| HS Code | 186669 |
| Product Name | Rifaximin Intramammary Infusion Veterinary Grade API |
| Active Pharmaceutical Ingredient | Rifaximin |
| Grade | Veterinary Grade |
| Dosage Forms | Tablets, Injections, Capsules, Powders, Granules, Premix, Solutions |
| Cas Number | 80621-81-4 |
| Molecular Formula | C43H51N3O11 |
| Molecular Weight | 785.88 g/mol |
| Appearance | Orange to red crystalline powder |
| Solubility | Practically insoluble in water; soluble in organic solvents such as ethanol and acetone |
| Storage Conditions | Store in a cool, dry place, protected from light and moisture |
As an accredited Rifaximin Intramammary 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 | Packaging: 25kg per drum, double polyethylene bags inside, sealed aluminium foil bag for Rifaximin veterinary grade API, ensuring stability and contamination-free delivery. |
| Container Loading (20′ FCL) | One 20-foot container loaded with palletized, drummed Rifaximin veterinary-grade API, securely stowed for safe transport. |
| Shipping | Ship in sealed, light-protected, moisture-resistant containers with desiccant, away from direct sunlight. Maintain ambient controlled temperature (15–30°C) during transit. Ensure tamper-evident packaging, clearly labeled as veterinary API, with SDS and COA. Use validated courier for pharmaceutical raw materials; avoid freezing and excessive humidity. |
| Storage | Store Rifaximin Intramammary Infusion Veterinary Grade API in a tightly sealed, original container, protected from light and moisture. Keep in a cool, dry, well-ventilated area at controlled room temperature, typically 15–30°C, away from heat sources and incompatible substances. Avoid prolonged exposure to humidity and sunlight to maintain stability, potency, and pharmaceutical-grade quality. |
| Shelf Life | Shelf life is typically 24 months from manufacture date when stored as recommended. Use before expiry date. |
Rifaximin intramammary infusion veterinary grade API is a poorly water-soluble rifamycin derivative processed into a limited set of dosage forms in which local exposure rather than systemic absorption is the critical quality target. The scenarios below are restricted to manufacturing routes for which the API has been handled in commercial veterinary pharmaceutical production or is supported by published technical dossiers; they do not constitute regulatory clearance for any specific market. Systemic injectable presentations are excluded from the downstream scenarios because published data for this specific configuration are limited; the intramammary infusion is the injection-like route for which batch-level manufacturing data exist.
| Dosage form | API addition ratio | Primary process equipment | Compliance anchor |
|---|---|---|---|
| Lactating-cow intramammary infusion | 1.0% w/w (100 mg/10 g) | Rotor-stator homogenizer and aseptic filling line | Ph. Eur. 2.6.12, 2.6.14, Regulation (EU) No 37/2010 |
| Dry-cow intramammary infusion | 2.0% w/w (200 mg/10 g) | Planetary mixer and viscous-product aseptic filling line | Ph. Eur. 2.2.10, VICH GL8, Regulation (EU) 2019/6 |
| Oral film-coated tablet | 25.0% w/w (50 mg/200 mg) | Fluid-bed granulator and rotary tablet press | Ph. Eur. 2.9.5, 2.9.3, VICH GL8 |
| Hard gelatin capsule | 33.3% w/w (50 mg/150 mg) | Slugging press and intermittent-motion capsule machine | Ph. Eur. 2.9.5, 2.9.3, VICH GL10 |
| Oral suspension | 2.0% w/v (20 mg/mL) | High-shear mixer with vacuum deaeration | Ph. Eur. 5.1.4, Ph. Eur. 2.2.10, VICH GL8 |
| Oral powder/granules/premix | 10.0% w/w (100 mg/g) | High-shear granulator, fluid-bed dryer, ribbon blender | Ph. Eur. 2.9.12, Ph. Eur. 2.2.32, Regulation (EU) 2019/4 |
When lactating-cow intramammary therapy is manufactured, the primary batch release risk is not potency but sterility, bacterial endotoxin load, and particle size distribution. The API is pre-micronized and dispersed into an anhydrous vehicle prepared from medium-chain triglycerides and fumed silica; the vehicle phase is heated to 160–180°C for 2 h to remove moisture and is then cooled to 35°C before the API is added. Aseptic processing is required because terminal steam sterilization of the finished suspension is not universally validated for rifaximin. A rotor-stator homogenizer operating at 3,000–5,000 rpm deagglomerates the API until laser diffraction per Ph. Eur. 2.9.31 shows the D90 below 20 µm, which is necessary to avoid teat canal plugging during infusion. The suspension is transferred to a filling line equipped with peristaltic pumps and volumetric dosing into HDPE intramammary applicators; in-process fill weight checks are performed at 10-minute intervals. The addition ratio for a 100 mg rifaximin dose in a 10 g single-dose applicator is 1.0% w/w; the actual weighed amount is adjusted for the assay loss observed after homogenization. The finished product must meet Ph. Eur. 2.6.12 sterility and Ph. Eur. 2.6.14 bacterial endotoxins; where the product is authorized for lactating dairy cattle, the dossier must verify the rifaximin residue entry in Regulation (EU) No 37/2010 and the assigned milk withdrawal period. The terminal product type is a single-dose intramammary suspension for lactating dairy cattle.
The dry-cow product differs from lactating-cow therapy because the vehicle must persist in the udder quarter during the entire dry period rather than disperse rapidly in milk. A higher-viscosity anhydrous oleogel is prepared by heating low-moisture peanut oil with aluminum distearate to 150°C for moisture removal, cooling to 35°C, and then incorporating micronized rifaximin under low-shear planetary mixing to avoid air entrapment. The formulation addition ratio for a 200 mg rifaximin dose in a 10 g applicator is 2.0% w/w. The product is filled into single-dose intramammary applicators under class C background and class A laminar flow; in-process viscosity is tested on a rotational viscometer per Ph. Eur. 2.2.10 at 25°C and controlled in the range of 1,500–3,500 mPa·s. Unlike oral tablets, this dosage form is not evaluated by disintegration or dissolution; release is governed by erosion of the oleogel matrix in mammary secretions, and the dossier must demonstrate syringeability, sedimentation rate, and redispersibility after storage. Redispersibility testing is performed after 24 h of sedimentation by manual shaking for 30 s; failure to redisperse is corrected by adjusting the oleogel thickener concentration. Compliance is anchored to VICH GL8 stability testing, Ph. Eur. 2.6.12 sterility, and the applicable veterinary medicinal product requirements of Regulation (EU) 2019/6. The terminal product type is a dry-cow intramammary infusion for non-lactating cattle.
In companion animal tablet production, direct compression is avoided because rifaximin exhibits low bulk density, poor flow, and a tendency to segregate when blended with common fillers. The process instead begins with fluid-bed wet granulation in which the API is mixed with lactose monohydrate and microcrystalline cellulose, sprayed with purified water and polyvinylpyrrolidone K30 as binder, and dried at an inlet air temperature of 50–60°C until the granule moisture is below 2.0%. The dried granules are milled through a 1.0 mm screen, blended with crospovidone and magnesium stearate in a bin blender, and compressed on a rotary tablet press using 8 mm round punches. A target finished tablet mass of 200 mg containing 50 mg rifaximin corresponds to an addition ratio of 25.0% w/w, adjusted for potency. Film coating is performed with an aqueous polyvinyl alcohol-based dispersion at a pan speed of 6–10 rpm; coating weight gain is controlled at 2–3% to mask the bitter taste of rifaximin without materially delaying disintegration. The finished tablet is tested for uniformity of mass per Ph. Eur. 2.9.5, dissolution per Ph. Eur. 2.9.3 in a medium containing 0.5% sodium lauryl sulfate, and stability per VICH GL8. The terminal product type is a film-coated tablet for oral administration to dogs where national authorization exists.
When the intended presentation is a hard gelatin capsule, micronized rifaximin cannot be filled directly because its low bulk density causes excessive weight variability and dusting on high-speed capsule machines. The API is first dry granulated by slugging on a rotary tablet press at a compression force of 5–10 kN, then milled through a 1.0 mm screen to create flowable granules. The granules are blended with lactose monohydrate, croscarmellose sodium, and colloidal silica in a V-blender, then filled into size 2 hard gelatin capsules on an intermittent-motion machine at a fill weight of 150 mg per capsule. An API content of 50 mg per capsule corresponds to an addition ratio of 33.3% w/w. Dissolution testing is performed per Ph. Eur. 2.9.3 in 900 mL of 0.5% sodium lauryl sulfate at 37°C, with samples at 15 min, 30 min, 45 min, and 60 min. The capsule shell moisture content is controlled below 13% because rifaximin granules can transfer moisture and cause shell softening in long-term stability batches. Compliance is anchored to Ph. Eur. 2.9.5 for mass uniformity, Ph. Eur. 2.9.3 for dissolution, and VICH GL10 bioequivalence where a generic claim is filed. The terminal product type is a hard gelatin capsule for oral administration to non-food species.
When an oral suspension is required for companion animals, the primary process failure is particle reagglomeration and foam formation during vacuum deaeration. The API is micronized to a D90 below 15 µm and then dispersed into a vehicle containing xanthan gum, microcrystalline cellulose-carrageenan co-processed thickener, and a preservative system validated at pH 4.0–4.8. The addition ratio for a 20 mg/mL suspension is 2.0% w/v, expressed as rifaximin base on the anhydrous basis. Dispersion is performed in a high-shear mixer equipped with a slotted head at 4,000 rpm for 15 min; the batch is then deaerated under vacuum at -0.85 bar. In-process controls include pH, viscosity per Ph. Eur. 2.2.10, and particle size by laser diffraction; viscosity is adjusted with additional xanthan gum to remain within the target range of 200–600 mPa·s at 25°C. A single-phase oral solution is not feasible for this API because rifaximin is practically insoluble in water; published data for a true solution formulation are limited. The container closure system is an amber glass bottle with a child-resistant closure and a graduated oral syringe. The terminal product type is an oral suspension for dogs and cats. The compliance basis for non-sterile oral liquids includes Ph. Eur. 5.1.4 and VICH GL8.
Powder and granule presentations of rifaximin are manufactured through high-shear granulation followed by carrier blending, because direct mixing of micronized API into feed-grade carriers produces segregation and dust exposure. The API is combined with corn starch and microcrystalline cellulose in a high-shear granulator, dried in a fluid-bed dryer to a loss on drying of ≤2.5%, milled through a 0.8 mm screen, and blended with sodium starch glycolate and colloidal silica in a ribbon blender. An addition ratio of 100 mg/g rifaximin in the final powder corresponds to 10.0% w/w; the granulation step is adjusted to maintain assay uniformity across 1 g, 2 g, and 5 g sachet fill weights. Sieve testing is performed per Ph. Eur. 2.9.12, and loss on drying per Ph. Eur. 2.2.32. For feed premixes intended for non-food species, the manufacturer must still document batch-level homogeneity and carry-over prevention in the feed mill. For any food-producing species claim, the current rifaximin residue entry, milk/meat withdrawal period, and medicated feed requirements under Regulation (EU) 2019/4 must be verified before market release. The terminal product types are oral powder sachets, granules, or a diluted feed premix for non-food species.
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Product code RXF-VET-IM-API-220 denotes a sterile micronized rifaximin active pharmaceutical ingredient prepared for veterinary dosage form manufacture across intramammary infusion suspensions, tablets, injectable preparations, capsules, powders, granules, premix, and non-aqueous solutions. The molecule is 4-deoxy-pyrido[1′,2′:1,2]imidazo[5,4-c]rifamycin SV, CAS 80621-81-4, molecular weight 785.88 g/mol, and appears as a reddish-orange to orange-brown crystalline powder. It is practically insoluble in water, freely soluble in dichloromethane, slightly soluble in ethanol, and sparingly soluble in acetone, which limits aqueous solution formulation unless co-solvent or complexation strategies are used. The grade is controlled for bacterial endotoxin, sterility, particle size distribution, residual solvents, heavy metals, and water content to support both aseptic intramammary preparation and oral solid dosage form manufacture in veterinary facilities operating under EU GMP Part II or equivalent. The material is not interchangeable with unmicronized oral rifaximin API because the intramammary specification imposes a D90 particle size control measured by laser diffraction according to ISO 13320:2020 and a sterile claim supported by Ph. Eur. 2.6.1. The low endotoxin acceptance limit of < 0.050 EU/mg is derived from the requirement to avoid pyrogenic reaction after intramammary administration, and the sterile micronized particle population is intended to remain suspended in oleaginous vehicles long enough to deliver the dose from a single-dose intramammary syringe.
Compliance assessment includes the USP Rifaximin monograph, Ph. Eur. methods for sterility and endotoxin, and ICH residual solvent classes. Batch-to-batch variance in micronized rifaximin is evaluated by laser diffraction and scanning electron microscopy because particle agglomeration during micronization can shift the D50 and D90 values, altering syringeability in oleaginous intramammary vehicles. The production line uses a nitrogen-inerted spiral jet mill with grinding nozzle pressure maintained within the validated range; feed rate is reduced when inlet humidity exceeds 60 % RH because adsorbed moisture promotes particle agglomeration. Milling is followed by classification and packing under Grade C cleanroom conditions according to ISO 14644-1:2015; aseptic filling of final intramammary suspensions is performed under Grade A conditions at the point of fill. The sterile API is claimed sterile with a sterility assurance level of 10⁻⁶ when gamma irradiation is used as the terminal sterilisation step for the drug substance. Dry heat sterilisation at 160 °C for 120 min is not used because micronized rifaximin may show colour change and related substance increase under these conditions; gamma irradiation above 25 kGy is avoided because degradation products may increase. Table 1 lists batch release controls. Table 2 summarises the interchangeability constraints against conventional oral veterinary rifaximin grades.
| Attribute | Acceptance criterion | Reference method |
|---|---|---|
| Appearance | Reddish-orange to orange-brown powder; free of visible agglomerates | Visual examination against qualified reference standard |
| Identification | IR spectrum concordant with reference; HPLC retention time concordant | Ph. Eur. 2.2.24; USP <621> |
| Assay (anhydrous and solvent-free basis) | 98.0 %–102.0 % | USP <621> HPLC |
| Related substances | Total impurities ≤ 2.0 %; individual unspecified impurity ≤ 0.50 % | Validated HPLC; ICH Q2(R1) |
| Water content | ≤ 2.5 % | USP <921> Method Ic |
| Residue on ignition | ≤ 0.1 % | USP <281> |
| Heavy metals | ≤ 20 ppm | USP <232>/<233> |
| Bacterial endotoxins | < 0.050 EU/mg | Ph. Eur. 2.6.14 |
| Sterility | Meets test for sterility | Ph. Eur. 2.6.1 |
| Particle size distribution | D90 ≤ 20 µm; D50 3–8 µm | Laser diffraction; ISO 13320:2020 |
| Residual solvents | Methanol ≤ 3000 ppm; ethanol ≤ 5000 ppm; dichloromethane ≤ 600 ppm | ICH Q3C Option 1 |
| Attribute | Intramammary infusion grade RXF-VET-IM-API-220 | Conventional oral veterinary rifaximin grade |
|---|---|---|
| Sterility claim | Ph. Eur. 2.6.1 compliant | Not sterile; microbial limits only |
| Bacterial endotoxin | < 0.050 EU/mg | Higher endotoxin limit or not specified for parenteral use |
| Particle size | D90 ≤ 20 µm; D50 3–8 µm | D90 typically up to 75 µm; D50 15–30 µm |
| Primary packaging | Double low-density polyethylene liners inside aluminium foil laminate, nitrogen-flushed | Fibre drum with single low-density polyethylene liner |
| Intended downstream routes | Aseptic intramammary suspensions and injectable suspensions | Tablets, capsules, powders, granules, premix |
In addition to the tabulated controls, the intramammary grade is audited for absence of β-lactam cross-contamination because rifaximin may be processed in facilities that also handle cephalosporin or penicillin APIs. Cleaning validation follows EMA guidance and uses a target carryover limit based on the permitted daily exposure of the most toxicologically active compound. The sterile API is supplied in double low-density polyethylene liners inside aluminium foil laminate; the foil provides a moisture vapour transmission rate below 0.01 g/m²/day at 38 °C/90 % RH and an oxygen transmission rate below 0.01 cm³/m²/day/atm, according to ASTM F1249 and ASTM D3985. This barrier is required because the micronized material adsorbs moisture above 60 % RH, leading to agglomeration and loss of syringeability. Unmicronized oral grade rifaximin is often packed in non-barrier fibre drums and is not suitable for aseptic processing without further micronization and sterilisation.
Direct compression of RXF-VET-IM-API-220 into veterinary tablets is not recommended as a primary route because the micronized D90 ≤ 20 µm population reduces bulk density and flow, typically requiring forced-cage or power-assisted feeders on rotary tablet presses. The powder has high specific surface area and is sensitive to moisture adsorption above 60 % RH; pre-drying in a vacuum tray dryer at 40 °C ± 2 °C for 4–6 h is required when water content exceeds 2.5 %. For capsule filling, tamping-force settings on an automatic capsule machine are adjusted because the micronized powder compresses under excessive tamping, causing weight variability. In one production scenario, a dosator nozzle capsule filler is preferred over tamping-disc machines when the formulation is a simple trituration with lactose monohydrate, because the dosator ejector pin compresses the powder column to a defined height rather than repeatedly tapping the bed. The powder blend should be characterised by angle of repose, bulk density, tapped density, and compressibility index according to USP <1174> before compression. Published data for this specific configuration is limited; therefore each blend must be qualified on the intended rotary press at minimum compaction force and speed settings to avoid punch binding due to particle adhesion to tooling surfaces.
Intramammary infusion suspensions generally formulate the sterile micronized API in an oleaginous or gel vehicle. High-shear rotor-stator mixing is used to deagglomerate the micronized powder; impeller tip speed and residence time are limited because prolonged shear above 60 °C or repeated passes can induce vehicle viscosity loss and particle aggregation. A representative development protocol uses a rotor-stator mixer at 3000 min⁻¹ for 15 min while maintaining the vessel at 20 °C ± 2 °C. After mixing, the suspension is passed through a 150 µm inline screen and filled under aseptic conditions into single-dose intramammary syringes. Syringeability is assessed by measuring ejection force through a 24 G cannula at 25 °C; the target range is formulation-specific, and published data for this specific configuration is limited. Rheological evaluation according to ISO 3219 records yield stress and plastic viscosity because both parameters control retention in the udder cistern and removal by milking. A pronounced yield stress can prevent sedimentation but may also increase ejection force, so a controlled-stress rheometer is used to measure the cross-over stress where the elastic modulus G′ becomes equal to the viscous modulus G″; formulations are adjusted to keep this value low enough for syringability while avoiding hard settling. Terminal moist-heat sterilisation at 121 °C is not applied to rifaximin suspensions because stability data under saturated steam for this molecule are limited; aseptic processing and sterile API input are therefore mandatory. Particle size during scale-up is monitored because micronized rifaximin tends to form loose agglomerates that are not fully dispersed by low-shear planetary mixers; a rotor-stator mixer with a screen-type stator is specified rather than a simple propeller agitator.
For premix and granule applications, RXF-VET-IM-API-220 is blended with lactose monohydrate or microcrystalline cellulose and wetted with polyvinylpyrrolidone solution in a high-shear granulator. The wet mass is passed through a 1.0 mm screen and dried in a fluid-bed dryer at inlet air temperature 55 °C ± 3 °C until loss-on-drying is ≤ 2.0 %. Granule sieve distribution is controlled between 150 µm and 850 µm; oversize granules are dry-milled and re-screened. The micronized API tends to segregate in low-drug-load premixes if the carrier particle size differs widely, so a two-stage geometric dilution step is required before final blending. For extruded granule forms, a twin-screw extruder with a length-to-diameter ratio of 25:1 and segmented conveying elements is used without kneading blocks in the first barrel zone to avoid frictional heat above 40 °C; the die plate is sized to 0.8 mm and spheronisation is performed at 800–1200 rpm in a spheronizer for 2–5 min. Blend uniformity validation should follow USP <905> or an equivalent veterinary standard, and published data for this specific configuration is limited until process qualification is completed.
Rifaximin is practically insoluble in water, so injectable solutions are constrained to non-aqueous vehicles or co-solvent systems. The API dissolves slowly in propylene glycol, benzyl alcohol, and certain glyceryl esters; dissolution is accelerated by heating to 40 °C ± 2 °C under nitrogen, but prolonged heating above 50 °C should be avoided because degradation products may increase. For injectable suspensions, the sterile micronized powder is wetted with the vehicle under aseptic conditions and deagglomerated using a high-shear mixer. Terminal sterile filtration of the final suspension is not feasible because the suspended particles exceed the sterilising filter pore size; therefore the drug substance must be sterile and aseptic processing is mandatory. The final injectable product is filled in amber glass vials under nitrogen. Subvisible particulate matter is controlled according to USP <788>, with limits for particles ≥ 10 µm and ≥ 25 µm applied to the reconstituted or diluted suspension. This formulation type is not interchangeable with oral powders because the non-aqueous vehicle must be selected for tissue irritation and depot release. Stability studies should follow ICH Q1A(R2) with photostability testing under ICH Q1B; published data for this specific configuration is limited.
Packaging for tropical veterinary distribution uses double low-density polyethylene liners inside a foil laminate pouch, sealed under nitrogen; a desiccant sachet is added when water content exceeds 2.5 %. The material is photolabile in solution, so primary packaging for ampoules or vials is amber glass or opaque polymer. Storage is specified at 2–8 °C for the sterile intramammary grade, with transport excursions not exceeding 25 °C for more than 48 h. Shipment containers include temperature loggers calibrated to ISO 17025; excursions above 25 °C for more than 48 h require stability assessment before use. The product is not stored in unlined high-density polyethylene drums because oxygen permeability and electrostatic attraction of micronized powder cause wall losses. Compatibility with amine-functional excipients must be tested before solution formulation because rifaximin can exhibit oxidative degradation in alkaline media. Each lot is shipped with a certificate of analysis documenting the batch release controls listed in Table 1 and a tamper-evident seal on the outer aluminium pouch.