| HS Code | 853916 |
| Product Name | Halofuginone Premix Veterinary Grade API for Tablets / Injections / Capsules / Powders / Granules / Premix / Solutions |
| Api Type | Veterinary Grade Active Pharmaceutical Ingredient |
| Active Substance | Halofuginone hydrobromide |
| Cas Number | 64924-67-0 (hydrobromide); 55837-20-2 (free base) |
| Molecular Formula | C16H17BrClN3O3·HBr (hydrobromide salt) |
| Molecular Weight | Approximately 495.4 g/mol (hydrobromide); approximately 414.3 g/mol (free base) |
| Appearance | White to off-white crystalline powder |
| Solubility | Soluble in water and lower alcohols; sparingly soluble in most organic solvents; practically insoluble in non-polar solvents |
| Assay Purity | Minimum 98.0% on dried basis (HPLC) |
| Dosage Form Compatibility | Tablets, injections, capsules, powders, granules, premix, and oral solutions |
| Pharmacological Category | Antiprotozoal and coccidiostat |
| Veterinary Indication | Treatment and prevention of coccidiosis and cryptosporidiosis in poultry, calves, sheep, and goats |
| Storage Conditions | Store in tight, light-resistant containers in a cool, dry place; protect from moisture and direct sunlight |
| Shelf Life | 24 months from date of manufacture when stored unopened under recommended conditions |
| Packaging | Supplied as bulk API premix powder in sealed multi-layer bags, drums, or customized veterinary packaging |
As an accredited Halofuginone Premix 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 | Packaged in sealed, light-resistant containers (1 kg/bag, 25 kg/drum) to protect Halofuginone Premix veterinary API for various dosage forms. |
| Container Loading (20′ FCL) | A 20′ FCL safely loads Halofuginone Premix API in sealed drums/cartons, palletized, secured, with proper ventilation and labeling. |
| Shipping | Halofuginone Premix is shipped in sealed, moisture-proof containers with tamper-evident seals, labeled for veterinary use. Transport in dry, ventilated areas away from food, direct sunlight, and heat. Maintain temperatures 20–25°C, protect from humidity. Follow hazardous material regulations; use dedicated or non-food vehicles to prevent contamination. |
| Storage | Store in a tightly sealed, original container in a cool, dry, well-ventilated area. Protect from direct sunlight, moisture, and extreme heat. Keep away from food, feed, incompatible substances, and out of reach of children. Ensure proper labeling and use personal protective equipment when handling. Follow manufacturer’s shelf-life guidelines. |
| Shelf Life | Store in a cool, dry place, protected from light and moisture. Shelf life: 24 months from manufacture date. |
Halofuginone hydrobromide is authorized as a synthetic quinazolinone alkaloid anticoccidial for broiler chickens and turkeys, and its use is regulated as a feed additive rather than as a therapeutic veterinary prescription. The veterinary-grade API for feed applications is supplied as a 0.6% w/w Type A medicated article; when incorporated at 0.5 kg/t complete feed, the finished feed delivers 3 mg/kg halofuginone hydrobromide. Regional compliance for this application is anchored to Regulation (EC) No 1831/2003 for feed additives, Regulation (EC) No 183/2005 for feed hygiene, and FDA 21 CFR Part 558 for new animal drugs in medicated feed. The downstream production sequence begins with an API preblend step, in which the active is geometrically diluted onto a carrier such as wheat middlings, calcium carbonate, or ground limestone in a horizontal ribbon blender; blend homogeneity is monitored by sampling according to ISO 6497:2002 and controlling relative standard deviation to ≤5% for preblend limits. Batch-to-batch variance on commercial lines is most frequently introduced by electrostatic adhesion of micrometer-range API particles to mixer walls, by poor sequencing of bucket elevator discharge, or by overfilling of ribbon troughs beyond the designed working volume. Terminal dosage forms for this downstream route are Type A 0.6% premix, Type B intermediate, and Type C medicated mash, pellet, or crumble feed intended for broiler chicken and turkey meat production. Halofuginone hydrobromide is not authorized for laying hens producing eggs for human consumption, and a 5-day withdrawal period is commonly applied to broiler chicken meat in authorized markets. The margin between the 3 mg/kg therapeutic feed concentration and adverse performance effects is narrow; feed mill metering systems should be calibrated for gravimetric accuracy not exceeding ±5% of setpoint before each production campaign. No recognized injectable or tablet dosage form for this molecule is currently authorized in major jurisdictions, and the API form selected for oral solid dosage development would require separate stability, dissolution, and bioavailability evaluation.
| Process step | Reference standard or method | Acceptance criterion |
|---|---|---|
| Premix blend homogeneity | ISO 6497:2002 | RSD ≤5% across 10–20 sampling points |
| Finished feed assay | FDA 21 CFR Part 558 / Regulation (EC) No 1831/2003 | 90–110% of label claim |
| Metering accuracy | In-house gravimetric calibration | ±5% of setpoint |
In neonatal calf rearing, halofuginone lactate is formulated as a 0.5 mg/mL oral solution for the prevention of diarrhoea caused by Cryptosporidium parvum, and this dosage form is governed as a veterinary medicinal product under Regulation (EU) 2019/6 rather than as a feed additive. The clinical administration protocol is 120 µg/kg body weight once daily for 7 consecutive days, beginning within the first 24–48 hours after birth; dosing is split by bodyweight bands and delivered via an oral syringe or dosing pump, not via bulk mixing into milk replacer. Formulation and production of the oral solution require dissolution in purified water, pH adjustment to stabilize halofuginone lactate in solution, filtration through a clarifier, and filling into high-density polyethylene bottles with tamper-evident closures; in-process checkweighing and delivered-dose verification are used to control fill volume variability, and the finished product must meet pharmacopoeial limits for solution clarity, assay, and degradation products. The downstream terminal type is a 0.5 mg/mL oral solution for calf drench, with pack presentations matching seven-day treatment course volumes. Direct oral drench before milk feeding is the standard administration route because dilution in milk replacer or colostrum produces variable intake and cannot guarantee the 120 µg/kg dose within an acceptable margin. The species-specific withdrawal period for bovine meat is stated in the marketing authorization SPC, and it must be applied at batch level with records that tie treated calves to slaughter age. Published data for oral solution compatibility with milk replacer matrices are limited, and the recommendation is to avoid mixing with feeding liquids.
Across integrated broiler complexes, steam-conditioned pellet presses and crumble mills impose thermal and moisture stresses on halofuginone hydrobromide that are not replicated in laboratory blend studies, and the lack of forced pre- and post-pelleting assay is a common root cause of ineffective coccidiosis control. Pellet conditioning in broiler feed lines typically operates between 70–85°C with moisture addition of 15–18%, and the feed then passes through a die with a compression ratio determined by feed manufacturer die inventory rather than by halofuginone stability requirements. Because published recovery data for halofuginone hydrobromide under commercial steam conditioning are limited, each feed mill must validate the specific combination of conditioner residence time, die compression ratio, and crumbler roll gap with forced assay of the 3 mg/kg target feed before and after the pellet press; a practical release range of 90–110% of label claim is applied for Type C medicated feed in many quality systems. The downstream production process includes post-pellet cooling to ≤5°C above ambient and crumble milling to a coarse granule or crumb size, with sieve analysis used to separate fines; active distribution is not uniform across particle-size fractions, and excessive fines can produce higher local halofuginone exposure at pan feeders while reducing actual intake in larger pellets. Terminal dosage forms include pelleted broiler starter, grower, and finisher rations, crumbled starter feed, and granulated medicated premises for on-farm mixing. Compliance anchors include Regulation (EC) No 183/2005 for feed hygiene, ISO 22000:2018 for food safety management systems, and the relevant coccidiostat carryover provisions of Regulation (EU) 2019/4. Feed mills with multiple animal species lines use flush batches of ground corn, rice hulls, or soya hulls after medicated runs to reduce accidental carryover into non-target feed, and bucket elevators and drag conveyors are cleaned at intervals documented in the HACCP plan.
Replacement pullet operations differ from broiler operations because the same feed mill may supply layer rations that cannot contain halofuginone hydrobromide, making sequencing control and withdrawal stratification the central technical challenge. The authorized addition level for medicated pullet grower feed is 0.5 kg/t of 0.6% premix to deliver 3 mg/kg active in complete feed; however, the product is not approved for hens producing eggs for human consumption, so feed mill scheduling must separate medicated pullet grower production from layer or breeder rations. Compliance for this application is anchored to Regulation (EC) No 1831/2003, FDA 21 CFR Part 558, and the cross-contamination prevention obligations of Regulation (EU) 2019/4; regional carryover thresholds for non-target feed are applied by the competent authority, and internal validation typically targets the lowest practical analytical detection rather than the regulatory ceiling. The production process uses unmedicated flush batches composed of ground corn or rice hulls immediately after medicated batches, and extended cleanout of drag conveyors, elevators, and mixer dead zones is scheduled before switching to non-target feed. Terminal forms are medicated pullet starter/grower feed followed by unmedicated layer rations, with 5-day withdrawal periods applied to pullets only where regional authorization supports meat use. The operational boundary is that halofuginone carryover into layer rations cannot be corrected by dilution once mixed, so batch release must include assay of the first unmedicated lot following a medicated sequence.
Where high-shear granulation is installed as an alternative to direct powder blending, the halofuginone hydrobromide premix is converted from a dusty 0.6% w/w powder into a granulated intermediate that reduces respirable dust exposure during bag docking, tipping, and in-line addition. The addition ratio in the granulated premix remains 0.6% w/w active, but the carrier system is typically calcium carbonate or wheat gluten granules bound with a food-grade binder and dried to a moisture content below 5%. The production process begins with high-shear granulation of the active with pre-blended carrier, followed by fluid-bed drying at a product temperature not exceeding 60°C, then screening to remove oversize and fines; sieve cut is selected to prevent segregation when the granulated premix is conveyed alongside ground corn or cereal by-products. The terminal dosage form is a low-dust granulated premix packed in multi-wall paper bags or bulk tote bags, suitable for metering into Type B intermediate and Type C medicated feed lines. Compliance for worker exposure is managed under REACH registration duties and national occupational exposure frameworks, with engineering controls such as local exhaust ventilation and bag dump containment at the tipping station. Published data for halofuginone-specific occupational exposure limits are limited; therefore, containment performance is verified by dust monitoring rather than by a defined regulatory threshold.
No-antibiotic-ever broiler production removes ionophore antibiotics but does not remove Eimeria spp. pressure, and halofuginone hydrobromide occupies a non-ionophore anticoccidial segment within rotational programs. In this application, the same 0.5 kg/t of 0.6% premix delivers 3 mg/kg complete feed, but the production pattern is usually a shuttle or rotation rather than a continuous single-product program. Compliance remains anchored to FDA 21 CFR Part 558 and Regulation (EC) No 1831/2003; the NAE claim itself is a commercial production standard audited by third-party certification bodies, not a regulatory status. Downstream feed production uses the same Type C medicated feed lines, but the feed mill must document that halofuginone-containing rations are separated from ionophore-free rations only when rotation programs require withdrawals; this is achieved by batching, line flushing, and separate bin assignment. Terminal forms are NAE broiler starter, grower, and finisher feeds containing halofuginone hydrobromide at the authorized inclusion. Reduced field sensitivity of Eimeria spp. to halofuginone has been reported in poultry-producing regions, so the product is placed in rotation with chemically unrelated anticoccidials rather than as a single-agent control indefinitely. Published data for specific rotational resistance thresholds are limited, and coccidiosis control programs should be adjusted based on oocyst counts, lesion scoring, and performance data from each integration.
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Halofuginone premix veterinary-grade active pharmaceutical ingredient for tablets, injections, capsules, powders, granules, premix, and solutions is a source material intended for secondary manufacture, not a finished dosage unit. The active moiety is a synthetic halogenated quinazolinone alkaloid derived from febrifugine, generally supplied as the hydrobromide salt. In the premix presentation, the API is triturated with a carrier such as lactose monohydrate, maize starch, calcium carbonate, or a combination selected for downstream compatibility. Because the product is labeled by halofuginone base equivalent, the gross powder weight is not equivalent to the active dose. High-performance liquid chromatography against a certified reference standard must be used to confirm the base-equivalent concentration before any tablet compression, capsule filling, or solution compounding begins. No single pharmacopoeial model number is assigned; the product is identified by the manufacturer’s batch code, the stated base-equivalent concentration, and the carrier type. Material intended for dry dosage forms is controlled for particle size, bulk density, and flow; material intended for aqueous solution is controlled for solubility, clarity, and pH of a diluted sample. The premix must not be administered directly to animals without dilution.
The release panel for halofuginone hydrobromide premix-grade API includes identity, assay, related substances, residual solvents, loss on drying, residue on ignition, and particle size distribution. A representative acceptance window for the assay on dried basis is 98.0% to 102.0%. Total related substances are commonly controlled at not more than 1.0%, with any single unspecified impurity limited to 0.5%. Loss on drying is typically set at not more than 1.0%, and residue on ignition at not more than 0.1%. Residual solvent testing under VICH GL18 or ICH Q3C sets a default methanol limit not exceeding 3000 ppm and a methylene chloride limit not exceeding 600 ppm, unless a filing-specific limit applies. Identification is performed by infrared absorption spectrophotometry and by retention time agreement in HPLC. The HPLC assay uses a reversed-phase C18 column with UV detection; system suitability requires relative standard deviation below 2.0% for repeated reference injections. Sample preparation must protect the brominated quinazolinone from direct UV light, since photolytic debromination can elevate impurity levels and suppress the active peak.
| Test | Method | Typical limit |
|---|---|---|
| Assay on dried basis | HPLC, C18, UV detection | 98.0%–102.0% |
| Total related substances | HPLC area normalization | ≤ 1.0% |
| Single unspecified impurity | HPLC area normalization | ≤ 0.5% |
| Loss on drying | Vacuum oven | ≤ 1.0% |
| Residue on ignition | Muffle furnace | ≤ 0.1% |
| Methanol | VICH GL18 / ICH Q3C | ≤ 3000 ppm |
| Methylene chloride | VICH GL18 / ICH Q3C | ≤ 600 ppm |
| Particle size D90 | Laser diffraction | ≤ 150 µm |
The release matrix above is a representative control framework. Lot-to-lot acceptance must be based on the specific certificate of analysis and the registered specification; published data for this specific configuration is limited. Pharmacopoeial changes may alter limit values; therefore, the current monograph should be consulted before release.
Production-scale dilution of halofuginone premix into final feed or carrier systems follows a geometric dilution sequence because the target complete feed concentration is in the low milligram-per-kilogram range. A common sequence is a 1:10 pre-blend, followed by a 1:10 secondary dilution, then a final 1:100 ribbon blender run. Blend uniformity is evaluated by sampling at ten points and calculating coefficient of variation; values above 5.0% indicate segregation, insufficient mixing time, or electrostatic adhesion. Ribbon blenders with an intensifier bar are preferred over single-shaft paddle mixers when the API has a D90 above 150 µm or when the carrier bulk density is below 0.55 g/cm³. Milling through a 0.5 mm screen may be required before dry granulation to reduce agglomerates. Relative humidity above 60% can cause the hydrobromide salt to gain moisture and adhere to blender surfaces, producing carryover between batches. Cleaning validation should include wipe sampling of the mixer shaft, discharge gate, and dust collection duct because low-dose actives can accumulate in dead zones. When the final dry blend is used for tablet compression, magnesium stearate should be limited to 0.5%–1.0% and added as the final lubricant to avoid hydrophobic film formation on halofuginone particles.
Batch-to-batch variance in halofuginone premix manufacture is controlled by in-process sampling after each geometric dilution stage. On a production-scale ribbon blender with a working volume of 600 L, charging order should be carrier, API pre-blend, then remaining carrier; mixing time is typically 8–12 min at 15 rpm, but the endpoint is determined by near-infrared spectroscopy or HPLC of ten sampling ports. A coefficient of variation above 5.0% requires an additional 3 min of mixing and resampling. The discharge gate is sampled separately because segregation may occur during free-fall transfer. When tableting, tablet press turret speed should be reduced if the Carr index exceeds 25 because poor flow can cause weight variation. Granule friability is measured by rotating granules for 10 min in a Roche friabilitor; acceptable weight loss is below 1.0%. These controls reduce batch rejection but do not replace pharmacopoeial release testing.
Tablet formulations containing halofuginone hydrobromide at low dose require content uniformity testing under Ph. Eur. 2.9.40 or USP <905>. The acceptance value should not exceed 15, and individual units should remain within 85.0% to 115.0% of label claim unless a more stringent filing limit applies. The active is shear-sensitive under prolonged dry milling; milling time should not exceed 15 min without temperature monitoring. Immediate-release tablets are tested by dissolution in 0.1 N hydrochloric acid at 37 ± 0.5 °C, using USP apparatus II at 50 rpm. Hardness is maintained between 40 N and 80 N to avoid capping. For capsule filling, the blend is passed through a 30-mesh screen and filled using a dosator or tamping pin machine; fill weight variation should not exceed ±5.0%. Granules and powders for oral administration include a buffering agent to keep the local pH in the acidic range because the free base precipitates at neutral to alkaline pH.
Halofuginone belongs to the quinazolinone alkaloid class and inhibits prolyl-tRNA synthetase, a target distinct from the triazine coccidiostats toltrazuril and diclazuril. This mechanistic separation means that cross-resistance to triazines is not automatic, although field isolates should still be subjected to sensitivity testing because multidrug efflux can alter susceptibility. Unlike ionophore antibiotics such as monensin and salinomycin, halofuginone does not function primarily as a cation carrier. Its activity is directed against apicomplexan parasites, including Eimeria species in poultry and Cryptosporidium parvum in neonatal calves. In the licensed calf oral solution, the concentration of halofuginone base is 0.5 mg/mL, and the dose is 0.1 mg/kg body weight once daily for seven consecutive days. This regimen is specific to prevention of cryptosporidial diarrhea and is not interchangeable with coccidiostat feed premix use. Residue methods for halofuginone are based on HPLC-MS/MS rather than simple UV methods used for some triazine formulations because the brominated chlorinated structure requires selective detection. Regulatory withdrawal periods must be taken from the authorized premix label in the country of use; no universal withdrawal period applies. Halofuginone has a narrower therapeutic index in some species than diclazuril, so dose calculation and avoidance of accidental exposure to non-target animals are critical. The hydrobromide salt is supplied as a separate API, whereas many triazine products are ready-to-use oral suspensions.
For solution and injection development, the halofuginone hydrobromide premix-grade API must be fully dissolved and filtered to remove any insoluble carrier residues if the premix contains a filler. The licensed oral solution demonstrates that an aqueous concentration of 0.5 mg/mL is feasible. Injection formulations require additional data on sterility, endotoxin limit, pH stability, and compatibility with primary packaging. Sterile filtration through a 0.22 µm polyvinylidene fluoride or polyethersulfone membrane is acceptable only after the solution is buffered to prevent precipitation of the free base. Autoclaving may degrade the brominated quinazolinone ring; therefore, aseptic filtration is preferred unless terminal sterilization studies demonstrate sufficient thermal stability. The product should be protected from light because halofuginone is susceptible to photolytic debromination. Long-term liquid stability is evaluated at 25 ± 2 °C and 60 ± 5% relative humidity; accelerated testing at 40 ± 2 °C and 75 ± 5% relative humidity is used to estimate shelf life. Published data for injectable halofuginone configuration is limited.
The conversion sequence begins with a potency calculation based on halofuginone base equivalent, not hydrobromide salt weight. A 0.5 mg/mL oral solution requires 0.5 g of halofuginone base equivalent per litre; if the premix contains 10% base equivalent, then 5.0 g of premix is used per litre. The premix is added to the aqueous vehicle under high-shear mixing at 500–1000 rpm for 15–30 min to ensure complete wetting. The vehicle should be buffered with citrate or acetate to maintain pH below 5.0; above neutral pH, the free base may precipitate. Preservative systems containing benzalkonium chloride at 0.01%–0.02% may be used if compatibility is demonstrated. The solution is filtered through a 0.45 µm clarifying filter and filled into amber glass or high-density polyethylene bottles. In neonatal calves, the solution is administered after colostrum to reduce the risk of gastrointestinal stasis. The dose is calculated as 0.1 mg/kg body weight once daily for seven consecutive days. Overdose can produce feed refusal, diarrhea, and weight loss; the dosing syringe should be calibrated to within ±5% of the intended volume. The in-use period should be confirmed by product-specific stability data; no universal figure applies.
Carrier selection for the premix grade API is not trivial. Lactose monohydrate is preferred for tablet and capsule blends because it has a median particle size near 100 µm and good compressibility. Maize starch is used when moisture-sensitive granules are required, but starch-based premixes can segregate if the API particle size is below 10 µm. Calcium carbonate carriers are used in some feed premixes, but their alkaline surface can raise the local pH and reduce dissolution of halofuginone hydrobromide in acidic gastric fluid; this incompatibility should be assessed during formulation screening. The premix should be tested for tapped density and Hausner ratio; a Hausner ratio above 1.35 indicates poor flow and the need for granulation. When direct compression is attempted, microcrystalline cellulose is included at 25%–40% to improve compressibility. The final blend should be protected from light and humidity until compression or filling.
Scale-up failure modes observed with low-dose veterinary actives include assay loss to filter media, electrostatic adhesion to stainless steel, and cap formation during compression. For halofuginone hydrobromide premix, these failures are prevented by pre-conditioning the blending suite to 45%–55% relative humidity, grounding the mixer and vacuum transfer lines, and adding colloidal silicon dioxide at 0.1%–0.5% to coat the active and reduce electrostatic charge. If the API is mixed in a high-shear granulator, the impeller speed should be limited to 200–400 rpm and the chopper to 1000–2000 rpm; higher energy input may raise product temperature and accelerate degradation of the brominated quinazolinone ring. The granulation endpoint is reached when the granule size distribution has D50 between 100 µm and 300 µm. Overgranulation produces hard granules that resist disintegration and slow the release of halofuginone.
Method transfer from the release assay to LC-MS/MS residue monitoring requires ion source optimization. Halofuginone hydrobromide ionizes in positive electrospray mode with a protonated molecular ion. The method should separate halofuginone from febrifugine and related alkaloids; relative retention time between halofuginone and febrifugine should not be less than 1.2. A limit of quantification of 0.1 mg/kg in feed is achievable but must be validated for each matrix. Sample extraction uses acidified acetonitrile-water, and matrix effects are corrected by isotope-labeled internal standard where available. Because halofuginone binds to particulate matter in feed, extraction recovery below 80% indicates incomplete wetting. The premix-grade API must be fully solubilized before HPLC injection. These method parameters are matrix-dependent and are not universal; published data for this specific configuration is limited.
Compared with diclazuril and toltrazuril premixes, halofuginone premix requires stricter light protection because the brominated heterocycle is more susceptible to photolytic debromination. It also requires tighter humidity control because the hydrobromide salt is hygroscopic; triazine coccidiostats are generally less hygroscopic. These differences influence packaging, sampling, and in-process hold times. Halofuginone should not be stored in unlined metal containers because the halide salt can corrode steel; high-density polyethylene or fiber drums with inner polyethylene liners are used. In contrast, ionophore premixes may require different safety precautions because monensin and salinomycin are cardiotoxic to horses; halofuginone is not an ionophore, but accidental exposure to horses and other non-target species should still be prevented. These product-specific differences should be reflected in the material safety data sheet and in the site risk assessment.
Bulk halofuginone hydrobromide premix-grade API should be stored in tightly closed, light-resistant containers at controlled room temperature. The material should not be exposed to strong oxidizing agents, and contact with alkaline detergents during equipment cleaning may generate the less water-soluble free base. When the product is repackaged, the receiving container should be purged with nitrogen if the carrier contains hygroscopic components. Labels should state the base-equivalent concentration, the carrier type, and the retest date. Weighing and sampling should be performed in a downflow booth with local exhaust ventilation because the API is a potent low-dose veterinary drug.