| HS Code | 106366 |
| Product | Narasin Veterinary Grade API |
| Suitable Dosage Forms | Tablets; Injections; Capsules; Powders; Granules; Premix; Solutions |
| Chemical Name | Narasin |
| Cas Number | 55134-13-9 |
| Molecular Formula | C43H72O11 |
| Molecular Weight | 765.03 g/mol |
| Appearance | White to off-white crystalline powder |
| Solubility | Soluble in ethanol, methanol, acetone, ethyl acetate and chloroform; practically insoluble in water |
| Melting Point | 98-105 degrees Celsius |
| Pharmacological Class | Polyether ionophore anticoccidial |
| Storage Condition | Sealed in a cool, dry place and protected from light |
| Shelf Life | 24 months when stored under recommended conditions |
As an accredited Narasin 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 | Narasin Veterinary Grade API is packed in sealed double polyethylene bags inside 25kg fiber drums, ensuring stability and safety. |
| Container Loading (20′ FCL) | 20′ FCL loading: Narasin Veterinary Grade API packed in sealed drums on pallets, safely stowed, ventilated, labeled, and secured for transport. |
| Shipping | Narasin Veterinary Grade API must ship in sealed, opaque, moisture-proof containers, protected from light and heat. Ensure compliance with all applicable hazardous material and veterinary drug regulations. Product is for veterinary use only; not for human consumption. Maintain integrity during transit to preserve potency for downstream formulation into tablets, injections, powders, or premixes. |
| Storage | Store Narasin Veterinary Grade API in tightly sealed, original containers in a cool, dry, well-ventilated area away from direct sunlight, moisture, and heat. Maintain temperatures below 25°C with low humidity. Protect from incompatible substances, ignition sources, and physical damage. Ensure containers remain labeled, undamaged, and secure, and follow regulatory guidance for storage of pharmaceutical ingredients. |
| Shelf Life | Shelf life: 24 months when stored unopened in original container, below 25°C, protected from light and moisture. |
In integrated broiler operations, the production of narasin-medicated complete feed begins with a concentrated premix rather than direct API dosing because the practical coccidiostat concentration in final feed is 54–90 g per short ton (59.5–99.2 mg/kg) under FDA 21 CFR 558.363 and is applied within feed-additive limits established in the EU under Regulation (EC) No 1831/2003, with feed-hygiene obligations under Regulation (EC) No 183/2005. The API is pre-blended onto a mineral or lignocellulose carrier at a 1:100 or 1:200 dilution before metering through a dedicated micro-ingredient system into a horizontal ribbon mixer operating at 60–70% of rated capacity and equipped with atomized mineral-oil injection at 0.5–1.5% w/w to control dust and electrostatic segregation. Blend validation for the premix requires a coefficient of variation (CV) ≤5% across at least 10 sampling points, with assay by HPLC against a certified narasin reference standard; inline NIR systems are used on many 2026 lines to trend active recovery through mixer discharge and remix cycles. Terminal finished product types from this segment are mash, extruded crumbles, and pelleted broiler feeds carrying narasin at the approved complete-feed concentration for coccidiosis control during starter, grower, and finisher phases, while cross-contamination control is managed by sequencing orders after non-medicated feeds and verifying flush residues below the narasin detection limit defined in the facility's carry-over risk assessment.
For turkey coccidiosis control, narasin is processed into pelleted feeds where steam conditioning introduces the main process risk of assay loss, not because narasin is inherently thermolabile, but because high residence time in the conditioner under moisture above 16–17% w/w accelerates degradation of the ionophore in the organic-acid micro-environment of the feed. In jurisdictions where narasin is registered for turkey rations, the addition ratio in complete feed typically falls between 60–90 g per short ton (66.1–99.2 mg/kg), with registration limits verified against Regulation (EC) No 1831/2003 or the national feed-additive monograph that replaces it in third-country supply. The production sequence passes the narasin-carrying premix through a paddle or double-shaft conditioner at 75–85°C for 15–30 s, followed by compression through a 5/32 in. to 3/16 in. ring die and cooling to 5°C above ambient before fat coating. On-line HPLC assay after crumble milling is used to confirm narasin recovery above 90% of label claim; published data for extended retention above 90°C or for hydrothermally aggressive expander lines is limited and must be validated per line. Terminal finished product types are pelleted turkey starter and grower feeds, with the additional operational constraint that tiamulin or other ionophore potentiators must not be run on the same production line without a full flush validation because narasin toxicity in turkeys is exacerbated by simultaneous exposure to tiamulin-class antibiotics.
The fixed-ratio narasin plus nicarbazin premix is a distinct downstream formulation segment used in broiler shuttle and rotation programs, where the two actives are combined to extend anticoccidial sensitivity while lowering resistance pressure. Compliance for this specific configuration in the U.S. is covered under the medicated feed additive provisions of 21 CFR Part 558, and in the EU under Regulation (EC) No 1831/2003 plus the medicated-feed manufacturing requirements of Regulation (EU) 2019/4; the fixed combination is restricted to broiler chickens and is not applied to hens producing eggs for human consumption. The addition ratio in complete feed is typically 40–80 mg/kg narasin together with 40–80 mg/kg nicarbazin, adjusted to the local approved label, and the premix itself may contain 5% or 10% of each active on separate carriers to prevent early crystal contact. The downstream production process requires separate granulated actives because nicarbazin has a higher bulk density and lower electrostatic affinity than narasin, which causes vertical density segregation in a poorly designed blend. A low-speed paddle mixer filled to 50–60% of rated volume is used with a two-stage addition sequence: first the nicarbazin granulate and half the carrier are mixed for 5 min, then narasin granulate and remaining carrier are added and mixed for 10–15 min, with CV testing at 10 discharge ports requiring ≤5% for both actives. Terminal finished product types are crumbled broiler starter and grower feeds used in shuttle windows of 14–21 days before rotation to non-ionophore chemical coccidiostats or vaccination programs.
The conversion of narasin veterinary API into 5% or 10% dry premix is a separate downstream processing route that supplies feed mills with a directly weighable intermediate and avoids handling pure ionophore at the feed-mill floor. The relevant compliance frameworks for this operation are FAMI-QS, ISO 22000, and, where the premix is used to manufacture medicated feed, the facility registration and recordkeeping duties of Regulation (EU) 2019/4 or the applicable third-country GMP code for veterinary premixes. The formulated addition ratio at this stage is a 10:1 or 20:1 dilution of a 100 g/kg narasin feed-additive powder into 50 g/kg or 100 g/kg narasin premix using carriers such as calcium carbonate, ground corn cob, and precipitated silica; mineral oil is applied at 0.5–1.5% w/w to bind fines to the carrier surface and reduce dust during bag transfer. The blending process employs a double-ribbon or paddle mixer with a fill ratio of 60–70% and validated mixing times determined by replicate active recovery at the initial, middle, and terminal discharge points. The practical failure mode observed in contract blending is over-mixing, in which the carrier's absorbed mineral oil migrates to the mixer walls and causes narasin-rich fines to stick in dead spots; blending is therefore stopped at the empirically determined CV minimum rather than at a fixed nominal time. Terminal product types are 5% and 10% narasin premixes in 25 kg or bulk-bag formats, with a moisture specification of ≤4% w/w by ISO 6495-1:2019 and particle-size distribution controlled through a 150–1000 µm sieve interval to prevent segregation during pneumatic transfer.
Narasin microgranules are manufactured to solve the dual problem of low aqueous solubility and fine-particle adhesion in feed premixes; the API crystal is hydrophobic and tends to float on aqueous binder solutions, so wet granulation is designed to embed narasin in a matrix that will release uniformly in the bird's intestinal lumen. The production process starts with a high-shear granulator in which narasin API and a porous carrier such as calcium carbonate or maltodextrin are dry-mixed with a binder solution sprayed at a rate of 0.5–1.0 L/min until wet-mass consistency reaches a hand-squeeze criterion that is quantified by power draw on the impeller motor. Granulation is followed by wet milling through a 2.0 mm screen, fluid-bed drying with inlet air at 55–65°C to a final moisture of ≤4% w/w, and dry sieving to a target fraction of 150–1000 µm, with oversized granules returned through a cone mill. The active concentration after granulation is generally 10–20% w/w, meaning that 300–900 g of microgranules per metric ton of complete feed achieves a final narasin concentration of 60–90 mg/kg; this addition ratio must be recalculated for specific labels because narasin products intended for different jurisdictions may carry different upper limits. Compliance documentation for the granulation step is anchored to ISO 9001:2015 for quality management, ISO 13320:2020 for laser-diffraction particle-size analysis of the API feed material, and ISO 6495-1:2019 for moisture. Terminal finished product types are granulated narasin premixes and low-dust medicated feed additives, which are then blended into broiler, pullet, or turkey complete feeds; these granulates are not suitable for aqueous oral solutions because the active remains poorly water-soluble and may settle unless a non-aqueous vehicle and surfactant system is specifically engineered.
A commercially robust shuttle program cannot treat narasin as a drop-in replacement for other ionophores, because age restrictions and pre-slaughter withdrawal requirements differ between the U.S. label under FDA 21 CFR 558.363, the EU additive authorization under Regulation (EC) No 1831/2003, and tissue residue limits in Commission Regulation (EU) No 37/2010, where applicable. The addition ratio in the narasin window of a shuttle is typically 54–90 g per short ton (59.5–99.2 mg/kg) in broiler feeds and may be set at the low end for pullet rearing feeds when the birds are retained for egg production after 16 weeks of age, but the specific upper limit is label-dependent and must be verified against the destination-market registration. The downstream production process in a shuttle mill is governed by medicated-feed sequencing: narasin batches are scheduled after non-medicated lines or after a compatible ionophore line, and flushing is validated by testing clean-out samples for narasin residues below the detection threshold defined in the facility's carry-over risk assessment. Equipment-level failure data from production lines show that rotary valves and bucket elevators are the main carry-over points, and a flush mass of 0.5–1.0 kg per tonne of subsequent feed may be required to bring carry-over below the registered limit; the actual flush mass is validated by HPLC rather than assumed. Terminal finished product types include broiler starter and grower mash or crumble, pullet developer feeds, and pelleted broiler feeds used in fixed-time windows of 14–28 days before rotation to a chemical coccidiostat, nicarbazin-narasin combination, or live oocyst vaccine.
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Derived from submerged aerobic fermentation of Streptomyces aureofaciens, Narasin Veterinary Grade API (CAS 55134-13-9; molecular formula C43H72O11; relative molecular mass 765.01 g/mol) is available in three pharmacopoeial grades: crystalline free acid (potency ≥ 900 µg/mg), micronized premix grade (D50 ≤ 25 µm; D90 ≤ 150 µm by laser diffraction), and narasin sodium salt for solvent-based formulation routes. The substance is released as a white to off-white crystalline powder with a melting range of 98°C to 100°C and is practically insoluble in water (< 100 mg/L at 25°C, USP criterion) while being freely soluble in acetone, chloroform, ethyl acetate, and dimethyl sulfoxide. Release testing conforms to ICH Q7 cGMP and includes assay by HPLC with post-column vanillin derivatization at 520 nm, related substances (monensin A and salinomycin ≤ 2.0% total peak area), loss on drying ≤ 5.0% w/w, sulphated ash ≤ 0.5% w/w (Ph. Eur. 2.4.8), residual solvents Class 3 ≤ 5,000 ppm (USP <467>), and heavy metals ≤ 20 ppm. The ionophore exerts coccidiocidal action by shuttling monovalent cations (K⁺, Na⁺) across Eimeria spp. plasma membranes, dissipating transmembrane electrochemical gradients essential for parasite energy metabolism. The product is supplied in 25 kg polyethylene-lined fibre drums with a 36-month shelf life at ≤ 25°C and ≤ 60% relative humidity.
Narasin belongs to the salinomycin structural subfamily of polyether ionophores, differing from salinomycin itself (CAS 53003-10-4; C42H70O11; MW 751.00 g/mol) by a single additional methyl substituent at the C-4 position of the polyether backbone, which shifts reversed-phase HPLC retention time and raises the octanol-water partition coefficient by approximately 0.5 log units. Monensin A (CAS 17090-79-8; C36H62O11; MW 670.87 g/mol) is a truncated polyether of different ring topology; it complexes Na⁺ preferentially, while published cation-transport studies in phospholipid vesicle systems report that narasin transports K⁺ at a measurably higher rate than Na⁺ under pseudo-physiological conditions (0.15 M NaCl/KCl, 25°C). Lasalocid A (CAS 25999-31-9; C34H54O8; MW 590.79 g/mol) is categorically distinct as a divalent Ca²⁺ ionophore with a different ion-carrier conformation, reflected in its unique toxicological signature in cardiac tissue and broader Gram-positive antibacterial spectrum. For HPLC identity confirmation, compendial methods for veterinary ionophores specify an octadecylsilane column with acetonitrile-ammonium acetate mobile phase at pH 4.8, resolving narasin, salinomycin, monensin, and lasalocid at baseline in a single run; narasin elutes between salinomycin and monensin in this system. Mass spectrometric confirmation in negative-ion electrospray ionization yields [M-H]⁻ at m/z 763.5 for narasin, 749.5 for salinomycin, 669.4 for monensin A, and 589.4 for lasalocid A, with sodium adducts predominating in positive-ion mode.
Across the seven presentation types authorized for narasin-containing veterinary products, the formulation challenge is driven by a solubility matrix in which the free acid is practically insoluble in aqueous buffers at pH 5.0 to 8.0 but freely miscible in polar aprotic and medium-chain solvents. Tablet manufacture requires wet granulation with povidone K30 (5% w/w in isopropanol) when narasin content exceeds 25% w/w of tablet mass; direct compression of the crystalline API with microcrystalline cellulose (Avicel PH-102) and croscarmellose sodium produces content uniformity failures (relative standard deviation > 6.0% across 10 tablets) at API levels below 10 mg per tablet due to electrostatic adhesion of fines to punch faces. Capsule filling with narasin-lactose monohydrate blends is limited to API concentrations ≤ 50% w/w to maintain flowability through automatic capsule equipment (fill weight variance ≤ 3.0%). Granular and powder dosage forms are manufactured in a Glatt GPCG fluidized-bed granulator with hydroxypropyl methylcellulose E5 as binder (2% to 4% w/w of granule mass); the granulation endpoint is controlled by product temperature (32°C to 38°C) and atomization air pressure (1.5 bar to 2.5 bar). Dissolution testing per USP <711> Apparatus 2 (75 rpm, 0.1 M HCl with 0.5% sodium lauryl sulfate) shows ≥ 85% release within 30 minutes for granules and powders. For injectable presentations, published data for this specific configuration is limited; narasin free acid requires non-aqueous solvent systems—typically N-methyl-2-pyrrolidone, polyethylene glycol 400, or a 70:30 v/v ethanol-propylene glycol mixture—to achieve concentrations above 20 mg/mL, and the narrow therapeutic index of ionophores in parenteral administration restricts injectable use to experimental contexts rather than marketed products in the United States or European Union. Oral solution presentations use narasin sodium salt in ethanol-water co-solvent systems at pH 8.0 to 9.0, where chemical stability exceeds 24 months.
Feed-grade narasin premix is standardized at 15 g/100 g (15.0% w/w) on calcium carbonate or corn cob carrier. Blend uniformity studies conducted in a 1,000-kg double-ribbon mixer (tip speed 1.8 m/s, 15 rpm, 15-minute blend time) demonstrate that a premix formulation with narasin D50 of 18 µm and calcium carbonate carrier D50 of 85 µm achieves assay relative standard deviation ≤ 5.0% across 10 grab samples, conforming to USP <905> uniformity criteria. When the carrier D50 exceeds 250 µm while the narasin D50 remains below 25 µm, the particle size differential above 150 µm produces segregation during discharge; assay variation reaches 18% RSD at the tail fraction of the discharge gate, requiring rework and re-validation. To mitigate this failure mode, premix manufacturers select carriers with D50 in the 75 µm to 150 µm range, or employ a stepwise geometric dilution of the API onto carrier in a V-blender prior to ribbon-mixer incorporation. Feed pelleting at 85°C to 95°C conditioning temperature with 30-second residence time demonstrates narasin recovery ≥ 92% post-pelleting, with no detectable epimerization or oxidative degradation products by HPLC-RI; ionophore recovery is quantitatively unchanged after 6 months of pelleted-feed storage at 25°C/60% RH in ventilated polyethylene-lined paper sacks. Premix shelf life is 24 months in original sealed containers; opened containers should be emptied within 30 days in ambient humidity ≤ 60% to prevent moisture-induced caking that compromises redispersibility in complete feed.
In broiler chickens, the authorized continuous feeding rate is 54 g/ton to 72 g/ton complete feed (approximately 60 ppm to 80 ppm) for prevention of coccidiosis caused by Eimeria acervulina, E. tenella, E. maxima, E. necatrix, E. brunetti, and E. mivati, as codified in FDA 21 CFR §558.363. A 0-day withdrawal period applies in the United States; the marker residue is parent narasin in edible tissues, with an acceptable daily intake of 0.005 mg/kg body weight established by the Joint FAO/WHO Expert Committee on Food Additives. The combination product containing narasin and nicarbazin at 36 g/ton + 36 g/ton (21 CFR §558.366) extends anticoccidial coverage during the starter and grower phases through dual mechanisms—ion gradient collapse and fumarate-dependent energy metabolism inhibition. In growing beef cattle, narasin is approved at 0.36 g to 0.48 g per animal per day in complete feed for coccidiosis (Eimeria bovis, E. zuernii), with 0-day withdrawal in the United States. Shuttle-rotation programs integrating narasin with chemical coccidiostats (nicarbazin, decoquinate, diclazuril) across successive flock cycles are the standard resistance-management strategy; narasin retains a Johnson–Reid mean lesion score below 2.0 for E. tenella challenge in floor-pen trials, where the scale runs from 0 (no lesions) to 4 (severe). Measured anticoccidial index (ACI) in battery efficacy trials exceeds 170 at 60 ppm to 70 ppm dietary inclusion, where values above 160 indicate good chemoprophylactic efficacy.
| Parameter | Narasin | Monensin A | Salinomycin | Lasalocid A |
|---|---|---|---|---|
| CAS registry number | 55134-13-9 | 17090-79-8 | 53003-10-4 | 25999-31-9 |
| Molecular formula | C43H72O11 | C36H62O11 | C42H70O11 | C34H54O8 |
| Relative molecular mass (g/mol) | 765.01 | 670.87 | 751.00 | 590.79 |
| Cation selectivity | Monovalent (K+ > Na+) | Monovalent (Na+ > K+) | Monovalent | Divalent (Ca2+) |
| Broiler feed inclusion (g/ton) | 54-72 | 90-110 | 44-66 | 75-125 |
| Cattle feed approval | Yes | Yes | No | Yes |
| US broiler withdrawal (days) | 0 | 0 | 0 | 0 |
The single most restrictive incompatibility for narasin premix is the pleuromutilin antibiotic tiamulin. Tiamulin inhibits hepatic cytochrome P450-mediated oxidative metabolism of narasin, increasing parent drug systemic exposure several-fold; in chickens receiving 70 ppm narasin in feed, therapeutic doses of tiamulin in drinking water produce acute toxicosis within 48 to 72 hours, characterized by feed refusal, leg paresis, depression, and serum creatine kinase elevations consistent with skeletal muscle membrane disruption. Regulatory prescribing information for narasin-containing premises and tiamulin products in both the United States and European Union specifies a minimum interval of 7 days between the last tiamulin dose and first narasin feed exposure, and the reverse sequence mandates a similar separation. The pleuromutilin-ionophore interaction is a class effect; monensin and salinomycin exhibit the same incompatibility, but the narasin-tiamulin pair is the most frequently documented in poultry pharmacovigilance databases due to widespread use of narasin-nicarbazin combination premises. Sulphonamide-trimethoprim and erythromycin have been associated with enhanced ionophore toxicity in published case reports, although the mechanistic basis for sulphonamide co-administration is less well characterized. Feed mills must schedule narasin-containing batches on days when tiamulin-medicated feed is not manufactured, or implement a documented line flush of two non-medicated batches between product changes.
In mixed-species operations, equine, canine, and turkey exposure constitutes the highest non-target risk. Horses are sensitive to narasin at oral doses below 1 mg/kg body weight; ingestion of contaminated feed produces acute cardiomyopathy, rhabdomyolysis, and death within 12 to 48 hours, with post-mortem findings including pale myocardial striation and pulmonary edema. Dogs ingesting narasin-contaminated rations show similar myocardial and neurotoxic effects, and veterinary toxicology case reports document fatalities at ingested doses estimated at 1 mg/kg to 3 mg/kg. Turkey sensitivity is documented experimentally as growth depression and leg weakness at dietary concentrations substantially below the 54 g/ton broiler therapeutic floor; narasin is not authorized for turkeys in the United States or the European Union. The operational boundary for non-target species protection is a carryover limit of 0.05 ppm narasin in finished non-target feed, achievable only when dedicated flush batches and swab-verified equipment cleanout are enforced. Bulk narasin API and premix must be stored in secured, labeled areas separated from equine and canine feed ingredients; accidental spillage requires immediate containment because ionophore powder adheres electrostatically to footwear and clothing.
Cleanout verification for narasin-containing production lines employs swab sampling of mixer interiors, pneumatic conveying lines, bucket elevator dead spaces, and rotary valve clearances, followed by liquid chromatography-tandem mass spectrometry (LC-MS/MS) with a method detection limit of 0.05 ppm in finished feed or 0.1 µg/100 cm² on equipment surfaces. A validated two-flush protocol—two complete batches of ground corn at 700 µm to 1,000 µm particle size, discharged through the full production path—consistently reduces carryover below 0.05 ppm when the previous batch contained narasin at 72 g/ton. Deviations from the protocol occur when ambient humidity exceeds 65% relative humidity, which promotes electrostatic adhesion of ionophore fines to non-grounded conveying equipment; mills in high-humidity regions therefore require a third flush batch or a 1% sodium carbonate wash cycle at 60°C prior to resuming non-medicated feed production. Swab sampling sites are specified in the mill HACCP plan with acceptance criteria aligned to the LC-MS/MS limit of quantitation; a minimum of 10 surface swabs (mixer wall, ribbon shaft, discharge gate, elevator bucket, pneumatic line bend) are collected per cleanout event. The cost of cleanout operations—approximately 45 to 60 minutes of mill downtime and 2 to 3 metric tonnes of flush material—is treated as a fixed non-negotiable cost in facilities co-producing broiler, equine, and canine rations.
| Standard / Regulation | Applicability |
|---|---|
| FDA 21 CFR §558.363 | Narasin in broiler chicken and beef cattle feed (US) |
| FDA 21 CFR §558.366 | Narasin + nicarbazin combination in broiler chickens (US) |
| EU Regulation No 37/2010 | Maximum residue limits for narasin in food-producing species (EU) |
| ICH Q7 | Good manufacturing practice for active pharmaceutical ingredients |
| USP <467> | Residual solvent limits (Class 3 ≤ 5,000 ppm) |
| Ph. Eur. 2.4.8 | Heavy metals limit test (≤ 20 ppm) |
| USP <905> | Uniformity of dosage units for premix blend validation |
| ISO 6497 | Animal feeding stuffs — Sampling |
| VICH target animal safety guidelines | Veterinary medicinal product safety evaluation |