/mol. The product designation covers a low-endotoxin, low-bioburden release tier intended for further manufacture of tablets, injections, capsules, powders, granules, premix, and intrauterine solutions. The specification is defined by HPLC assay 98.0–102.0% on the dried basis, loss on drying ≤0.5%, residue on ignition ≤0.1%, and related substances controlled by area normalisation. Micronised and unmicronised lots are available; laser diffraction per ISO 13320:2020 controls unmicronised D90 at ≤150 µm and micronised D90 at ≤25 µm for injectable and intrauterine use. The API is not a sterile finished dosage form; sterile preparations require aseptic filtration or terminal sterilisation, and non-sterile oral or feed premix routes require target-market authorisation.

    Does the 3-Fluoro Modification Confer Clinically Relevant Resistance Coverage?

    Florfenicol is a fluorinated analogue of thiamphenicol in which the p-nitro group of chloramphenicol is replaced by a methylsulfonyl group and the C-3 hydroxyl is replaced by fluorine. Inhibition of bacterial protein synthesis occurs at the 50S ribosomal subunit through interference with peptidyl transferase, a mechanism shared with chloramphenicol and thiamphenicol. The structural difference is not cosmetic: chloramphenicol acetyltransferase inactivates chloramphenicol and thiamphenicol by acetylating the C-3 hydroxyl, whereas florfenicol is not a substrate for this enzyme. This property extends the spectrum against bovine pathogens that carry acquired acetyltransferase resistance, including Pasteurella multocida, Mannheimia haemolytica, Histophilus somni, and Trueperella pyogenes isolated from uterine disease. However, florfenicol remains susceptible to efflux transporters encoded by floR and to ribosomal methyltransferase encoded by cfr; minimum inhibitory concentration data from CLSI VET08/VET01S should therefore guide herd-level use. Published intrauterine MIC distributions for Trueperella pyogenes are limited; extrapolation from respiratory breakpoints should be avoided.

    Comparative structural, toxicological, and resistance-profile features of florfenicol and related amphenicols
    FeatureFlorfenicolChloramphenicolThiamphenicol
    p-SubstitutionMethylsulfonylNitroMethylsulfonyl
    C-3 substituentFluorineHydroxylHydroxyl
    Substrate for chloramphenicol acetyltransferaseNoYesYes
    Food-animal regulatory statusVeterinary use with withdrawal periods; no p-nitro groupProhibited in food-producing animals in many jurisdictions due to human aplastic anaemia signalVeterinary use subject to national residue limits
    Typical formulation routeInjection, oral solution, premix, intrauterine infusionHistorical oral and injectable; not current food-animal useOral solution, injection, water-soluble powder

    Compliance of the API with pharmacopeial expectations is verified by infrared absorption against a reference standard and by HPLC assay with UV detection. Residual solvents are controlled by headspace GC according to USP <467>; chlorinated solvents and benzene are limited below Option 1 concentrations. Bacterial endotoxins for injectable and intrauterine uses are determined by Limulus amebocyte lysate per Ph. Eur. 2.6.14 / USP <85>, with an action limit agreed for the finished sterile dosage form. Total aerobic microbial count for non-sterile powder is controlled below 10² CFU/g, total combined yeast and mould below 10¹ CFU/g; material intended for aseptic filtration must be dissolved in a vehicle that supports membrane integrity. Heavy metals are controlled by the current pharmacopeial method Ph. Eur. 2.4.8; limit values are set according to the final product type and target species.

    Pharmacopeial Alignment and Release Testing Boundaries

    The API is released against a matrix of tests that reflects the intended downstream route. For solid oral and feed premix manufacture, particle size and density are more critical than endotoxin load; for injectable and intrauterine manufacture, endotoxin and bioburden control dominate. Data from a representative release test matrix are shown below. The values are not universal pharmacopeial limits; they are supply-chain specification examples that must be justified in the marketing authorisation dossier.

    Representative release test matrix for veterinary-grade florfenicol API
    TestMethod referenceTypical limit
    AppearanceVisualWhite to off-white crystalline powder
    IdentificationPh. Eur. 2.2.24 / USP <197>Infrared spectrum matches reference standard
    AssayHPLC-UV98.0–102.0% on dried basis
    Related substancesHPLC area normalisationTotal impurities ≤2.0%; unspecified impurity ≤0.5%
    Loss on dryingPh. Eur. 2.2.32≤0.5%
    Residue on ignitionPh. Eur. 2.4.14≤0.1%
    Bacterial endotoxinsPh. Eur. 2.6.14 / USP <85>Action limit per finished product; injectable-grade API typically <0.5 EU/mg
    Residual solventsUSP <467>Option 1 limits

    When Intrauterine Exposure Demands Preformulation Stability Screening

    Intrauterine administration places the API into a variable matrix of uterine fluid, inflammatory exudate, and anaerobic bacterial metabolites. Aqueous solubility of florfenicol is low; therefore, intrauterine solutions are commonly prepared in non-aqueous or mixed solvent systems using N-methyl-2-pyrrolidone, propylene glycol, and polyethylene glycol to achieve a target concentration of 300 mg/mL. Preformulation screening should evaluate chemical stability over the pH range of infected uterine fluid, which may shift from pH 6.5 in early postpartum involution to above pH 8.0 with heavy anaerobic contamination. Because the dichloroacetamide moiety undergoes alkaline hydrolysis, buffering or non-aqueous formulation reduces degradation. Sterile filtration through 0.22 µm PVDF is preferred; nylon membranes may swell in dipolar aprotic solvents and fail integrity testing. Terminal steam sterilisation of anhydrous vehicles is limited by the vapour pressure of glycol co-solvents, so aseptic compounding is the standard terminal-sterile strategy.

    Particle size of the API in suspension formulations influences sedimentation and in vivo retention. Laser diffraction D90 controlled below 40 µm with a narrow span reduces caking; suspensions with D90 above 75 µm may sediment too quickly and cause dose non-uniformity during intrauterine infusion. Viscosity of the finished infusion is adjusted to 30–50 mPa·s at 25 °C using a suitable suspending agent; this range supports retention in the uterine lumen without preventing drainage of inflammatory exudate. All excipients must be screened for compatibility with florfenicol; amine-functional polymers and alkaline buffers accelerate degradation and should be avoided. The difference from oxytetracycline is relevant here: oxytetracycline chelates divalent cations present in uterine exudate, reducing free drug concentration, whereas florfenicol does not bind calcium by the same mechanism. Ceftiofur is a beta-lactam requiring reconstitution and has a different withdrawal profile. These distinctions influence formulation strategy rather than replacement of susceptibility testing according to CLSI VET08.

    Manufacture of tablets and capsules from the API requires attention to flow and compressibility. As-supplied florfenicol powder can exhibit bulk density below 0.45 g/cm³ and a Hausner ratio above 1.30, leading to powder bridging in hoppers and tablet weight variation above 3% relative standard deviation on rotary presses operating above 40,000 tablets/h. Direct compression is therefore uncommon; roller compaction at 25–45 kN with a 2 mm gap and subsequent milling through a 0.8 mm screen produces granules with a Hausner ratio below 1.25. For wet granulation, povidone K30 at 5% w/w aqueous solution is added in a high-shear mixer until main impeller torque reaches 40–60% of maximum load; the wet mass is dried in a fluid-bed dryer with inlet air at 50 °C to a final loss on drying below 2.0%. These are process boundaries, not release specifications.

    Granulation Endpoint Control for Tablets and Premix

    Granulation endpoint control determines dissolution and content uniformity in tablets and premix. Over-granulation produces dense, hard granules that retard API release in 0.1 N HCl with 1% Tween 80; under-granulation leaves fine particles that segregate in the feed hopper. Dissolution testing per USP <711> with a paddle speed of 50 rpm and a Q value of 75% in 45 min is used to monitor the effect of granulation variables. Magnesium stearate at 0.5% w/w blended for 3 min reduces ejection force; extending lubrication beyond 10 min can form hydrophobic films that reduce wetting. For premix powders and granules intended for oral dosing or feed admixture, sieve analysis is controlled with not more than 10% retained on 850 µm and not more than 20% through 150 µm to ensure homogeneous mixing in a double-cone blender. Batch production of premix should avoid alkaline carriers because the dichloroacetamide group is hydrolysed above pH 8.0; published data for this specific carrier interaction is limited, but the avoidance of alkaline carriers is consistent with the pH-instability of the amphenicol amide bond.

    Injectable and solution manufacture uses a different API quality attribute profile than solid oral forms. The vehicle must be anhydrous or water-miscible because the API is sparingly soluble in water; solutions are typically prepared at 300 mg/mL. Terminal heat sterilisation of the finished injection is evaluated by autoclave mapping at 121 °C for 15 min; if the solvent system does not permit this, aseptic filtration through 0.22 µm is validated by media fill. Capsule filling uses granules with tap density below 0.7 g/cm³; capsule fill weight variation is controlled at ±5% for capsule sizes 0–3. Powders, granules, and premix should not be combined with alkaline carriers such as sodium bicarbonate. Cleaning validation for shared equipment uses high-performance liquid chromatography with a carry-over limit of 10 ppm on product-contact surfaces; air handling for non-sterile powder processing is controlled to ISO 14644-1 Class 8. Micronised material is discharged through a split-flap valve to reduce aerosol exposure, and operators handle the dry powder with local exhaust ventilation because aerosolised API requires dust control.

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