| HS Code | 491036 |
| Product Name | 10% Avilamycin Premix Pharma Grade API for Tablet / Capsule / Granule / Injection, Oral & Injectable |
| Active Ingredient | Avilamycin |
| Concentration | 10% w/w |
| Api Grade | Pharmaceutical Grade API Premix |
| Dosage Forms | Tablet, Capsule, Granule, Injection |
| Administration Routes | Oral and Injectable |
| Appearance | White to light yellow homogeneous free-flowing powder |
| Solubility | Dispersible in water; compatible with aqueous and organic excipient systems used for oral and injectable formulations |
| Particle Size Profile | Uniform micrometric particles suitable for premixing and compression or filling |
| Moisture Content | Low moisture; controlled to ensure stability and flowability |
| Storage Conditions | Store in tight, light-resistant containers in a cool, dry place below 25°C |
| Shell Life | Typically 24 months when stored under recommended conditions |
| Packaging Note | Sealed polyethylene-lined drums or multilayer bags to protect against moisture and oxidation |
As an accredited 10% Avilamycin Premix 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.
| Packing | 10% Avilamycin Premix Pharma Grade API: supplied in 25 kg net drums with double polyethylene-lined bags, sealed and labeled. |
| Container Loading (20′ FCL) | 20′ FCL container loading: palletized, sealed drums/bags, secured to prevent shift, protected from moisture, for pharmaceutical premix shipment. |
| Shipping | Ship as temperature-controlled, tightly sealed, moisture-proof containers to preserve potency. Ensure compliance with pharmaceutical transport regulations, secure labeling, and traceability. Avoid exposure to extreme heat or humidity during transit to maintain the 10% Avilamycin premix’s stability and suitability for oral or injectable dosage production. |
| Storage | Store in a cool, dry, well-ventilated area below 25°C, protected from light, moisture, and heat. Keep in a tightly sealed original container, away from incompatible substances and food. Do not freeze. Use under clean conditions and avoid dust generation. Handle with appropriate PPE. Follow expiry date after opening. |
| Shelf Life | Shelf life is typically 24 months from manufacture when stored in original containers below 25°C, protected from moisture and light. |
In feed mill operations, the 10% avilamycin premix functions as an intermediate active carrier rather than a final dosage form. The first processing stage is a pre-blend, typically one part 10% premix to nine parts ground maize or wheat middlings by mass, yielding a 1% active pre-blend. This step reduces segregation risk when the pre-blend is metered into complete feed at a horizontal ribbon mixer. The pre-blend is discharged through a 500 μm vibratory sieve prior to the main mixer to break agglomerates. Complete feed inclusion is calculated on the active concentration: 0.100 kg of 10% premix per 1,000 kg finished feed delivers 10 g active per tonne, equivalent to 10 ppm; 0.200 kg per 1,000 kg delivers 20 g active per tonne, equivalent to 20 ppm. In jurisdictions where avilamycin is registered as a feed additive or veterinary medicinal product, mixer homogeneity is verified in accordance with ISO 6497:2002 sampling and a coefficient of variation target below 10%. Carryover prevention requires sequential flush batches with pre-determined rinsing material and cleanout of dead spaces in bucket elevators, because avilamycin residues have analytical detection limits below 0.1 ppm in some laboratory methods. The terminal product is a Type C medicated feed or a top-dress pellet manufactured to the registration label.
The main process constraint in swine top-dress granulation is the carrier-to-active ratio and particle size disparity between the premix carrier and the binder matrix. A 10% premix contains 100 mg active per 1 g, so a final granule targeting 40 mg/g active requires 400 g premix per 1,000 g total granule mass. Direct adsorption of the premix onto lactose monohydrate or maltodextrin followed by low-shear wet granulation is used; however, water addition is maintained at 8–12% w/w of the dry mass because the premix shows dust carry-over and uneven wetting at higher moisture. Granulation endpoints are monitored by impeller torque rather than fixed time. The wet mass is passed through an oscillating granulator fitted with a 1.0 mm screen and dried in a fluid-bed drier with inlet air temperature below 45°C because published forced degradation data for avilamycin at higher inlet temperatures is limited. Batch-to-batch variance in granule friability is controlled by a final dry screening step through a 1.6 mm sieve. The terminal oral granule is filled into 100 g or 500 g high-barrier laminated pouches with desiccant. The finished product is tested for loss on drying according to Ph. Eur. 2.2.32 and for uniformity of dosage units according to Ph. Eur. 2.9.40 where a monograph exists. Compliance in destination markets is based on veterinary medicinal product registration or feed additive registration; current withdrawal periods must appear on the label and are jurisdiction-specific.
For oral solid dosage forms, the 10% premix is incorporated into direct compression or dry granulation lines. A 250 mg active tablet requires 2.50 g of 10% premix per tablet, which produces a high tablet mass unless the premix is further concentrated by compression. More commonly, the premix is blended with silicified microcrystalline cellulose, lactose monohydrate, croscarmellose sodium, and magnesium stearate at a final active load of 10–25 mg per unit. Segregation of active-coated carrier particles is minimized by dry granulation with roller compaction at roll pressure 3–5 kN/cm and screen milling through 800 μm. Content uniformity is evaluated according to USP <905> or Ph. Eur. 2.9.40 with an acceptance value not exceeding 15.0. Dissolution testing in 0.1 M hydrochloric acid with 0.5% sodium lauryl sulfate at 75 rpm using USP apparatus II is used when a dissolution specification exists; published data for avilamycin dissolution in this specific configuration is limited. Tablet hardness is set at 40–80 N for tablet weights between 250 mg and 1,000 mg, with friability below 1.0% as per USP <1216>. The terminal products are film-coated tablets or hard gelatin capsules for oral administration in target animal species where authorized.
Published data for licensed injectable avilamycin formulations is limited. A development-scale non-aqueous suspension is technically assessable because avilamycin has low aqueous solubility, and micronization rather than dissolution is required. In such a design, the 10% premix is first delipidized and passed through a jet mill with grinding gas pressure of 6–8 bar to a D90 below 10 μm. The micronized solid is dispersed in ethyl oleate containing 0.5% w/v polysorbate 80 and 0.2% w/v butylated hydroxytoluene. A high-shear rotor-stator mixer at 10,000–15,000 rpm for 10 minutes is followed by aseptic filling because terminal steam sterilization may degrade the active or break the suspension. For injectable veterinary products, sterility is tested according to Ph. Eur. 2.6.1, bacterial endotoxins by Ph. Eur. 2.6.14, and subvisible particulate matter by Ph. Eur. 2.9.19. The formulation must be used only where a veterinary injectable route is expressly authorized; absence of published monographs means the development batch requires full method validation.
Oral paste formulation of avilamycin for pre-ruminant calves is constrained by syringeability and active-carrier sedimentation. A 10% premix is dispersed in a non-aqueous carrier system composed of medium-chain triglycerides, colloidal silicon dioxide, and a polymeric suspending agent. The target dispersion is passed through a colloid mill with gap setting 0.15 mm. Viscosity is measured on a rotational viscometer with spindle SC4-27 at 25°C and shear rate 10 s⁻¹; a workable range is 1,200–2,500 mPa·s, because values above 2,500 mPa·s cause inconsistent extrusion from multi-dose dial-a-dose syringes. Sedimentation volume after 72 hours is evaluated after storage at 25°C and 60% RH. The terminal product is a ready-to-use oral paste in a 30 mL multi-dose syringe. Uniformity of delivered dose is tested by extruding 10 consecutive doses from the same syringe and assaying active content by HPLC-UV; relative standard deviation should not exceed 5.0%. Compliance is based on national veterinary medicinal product requirements.
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Supplied as a dilutable orthosomycin intermediate rather than a neat active pharmaceutical ingredient, the 10% avilamycin premix designated for tablet, capsule, granule, oral liquid, and injectable compounding is standardized to 100 g/kg avilamycin activity on an as-is basis. The designation is a mass-based potency statement, not the purity of a single molecular entity. Avilamycin is a fermentation-derived complex of closely related orthosomycins, the principal component being avilamycin A, with the complex associated with CAS RN 11051-71-1. Because no harmonized EP, USP, or Ph. Eur. monograph exists for avilamycin premix as a dosage-form intermediate, release acceptance criteria must be derived from the supplier’s validated HPLC or microbiological potency method and from the carrier-specific certificate of analysis. The material is therefore not equivalent to a pure avilamycin API, nor is it directly interchangeable with other 10% antibiotic premixes without reformulation and stability verification. Model identification is manufacturer-specific; there is no global model code. The relevant identifiers are the active concentration, CAS RN, and the supplier’s product code.
The remaining 90% of the premix is not formulation-inert. The carrier may be a carbonate, silica, dextrose, lactose, or another flow-regulating diluent that determines bulk density, particle size distribution, moisture uptake, angle of repose, and segregation tendency. In tablet or capsule manufacturing, the carrier dominates blend behavior because the active fraction is only 10%; the system is therefore processed as a formulated intermediate rather than as a drug substance. A carrier that is not specified or controlled can shift the compression profile, alter disintegration time, and produce low-potency pockets during transfer and hopper discharge. Because avilamycin is used in veterinary medicine, the regulatory status of the premix is not automatically harmonized: use in food-producing species is subject to national prescription rules, maximum residue limits, and withdrawal periods.
No single set of compendial limits is universally applicable. A minimum release data package for a non-sterile pharma-grade premix of this type should include active content, identification, loss on drying, bulk density, particle size, and microbial quality. Table 1 lists representative parameters used to evaluate such powders; the values are typical of non-sterile pharmaceutical powder intermediates but must be replaced with the actual manufacturer’s limits for the specific batch and carrier. Potency by HPLC is normally expressed against an avilamycin reference standard and is preferably supported by a microbiological assay because the fermentation complex may contain biologically active minor components. For facilities using the premix in a cGMP product, operations should comply with FDA 21 CFR 211 or equivalent EudraLex Volume 4 requirements for handling, sampling, and batch release.
Pharmacopoeial status is critical: because the premix is not the subject of an EP or USP monograph, the analytical method is often supplied by the manufacturer. The HPLC method should be validated according to ICH Q2(R1) for specificity against avilamycin complex components, linearity over 80–120% of nominal concentration, accuracy, precision, and robustness. The microbiological assay, if used, should be performed with a defined indicator organism and reference standard; the result is reported in µg of avilamycin activity per mg or g. When both HPLC and microbiological assay are used, the latter may detect biologically active minor components that are not fully separated by HPLC, creating apparent assay differences that must be investigated before batch release.
| Parameter | Representative release target | Method/standard | Processing relevance |
|---|---|---|---|
| Avilamycin activity | 9.5–10.5% w/w as-is | HPLC vs reference standard; confirm by microbiological assay | Defines dose calculation and blend potency |
| Identification | Retention time and UV spectrum consistent with avilamycin A | HPLC with diode-array detection | Prevents carrier-only mix-up |
| Loss on drying | ≤5.0% w/w | Ph. Eur. 2.2.32 | Controls sticking, granulation endpoint, and tablet hardness |
| Bulk density | Report value; carrier-specific | Ph. Eur. 2.9.34 | Influences hopper discharge and die filling |
| Water activity | ≤0.60 | USP <1112> | Reduces microbial growth and hydrolytic degradation |
| Microbial limits | TAMC ≤10³ CFU/g; TYMC ≤10² CFU/g; E. coli absent in 1 g | Ph. Eur. 5.1.4 | Fails oral solid release at high bioburden; injection requires further sterilization |
| Heavy metals | ≤20 ppm total heavy metals as Pb | Ph. Eur. 2.4.8 | General safety control |
| Residual solvents | Class 1/2/3 limits applied to fermentation and carrier residues | ICH Q3C | Required for pharma-grade use in injectable or oral liquid |
For granule and oral powder applications, particle-size distribution should also be reported with D10, D50, and D90 values. A broad distribution increases segregation and makes the dry blend sensitive to transfer. If the premix is intended for wet granulation, the solubility of the carrier in the granulation fluid should be tested; a highly soluble carrier can produce a viscous mass that overloads the wet mill, while an insoluble carrier can remain as visible particles in the final tablet core.
For tablet and capsule manufacturing, the premix is not directly compressible in most carrier configurations. A delumping step through a 0.5 mm or 0.8 mm screen on a conical mill or oscillating granulator is required to break soft agglomerates, reduce electrostatic clumping, and narrow the particle-size gap between the premix and direct-compression diluents. After delumping, the premix is combined with diluent in a bin blender or V-blender; blending should be validated by sampling at least 10 positions and assaying for avilamycin. A blend uniformity coefficient of variation ≤ 5.0% is a common acceptance target for low-dose solid oral products, but the acceptance value must be derived from process capability and the regulatory filing.
If flow problems appear as a compressibility index above 25% or a Hausner ratio above 1.40, colloidal silicon dioxide at 0.5% to 1.0% w/w may be added. The mixer speed and total blending time should not exceed the validated limits because hydrophobic silica can coat the carrier and reduce tablet tensile strength while increasing disintegration time. Charged excipients such as croscarmellose sodium are added only after the active blend uniformity step is completed because they can interact with the carrier and create hotspots under high-shear mixing.
Wet granulation is preferred when the carrier is hygroscopic or when the dose is so low that dry blending cannot maintain uniformity through transfer and compression. In a high-shear mixer, the premix is dry-mixed with a diluent, binder, and disintegrant before aqueous or hydroalcoholic granulation fluid is added. The liquid-to-solid ratio, impeller speed, and chopper speed are adjusted to reach a granule endpoint; overmassing can dissolve the carrier and block the wet mill. After fluid-bed drying to a residual moisture of typically 2.0% to 3.0% w/w for oral solids, the dried granules are size-reduced through a 1.0 mm screen, lubricated, and compressed. The exact residual moisture depends on the carrier; no single value is universal across carbonate, dextrose, and silica carriers. Drying inlet air temperature should be kept conservative, often below 60°C, because avilamycin orthosomycin stability can be affected by heat and local moisture.
During compression, a compaction simulator or a single-punch instrumented press should be used to define the compressibility curve. The premix contributes only 10% active; therefore, the compaction behavior is largely controlled by the diluent. Formulations containing brittle diluents such as dicalcium phosphate may produce tablets with acceptable hardness but variable porosity, while plastic diluents such as microcrystalline cellulose may produce robust tablets with longer disintegration. Compression force, punch penetration, and press speed are set from the granule D10/D50/D90 and residual moisture; if granule fines exceed 30%, segregation and weight variation can increase. A release test for content uniformity according to Ph. Eur. 2.9.40 may be used for the finished dosage form, with the acceptance value dependent on the dose and number of units.
For capsule filling, the granule flow and particle size distribution affect die-filling consistency; a D90 above 1.0 mm may cause weight variation in high-speed dosator or tamping-pin capsule machines. For granules filled into sachets, the powder must be free-flowing and non-dusting, and the carrier must not be hygroscopic enough to cause caking. In feed premix applications, the product is typically diluted into a carrier such as ground corn or soybean meal before addition to feed, using a ribbon mixer or twin-shaft paddle mixer; the mixing time is determined by tracer studies, not by a fixed number of minutes.
For injectable or oral liquid preparation, the carrier-rich premix introduces additional variables. Avilamycin has limited aqueous solubility; the resulting formulation may require a non-aqueous vehicle, a solubilizing co-solvent, a surfactant system, or a particle-size-reduction step such as micronization or high-pressure homogenization. The premix carrier may not be suitable for injection because insoluble carrier particles can violate particulate-matter limits and cause injection-site reactions. Consequently, the use of this 10% premix in injectable compounding is only technically viable where the carrier is fully soluble in the selected vehicle or is removed during sterile filtration, and where the selected membrane is validated for avilamycin adsorption. Published data for this specific configuration is limited; formulation development must include a solubility screen, filter compatibility study, and extractables assessment.
Sterility assurance for an injectable finished product is governed by the finished dosage form’s pharmacopoeial requirements. If terminal moist-heat sterilization is not feasible due to orthosomycin thermolability, aseptic processing under an ISO 14644-1 cleanroom envelope is required, with batch sterility testing according to USP <71> and bacterial endotoxin limits defined for the target species using USP <85> or Ph. Eur. 2.6.14. The premix itself is non-sterile and cannot be rendered sterile by dry heat without risk of potency loss. Any claim that a 10% avilamycin premix is suitable for injection must be supported by a development report that includes bioburden reduction, filter validation, and stability data. Carbonate carriers should not be acidified without venting because carbon dioxide evolution can rupture sealed containers; this restricts the choice of aqueous vehicles and buffer systems.
Oral liquid suspensions require antimicrobial preservation, but avilamycin activity should be confirmed in the presence of preservatives because some preservatives may alter the orthosomycin lactone ring or interact with the carrier. The final oral liquid pH should be controlled to the stability range established by stress testing; if no pH stability data exist for the supplier’s premix, a pH-rate profile must be generated before batch manufacture. The oral route and the injectable route are not interchangeable processing paths: oral administration targets gastrointestinal exposure, while injectable administration requires systemic safety, sterility, particle control, and endotoxin control that are absent from a non-sterile premix.
The processing and clinical differences between this product and other antimicrobial premixes arise from its orthosomycin class, its fermentation-derived complex, and its concentration as a 10% intermediate. Unlike ionophore premixes such as monensin or lasalocid, which are polyether ionophores used mainly for coccidiosis control, avilamycin premix is not considered a coccidiostat in the same class; its activity is oriented toward Gram-positive enteric organisms. Unlike macrolide or lincosamide premixes, avilamycin is an orthosomycin and is structurally distinct from tylosin or lincomycin. Cross-resistance between orthosomycins and macrolides/lincosamides cannot be assumed from structural class alone because the target binding site may differ; however, the absence of globally harmonized clinical breakpoints means that susceptibility statements should be derived from regional veterinary diagnostic data. Table 2 outlines the practical distinctions relevant to manufacturing and formulation.
| Product or class | Active load and form | Manufacturing impact | Differentiating factor |
|---|---|---|---|
| 10% avilamycin premix | 100 g/kg orthosomycin complex on carrier | Low-dose carrier-rich intermediate; segregation risk; granulation required for most solid oral formats; injection requires carrier removal or solubility | No harmonized monograph; class-specific release tests |
| Neat avilamycin API | Potency defined by supplier; not carrier-diluted | May be used for injectable or specialized formulations after solubilization and sterile filtration; occupational exposure controls required | Purity and route flexibility; not a direct premix replacement |
| Macrolide premix, e.g. tylosin | Varying active load on carrier | Similar low-dose blending but different solubility, stability, and analytical methods | Macrolide class spectrum and resistance mechanisms |
| Ionophore premix, e.g. monensin | Varying active load on carrier | Feed-only in most jurisdictions; toxic by injection; not interchangeable with orthosomycin premix | Polyether ionophore chemistry; different safety boundary |
Regulatory status is the most significant external difference. In the European Union, antibiotic growth-promoting feed additives were withdrawn under Regulation (EC) No 1831/2003, and avilamycin is not authorized as a feed additive for growth promotion. Where the product is used in food-producing animals under veterinary prescription, the prescriber must apply the relevant maximum residue limit, withdrawal period, and national antimicrobial stewardship requirements. The designation “pharma grade” does not confer automatic regulatory clearance; jurisdiction-specific approval remains mandatory for any finished oral or injectable product.
Stored in a dry area at 20°C to 25°C and relative humidity ≤ 60%, the unopened premix should be retested for moisture and microbial quality at intervals defined by the manufacturer’s stability protocol. Open bags or drums should be consumed in a single campaign because repeated exposure to ambient humidity can change carrier moisture and flow, causing sticking during compression and inaccurate potency calculations. The product should not be blended with amine-containing excipients or strong alkaline agents without compatibility data because orthosomycin lactone ring stability may be pH-dependent. If a customer-specific granule or powder blend is required, the manufacturer should confirm particle-size distribution, bulk density, and dispersibility before filling; the high low-dose potency of 10% does not remove the need for blend uniformity validation on the final dosage form.